96-21941. National Emission Standards for Hazardous Air Pollutant Emissions: Group I Polymers and Resins  

  • [Federal Register Volume 61, Number 173 (Thursday, September 5, 1996)]
    [Rules and Regulations]
    [Pages 46906-46985]
    From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
    [FR Doc No: 96-21941]
    
    
    
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    Part II
    
    
    
    
    
    Environmental Protection Agency
    
    
    
    
    
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    40 CFR Part 63
    
    
    
    National Emissions Standards for Hazardous Air Pollutant Emissions: 
    Group I Polymers and Resins; Final Rule
    
    Federal Register / Vol. 61, No. 173 / Thursday, September 5, 1996 / 
    Rules and Regulations
    
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    ENVIRONMENTAL PROTECTION AGENCY
    
    40 CFR Part 63
    
    [AD-FRL-5543-1]
    RIN 2060-AE37
    
    
    National Emission Standards for Hazardous Air Pollutant 
    Emissions: Group I Polymers and Resins
    
    AGENCY: Environmental Protection Agency (EPA).
    
    ACTION: Final rule.
    
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    SUMMARY: This action promulgates national emission standards for 
    hazardous air pollutants (NESHAP) from existing and new plant sites 
    that emit organic hazardous air pollutants (HAP) identified on the 
    EPA's list of 189 HAP. The organic HAP are emitted during the 
    manufacture of one or more elastomers.
        In the production of elastomers, a variety of organic HAP are used 
    as monomers or process solvents. Available emissions data gathered in 
    conjunction with the development of the elastomer standards show that 
    the following organic HAP are those which have the potential for 
    reduction by implementation of the standard: Styrene, n-hexane, 1,3-
    butadiene, acrylonitrile, methyl chloride, hydrogen chloride, carbon 
    tetrachloride, chloroprene, and toluene. Some of these pollutants are 
    considered to be mutagens and carcinogens, and all can cause reversible 
    or irreversible toxic effects following exposure. The potential toxic 
    effects include eye, nose, throat, and skin irritation; liver and 
    kidney toxicity, and neurotoxicity. These effects can range from mild 
    to severe. The rule is estimated to reduce organic HAP emissions from 
    existing affected sources by over 6,300 megagrams per year (Mg/yr). The 
    majority of the organic HAP regulated by these standards are also 
    volatile organic compounds (VOC). In reducing emissions of organic HAP, 
    VOC are also reduced.
        The rule implements section 112(d) of the Act, which requires the 
    Administrator to regulate emissions of HAP listed in section 112(b) of 
    the Act. The intended effect of this rule is to protect the public by 
    requiring the maximum degree of reduction in emissions of organic HAP 
    from new and existing major sources that the Administrator determines 
    is achievable, taking into consideration the cost of achieving such 
    emission reduction, and any nonair quality, health and environmental 
    impacts, and energy requirements.
    
    EFFECTIVE DATE: September 5, 1996. See the Supplementary Information 
    section concerning judicial review.
    
    ADDRESSES: Docket. Docket No. A-92-44, containing information 
    considered by the EPA in development of the promulgated standards, is 
    available for public inspection and copying between 8 a.m. and 4 p.m., 
    Monday through Friday, at the following address in room M-1500, 
    Waterside Mall (ground floor): U. S. Environmental Protection Agency, 
    Air and Radiation Docket and Information Center (MC-6102), 401 M Street 
    SW., Washington, DC 20460; telephone: (202) 260-7548. A reasonable fee 
    may be charged for copying docket materials.
    
    FOR FURTHER INFORMATION CONTACT: For questions concerning applicability 
    and other rule determinations, inquiries should be directed to the 
    appropriate regional office contact listed below:
    
    Greg Roscoe, Air Programs Compliance, Branch Chief, U.S. EPA Region I, 
    5EA, JFK Federal Building, Boston, MA 02203, (617) 565-3221.
    Kenneth Eng, Air Compliance Branch Chief, U.S. EPA Region II, 290 
    Broadway, New York, NY 10007-1866, (212) 637-4000.
    Bernard Turlinski, Air Enforcement Branch Chief, U.S. EPA Region III 
    (3AT10), 841 Chestnut Building, Philadelphia, PA 19107, (215) 597-3989.
    Jewell A. Harper, Air Enforcement Branch, U.S. EPA Region IV, 3345 
    Courtland Street, NE., Atlanta, GA 30365, (404) 347-2904.
    George T. Czerniak, Jr., Air Enforcement Branch Chief, U.S. EPA Region 
    V (5AE-26), 77 West Jackson Street, Chicago, IL 60604, (312) 353-2088.
    John R. Hepola, Air Enforcement Branch Chief, U.S. EPA Region VI, 1445 
    Ross Avenue, Suite 1200, Dallas, TX 75202-2733, (214) 665-7220.
    Donald Toensing, Chief, Air Permitting and Compliance Branch, U.S. EPA 
    Region VII, 726 Minnesota Avenue, Kansas City, KS 66101, (913) 551-
    7446.
    Douglas M. Skie, Air and Technical Operations, Branch Chief, U.S. EPA 
    Region VIII, 999 18th Street, Suite 500, Denver, CO 80202-2466, (303) 
    312-6432.
    Colleen W. McKaughan, Air Compliance Branch Chief, U.S. EPA Region IX, 
    75 Hawthorne Street, San Francisco, CA 94105, (415) 744-1198.
    Christopher Hall, Air Toxics Program Manager, U.S. EPA Region X, 1200 
    Sixth Avenue, OAQ-107, Seattle, WA 98101-9797, (206) 553-1949.
    
        For information concerning the technical analysis for this rule, 
    contact Mr. Robert Rosensteel at (919) 541-5608, Organic Chemicals 
    Group, Emission Standards Division (MD-13), U.S. Environmental 
    Protection Agency, Research Triangle Park, North Carolina 27711.
    
    SUPPLEMENTARY INFORMATION: Regulated entities. Entities potentially 
    regulated by this action are elastomer product process units (EPPUs) 
    manufacturing the same primary product and located at a plant site that 
    is a major source of HAP. Regulated categories and entities include:
    
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                Category                  Examples of regulated entities    
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    Industry........................  Producers of butyl rubber, halobutyl  
                                       rubber, epichlorohydrin elastomers,  
                                       ethylene propylene rubber, HypalonTM,
                                       neoprene, nitrile butadiene rubber,  
                                       nitrile butadiene latex, polysulfide 
                                       rubber, polybutadiene rubber/styrene 
                                       butadiene rubber by solution, styrene
                                       butadiene latex, and styrene         
                                       butadiene rubber by emulsion.        
    ------------------------------------------------------------------------
    
        This table is not intended to be exhaustive, but rather provides a 
    guide for readers regarding entities likely to be regulated by this 
    action. This table lists the types of entities that EPA is now aware 
    could potentially be regulated by this action. Other types of entities 
    not listed in the table could also be regulated. To determine whether 
    your facility is regulated by this action, you should carefully examine 
    the applicability criteria in Sec. 63.480 of the rule. If you have 
    questions regarding the applicability of this action to a particular 
    entity, consult the person listed in the preceding FOR FURTHER 
    INFORMATION CONTACT section.
        Response to Comment Document. The response to comment document for 
    the promulgated standards contains: (1) A summary of the public 
    comments made on the proposed standards and the Administrator's 
    response to the comments; and (2) A summary of the changes made to the 
    standards since proposal. The document may be obtained from the U.S. 
    EPA Library (MD-35), Research Triangle Park, North Carolina 27711, 
    telephone (919) 541-2777; or from the National Technical Information 
    Services, 5285 Port Royal Road, Springfield, Virginia 22151, telephone 
    (703) 487-4650. Please refer to ``Hazardous Air Pollutant Emissions 
    from Process Units in the Elastomers Manufacturing Industry--Basis and 
    Purpose Document for Final Standards, Summary of Public Comments and
    
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    Responses'' (EPA-453/R-96-006b; May 1996). This document is also 
    located in the docket (Docket Item No. V-C-1) and is available for 
    downloading from the Technology Transfer Network. The Technology 
    Transfer Network is one of the EPA's electronic bulletin boards. The 
    Technology Transfer Network provides information and technology 
    exchange in various areas of air pollution control. The service is free 
    except for the cost of a phone call. Dial (919) 541-5742 for up to a 
    14,400 bps modem. If more information on the Technology Transfer 
    Network is needed, call the HELP line at (919) 541-5384.
        Previous Background Documents. The following is a listing of 
    background documents pertaining to this rulemaking. The complete title, 
    EPA publication number, publication date, and docket number are 
    included. Where appropriate, the abbreviated descriptive title is used 
    to refer to the document throughout this notice.
        (1) Hazardous Air Pollutant Emissions from Process Units in the 
    Elastomer Manufacturing Industry--Supplementary Information Document 
    for Proposed Standards. EPA-453/R-95-005a, May 1995; Docket number A-
    92-44, item number III-B-2.
        (2) Hazardous Air Pollutant Emissions from Process Units in the 
    Elastomer Manufacturing Industry--Basis and Purpose Document for 
    Proposed Standards. EPA-453/R-95-006a, May 1995; Docket number A-92-44, 
    item number III-B-1.
        Judicial Review. Under section 307(b)(1) of the Act, judicial 
    review of the final rule is available only by filing a petition for 
    review in the U.S. Court of Appeals for the District of Columbia 
    Circuit within 60 days of today's publication of this final rule. Under 
    section 307(b)(2) of the Act, the requirements that are the subject of 
    today's notice may not be challenged later in civil or criminal 
    proceedings brought by the EPA to enforce these requirements.
        The information presented in this preamble is organized as follows:
    
    I. Summary of Considerations Made in Developing This Standard
    
    A. Background and Purpose of the Regulation
    B. Source of Authority
    C. Technical Basis of Regulation
    D. Stakeholder and Public Participation
    
    II. Summary of Promulgated Standards
    
    A. Storage Vessel Provisions
    B. Front-End Process Vent Provisions
    C. Back-end Process Provisions
    D. Wastewater Provisions
    E. Equipment Leak Provisions
    F. Emissions Averaging Provisions
    G. Compliance and Performance Test Provisions and Monitoring 
    Requirements
    H. Recordkeeping and Reporting Provisions
    
    III. Summary of Impacts
    
    A. Facilities Affected by these NESHAP
    B. Primary Air Impacts
    C. Other Environmental Impacts
    D. Energy Impacts
    E. Cost Impacts
    F. Economic Impacts
    
    IV. Significant Comments and Changes to the Proposed Standards
    
    A. Applicability Provisions and Definitions
    B. Storage Vessel Provisions
    C. Continuous Front-end Process Vent Provisions
    D. Batch Front-end Process Vent Provisions
    E. Back-end Process Operation Provisions
    F. Wastewater Operations Provisions
    G. Equipment Leak Provisions
    H. Emissions Averaging Provisions
    I. Monitoring
    J. Recordkeeping and Reporting
    
    V. Administrative Requirements
    
    A. Docket
    B. Executive Order 12866
    C. Paperwork Reduction Act
    D. Regulatory Flexibility Act
    E. Small Business Regulatory Enforcement Fairness Act of 1996 
    (SBREFA)
    F. Unfunded Mandates
    
    I. Summary of Considerations Made in Developing This Standard
    
    A. Background and Purpose of Regulation
    
        The Clean Air Act was created in part ``to protect and enhance the 
    quality of the Nation's air resources so as to promote the public 
    health and welfare and the productive capacity of its population'' 
    (CAA, section 101(b)(1)). Section 112(b) lists 189 HAP believed to 
    cause adverse health or environmental effects. Section 112(d) requires 
    that emission standards be promulgated for all categories and 
    subcategories of major sources of these HAP and for many smaller 
    ``area'' sources listed for regulation, pursuant to section 112(c). 
    Major sources are defined as those that emit or have the potential to 
    emit at least 10 tons per year of any single HAP or 25 tons per year of 
    any combination of HAP.
        On July 16, 1992 (57 FR 31576), the EPA published a list of 
    categories of sources slated for regulation. This list included all 
    nine of the source categories regulated by the standards being 
    promulgated today. The statute requires emissions standards for the 
    listed source categories to be promulgated between November 1992 and 
    November 2000. On December 3, 1993, the EPA published a schedule for 
    promulgating these standards (58 FR 83841). Standards for the nine 
    source categories covered by today's rule were proposed on June 12, 
    1995 (60 FR 30801).
        For the purpose of this rule, the EPA has separated the 9 Group 1 
    polymers into 12 elastomer products (i.e., subcategories). These 
    products are butyl rubber (BR), halobutyl rubber (HBR), epichlorohydrin 
    elastomers (EPI), ethylene propylene rubber (EPR), HypalonTM 
    (HYP), neoprene (NEO), nitrile butadiene rubber (NBR), nitrile 
    butadiene latex (NBL), polysulfide rubber (PSR), polybutadiene rubber/
    styrene butadiene rubber by solution (PBR/SBRS), styrene butadiene 
    latex (SBL), and styrene butadiene rubber by emulsion (SBRE).
        In the 1990 Amendments to the Clean Air Act, Congress specified 
    that each standard for major sources must require the maximum reduction 
    in emissions of HAP that the EPA determines is achievable, considering 
    cost, non-air quality health and environmental impacts, and energy 
    requirements. In essence, these Maximum Achievable Control Technology 
    (MACT) standards would ensure that all major sources of air toxics 
    achieve the level of control already being achieved by the better 
    controlled and lower emitting sources in each category. This approach 
    provides assurance to citizens that each major source of toxic air 
    pollution will be required to employ good control measures to limit its 
    emissions.
        Available emission data, collected during the development of this 
    rule, shows that pollutants that are listed in section 112(b)(1) and 
    are emitted by Group I Polymer and Resins sources include n-hexane, 
    styrene, 1,3-butadiene, acrylonitrile, methyl chloride, carbon 
    tetrachloride, chloroprene, and toluene. Some of these pollutants are 
    considered to be probable human carcinogens when inhaled, and all can 
    cause reversible and irreversible toxic effects following exposure. 
    These effects include respiratory and skin irritation, effects upon the 
    eye, various systemic effects including effects upon the liver, kidney, 
    heart and circulatory systems, neurotoxic effects, and in extreme 
    cases, death.
        The EPA does recognize that the degree of adverse effects to health 
    can range from mild to severe. The extent and degree to which the 
    health effects may be experienced is dependent upon (1) the ambient 
    concentrations observed in the area (e.g., as influenced by emission 
    rates, meteorological conditions, and terrain), (2) the frequency of 
    and duration of exposures, (3) characteristics of the exposed 
    individuals (e.g., genetics, age, pre-existing health conditions, and 
    lifestyle) which vary significantly with the
    
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    population, and (4) pollutant specific characteristics (e.g., toxicity, 
    half-life in the environment, bioaccumulation, and persistence).
        Due to the volatility and relatively low potential for 
    bioaccumulation of these pollutants, air emissions are not expected to 
    deposit on land or water and cause subsequent adverse health or 
    ecosystem effects.
        The alternatives considered in the development of this regulation, 
    including those alternatives selected as standards for new and existing 
    elastomer sources, are based on process and emissions data received 
    from every existing elastomer facility known to be in operation at the 
    time of the initial data collection. During the development of today's 
    rule, the EPA met with industry several times to discuss this data. In 
    addition, facilities and State regulatory authorities had the 
    opportunity to comment on draft versions of the proposed regulation and 
    to provide additional information. The EPA published the proposed rule 
    for comment on June 12, 1995 (60 FR 30801). The public comments that 
    were received on the proposed rule are summarized in the Basis and 
    Purpose Document for Final Standards, Summary of Public Comments and 
    Responses (Docket Item No. V-C-1). These comments were considered, and 
    in some cases, today's standards reflect these comments. Of major 
    concern to commenters were the reporting and recordkeeping burden and 
    the requirements for back-end process operations and wastewater 
    control.
        The final standards give existing sources 3 years from the date of 
    promulgation to comply. Subject to certain limited exceptions, this is 
    the maximum amount of time allowed under the Clean Air Act. New sources 
    are required to comply with the standard upon startup. The EPA believes 
    these standards to be achievable for affected sources within the 
    timeframes provided. The number of existing sources affected by this 
    rule is less than 50; therefore, the EPA does not believe that required 
    retrofits or other actions cannot be achieved in the time frame 
    allotted.
        Included in the final rule are methods for determining initial 
    compliance as well as monitoring, recordkeeping, and reporting 
    requirements. All of these components are necessary to ensure that 
    sources will comply with the standards both initially and over time. 
    However, the EPA has made every effort to simplify the requirements in 
    the rule. The Agency has also attempted to maintain consistency with 
    existing regulations by either incorporating text from existing 
    regulations or referencing the applicable sections, depending on which 
    method would be least confusing for a given situation.
        As described in the ``Basis and Purpose Document for Proposed 
    Standards'' (EPA-453/R-95-006a), regulatory alternatives were 
    considered that included a combination of requirements equal to, and 
    above, the MACT floor. Cost-effectiveness was a factor considered in 
    evaluating options above the floor; in cases where options more 
    stringent than the floor were selected, they were judged to have a 
    reasonable cost effectiveness. For epichlorohydrin rubber (EPR), 
    polybutadiene rubber (PBR)/styrene butadiene rubber (SBR) (by 
    solution), and SBR (by emulsion) the estimated cost effectiveness was 
    found to be relatively high at the MACT floor level due to the 
    requirements for process back-end operations. However, the back-end 
    provisions of the regulation contain several options for compliance 
    that will allow facilities to select the most cost-effective option 
    based on facility-specific considerations.
        Representatives from other interested EPA offices and programs are 
    included in the regulatory development process as members of the Work 
    Group. The Work Group is involved in the regulatory development 
    process, and must review and concur with the regulation before proposal 
    and promulgation. Therefore, the EPA believes that the implications to 
    other EPA offices and programs have been adequately considered during 
    the development of these standards.
    
    B. Source of Authority
    
        National emission standards for new and existing sources of HAP 
    established under section 112(d) reflect MACT or
    
        * * * the maximum degree of reduction in emissions of the HAP * 
    * * that the Administrator, taking into consideration the cost of 
    achieving such emission reduction, and any nonair quality health and 
    environmental impacts and energy requirements, determines is 
    achievable for new or existing sources in the category or 
    subcategory to which such emission standard applies * * * (42 U.S.C. 
    7412(d)(2)).
    
        For new sources, section 112(d)(3) provides that the standards for 
    a source category or subcategory ``shall not be less stringent than the 
    emission control that is achieved in practice by the best controlled 
    similar source, as determined by the Administrator.'' Section 112(d)(3) 
    provides further that for existing sources the standards shall be no 
    less stringent than the average emission limitation achieved by the 
    best performing 12 percent of the existing sources for source 
    categories and subcategories with 30 or more sources or the average 
    emission limitation achieved by the best performing 5 sources for 
    source categories or subcategories with fewer than 30 sources. These 
    two minimum levels of control define the MACT floor for new and 
    existing sources.
        The regulatory alternatives considered in the development of this 
    regulation, including those regulatory alternatives selected as 
    standards for new and existing affected sources, are based on process 
    and emissions data received from the existing plant sites known by the 
    EPA to be in operation.
        As stated above, the MACT floor represents the least stringent 
    standard permitted by law for new and existing sources. The EPA may 
    establish standards more stringent than the MACT floor when it 
    determines that such standards are achievable, ``taking into 
    consideration the cost of achieving such emission reduction, and any 
    nonair quality health and environmental impacts, and energy 
    requirements'' (42 U.S.C. 7412(d)(2)). In a few instances, the 
    standards in today's rule are more stringent than the MACT floor. In 
    each case, the EPA determined, based on available data, that such 
    standards were achievable within the meaning of section 112(d). Table 1 
    shows the subcategory-specific instances where an option was selected 
    that was more stringent than the MACT floor, along with the 
    corresponding incremental cost-effectiveness from the MACT floor.
    
                           Table 1.--Incremental Cost Effectiveness Values of Regulatory Options More Stringent Than the MACT Floor a                       
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                                                                               Incremental cost effectiveness b ($/Mg)                                      
                                        --------------------------------------------------------------------------------------------------------------------
                Subcategory                                         Front-end process                                                                       
                                                 Storage                  vents             Back-end process          Wastewater          Equipment leaks   
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    Butyl..............................  floor.................  $3,100................  floor................  $1,600...............  $1,700               
    
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    Epichlorohydrin....................  floor.................  floor.................  floor................  floor................  $2,000               
    Ethylene propylene.................  floor.................  floor.................  floor................  floor................  $2,000               
    Halobutyl..........................  $300..................  $1,400................  floor................  floor................  $1,100               
    Hypalon..................  floor.................  floor.................  floor................  floor................  floor                
    Neoprene...........................  floor.................  $2,900................  floor................  floor................  c $1,600             
    Nitrile butadiene latex............  floor.................  floor.................  floor................  floor................  c $2,600             
    Nitrile butadiene rubber...........  floor.................  floor.................  floor................  floor................  c $1,200             
    Polybutadiene/styrene butadiene      floor.................  floor.................  floor................  floor................  c $2,600             
     rubber by solution.                                                                                                                                    
    Polysulfide........................  floor.................  floor.................  floor................  floor................  floor                
    Styrene butadiene latex............  floor.................  floor.................  floor................  floor................  floor                
    Styrene butadiene rubber by          floor.................  floor.................  floor................  floor................  floor                
     emulsion.                                                                                                                                              
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    a In the table, ``floor'' indicates that the level of the promulgated standard is equivalent to the MACT floor.                                         
    b The incremental cost effectiveness reflects the cost and emission reduction from the MACT floor to the level of the promulgated standard.             
    c Equipment leak control programs at elastomer production facilities consisted of a complex combination of controls for the numerous components that can
      leak and cause HAP emissions. This complexity made it impractical to define a MACT floor ``program'' for which impacts could be assessed for multiple-
      plant subcategories. Therefore, the cost effectiveness values shown in the table represent the incremental cost effectiveness values from baseline.   
    
    C. Technical Basis of Regulation
    
        Potential regulatory alternatives were developed based on the 
    Hazardous Organic NESHAP (HON) (subparts F, G, and H of 40 CFR part 
    63), and the Batch Processes Alternative Control Techniques (ACT) 
    document (EPA 453/R-93-017; November 1993). The HON was selected as a 
    basis for regulatory alternatives because: (1) The characteristics of 
    the emissions from storage vessels, continuous front-end process vents, 
    equipment leaks, and wastewater at Group I elastomer facilities are 
    similar or identical to those addressed by the HON; and (2) the levels 
    of control required under the HON were already determined through 
    extensive analyses to be reasonable from a cost and impact perspective.
        Finally, the Batch Processes ACT was selected to identify 
    regulatory alternatives for batch process vents, which are not 
    addressed by the HON. The Batch Processes ACT addresses the control of 
    VOC emissions, and all of the organic HAP identified for the Group I 
    elastomers facilities are also VOC. Unlike the HON, the Batch Processes 
    ACT is not a regulation and, therefore, does not specify a level of 
    control that must be met. Instead, the Batch Processes ACT provides 
    information on potential levels of control, their costs, etc. Based on 
    the review of the Batch Processes ACT, the EPA selected a level of 
    control equivalent to 90 percent reduction for batch front-end process 
    vents. This level of control was selected for regulatory analysis 
    purposes because it represents a reasonable level of control 
    considering costs and other impacts.
    
    D. Stakeholder and Public Participation
    
        In the development of this standard, numerous representatives of 
    the elastomers industry were consulted. Industry representatives have 
    included trade associations and elastomer producers responding to 
    section 114 questionnaires and information collection requests (ICR's). 
    The EPA also received input from representatives from State and 
    Regional environmental agencies. Representatives from other interested 
    EPA offices and programs participated in the regulatory development 
    process as members of the Work Group. The Work Group is involved in the 
    regulatory development process, and is given opportunities to review 
    and comment on the standards before proposal and promulgation. 
    Therefore, the EPA believes that the impact on other EPA offices and 
    programs has been adequately considered during the development of these 
    standards. In addition, the EPA has met with members of industry 
    concerning these standards. Finally, industry representatives, 
    regulatory authorities, and environmental groups had the opportunity to 
    comment on the proposed standards and to provide additional information 
    during the public comment period that followed proposal.
        The standards were proposed in the Federal Register on June 12, 
    1995 (60 FR 30801). The preamble to the proposed standards described 
    the rationale for the proposed standards. Public comments were 
    solicited at the time of proposal. To provide interested persons the 
    opportunity for oral presentation of data, views, or arguments 
    concerning the proposed standards, a public hearing was offered at 
    proposal. However, the public did not request a hearing and, therefore, 
    one was not held. The public comment period was from June 12, 1995 to 
    August 11, 1995. A total of twenty-nine comment letters were received. 
    Commenters included industry representatives and State agencies. The 
    comments were carefully considered, and changes were made in the 
    proposed standards when determined by the EPA to be appropriate. A 
    detailed discussion of these comments and responses can be found in the 
    Basis and Purpose Document for Final Standards, which is referenced in 
    the ADDRESSES section of this preamble. The summary of comments and 
    responses in the Basis and Purpose Document for the Final Standards 
    serves as the basis for the revisions that have been made to the 
    standards between proposal and promulgation. Section IV of this 
    preamble discusses some of the major changes made to the standards.
    
    II. Summary of Promulgated Standards
    
        Emissions of specific organic HAP from the following types of 
    emission points (i.e., emission source types) are being covered by the 
    final standard: Storage vessels, continuous front-end process vents, 
    batch front-end process vents, back-end processes operations, equipment 
    leaks, and wastewater operations. The organic HAP emitted and required 
    to be controlled by these standards vary by subcategory. Each of the 
    twelve elastomer products constitutes a separate subcategory, each of 
    which belongs to one of the nine
    
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    source categories regulated by these standards.
        The existing affected source is defined as each group of one or 
    more EPPUs that manufacture the same elastomer product as their primary 
    product, and (1) are located at a major source plant site, (2) are not 
    exempt, and (3) are not part of a new affected source. This means that 
    each plant site will have only one existing affected source in any 
    given subcategory.
        If a plant site with an existing affected source producing 
    elastomer A as its primary product constructs a new EPPU also producing 
    elastomer A as its primary product, the new EPPU is a new affected 
    source if the new EPPU has the potential to emit more than 10 tons per 
    year of a single HAP, or 25 tons per year of all HAP. In this 
    situation, the plant site would have an existing affected source 
    producing elastomer A, and a new affected source producing elastomer A. 
    Each subsequent new EPPU with potential HAP emissions above the levels 
    cited above would be a separate new affected source.
        New affected sources are also created when an EPPU is constructed 
    at a major source plant site where the elastomer product was not 
    previously produced, with no regard to the potential HAP emissions from 
    the EPPU. Another instance where a new affected source is created is if 
    a new EPPU is constructed at a new plant site (i.e., green field site) 
    that will be a major source. The final manner in which a new affected 
    source is created is when an existing affected source undergoes 
    reconstruction, thus making the previously existing source subject to 
    new source standards.
        With relatively few exceptions, the final standards for storage 
    vessels, continuous front-end process vents, equipment leaks, and 
    wastewater streams are the same as those promulgated for the 
    corresponding types of emission points at facilities subject to the 
    HON. As shown in Tables 2 and 3, some subcategories have requirements 
    that differ from the HON; these cases are designated by ``MACT Floor.'' 
    These different requirements are specified in the final standards.
        As in the HON, if an emission point within an affected source meets 
    the applicability criteria and is required to be controlled under the 
    standard, it is referred to as a Group 1 emission point. If an emission 
    point within the affected source is not required to apply controls, it 
    is referred to as a Group 2 emission point.
    
    A. Storage Vessel Provisions
    
        For all subcategories, the storage vessel requirements are 
    identical to the HON storage vessel requirements in subpart G. A 
    storage vessel means a tank or other vessel that is associated with an 
    elastomer product process unit and that stores a liquid containing one 
    or more organic HAP. The rule specifies assignment procedures for 
    determining whether a storage vessel is associated with an elastomer 
    product process unit. The storage vessel provisions do not apply to the 
    following: (1) Vessels permanently attached to motor vehicles, (2) 
    pressure vessels designed to operate in excess of 204.9 kpa (29.7 psia) 
    and without emissions to the atmosphere, (3) vessels with capacities 
    smaller than 38 m\3\ (10,000 gal), (4) vessels and equipment storing 
    and/or handling material that contains no detectable organic HAP, and/
    or organic HAP as impurities only, (5) surge control vessels and 
    bottoms receiver tanks, and (6) wastewater storage tanks. An impurity 
    is produced coincidentally with another chemical substance and is 
    processed, used, or distributed with it.
        In addition to those vessels that do not meet the definition of 
    storage vessels, the standards exempt certain storage vessels 
    containing latex. Specifically, storage vessels containing a latex, 
    located downstream of the stripping operations, all storage vessels 
    containing styrene butadiene latex, and storage vessels containing 
    styrene, acrylamide, and epichlorohydrin, are exempt from the storage 
    vessel requirements of the final rule.
        The owner or operator must determine whether a storage vessel is 
    Group 1 or Group 2; Group 1 storage vessels require control. The 
    criteria for determining whether a storage vessel is Group 1 or Group 2 
    are the same as the HON criteria.
    
                                               Table 2.--Summary of Final Standards for Existing Affected Sources                                           
    --------------------------------------------------------------------------------------------------------------------------------------------------------
                                                                                     Level of final standard a                                              
                                      ----------------------------------------------------------------------------------------------------------------------
               Subcategory                                                                     Back-end process                                             
                                              Storage            Front-end process vents           emissions            Wastewater         Equipment leaks  
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    BR, HBR..........................  HON.................  HON/ACT, exempting halogenated  no control..........  HON.................  HON.               
                                                              vent streams controlled by                                                                    
                                                              flare or boiler before June                                                                   
                                                              12, 1995.                                                                                     
    EPI, HYP, NEO, NBL, NBR, PSR, SBL  HON.................  HON/ACT.......................  no control..........  HON.................  HON.               
    EPR..............................  HON.................  HON/ACT, exempting halogenated  MACT floor residual   HON.................  HON.               
                                                              vent streams controlled by      HAP limit.                                                    
                                                              flare or boiler before June                                                                   
                                                              12, 1995.                                                                                     
    PBR/SBRS, SBRE...................  HON.................  HON/ACT.......................  MACT floor residual   HON.................  HON.               
                                                                                              HAP limit.                                                    
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    a HON=the level of the standard is equivalent to existing source provisions of subpart G of 40 CFR 63 for storage and wastewater, and subpart H of 40   
      CFR 63 for equipment leaks.                                                                                                                           
     HON/ACT=the level of the standard for continuous front-end process vents is equal to the existing source process vent provisions in subpart G of 40 CFR
      63, and the level of the standard for batch front-end process vents is equal to the 90 percent control level from the Batch Processes ACT.            
    
    
    [[Page 46911]]
    
    
    
                                                  Table 3.--Summary of Final Standards for New Affected Sources                                             
    --------------------------------------------------------------------------------------------------------------------------------------------------------
                                                                                         Level of standard a                                                
                                        --------------------------------------------------------------------------------------------------------------------
                Subcategory                                         Front-end process       Back-end process                                                
                                                 Storage                  vents                emissions              Wastewater          Equipment leaks   
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    BR, EPI, HBR, HYP, NEO, NBL, NBR,    New source HON........  New source HON/ACT....  No control...........  Existing source HON..  New source HON       
     SBL.                                                                                                                                                   
    EPR, PBR/SBRS, SBRE................  New source HON........  New source HON/ACT....  New source floor       Existing source HON..  New source HON       
                                                                                          residual HAP limit.                                               
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    a HON=the level of the standard is equivalent to the provisions of subpart G of 40 CFR 63 for storage and wastewater, and subpart H of 40 CFR 63 for    
      equipment leaks.                                                                                                                                      
     HON/ACT=the level of the standard for continuous front-end process vents is equal to the new source process vent provisions in subpart G of 40 CFR 63, 
      and the level of the standard for batch front-end process vents is equal to the 90 percent control level from the Batch Processes ACT.                
    
        The storage provisions require that one of the following control 
    systems be applied to Group 1 storage vessels: (1) An internal floating 
    roof with proper seals and fittings; (2) an external floating roof with 
    proper seals and fittings; (3) an external floating roof converted to 
    an internal floating roof with proper seals and fittings; or (4) a 
    closed vent system with a 95-percent efficient control device. The 
    storage provisions give details on the types of seals and fittings 
    required. Monitoring and compliance provisions include periodic visual 
    inspections of vessels, roof seals, and fittings, as well as internal 
    inspections. If a closed vent system and control device is used, the 
    owner or operator must establish appropriate monitoring procedures. 
    Reports and records of inspections, repairs, and other information 
    necessary to determine compliance are also required by the storage 
    provisions. No controls are required for Group 2 storage vessels.
    
    B. Front-End Process Vent Provisions
    
        There are separate provisions in the rule for front-end process 
    vents that originate from unit operations operated in a continuous 
    mode, and those from unit operations operated in a batch mode. An 
    affected source could be subject to both the continuous and batch 
    front-end process vent provisions if front-end operations at an 
    elastomer production process unit consist of a combination of 
    continuous and batch unit operations. The continuous provisions would 
    be applied to those vents from continuous unit operations, and the 
    batch provisions to vents from batch unit operations.
    1. Continuous Front-End Process Vent Provisions
        The provisions in the final rule for continuous front-end process 
    vents are the same as the HON process vent provisions in subpart G. 
    Continuous front-end process vents are gas streams that originate from 
    continuously operated units in the front-end of an elastomer process, 
    and include gas streams discharged directly to the atmosphere and gas 
    streams discharged to the atmosphere after diversion through a product 
    recovery device. The continuous front-end process vent provisions apply 
    only to vents that emit gas streams containing more than 0.005 weight-
    percent HAP.
        A Group 1 continuous front-end process vent is defined as a 
    continuous front-end process vent with a flow rate greater than or 
    equal to 0.005 scmm, an organic HAP concentration greater than or equal 
    to 50 ppmv, and a total resource effectiveness (TRE) index value less 
    than or equal to 1.0. The continuous front-end process vent provisions 
    require the owner or operator of a Group 1 continuous front-end process 
    vent stream to: (1) Reduce the emissions of organic HAP using a flare; 
    (2) reduce emissions of organic HAP by 98 weight-percent or to a 
    concentration of 20 ppmv or less; or (3) achieve and maintain a TRE 
    index above 1. Performance test provisions are included for Group 1 
    continuous front-end process vents to verify that the control device 
    achieves the required performance.
        The organic HAP reduction is based on the level of control achieved 
    by the reference control technology. Group 2 continuous front-end 
    process vent streams with TRE index values between 1.0 and 4.0 are 
    required to monitor those process vent streams to ensure those streams 
    do not become Group 1, which require control.
        The owner or operator can calculate a TRE index value to determine 
    whether each process vent is a Group 1 or Group 2 continuous front-end 
    process vent, or the owner or operator can elect to comply directly 
    with the control requirements without calculating the TRE index. The 
    TRE index value is determined after the final recovery device in the 
    process or prior to venting to the atmosphere. The TRE calculation 
    involves an emissions test or engineering assessment and use of the TRE 
    equations in Sec. 63.115 of subpart G.
        The rule encourages pollution prevention through product recovery 
    because an owner or operator of a Group 1 continuous front-end process 
    vent may add recovery devices or otherwise reduce emissions to the 
    extent that the TRE becomes greater than 1.0 and the Group 1 continuous 
    front-end process vent becomes a Group 2 continuous front-end process 
    vent.
        Group 1 halogenated streams controlled using a combustion device 
    must vent the emissions from the combustor to an acid gas scrubber or 
    other device to limit emissions of halogens prior to venting to the 
    atmosphere. The control device must reduce the overall emissions of 
    hydrogen halides and halogens by 99 percent or reduce the outlet mass 
    emission rate of total hydrogen halides and halogens to less than 0.45 
    kg/hr.
        The rule exempts certain halogenated process vent streams from the 
    requirement to control the halogens at the exit from a combustion 
    device. Specifically, halogenated continuous front-end process vents at 
    existing affected sources producing butyl rubber, halobutyl rubber, or 
    ethylene-propylene rubber are exempt from the requirements to control 
    hydrogen halides and halogens from the outlet of combustion devices. 
    However, the rule requires that these vent streams be controlled in 
    accordance with the other Group 1 requirements for continuous front-end 
    process vents.
        Monitoring, reporting, and recordkeeping provisions necessary to 
    demonstrate compliance are also included in the continuous front-end 
    process vent provisions. Compliance with the monitoring provisions is 
    based on a comparison of daily average monitored values to enforceable 
    parameter ``levels'' established by the owner or operator.
    
    [[Page 46912]]
    
    2. Batch Front--End Process Vent Provisions
        Process vents that include gas streams originating from batch unit 
    operations in the front-end of an elastomer product process unit are 
    subject to the batch front-end process vent provisions of the rule. 
    Consistent with provisions in the rule for other emission source types, 
    batch front-end process vents are classified as Group 1 or Group 2, 
    with control being required for Group 1 batch front-end process vents.
        An important aspect of the batch front-end process vent provisions 
    is that applicability is on an individual vent basis. All batch 
    emission episodes that are emitted to the atmosphere through the vent 
    are to be considered in the group determination. The rule does not 
    require that emissions from similar batch unit operations emitted from 
    different vents be combined for applicability determinations. In other 
    words, if a process included four batch reactors, and each reactor had 
    a dedicated vent to the atmosphere, applicability would be determined 
    for each reactor.
        The applicability criteria of the batch front-end process vent 
    provisions are from the Batch Processes ACT, and are based on annual 
    emissions of the HAP emitted from the vent, and the average flow rate 
    of the vent stream. The vent stream characteristics are determined at 
    the exit from the batch unit operation before any emission control or 
    recovery device. The rule specifies that reflux condensers, condensers 
    recovering monomer or solvent from a batch stripping operation, and 
    condensers recovering monomer or solvent from a batch distillation 
    operation are considered part of the unit operation. Therefore, the 
    batch front-end process vent applicability criteria would be applied 
    after these condensers.
        The first step in the applicability determination is to calculate 
    the annual HAP emissions. Annual HAP emissions may be calculated using 
    equations contained in the regulation (which are from the Batch 
    Processes ACT). Testing or engineering assessment may also be used if 
    the equations are not appropriate. Batch front-end process vents with 
    annual HAP emissions less than 225 kilograms per year are exempt from 
    all batch front-end process vent requirements, other than the 
    requirement to estimate annual HAP emissions.
        There are two tiers of Group 2 batch front-end process vents. 
    First, if the annual HAP emissions of a vent are below specified cutoff 
    levels, the batch front-end process vent is classified as a Group 2 
    vent, and a batch cycle limitation must be established (discussed 
    below). The cutoff emission level is 11,800 kilograms HAP per year.
        If annual HAP emissions are greater than the cutoff emission level 
    specified above, the owner must determine the annual average flow rate 
    of the batch front-end process vent, and the ``cutoff flow rate'' using 
    the equation in Sec. 63.488(f). The Group 1/Group 2 classification is 
    then based on a comparison between the actual annual average flow rate, 
    and the cutoff flow rate. If the actual flow rate is less than the 
    calculated cutoff flow rate, then the batch process vent is a Group 1 
    vent, and control is required. If the actual flow rate is greater than 
    the calculated cutoff flow rate, then the batch process vent is a Group 
    2 batch front-end process vent, and the owner or operator must 
    establish a batch cycle limitation.
        Owners and operators of Group 2 batch front-end process vents must 
    establish a batch cycle limitation that ensures that HAP emissions from 
    the vent do not increase to a level that would make the batch front-end 
    process vent Group 1. The batch cycle limitation is an enforceable 
    restriction on the number of batch cycles that can be performed in a 
    year. An owner or operator has two choices regarding the level of the 
    batch cycle limitation. The limitation may be set to maintain emissions 
    below the annual emission cutoff level listed above, or the limitation 
    may be set to ensure that annual emissions do not increase to a level 
    that makes the calculated cutoff flow rate increase beyond the actual 
    annual average flow rate. The advantage to the first option is that the 
    owner or operator would not be required to determine the annual average 
    flow rate of the vent. A batch cycle limitation does not limit 
    production to any previous production level, but is based on the number 
    of cycles necessary to exceed one of the two batch front-end process 
    vent applicability criteria discussed above.
        The batch front-end process vent provisions require the owner or 
    operator of a Group 1 batch front-end process vent stream to: (1) 
    Reduce the emissions of organic HAP using a flare or (2) reduce 
    emissions of organic HAP by 90 weight-percent over each batch cycle 
    using a control or recovery device. If a halogenated batch vent stream 
    (defined as a vent that has a mass emission rate of halogen atoms in 
    organic compounds of 3,750 kilograms per year or greater) is sent to a 
    combustion device, the outlet stream must be controlled to reduce 
    emissions of hydrogen halides and halogens by 99 percent. Control could 
    be achieved at varying levels for different emission episodes as long 
    as the required level of control for the batch cycle was achieved. The 
    owner or operator could even elect to control some emission episodes 
    and by-pass control for others. Performance test provisions are 
    included for Group 1 batch front-end process vents to verify that the 
    control device achieves the required performance.
        Monitoring, reporting, and recordkeeping provisions necessary to 
    demonstrate compliance are also included in the batch front-end process 
    vent provisions. These provisions are modeled after the analogous 
    continuous process vent provisions in the HON. Compliance with the 
    monitoring provisions is based on a comparison of batch cycle daily 
    average monitored values to enforceable parameter monitoring levels 
    established by the owner or operator.
        The provisions for batch front-end process vents contain three 
    conditions that can greatly simplify compliance. First, an owner or 
    operator can control a batch front-end process vent in accordance with 
    the Group 1 batch front-end process vent requirements and bypass the 
    applicability determination. Second, if a batch front-end process vent 
    is combined with a continuous vent stream before a recovery or control 
    device, the owner or operator is exempt from all batch front-end 
    process vent requirements. However, applicability determinations and 
    performance tests for the continuous vent must be conducted at 
    conditions when the addition of the batch vent streams makes the HAP 
    concentration in the combined stream greatest. Finally, if batch front-
    end process vents combine to create a ``continuous'' flow to a control 
    or recovery device, the less complicated continuous process vent 
    monitoring requirements are used.
    
    C. Back-End Process Provisions
    
        Back-end process operations include all operations at an EPPU that 
    occur after the stripping operations. These operations include, but are 
    not limited to, filtering, drying, separating, and other finishing 
    operations, as well as product storage.
        The back-end process provisions contain residual HAP limitations 
    for three subcategories: EPR, PBR/SBRS, and SBRE. The limitations for 
    EPR and PBR/SBRS are in units of kilograms HAP per megagram of crumb 
    rubber dry weight (crumb rubber dry weight means the weight of the 
    polymer, minus the weight of water and residual organics), and the 
    limitation for SBRE is in units of kilogram HAP per megagram latex.
    
    [[Page 46913]]
    
    The limitation is a monthly average weighted based on the weight of 
    rubber or latex processed in the stripper. Two methods of compliance 
    are available: (1) Stripping the polymer to remove the residual HAP to 
    the levels in the standards, on a monthly weighted average basis, or 
    (2) reducing emissions using add-on control to a level equivalent to 
    the level that would be achieved if stripping was used.
    1. Compliance Using Stripping Technology
        If stripping is the method of compliance selected, the rule allows 
    two options for demonstrating compliance: by sampling and by monitoring 
    stripper operating parameters. If compliance is demonstrated by 
    sampling, samples of the stripped wet crumb or stripped latex must be 
    taken as soon as safe and feasible after the stripping operation, but 
    no later than the entry point for the first unit operation following 
    the stripper (e.g., the watering screen), and analyzed to determine the 
    residual HAP content. For styrene-butadiene rubber produced by the 
    emulsion process, the sample of latex shall be taken just prior to 
    entering the coagulation operations.
        A sample must be taken once per day for continuous processes, or 
    once per batch for batch processes. The sample must be analyzed to 
    determine the residual HAP content, and the corresponding weight of 
    rubber or latex processed in the stripper must be recorded. This 
    information is then used to calculate a monthly weighted average. A 
    monthly weighted average that is above the limitation is a violation of 
    the standard, as is a failure to sample and analyze at least 75 percent 
    of the samples required during the month. The EPA is in the process of 
    approving test methods that will be used to determine compliance with 
    the standard. These methods are being promulgated separately by the 
    EPA. Records of each test result would be required, along with the 
    corresponding weight of the polymer processed in the stripper. Records 
    of the monthly weighted averages must also be maintained.
        An owner or operator complying using stripping can also demonstrate 
    compliance by continuously monitoring stripper operating parameters. If 
    using this approach, the owner or operator must establish stripper 
    operating parameters for each grade of polymer processed in the 
    stripper, along with the corresponding residual HAP content of that 
    grade. The parameters that must be monitored include, at a minimum, 
    temperature, pressure, steaming rates (for steam strippers), and some 
    parameter that is indicative of residence time. The HAP content of the 
    grade must be determined initially using the residual HAP test methods 
    discussed above. The owner or operator can elect to establish a single 
    set of stripper operating parameters for multiple grades.
        The EPA believes that computer predictive modeling may be an 
    attractive alternative to the periodic sampling and stripper parametric 
    monitoring options in the rule, but did not specifically include 
    provisions for these options, because the use of computer predictive 
    modeling is so site-specific that it was not possible to include 
    general requirements for its use in subpart U. However, the rule does 
    allow the opportunity for site-specific approval of the use of computer 
    predictive modeling, stack test monitoring, or other alternative means 
    of compliance through the submittal of an alternative compliance plan.
        The difference in the demonstration of compliance by sampling, and 
    the demonstration of compliance by monitoring stripping parameters, is 
    that the monitoring option is entirely based on a grade or batch. To 
    further explain, if a particular grade of polymer is processed in the 
    stripper continuously for 32 hours, a sample of that grade is required 
    to be taken each operating day, if the sampling compliance 
    demonstration option is selected. However, if the stripping parameter 
    monitoring option is selected, the entire length of time the grade is 
    being processed in the stripper is treated as a single unit.
        During the operation of the stripper, the parameters must be 
    continuously monitored, with a reading of each parameter taken at least 
    once every 15 minutes. If, during the processing of a grade, all hourly 
    average parameter values are in accordance with the established levels, 
    the owner or operator can use the HAP content determined initially in 
    the calculation of the monthly weighted average, and sampling is not 
    required. However, if one hourly average value for any parameter is not 
    in accordance with the established operating parameter, a sample must 
    be taken and the HAP content determined using specified test methods.
        Records of the initial residual HAP content results, along with the 
    corresponding stripper parameter monitoring results for the sample, 
    must be maintained. The hourly average monitoring results are required 
    to be maintained, along with the results of any HAP content tests 
    conducted due to exceedance of the established parameter monitoring 
    levels. Records must also be kept of the weight of polymer processed in 
    each grade, and the monthly weighted average values.
        If complying with the residual HAP limitations using stripping 
    technology, and demonstrating compliance by monitoring stripper 
    parameters, there are three ways a facility can be in violation of the 
    standard. First, a monthly weighted average that is above the 
    limitation is a violation of the standard, as is a failure to sample 
    and analyze a sample for a grade with an hourly average parameter value 
    not in accordance with the established monitoring parameter levels. The 
    third way for a facility to be out of compliance is if the stripper 
    monitoring data are not sufficient for at least 75 percent of the 
    grades produced during the month. Stripper data are considered 
    insufficient if monitoring parameters are obtained for less than 75 
    percent of the 15-minute periods during the processing of a grade.
    2. Compliance Using Add-On Control
        If add-on control is the method of compliance selected, there are 
    two levels of compliance. Initial compliance is based on a source test, 
    and continuous compliance is based on the daily average of parameter 
    monitoring results for the control or recovery device.
        The initial performance test must consist of three 1-hour runs or 
    three complete batch cycles, if the duration of the batch cycle is less 
    than 1 hour. The test runs must be conducted during processing of 
    ``worst-case'' grade, which means the grade with the highest residual 
    HAP content leaving the stripper. The ``uncontrolled'' residual HAP 
    content in the latex or wet crumb rubber must be determined, using the 
    test methods, after the stripper. Then, when the crumb for which the 
    uncontrolled residual HAP was determined is being processed in the 
    back-end unit operation being controlled, the inlet and outlet 
    emissions for the control or recovery device must be determined using 
    Method 18 or Method 25A. The uncontrolled HAP content is then adjusted 
    to account for the reduction in emissions by the control or recovery 
    device, and compared to the levels in the standard. For initial 
    compliance, the adjusted residual HAP content level for each test run 
    must be less than the level in today's standards.
        During the initial test, the appropriate parameter must be 
    monitored, and an enforceable ``level'' established as a maximum or 
    minimum operating parameter based on this monitoring. As
    
    [[Page 46914]]
    
    with continuous front-end process vents, the level is established as 
    the average of the maximum (or minimum) point values for the three test 
    runs.
        Continuous monitoring must be conducted on the control or recovery 
    device, and compliance is based on the daily average of the monitoring 
    results. The monitoring, recordkeeping, and reporting provisions are 
    the same as the process vent provisions in the HON, which are required 
    for continuous front-end process vents in today's final standard.
    3. Carbon Disulfide Limitations For Styrene Butadiene Rubber By 
    Emulsion Producers
        Today's regulation would reduce carbon disulfide (CS2) 
    emissions from styrene butadiene rubber producers using an emulsion 
    process by limiting the concentration of CS2 in the dryer vent 
    stacks to 45 ppmv. Sulfur-containing shortstopping agents used to 
    produce certain grades of rubber have been determined to be the source 
    of CS2 in the dryer stacks. Owners or operators would be required 
    to develop standard operating procedures for each grade that uses a 
    sulfur-containing shortstopping agent. These standard operating 
    procedures would specify the type and amount of agent added, and the 
    point in the process where the agent is added. One standard operating 
    procedure can be used for more than one grade if possible.
        The owner or operator is required to validate each standard 
    operating procedure through either a performance test or a 
    demonstration using engineering assessment. The facility would be in 
    compliance with this the regulation if the appropriate standard 
    operating procedure is followed whenever a sulfur-containing 
    shortstopping agent is used. Facilities that route dryer vents to a 
    combustion device would be exempt from Sec. 63.500 of the regulation.
    
    D. Wastewater Provisions
    
        Except for back-end wastewater streams originating from equipment 
    that only produces latex products and back-end wastewater streams at 
    affected sources that are subject to the residual organic HAP 
    limitation, the standards require owners and operators to comply with 
    the wastewater provisions in the HON. Owners and operators of new and 
    existing sources are required to make a group determination for each 
    wastewater stream based on the existing source applicability criteria 
    in the HON: Flow rate and organic HAP concentration. The level of 
    control required for Group 1 wastewater streams is dependent upon the 
    organic HAP constituents in the wastewater stream.
        The standards also require owners and operators to comply with the 
    maintenance wastewater requirements in Sec. 63.105 of subpart F. These 
    provisions require owners and operators to include a description of 
    procedures for managing wastewaters generated during maintenance in 
    their startup, shutdown, and malfunction plan.
    
    E. Equipment Leak Provisions
    
        For all subcategories, both existing and new affected sources are 
    required to comply with the equipment leak standards specified in 
    subpart H of 40 CFR part 63. In general, subpart H requires owners and 
    operators to implement a leak detection and repair (LDAR) program, 
    including various work practice and equipment standards. The subpart H 
    standards are applicable to equipment in volatile HAP service for 300 
    or more hours per year (hr/yr). The standards define ``in volatile 
    organic HAP service'' as being in contact with or containing process 
    fluid that contains a total of 5 percent or more total HAP. Equipment 
    subject to the standards are: Valves, pumps, compressors, connectors, 
    pressure relief devices, open-ended valves or lines, sampling 
    connection systems, instrumentation systems, agitators, surge control 
    vessels, bottoms receivers, and closed-vent systems and control 
    devices.
        A few differences to the subpart H standards are contained in this 
    final rule. These differences include not requiring the submittal of an 
    Initial Notification or Implementation Plan and allowing 150 days 
    (rather than 90 days) to submit the Notification of Compliance Status. 
    In addition, the exemptions discussed earlier for storage vessels are 
    also applicable for surge control vessels and bottoms receivers.
        Affected sources subject to today's final rule and currently 
    complying with the NESHAP for Certain Processes Subject to the 
    Negotiated Regulation for Equipment Leaks (40 CFR part 63, subpart I) 
    are required to continue to comply with subpart I until the compliance 
    date of this final rule, at which point in time they must comply with 
    today's rule and are no longer subject to subpart I. Further, affected 
    sources complying with subpart I through a quality improvement program 
    are allowed to continue these programs without interruption as part of 
    complying with today's rule. In other words, becoming subject to 
    today's standards does not restart or reset the ``compliance clock'' as 
    it relates to reduced burden earned through a quality improvement 
    program.
    
    F. Emissions Averaging Provisions
    
        The EPA is allowing emissions averaging among continuous front-end 
    process vents, batch front-end process vents, aggregate batch vents, 
    back-end process operations, storage vessels, and wastewater streams 
    within an existing affected source. New affected sources are not 
    allowed to use emissions averaging. Emissions averaging is not allowed 
    between subcategories; it is only allowed between emission points 
    within the same affected source. Under emissions averaging, a system of 
    ``credits'' and ``debits'' is used to determine whether an affected 
    source is achieving the required emission reductions. Twenty emission 
    points per plant site are allowed in the set of emissions averaging 
    plans submitted for the plant site, with an additional 5 emission 
    points allowed if pollution prevention measures are used.
    
    G. Compliance and Performance Test Provisions and Monitoring 
    Requirements
    
        Compliance and performance test provisions and monitoring 
    requirements contained in the final standards are very similar to those 
    found in the HON. Each type of emission point included in the standards 
    is discussed briefly in the following paragraphs. Also, significant 
    differences from the parameter monitoring requirements found in the HON 
    are discussed.
    1. Storage Vessels
        Monitoring and compliance provisions for storage vessel 
    improvements include periodic visual inspections of vessels, roof 
    seals, and fittings, as well as internal inspections. If a control 
    device is used, the owner or operator must identify the appropriate 
    monitoring procedures to be followed in order to demonstrate 
    compliance. Monitoring parameters and procedures for many of the 
    control devices likely to be used are identified in the final 
    standards. Reports and records of inspections, repairs, and other 
    information necessary to determine compliance are also required by the 
    final standards.
    2. Continuous Front-end Process Vents
        The final standards for continuous front-end process vents require 
    the owner or operator to either calculate a TRE index value to 
    determine the group status of each continuous front-end process vent or 
    to comply with the control requirements. The TRE index value is 
    determined after the last recovery device in the process or prior to 
    venting to the atmosphere. The TRE calculation involves an emissions 
    test or
    
    [[Page 46915]]
    
    engineering assessment and use of the TRE equations specified in the 
    final standards.
        Performance test provisions are included for Group 1 continuous 
    front-end process vents to verify that control devices or recovery 
    achieve the required performance. Monitoring provisions necessary to 
    demonstrate compliance are also included in the standards.
    3. Batch Front-End Process Vents
        Similar to the provisions for continuous front-end process vents, 
    there is a procedure for determining the group status of batch front-
    end process vents. This procedure is based on annual emissions and 
    annual average flow rate of the batch front-end process vent. Equations 
    for estimating and procedures for measuring annual emissions and annual 
    average flow rates are provided in the final standards. The use of 
    engineering assessment for the group determination is also allowed.
        Performance test provisions are included for Group 1 batch front-
    end process vents to verify that control devices achieve the required 
    performance. Monitoring provisions necessary to demonstrate compliance 
    are also included in the final standard.
        For Group 2 batch front-end process vents, the standard requires 
    owners and operators to establish a batch cycle limitation. The batch 
    cycle limitation restricts the number of batch cycles that can be 
    accomplished per year. This enforceable limitation ensures that a Group 
    2 batch front-end process vent does not become a Group 1 batch front-
    end process vent as a result of running more batch cycles than 
    anticipated when the group determination was made. The determination of 
    the batch cycle limitation is not tied to any previous production 
    amounts. An affected source may set the batch cycle limitation at any 
    level it desires as long as the batch front-end process vent remains a 
    Group 2 batch front-end process vent. Alternatively the standards would 
    allow owners or operators to declare any Group 2 batch front-end 
    process vent to be a Group 1 batch front-end process vent. In such 
    cases, control of the batch process front-end vent is required.
    4. Back-End Process Vents
        The final rule specifies the performance tests, test methods (with 
    the exception of residual HAP reference test methods), and monitoring 
    requirements necessary to determine that the allowed back-end emission 
    limitations are achieved. The following paragraphs discuss each of 
    these.
        Performance tests and test methods for residual HAP limitations. 
    Initial performance tests, in the traditional sense, are required for 
    facilities complying with the back-end operations provisions using add-
    on control. Testing is required for all control and recovery devices, 
    other than flares and certain boilers and process heaters. The back-end 
    process provisions require the use of approved test methods.
        Initial tests are required for facilities complying by using 
    stripper parameter monitoring. The purpose of this initial testing is 
    to establish correlations between residual HAP contents and stripper 
    operating parameters. Within a few months of the promulgation of this 
    regulation, the EPA will promulgate test methods for determining the 
    residual HAP content in crumb and latex.
        If an owner or operator complies with the back-end standards by 
    sampling, periodic sampling and testing is required. The residual HAP 
    test methods would also be used for these analyses.
        Performance tests and test methods for carbon disulfide emission 
    limitations for SBRE facilities. Initial performance tests are one 
    option for ``verifying'' each standard operating procedure as an 
    acceptable procedure that results in carbon disulfide concentrations of 
    45 ppmv or less in the dryer stacks at SBRE facilities. Standard 
    operating procedures may also be verified through engineering 
    assessments. If the performance testing option is selected, one 
    performance test is required for each standard operating procedure. 
    Method 18 or 25A is specified to measure the carbon disulfide 
    concentration. Additional verifications are not required unless a new 
    standard operating procedure is added, or an existing standard 
    operating procedure is revised.
        Monitoring requirements. Control and recovery devices and strippers 
    used to comply with the final rule need to be maintained and operated 
    properly if the required level of control is to be achieved on a 
    continuing basis. Monitoring of control and recovery device and 
    stripper parameters can be used to ensure that such proper operation 
    and maintenance are occurring.
        For control and recovery devices, the back-end process operation 
    standard uses the same list of parameters discussed above for 
    continuous front-end process vents. For strippers, the regulation 
    requires the monitoring of temperature, pressure, steaming rates, and a 
    parameter indicative of residence time.
    5. Wastewater
        For demonstrating compliance with the various requirements, the 
    final standard allows the owners or operators to either conduct 
    performance tests or to document compliance using engineering 
    calculations. Appropriate compliance and monitoring provisions are 
    included in the final standard.
    6. Equipment Leaks
        The final standard retains the use of Method 21 to detect leaks. 
    Method 21 requires a portable organic vapor analyzer to monitor for 
    leaks from equipment in use. A ``leak'' is a concentration specified in 
    the regulation for the type of equipment being monitored and is based 
    on the instrument response to methane (the calibration gas) in the air. 
    The observed screening value may require adjustment for the response 
    factor relative to methane if the weighted response factor of the 
    stream exceeds a specified multiplier. The final rule requires the use 
    of Method 18 or Method 25A to determine the organic content of a 
    process stream. To test for leaks in a batch system, test procedures 
    using either a gas or a liquid for pressure testing the batch system 
    are specified to test for leaks.
    7. Continuous Parameter Monitoring
        The final standards require owners or operators to establish 
    parameter monitoring levels. The standards provide the owner or 
    operator the flexibility to establish the levels based on site-specific 
    information. Site-specific levels can best accommodate variation in 
    emission point characteristics and control device designs. Three 
    procedures for establishing these levels are provided in the final 
    standards. They are based on performance tests; engineering 
    assessments, performance tests, and/or manufacturer's recommendations; 
    and engineering assessments and/or manufacturer's recommendations. 
    While the establishment of a level based solely on performance tests is 
    preapproved by the Administrator, values determined using the last two 
    procedures, which may or may not use the results of performance tests, 
    must be approved by the Administrator for each individual case.
        The final standards require the availability of at least 75 percent 
    of monitoring data to constitute a valid day's worth of data for 
    continuous and batch front-end process vents. Failure to have a valid 
    day's worth of monitoring data is considered an excursion. The criteria 
    for determining a valid day's or
    
    [[Page 46916]]
    
    hour's worth of data are provided in the final standards. A certain 
    number of excused excursions have been allowed for in the final 
    standards; these provisions are the same as the provisions in the HON. 
    The standards allow a maximum of 6 excused excursions for the first 
    semiannual reporting period, decreasing by 1 excursion each semiannual 
    reporting period. Starting with the sixth semiannual reporting period 
    (i.e., the end of the third year of compliance) and thereafter, 
    affected sources are allowed one excused excursion per semiannual 
    reporting period. As is always the case, a State has the discretion to 
    impose more stringent requirements than the requirements of NESHAP and 
    other federal requirements and could choose not to allow the excused 
    excursion provisions contained in these final standards.
    
    H. Recordkeeping and Reporting Provisions
    
        The final standards require owners or operators of affected sources 
    to maintain required records for a period of at least 5 years. The 
    final standards require that the following reports be submitted, as 
    applicable: (1) Precompliance Report, (2) Emissions Averaging Plan, (3) 
    Notification of Compliance Status report, (4) Periodic Reports, and (5) 
    other reports (e.g., notifications of storage vessel internal 
    inspections).
        Specific recordkeeping and reporting requirements are specified in 
    each section that addresses an individual emission point (e.g., 
    Sec. 63.486 for batch front-end process vents). The recordkeeping and 
    reporting provisions related to the affected source as a whole (e.g., 
    types of reports, such as the Notification of Compliance Status) are 
    found in Sec. 63.506. For example, Sec. 63.491 requires an owner or 
    operator to record the batch cycle limitation for each Group 2 batch 
    front-end process vent. Section 63.492 goes on to require the owner or 
    operator to submit this information in the Notification of Compliance 
    Status as specified in Sec. 63.506. Finally, Sec. 63.506 requires 
    submittal of the information specified in Sec. 63.492.
    
    III. Summary of Impacts
    
        This section presents a summary of the air, non-air environmental 
    (waste and solid waste), energy, cost, and economic impacts resulting 
    from the control of HAP emissions under this final rule.
    
    A. Facilities Affected by These NESHAP
    
        The promulgated rule would affect BR, EPI, EPR, HYP, NEO, NBR, PBR, 
    PSR, and SBR facilities that are major sources in themselves, or that 
    are located at a major source. Based on available information, all of 
    the facilities at which these elastomers are produced were judged to be 
    major sources for the purpose of developing these standards. (Final 
    determination of major source status occurs as part of the compliance 
    determination process undertaken by each individual source.)
        Impacts are presented relative to a baseline reflecting the level 
    of control in the absence of the rule. The current level of control was 
    well understood, because emissions and control data were collected on 
    each facility included in the analysis. The impacts for existing 
    sources were estimated by bringing each facility's control level up to 
    today's standards.
        Impacts are not assessed for new sources because it was projected 
    that no new sources are expected to begin operation through 1999. For 
    more information on this projection, see the New Source Memo in the 
    SID.
    
    B. Primary Air Impacts
    
        Today's standards are estimated to reduce HAP emissions from all 
    existing sources of listed elastomers by 6,400 Mg/yr. This represents a 
    48 percent reduction from baseline. Table 4 summarizes the HAP emission 
    reductions for each individual subcategory.
    
    C. Other Environmental Impacts
    
        The total criteria air pollutant emissions resulting from process 
    vent and wastewater control of today's standards are estimated to be 
    around 178 Mg/yr, with NOX emissions from incinerators and boilers 
    accounting for around 155 Mg/yr. Minimal wastewater or solid and 
    hazardous waste impacts are projected.
    
    D. Energy Impacts
    
        The total nationwide energy demands that would result from 
    implementing the process vent and wastewater controls are around 1.10 
    x  1012 Btu annually.
    
                                                         Table 4. HAP Emission Reduction by Subcategory                                                     
    --------------------------------------------------------------------------------------------------------------------------------------------------------
                                                                                          HAP emission reduction (Mg/yr)                                    
                                                                  ------------------------------------------------------------------------------  Percentage
                             Subcategory                                         Front-end     Back-end                                           reduction 
                                                                     Storage      process      process     Wastewater   Equipment      Total         from   
                                                                                   vents      operations   operations     leaks                    baseline 
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    Butyl rubber.................................................            0          211            0          102          293          606           64
    Epichlorohydrin elastomer....................................            4            0            0            0          120          124           77
    Ethylene propylene rubber....................................            2           85          979            0        1,020        2,012           62
    Halobutyl rubber.............................................           62           38            0            0          233          335           26
    HypalonTM....................................................            0            0            0            0            0            0            0
    Neoprene.....................................................            0          258            0            0           96          354           48
    Nitrile butadiene latex......................................            0            0            0           94           41          135           85
    Nitrile butadiene rubber.....................................            1            0            0            0          364          365           62
    Polybutadiene rubber/styrene butadiene rubber by solution....            0            0          882            0          637        1,519           44
    Polysulfide rubber...........................................            0            0            0            0            0            0            0
    Styrene butadiene latex......................................            0           22            0          272          332          627           44
    Styrene butadiene rubber by emulsion.........................            0            0          195           48            0          243           23
    Total--(percent of total reduction)..........................      69, (1)    615, (10)  2,056, (32)     516, (8)  3,136, (49)        6,392           48
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    
    E. Cost Impacts
    
        Cost impacts include the capital costs of new control equipment, 
    the cost of energy (supplemental fuel, steam, and electricity) required 
    to operate control equipment, operation and maintenance costs, and the 
    cost savings generated by reducing the loss of valuable product in the 
    form of emissions. Also, cost impacts include the costs of monitoring, 
    recordkeeping, and reporting associated with today's standards. Average 
    cost
    
    [[Page 46917]]
    
    effectiveness ($/Mg of pollutant removed) is also presented as part of 
    cost impacts and is determined by dividing the annual cost by the 
    annual emission reduction. Table 5 summarizes the estimated capital and 
    annual costs and average cost effectiveness by subcategory.
        Under the promulgated rule, it is estimated that total capital 
    costs for existing sources would be $26 million (1989 dollars), and 
    total annual costs would by $18.4 million (1989 dollars) per year. It 
    is expected that the actual compliance cost impacts of the rule would 
    be less than presented because of the potential to use common control 
    devices, upgrade existing control devices, use other less expensive 
    control technologies, implement pollution prevention technologies, or 
    use emissions averaging. Because the effect of such practices is highly 
    site-specific and data were unavailable to estimate how often the lower 
    cost compliance practices could be utilized, it is not possible to 
    quantify the amount by which actual compliance costs would be reduced.
    
                                          Table 5. Summary of Regulatory Costs                                      
    ----------------------------------------------------------------------------------------------------------------
                                                                                     TAC b--    AER c--(Mg/ CE d--($/
                                                                       TCI a--      (1000$/yr)      yr)        Mg)  
    -------------------------------------------------------------------(1000$)--------------------------------------
    Butyl.........................................................          691          1,316        606      2,200
    Epichlorohydrin...............................................          491            241        124      1,900
    Ethylene Propylene............................................        5,854          3,506      2,012      1,700
    Halobutyl.....................................................          328            322        335      1,000
    Hypalon.............................................            0              0          0        N/A
    Neoprene......................................................          560            897        354      2,500
    Nitrile butadiene latex.......................................          465            243        135      1,800
    Nitrile butadiene rubber......................................          397            444        365      1,200
    Polybutadine/styrene butadiene rubber by solution.............       11,780          8,335      1,519    e 5,500
    Polysulfide...................................................            0              0          0        N/A
    Styrene butadiene latex.......................................        1,480          1,028        627      1,600
    Styrene butadiene rubber by emulsion..........................        3,942          2,112        243     e8,700
    ----------------------------------------------------------------------------------------------------------------
    a ``TCI'' represents Total Capital Investment.                                                                  
    b ``TAC'' represents Total Annualized Cost, including the monitoring, recordkeeping, and reporting cost.        
    c ``AER'' represents the Annual Emission Reduction.                                                             
    d ``CE'' represents Cost-Effectiveness.                                                                         
    e This cost-effectiveness is primarily due to the high costs estimated to control back-end process emissions to 
      the MACT floor level. The costs developed are costs for incineration devices to sufficient back-end vents so  
      that emissions will be reduced to a level equivalent to the level achieved by meeting the residual HAP limit  
      by stripping. Extrapolation of industry estimates of the cost of enhanced stripping place the cost of enhanced
      stripping as low as 10 percent of the cost of incineration.                                                   
    
    F. Economic Impacts
    
        Economic impacts for the regulatory alternatives analyzed at 
    proposal show that the estimated price increases for the affected 
    chemicals range from 0.2 percent for nitrile butadiene latex (NBL) to 
    2.5 percent for BR. Estimated decreases in production range from 0.7 
    percent for NBL to 5.0 percent for BR. With the reduced estimate in 
    costs from proposal, the economic impacts of the final rule should be 
    lower than those estimated at proposal. No closures of facilities are 
    expected as a result of the standard.
        Three aspects of the analysis are likely to lead to an overestimate 
    of the impacts. First, the economic analysis model assumes that all 
    affected firms compete in a national market, though in reality some 
    firms may be protected from competitors by regional or local trade 
    barriers. Second, facilities with the highest control cost per unit of 
    production are assumed to also have the highest baseline production 
    costs per unit. This assumption may not always be true, because the 
    baseline production costs per unit are not known, and thus, the 
    estimated impacts, particularly for the smaller firms, may be too high. 
    Finally, economic impacts may be overstated, because the alternative 
    for halobutyl rubber and butyl rubber that was used in this analysis is 
    more stringent and more costly than the selected regulatory 
    alternative.
        For more information regarding the impacts of the final standards, 
    consult the Basis and Purpose Document (see the Supplementary 
    Information section near the beginning of the preamble).
    
    IV. Significant Comments and Changes to the Proposed Standards
    
        In response to comments received on the proposed standards, changes 
    have been made to the final standards. While several of these changes 
    are clarifications designed to make the EPA's intent clearer, a number 
    of them are significant changes to the requirements of the proposed 
    standards. A summary of the substantive comments and/or changes made 
    since the proposal are described in the following sections. The 
    rationale for these changes and detailed responses to public comments 
    are included in the Basis and Purpose Document for the final standards. 
    Additional information is contained in the docket for these final 
    standards (see ADDRESSES section of this preamble).
        National Emission Standards for Hazardous Air Pollutant Emissions 
    from the Production of Acrylonitrile Butadiene Styrene (ABS) Resin, 
    Styrene Acrylonitrile (SAN) Resin, Methyl Methacrylate Acrylonitrile 
    Butadiene Styrene (MABS) Resin, Methyl Methacrylate Butadiene Styrene 
    (MBS) Resin, Polystyrene Resin, Poly(ethylene terephthalate) (PET) 
    Resin, and Nitrile Resin (Group IV Polymers and Resins) (40 CFR part 
    63, subpart JJJ), were developed concurrently with subpart U. Many of 
    the basic requirements of the two rules are alike, and in some cases 
    they are identical. Subpart V was proposed on March 29, 1995, and 
    comments from the public were received. In many instances, similar 
    comments were received on analogous sections of subparts U and V. In 
    these instances, the responses to comments and appropriate rule changes 
    were coordinated. However, in some instances, comments were received on 
    subpart V, and not on subpart U, that were applicable to provisions of 
    subpart U. A summary of these comments can be found in the ``Hazardous 
    Air Pollutant Emissions from Process Units in the Thermoplastics 
    Manufacturing Industry--Basis and Purpose Document for Final Standards, 
    Summary of Public Comments and Responses'' (EPA-453/R-96-001b, May 
    1996; Docket Number
    
    [[Page 46918]]
    
    A-92-45, Item Number V-C-1). In a few cases, the EPA decided that a 
    change to subpart U based on these comments was appropriate. These 
    changes did not result in a change in the stringency of the subpart U 
    provisions, but were typically changes to improve the clarity of the 
    rule. The one area where a subpart V comment resulted in a tangible 
    change to subpart U was in the batch vent applicability determination; 
    that is, an affected source is allowed to determine the group status of 
    a batch front-end process vent based on its primary product.
    
    A. Applicability Provisions and Definitions
    
    1. Designation of Affected Source and the Definition of EPPU
        Commenters expressed confusion about the definitions of affected 
    source and EPPU in the proposed rule. The EPA reviewed both definitions 
    and agreed the definitions needed clarification. Therefore, the EPA has 
    revised the language describing affected source and EPPU in the final 
    rule. The definition of affected source has been clarified, as 
    discussed in section II and paragraph A.3 of this section.
        The definition of EPPU was revised and now includes a list of the 
    equipment that comprises an EPPU. Because wastewater operations are 
    ancillary equipment and are often used by more than one EPPU and may be 
    used by more than one affected source, they are not included as part of 
    the EPPU.
    2. Definition of Organic HAP
        Numerous commenters recommended that the EPA restrict the list of 
    organic HAP in the final rule to those that are used or are present in 
    significant quantities at EPPUs or those that are listed in the HON, 
    subpart F, table 2. The EPA agreed with the commenters that a table 
    providing a listing of the specific organic HAP expected to be 
    regulated for each subcategory covered by the rule should be included 
    in the final rule. Therefore, the definition of organic HAP was revised 
    to specify those organic HAP known to be used or present in significant 
    quantities for each subcategory. This list is provided in table 7 of 
    the final rule.
        This revised definition of organic HAP was developed using 
    available process description information received from industry and 
    gathered from available literature. Because there may be additional 
    organic HAP present at an affected source, the final rule requires 
    owners or operators to notify the EPA of the presence of any additional 
    organic HAP based on the following criteria: (1) Organic HAP is 
    knowingly introduced into the manufacturing process, or has been or 
    will be reported under any Federal or State program, such as TRIS or 
    Title V; and (2) Organic HAP is presented in Table 2 of subpart F.
    3. Determining New Source Status
        The EPA received comments regarding the process for determining if 
    new or existing source requirements would apply to a particular EPPU. 
    In response to those comments, the EPA has revised the provisions in 
    the final standards. Under the final standards, new affected sources 
    are created under each of the following four situations: (1) If a plant 
    site with an existing affected source producing an elastomer product as 
    its primary product constructs a new EPPU also producing the same 
    elastomer product as it primary product, the new EPPU is a new affected 
    source if the new EPPU has the potential to emit more than 10 tons per 
    year of a single HAP, or 25 tons per year of all HAP; (2) when an EPPU 
    is constructed at a major source plant site where the elastomer product 
    was not previously produced; (3) if a new EPPU is constructed at a new 
    plant site (i.e., green field site) that will be a major source; and 
    (4) when an existing affected source undergoes reconstruction, thus 
    making the previously existing source subject to new source standards.
        This approach to defining a new affected source was selected in 
    order to make subpart U more consistent with the HON. This standard 
    differs from the HON, however, in that it applies to multiple source 
    categories. Thus, unlike the HON, a newly added EPPU at a facility is 
    covered by this rule even if that EPPU is in a different source 
    category from the existing EPPUs at the facility. It is the EPA's 
    position that the addition of a process unit in a different source 
    category is a new source and must meet the requirements for new sources 
    even though the EPPU may have the potential to emit less than 10 tons 
    per year of a single HAP or 25 tons per year of all HAP. Indeed, if a 
    source covered by another MACT standard (i.e., a different source 
    category) were built at a HON facility, that source would be subject to 
    the new source requirements under that MACT standard.
    4. Flexible Operation Units
        The final rule has retained the HON concept of flexible operation 
    units, but the language in the final rule has been significantly 
    modified to more adequately address polymer production facilities. The 
    final provisions require flexible operation units with an elastomer as 
    the primary product to commit to complying with the elastomers rule at 
    all times, regardless of what product they are producing at any 
    particular time. The primary product for a flexible operation unit is 
    determined based on projected production for the next 5 years.
    
    B. Storage Vessel Provisions
    
        In comments received on the storage tank provisions, the EPA noted 
    a common misinterpretation of the proposed regulation related to the 
    distinction between a ``storage vessel'' and a ``surge control 
    vessel''. The EPA determined that many of the comments received on 
    ``storage vessels'' were in fact referring to vessels that fall under 
    the definition of surge control vessel. The EPA suggests that owners 
    and operators of facilities subject to subpart U pay careful attention 
    to these definitions.
    1. Applicability Requirements
        Several comments were received requesting that the EPA consider the 
    exemption of vessels storing specific HAP or products. In fact, one 
    commenter indicated that the EPA should conduct a full floor analysis 
    for new and existing storage vessels, considering each chemical 
    separately and the various sizes of tanks for each subcategory. Other 
    commenters supported the exemption of stripped latex storage tanks from 
    control requirements, but also declared that high conversion SBR or 
    polybutadiene latex storage tanks should also be exempt. Another 
    commenter stated that tanks downstream of EPR stripping operations 
    should be exempt from storage vessel requirements, just as those 
    containing latex downstream of stripping operations are exempt.
        The EPA does not believe that the floor analyses for each HAP 
    stored at elastomer production facilities are required to be conducted 
    under the Act, nor should they be conducted. The Act requires the EPA 
    to set emission standards for HAP on a source category (or subcategory) 
    basis; it does not compel the EPA to establish separate control 
    measures for each HAP emitted by a source in the category. As suggested 
    by the commenter, this approach could result in an incomplete standard, 
    since it would not include a standard for a listed HAP that may be used 
    in the future by elastomer facilities. Further, consideration of 
    individual HAP storage vessel controls would not be representative of 
    facility-wide storage vessel control levels.
    
    [[Page 46919]]
    
        However, the EPA believes that it is reasonable to exempt a storage 
    vessel from the final regulation when it is clear that the vessel would 
    never be a Group 1 storage vessel. The EPA determined that the 
    following HAP used in the elastomer industry have low enough vapor 
    pressures that vessels storing these HAP would never be Group 1: 
    acrylamide, epichlorohydrin, and styrene. Therefore, the final rule 
    exempts storage vessels containing these HAP at existing sources. This 
    exemption is also extended to surge control vessels and bottoms 
    receivers at existing sources.
        In addition, the EPA is convinced that an SBL storage vessel (high 
    conversion or otherwise) would never contain sufficient HAP to exceed 
    the vapor pressure cutoff for Group 1 storage vessels. This is 
    primarily due to the low vapor pressure of styrene. Therefore, the 
    final rule exempts all SBL storage vessels, surge control vessels, and 
    bottoms receivers from the requirements of Secs. 63.484 and 63.502.
        Finally, the EPA agrees that storage vessels, surge control 
    vessels, and bottoms receivers downstream of stripping operations at 
    ethylene-propylene rubber facilities that are in compliance with the 
    provisions of Sec. 63.494 through the use of stripping technology 
    should be exempt from the storage vessel, surge control vessel, and 
    bottoms receiver requirements. Further, the EPA believes that these 
    exemptions should also extend to the other subcategories required to 
    comply with the residual organic HAP limitations in Sec. 63.494(a)(1)-
    (3). However, since the residual organic HAP content of rubber leaving 
    the stripping operations at ethylene propylene rubber and 
    polybutadiene/ styrene-butadiene rubber by solution facilities 
    complying with these provisions through the use of add-on control is 
    not restricted, these exemptions are not available to these facilities.
    2. Emission Limits
        Commenters requested that the regulation allow the use of 
    alternative storage vessel/surge control vessel control techniques. Two 
    commenters described specific control systems present at their 
    facilities, and asked that the EPA include allowances for these systems 
    in the rule. They stressed that such allowances should consider the 
    overall effectiveness of the control system, and not just the 
    efficiency of the control or recovery device.
        The EPA agrees that it is reasonable to consider the overall 
    effectiveness of a control ``system'' in determining compliance with 
    the rule, and that such systems that have been demonstrated to be 
    equivalent to the reference control technology should be allowed. While 
    the EPA believes the system described by the commenter could be 
    demonstrated to be equivalent to the reference control technology for 
    surge control vessels, the commenter did not provide sufficient 
    documentation to allow a complete evaluation of equivalence.
        However, the EPA maintains that subpart U, as proposed, already 
    provides the opportunity for the commenter, as well as other elastomer 
    production facilities, to demonstrate equivalency of alternative 
    control techniques. For storage vessels, Sec. 63.121 of subpart G 
    addresses the procedures to obtain approval of alternative means of 
    emission limitations. For surge control vessels and bottoms receivers, 
    these procedures are contained in Sec. 63.177 of subpart H. In summary, 
    these sections specify that the owner or operator must submit 
    documentation of the equivalency determination to the Administrator.
    
    C. Continuous Front-end Process Vent Provisions
    
    1. Applicability Requirements
        Several commenters stated that the exemption from halide controls 
    for butyl/halobutyl production should be extended to all rubber 
    manufacturers, since halogen-containing compounds or by-products have 
    historically been routed to flares. Another commenter agreed with the 
    exemptions for butyl and halobutyl production facilities, but pointed 
    out that this exemption should only be applicable to existing sources.
        Only one existing facility was identified in each the halobutyl and 
    the butyl rubber subcategories. At both of these facilities, 
    halogenated vent streams were vented to a flare and/or boiler. Since 
    both of these subcategories were single-facility subcategories, the 
    MACT floor was determined to be the existing level of control. The EPA 
    examined the impacts of requiring halogenated vent streams at the 
    halobutyl and butyl rubber facilities to comply with the proposed 
    requirements for all other elastomer subcategories (i.e, the HON-level 
    of control). The EPA concluded that the costs associated with this 
    level of control were not reasonable, given the associated emission 
    reduction. Therefore, the proposed regulation allowed halogenated 
    streams at halobutyl and butyl rubber facilities that were routed to a 
    flare or boiler prior to proposal to continue to be controlled with 
    these combustion devices, without additional control for the resulting 
    halides.
        Prior to proposal, the EPA was aware of one EPR facility that also 
    routed a halogenated vent stream to a boiler. However, since only one 
    of five EPR facilities reported this situation, the EPA concluded that 
    this level of control was not the MACT floor for EPR. Other EPR 
    producers claimed that they also had halogenated streams at their 
    facilities, but none offered any information to quantify the amount of 
    halogens in the stream to determine if the streams could be classified 
    as halogenated.
        After proposal, the EPA learned that chlorinated organic compounds 
    are present in streams at all of the EPR facilities. These compounds 
    are a by-product of the polymerization reaction, resulting from a 
    chlorinated catalyst. At all four of the facilities contacted, the 
    streams containing the chlorinated compounds are routed to either a 
    flare or boiler. Due to the widely varying concentration in the stream, 
    all facilities indicated that it was difficult, if not impossible, to 
    accurately determine the halogen atom concentration in the vent stream. 
    However, all expressed confidence that at times, the halide threshold 
    in the incoming stream was exceeded.
        Therefore, the EPA concluded that four of the five EPR facilities 
    have halogenated streams that are routed to either a boiler or flare. 
    For this reason, the EPA has determined that the floor for EPR is the 
    existing level of control for these halogenated vent streams. In 
    addition, as with halobutyl and butyl rubber, the EPA does not believe 
    that it would be cost-effective to require new incinerators and 
    scrubbers to be installed at these facilities, when the only net 
    emission reduction would be the reduction of the hydrochloric acid, 
    since the reduction of the halogenated organic compound in the 
    incinerator would be the same as was already being achieved in the 
    boiler or flare. However, as noted above, sufficient stream-specific 
    information was not available to conduct this analysis. Therefore, the 
    final rule has been changed to extend the exemption for existing 
    halogenated streams routed to a boiler or flare to EPR producers. 
    Further, the final rule specifies that this exemption does not apply to 
    new sources.
    2. Emission Limits
        Based on a commenter's request, the final rule exempts a vent 
    stream routed to an internal combustion engine as primary fuel from 
    source testing requirements. The final rule also requires that the on/
    off status of internal
    
    [[Page 46920]]
    
    combustion be monitored as a means of demonstrating compliance with 
    these control requirements.
    
    D. Batch Front-End Process Vent Provisions
    
        Commenters believed that batch front-end process vent provisions 
    were inappropriate and unnecessarily burdensome. Several commenters 
    disagreed with the EPA's reliance on the Batch Processes ACT document 
    in the development of the batch vent provisions, claiming that it was 
    not appropriate to the elastomer manufacturing industry.
        The EPA believes that the potential for HAP emissions from batch 
    operations at elastomer production facilities warrant control. While 
    the EPA disagrees with the statement that the provisions are 
    inappropriate, the EPA agrees with comments regarding the complexity of 
    the proposed batch vent provisions. Therefore, in the final rule these 
    provisions were simplified. Many of these changes are discussed below.
        In response to comments on the batch front-end process vent 
    applicability provisions, the volatility class concept has been 
    eliminated. The Batch Processes ACT developed an annual threshold 
    emission level for each of three volatility classes. The EPA initially 
    judged that selection of a single annual threshold emission level would 
    not be appropriate and included all three levels in the proposed 
    standards. However, upon further review, the EPA found no adverse 
    impact would result from the use of a single annual threshold emission 
    level and, indeed, the final standards have been significantly 
    simplified. Besides removing the requirement to determine the 
    volatility class, the final standards contain only one equation for 
    determining the cutoff flow rate (Sec. 63.488(f)) which is the last 
    step in the group determination process.
        A commenter on the proposed Polymers and Resins IV (40 CFR part 63, 
    subpart V) regulation suggested changing the batch vent group 
    determination provisions to only utilize emissions data from an EPPU's 
    primary product. The EPA agreed that to base the group determination on 
    a single product could, if appropriately applied, provide acceptable 
    results from an environmental perspective, while simplifying the 
    compliance requirements for and improving the enforceability of the 
    batch front-end process vent standards. Therefore, the final standards 
    contain provisions allowing the owner or operator of an affected source 
    to perform the group determination for batch front-end process vents 
    based on annualized production of a single batch product. However, the 
    EPA does not consider it to be appropriate from an environmental 
    perspective to allow anything other than the worst-case HAP emitting 
    batch product to be considered when basing applicability on a single 
    product. Therefore, the final standards specify that the worst-case HAP 
    emitting batch product be used when an owner or operator chooses to 
    annualize a single product for purposes of determining applicability. 
    The final standards define the worst-case HAP emitting product and 
    describe how emissions are to be annualized to represent full-time 
    production, where full-time production does not necessarily mean 
    operating at maximum production rate. Since the proposed batch vent 
    provisions were similar between subparts U and V, the EPA decided that 
    this change was also appropriate for subpart U.
        Several commenters stated that the proposed provisions for the 
    methods allowed for the calculation of batch front-end process vent 
    emissions were overly restrictive. The proposed rule required that 
    emissions be calculated using either the emission estimation equations 
    or source testing. If the owner or operator could demonstrate that both 
    the equations and source testing were inappropriate, then they were 
    allowed to use engineering assessment to calculate HAP emissions. The 
    commenters believed that an affected source should be allowed to use 
    engineering assessments without having to demonstrate that source 
    testing was inappropriate.
        The EPA maintains that it is imperative that a consistent technique 
    for the estimation of batch front-end process vent emissions be used, 
    which is provided through the emission estimation equations. The EPA 
    believes the data required to use the batch front-end process vent 
    emissions estimation equations should be obtainable with reasonable 
    effort. The final standards continue to require use of the emissions 
    estimation equations, unless the owner or operator can demonstrate that 
    these equations are inappropriate.
        However, the EPA has concluded that direct measurement of emissions 
    through testing may prove to be difficult and may or may not provide an 
    increased assurance of accuracy over the use of engineering assessment. 
    Therefore, if an owner or operator can demonstrate that the emissions 
    estimation equations are not appropriate, the final standards allow the 
    selection of either direct measurement or engineering assessment. 
    Further, criteria for demonstrating that the emissions estimation 
    equations are not appropriate to a specific batch emissions episode 
    have been added to the final standards. These criteria require either: 
    (1) The availability of test data that demonstrate a greater than 20 
    percent discrepancy between the test value and the estimated value, or 
    (2) that the owner or operator demonstrate to the Administrator that 
    the emissions estimation equations are not appropriate for a given 
    batch emissions episode.
    
    E. Back-End Process Operation Provisions
    
        The back-end process operation provisions received the majority of 
    the comments on the proposed rule. Significant comments were received 
    on practically every aspect of these provisions. Following is a summary 
    of the comments that resulted in notable changes to the back-end 
    process operation requirements.
    1. Averaging Period
        Several commenters declared that compliance based on a weekly 
    average HAP limitation was unreasonable, and that compliance should be 
    demonstrated on the basis of a monthly (or 30-day) rolling average 
    instead. These commenters claimed that requiring compliance based on a 
    weekly average fails to provide adequate operational flexibility for 
    manufacturers to produce different grades of polymers in accordance 
    with customer demands.
        Upon investigation of this issue, the EPA concluded that a monthly 
    averaging period for the residual HAP limitations was more appropriate. 
    Changing to a monthly averaging period would provide more operational 
    flexibility to elastomer producers, while maintaining the same annual 
    emission reduction.
    2. Residual Organic HAP Limitations
        Commenters objected to numerous aspects of the residual organic HAP 
    limitations. Most of these comments were directed towards the methods 
    used to determine the back-end MACT floors. Discussed below are 
    comments on definitions, test methods, and other areas that affect the 
    determination of the residual organic HAP limitations. The EPA 
    addressed these comments and re-assessed the MACT floors.
        Definition of crumb rubber dry weight. Comments stated that, for 
    solution processes, the definition of ``crumb rubber dry weight'' 
    should not exclude extender oils and carbon black for compliance 
    purposes, because these are an integral part of the polymer. The EPA 
    agrees with these comments, and has
    
    [[Page 46921]]
    
    revised the definition of crumb rubber dry weight to reflect this 
    decision.
        Residual organic HAP test methods. Concurrent with the proposal of 
    subpart U, the EPA proposed three residual HAP test methods--one each 
    for SBRE, PBR/SBRS, and EPR. Several commenters stated that no single 
    analytical method would produce consistent results for all polymers, 
    and consequently, each company should be allowed to demonstrate 
    compliance using a company-specific method that is comparable to the 
    EPA test method.
        After careful review and consideration of this issue, the EPA 
    agreed with the commenters and has undergone an extensive effort to 
    rectify this situation. The EPA concluded that it was appropriate to 
    allow every interested company to validate their own test method using 
    a modified version of 40 CFR part 63, appendix A, Method 301.
        A total of nine test methods were submitted (three for EPR, three 
    for SBRE, and three for PBR/SBRS). The modified Method 301 analysis 
    performed allows each company to validate their own test method, and 
    seven of the ten affected companies have done so. Therefore, each 
    source has a compliance method available for determining residual HAP. 
    The EPA believes that it would be helpful if the industry had access to 
    all validated test methods, and is in the process of reviewing the 
    methods and validation data that were submitted, and has preliminarily 
    indicated that approval of all nine methods is anticipated. The EPA 
    intends to promulgate these methods as appendix A Methods 310 a, b, and 
    c for EPR, Methods 312 a, b, and c for SBRE, and Methods 313 a, b, and 
    c for PBR/SBRS. However, since the approval and subsequent promulgation 
    of the methods has not yet occurred, this final rule does not stipulate 
    the methods to be used to determine residual organic HAP. Upon 
    promulgation of these methods, the Agency will propose modifications to 
    subpart U to specify that these methods be used to determine residual 
    organic HAP.
        Furthermore, the affected industry has been intimately involved 
    with all activity associated with the EPA's promulgation of the 
    residual organic HAP test methods. The EPA held meetings with industry 
    representatives to discuss their comments on the proposed methods, and 
    to discuss procedures for validating company test methods. Every 
    company that was expected to be subject to the back-end residual 
    organic HAP limitations was invited to these meetings. As noted above, 
    a total of nine test methods were submitted. These methods were from 
    seven companies, leaving only three affected companies that decided not 
    to submit methods. Representatives of each of those three companies 
    which did not submit test methods were in attendance at one or more of 
    the meetings and are therefore knowledgeable about the test methods. 
    Since industry's submittal of the test methods, the EPA has worked 
    closely with industry representatives to finalize the methods. 
    Therefore, the EPA contends that all affected companies should be well 
    aware of the methods that will be promulgated.
        As noted earlier, the final approval of these test methods is 
    upcoming. It is anticipated that these methods will be promulgated in 
    the autumn of 1996. The EPA does not believe that the interval between 
    the promulgation of subpart U and the promulgation of these residual 
    organic HAP test methods impairs the ability of any source to comply 
    with the requirements by the specified compliance date. This is the 
    case because affected sources are not required to be in compliance 
    until three years after promulgation of the rule.
        MACT floor determination. Commenters indicated that the selection 
    of a MACT floor ``somewhere between the mean, median, and mode'' did 
    not represent central tendency. They maintained that a mean is the 
    correct approach for establishing the MACT floor. The EPA agreed that 
    one measure of central tendency should be used to establish the average 
    and decided that the mean was the most appropriate measure for the 
    residual organic HAP limitations floor determinations. In some 
    situations, the use of the mean can result in a floor level of control 
    that is not represented by any available control technology. However, 
    this did not apply to this situation, where the emissions used to 
    determine the floor were a result of process-specific stripping 
    techniques, and not specific add-on control technologies.
        For EPR and PBR/SBRS, commenters stated that combining data 
    received from different companies using different sampling and 
    analytical methods, without establishing whether the methods achieve 
    comparable results, was not an appropriate way to establish residual 
    HAP limits. The commenters stated that if production figures and dryer 
    stack testing results were used to establish these limits, these 
    results cannot be equated to those from crumb sampling at the EPA's 
    designated sampling point, because there are numerous potential 
    emission sources between the proposed sampling point and the stack 
    testing locations. In addition, commenters indicated that the proposed 
    limitation did not recognize the fact that residual HAP may remain in 
    the polymer after finishing. Finally, the commenters also stated that 
    using annual emissions and limited weekly data to establish weekly 
    limits is inherently uncertain, and may have resulted in an 
    inappropriate standard.
        In the original MACT floor analyses, the EPA presumed that the 
    back-end emission factor calculated from the reported emissions and 
    production was equivalent to the residual HAP levels in the crumb 
    leaving the stripping operations. Inherent in this analysis was the 
    assumption that the companies reported total HAP emissions from all 
    back-end emission sources, rather than only a portion of these sources.
        Upon receipt of these comments, the EPA again contacted each EPR 
    and PBR/SBRS production facility to (1) verify the emissions numbers 
    used to determine the back-end emission factor, (2) discuss the 
    correlation of the methods used to estimate the original emission 
    estimates and the residual organic HAP test methods undergoing 
    validation, (3) determine the appropriate production, including oil 
    extender weight, to use in determining the emission factor, (4) obtain 
    information related to residual HAP remaining in the product after 
    finishing, and (5) obtain short-term residual HAP information to be 
    used in the adjustment of annual emissions to monthly.
        After obtaining this information, the EPA recalculated the MACT 
    floors for each subcategory. It should be noted that only one facility 
    indicated that the original emission estimates were calculated in a 
    manner that was inconsistent with the residual organic HAP test 
    methods. Two PBR/SBRS companies and one EPR company provided detailed 
    short-term residual HAP data to allow the conversion of the annual data 
    to a monthly limit. The resulting monthly limits were 8 kg/Mg for EPR 
    and 10 kg/Mg for PBR/SBRS.
        While no comments were received criticizing the MACT floor analysis 
    for SBRE, the change to a monthly average limit resulted in a change in 
    the SBRE limit. In the determination of the original SBRE back-end MACT 
    floor, residual HAP data were used from three of the four facilities. 
    The fourth facility provided residual HAP data, but it was in a monthly 
    average format and could not be used in the determination of a weekly 
    limit. However, the change to a monthly limit meant that the data from 
    this facility could also be used, resulting in a monthly limit of 0.4 
    kg styrene per
    
    [[Page 46922]]
    
    Mg latex leaving the stripping operation for existing SBRE sources.
    3. Monitoring Requirements
        Several comments were received regarding the proposed crumb and 
    latex sampling requirements. In both instances, the EPA decided that 
    the changes suggested by the commenters were technically appropriate, 
    and they did not result in any detrimental environmental impact.
        Specifically, commenters found the requirement to sample ``before 
    any opportunity for emissions to the atmosphere'' to be either 
    infeasible or unsafe for PBR/SBRS and EPR and suggested modifications 
    to the proposed sampling provisions. In response to these comments, the 
    final rule states that PBR/SBRS or EPR crumb samples must be taken ``as 
    soon as safe and feasible after the stripping operation, but no later 
    than the entry point for the first unit operation following the 
    stripper (e.g., the dewatering screen).''
        For SBRE, commenters pointed out that a more logical sampling 
    location for determining the initial HAP concentration in the SBL is 
    the mixed latex in the storage tank feeding the coagulator (rather than 
    directly after the stripper). The EPA agreed with these comments, and 
    the final rule has revised the SBL sampling location to be ``prior to 
    any coagulation operations.''
        Comments were also received opposing the proposed crumb or latex 
    sampling frequency provisions. Commenters believed that it is 
    impractical to take a rubber sample each operating day for every grade 
    of elastomer produced, because of the time required to reach 
    representative operating conditions and to run an accurate analytical 
    test. Suggested alternatives included one test per day, one test per 
    ``campaign,'' daily sampling that is reduced to weekly sampling upon 
    demonstration of daily compliance, and daily sampling with the 
    exception of grades produced for less than 4 hours in a day. Since the 
    variability of the residual HAP contents between elastomer grades is 
    relatively small, and since production schedules typically produce very 
    similar grades of polymer for extended periods of time, the EPA 
    concluded that reducing the sampling frequency to once per day for 
    continuous processes would greatly simplify the rule, while still 
    ensuring that practically all grades of elastomer are represented by 
    such sampling. This change is reflected in the final rule.
        Some commenters were concerned that compliance would be based on 
    one sample per day, and requested that an owner or operator be allowed 
    to sample crumb or latex more frequently, and include the residual 
    organic HAP results of these samples in the average. While the EPA 
    believes that the proposed rule did not preclude a company from using 
    more than one sample per day in determining the (weekly) average, the 
    EPA has revised the language in the final rule to make this opportunity 
    clearer.
        Several commenters stated that the rule should provide an allowance 
    for missed or invalid crumb or latex samples. The proposed rule 
    designated the failure to collect any single sample as an excursion. 
    These commenters suggested that the EPA should require 75 percent of 
    samples to be collected.
        The EPA recognizes that a number of circumstances could occur that 
    cause a sample not to be analyzed in accordance with the rule. These 
    may be in the form of sampling system malfunctions, mis-analysis, or 
    other problems. The EPA realizes that there are unique challenges 
    associated with the sampling of solid polymer, and agrees that problems 
    could occur that would cause a sample to be missed. The EPA also 
    recognizes that some of the test methods being validated to analyze the 
    residual organic HAP in the crumb take long periods of time to perform, 
    meaning that the opportunity to obtain a second sample may not be 
    available if a mis-analysis in the laboratory occurs. While the EPA 
    expects that sound company procedures could eliminate most of these and 
    other problems, the EPA agrees that it is unreasonable to expect that 
    no problems would ever occur that result in a missed sample. Therefore, 
    an excursion for back-end process operations is defined in the final 
    rule as when either (1) the monthly weighted average is above the 
    applicable limit, or (2) when less than 75 percent of the required 
    samples are taken, analyzed, and included in the monthly average.
        At proposal, the EPA specifically requested comments on the 
    feasibility of the use of computer predictive modeling as an 
    alternative to the daily crumb or latex sampling, or the stripper 
    parametric monitoring compliance alternatives. Numerous commenters 
    supported the allowance of such systems, while other expressed 
    reservations. While the EPA believes that computer predictive modeling 
    may be an attractive alternative to the periodic sampling and stripper 
    parametric monitoring compliance options, the EPA is convinced that the 
    use of computer predictive modeling is so site-specific that it is not 
    possible to include general requirements for the use of such a system 
    in subpart U. Nevertheless, the EPA believes that facilities should 
    have the opportunity to utilize techniques that are equivalent to the 
    two options of compliance provided in the proposed rule for facilities 
    using stripping technology. Therefore, the EPA has included a third 
    option that provides the opportunity for the site-specific approval of 
    alternative means of compliance through the submittal of an alternative 
    compliance plan.
    
    F. Wastewater Operations Provisions
    
        Several commenters pointed out that the wastewater provisions of 
    subpart G that are referenced in Sec. 63.501 of subpart U are the 
    subject of litigation brought by the Chemical Manufacturers' 
    Association against the EPA. Consequently, sources subject to these 
    provisions cannot know what the final wastewater provisions, proposed 
    to be incorporated into subpart U, will be. These commenters believed 
    that the EPA should ``reserve'' the provisions of Sec. 63.501 pending 
    the outcome of the litigation.
        As part of the HON litigation proposal, the EPA will request 
    comments specific to the elastomers rule. If comments specific to the 
    elastomers rule are received they will be addressed as part of the HON 
    rulemaking actions or in actions specific to the elastomers rule, 
    depending on the comments. Therefore, the comment period for this rule 
    will not be reopened.
        The EPA believes that the wastewater provisions and the other HON 
    provisions should be referenced in the elastomers rule so that final 
    resolutions of the HON litigation will be automatically included in the 
    elastomers rule. However, changes made to the HON will be evaluated by 
    the EPA for applicability to this rule. The ``automatic'' part refers 
    to the fact that text changes will not need to be made to this rule 
    once the EPA, following notice and an opportunity for comment, finds 
    the HON changes to be applicable. If the EPA determines that any 
    changes to the HON are not applicable to this rule, the elastomers rule 
    will be revised accordingly.
        Comments were received that the VOHAP threshold for regulation of 
    new source wastewater streams (10 ppmw) was too restrictive, and that 
    the EPA has not provided an economic justification regarding the 
    achievability of the limit. Another comment was received stating that 
    many elastomer product process wastewater streams will have VOHAP 
    concentrations less than 50 ppmw, and monitoring and recordkeeping 
    requirements are not needed for these streams. This comment recommended 
    that the EPA exempt from regulation
    
    [[Page 46923]]
    
    ``any process stream at an affected source with an average flow rate of 
    less than 0.02 liters per minute or an average VOHAP concentration of 
    less than 50 ppmw.''
        The EPA evaluated the new source MACT floor determinations for 
    wastewater, and determined that no facility in any subcategory reported 
    wastewater controls equivalent to the new source levels. In fact, no 
    facility-wide wastewater controls greater than the existing source HON 
    limitations were reported. Therefore, the EPA believes that this 
    comment is valid, and has changed the final rule so that the new 
    sources are subject to the same wastewater requirements as existing 
    sources.
        In the proposed rule, the definition of ``wastewater'' stated that 
    a stream must contain at least 5 ppmw of VOHAP and have a flow rate of 
    0.02 liter per minute. Given the change in the definition of a Group 1 
    wastewater stream for new sources, the EPA believes that it is 
    reasonable to revise the definition of wastewater in accordance with 
    the commenter's suggestion and therefore the wastewater definition has 
    been revised in the final rule.
    
    G. Equipment Leak Provisions
    
        One commenter requested that the proposed rule include an exclusion 
    for reciprocating pumps that must leak small quantities of product to 
    lubricate and cool the shaft and seal areas. The EPA agrees that an 
    exemption for the situation described by the commenter is reasonable. 
    The EPA reached a similar conclusion in the proposed Polymers and 
    Resins IV regulation (subpart V). Therefore, Sec. 63.502(d) has been 
    added to the final rule that exempts these reciprocating pump systems.
        Several commenters stated that 3 years should be allowed for 
    compliance with equipment leak provisions for compressors (instead of 6 
    months) under certain circumstances. The EPA agrees with the 
    commenters, and has amended the compliance schedule for compressors in 
    the following situations: (1) Existing reciprocating compressors which 
    would require design modifications to connect to a closed-vent or 
    recovery system; and (2) systems where existing compressors would be 
    replaced.
    
    H. Emissions Averaging Provisions
    
        Several commenters requested that batch front-end process vents be 
    eligible to average emissions. The EPA had not allowed emissions 
    averaging of batch front-end process vents at proposal because the EPA 
    considered the accuracy and consistency needed for emissions averaging 
    to be greater than that needed for applicability determinations. 
    However, upon reconsideration, the EPA determined that the accuracy and 
    consistency needs of emissions averaging could be met by applying a 
    ``discount'' factor (10 percent) to calculated emissions or by 
    requiring direct measurement of emissions. Therefore, the final rule 
    allows emissions averaging of existing batch front-end process vents.
    
    I. Monitoring
    
        Many commenters requested that the proposed rule allow excused 
    excursions in the same way that the HON rule allows excused excursions. 
    In the final rule, the EPA decided to excuse a certain number of 
    excursions for each reporting period. This decision was based on data 
    and information presented during public comment on the HON and 
    reiterated in public comments received on this rule, and during 
    industry meetings held subsequent to proposal that indicated that a 
    certain number of excursions could be expected even with properly 
    operated pollution control devices. The EPA also concluded that not 
    allowing excused excursions would impose significant additional capital 
    and operating costs on the affected source for only negligible 
    corresponding reductions in air emissions. As is always the case, a 
    State has the discretion to impose more stringent requirements than the 
    requirements of NESHAP and other Federal requirements and could choose 
    not to allow the excused excursion provisions of this rule.
        The EPA considered the number of excused excursions that would be 
    most appropriate for this standard and determined that the number of 
    excursions allowed in the HON would be reasonable. Therefore, the final 
    provisions allow a maximum of 6 excused excursions for the first 
    semiannual reporting period, decreasing by 1 excursion each semiannual 
    reporting period. Starting with the sixth semiannual reporting period 
    (i.e., the end of the third year of compliance) and thereafter, 
    affected sources are allowed one excused excursion per semiannual 
    reporting period.
    
    J. Recordkeeping and Reporting
    
        Several commenters stated that the recordkeeping and reporting 
    requirements of the proposed rule were extremely burdensome and 
    requested that the EPA reduce the burden. The EPA reexamined the 
    recordkeeping and reporting requirements of the rule after proposal and 
    determined that burden reductions were warranted. The EPA considers the 
    recordkeeping and reporting requirements of the final rule the minimum 
    necessary to ensure compliance with the final standards. The following 
    changes were made to reduce the recordkeeping and reporting burden:
        (1) The requirement to submit an Initial Notification has been 
    eliminated;
        (2) The requirement to submit an Implementation Plan has been 
    eliminated;
        (3) The requirement to record monitored parameters every 15 minutes 
    has been removed. The final rule requires hourly recording of monitored 
    parameters in place of the 15 minute records required in the proposed 
    rule.
        Although the above changes will reduce the burden on industry, the 
    level of this reduction was not quantified.
    
    V. Administrative Requirements
    
    A. Docket
    
        The docket is an organized and complete file of all the information 
    submitted to or otherwise considered by the EPA in the development of 
    the final standards. The principal purposes of the docket are:
        (1) To allow interested parties to readily identify and locate 
    documents so that they can intelligently and effectively participate in 
    the rulemaking process; and
        (2) To serve as the record in case of judicial review (except for 
    interagency review materials as provided for in section 307(d)(7)(A)).
    
    B. Executive Order 12866
    
        Under Executive Order 12866 (58 FR 5173 (October 4, 1993)), the EPA 
    must determine whether the regulatory action is ``significant'' and 
    therefore subject to Office of Management and Budget (OMB) review and 
    the requirements of the Executive Order. The Executive Order defines 
    ``significant regulatory action'' as one that is likely to result in 
    standards that may:
        (1) Have an annual effect on the economy of $100 million or more or 
    adversely affect, in a material way, the economy, a sector of the 
    economy, productivity, competition, jobs, the environment, public 
    health or safety, or State, local, or tribal governments or 
    communities;
        (2) Create a serious inconsistency or otherwise interfere with an 
    action taken or planned by another agency;
        (3) Materially alter the budgetary impact of entitlement, grants, 
    user fees, or loan programs or the rights and obligations of recipients 
    thereof; or
        (4) Raise novel legal or policy issues arising out of legal 
    mandates, the
    
    [[Page 46924]]
    
    President's priorities, or the principles set forth in the Executive 
    Order.
        Pursuant to the terms of the Executive Order, the OMB has notified 
    the EPA that it considers this a ``significant regulatory action'' 
    within the meaning of the Executive Order. The EPA submitted this 
    action to the OMB for review. Changes made in response to suggestions 
    or recommendations from the OMB were documented and included in the 
    public record.
    
    C. Paperwork Reduction Act
    
        The information collection requirements for this NESHAP have been 
    submitted for approval to the Office of Management and Budget (OMB) 
    under the Paperwork Reduction Act, 44 U.S.C. 3501 et seq. An 
    Information Collection Request (ICR) document has been prepared by the 
    EPA (ICR No. 1746.01), and a copy may be obtained from Sandy Farmer, 
    OPPE Regulatory Information Division (2137), U.S. Environmental 
    Protection Agency, 401 M Street, SW., Washington, DC 20460, or by 
    calling (202) 260-2740.
        The public recordkeeping and reporting burden for this collection 
    of information is estimated to average approximately 587 hours per 
    respondent for each of the first 3 years following promulgation of the 
    rule. These estimates include time for reviewing instructions, 
    searching existing data sources, gathering and maintaining the data 
    needed, and completing and reviewing the collection of information.
        Send comments regarding the recordkeeping and reporting burden 
    estimate or any other aspect of this collection of information, 
    including suggestions for reducing this burden, to Chief, Information 
    Policy Branch (2137), U.S. Environmental Protection Agency, 401 M 
    Street, SW., Washington, DC 20460; and to the Office of Information and 
    Regulatory Affairs, Office of Management and Budget, Washington, DC 
    20503, marked ``Attention: Desk Officer for EPA.''
    
    D. Regulatory Flexibility Act
    
        The EPA has determined that it is not necessary to prepare a 
    regulatory flexibility analysis in connection with this final rule. The 
    EPA has also determined that this rule will not have a significant 
    adverse economic impact on a substantial number of small businesses. 
    Consistent with Small Business Administration (SBA) size standards, an 
    elastomer producing firm is classified as a small entity if it has less 
    than 750 employees and is unaffiliated with a larger domestic entity. 
    Based upon this standard, three of the eighteen elastomer producing 
    firms are classified as small entities (i.e., having fewer than 750 
    employees). The EPA determined that annual compliance costs as a 
    percentage of sales are less than one percent for all of the small 
    entities affected by this regulation. This does not qualify as a 
    significant economic impact on a substantial number of small 
    businesses.
    
    E. Small Business Regulatory Enforcement Fairness Act of 1996 (SBREFA)
    
        Pursuant to Subtitle E of SBREFA, this rule, which is nonmajor, was 
    submitted to Congress before publication in the Federal Register.
    
    F. Unfunded Mandates
    
        Under section 202 of the Unfunded Mandates Reform Act of 1995 
    (``Unfunded Mandates Act''), signed into law on March 22, 1995, the EPA 
    must prepare a budgetary impact statement to accompany any proposed or 
    final standards that include a Federal mandate that may result in 
    estimated costs to State, local, or tribal governments, or to the 
    private sector, of, in the aggregate, $100 million or more. Under 
    section 205, the EPA must select the most cost effective and least 
    burdensome alternative that achieves the objectives of the standard and 
    is consistent with statutory requirements. Section 203 requires the EPA 
    to establish a plan for informing and advising any small governments 
    that may be significantly or uniquely impacted by the standards.
        The EPA has determined that the final standards do not include a 
    Federal mandate that may result in estimated costs of, in the 
    aggregate, $100 million or more to either State, local, or tribal 
    governments, or to the private sector, nor do the standards 
    significantly or uniquely impact small governments, because they 
    contain no requirements that apply to such governments or impose 
    obligations upon them. Therefore, the requirements of the Unfunded 
    Mandates Act do not apply to this final rule.
    
    List of Subjects in 40 CFR Part 63
    
        Environmental protection, Air pollution control, Hazardous 
    substances, Reporting and recordkeeping requirements.
    
        Dated: July 15, 1996.
    Fred Hansen,
    Acting Administrator.
    
        For the reasons set out in the preamble, part 63 of title 40, 
    chapter I of the Code of Federal Regulations is amended as follows:
    
    PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS 
    FOR AFFECTED SOURCE CATEGORIES
    
        1. The authority citation for part 63 continues to read as follows:
    
        Authority: 42 U.S.C. 7401, et seq.
    
        2. Part 63 is amended by adding subpart U to read as follows:
    Subpart U--National Emission Standards for Hazardous Air Pollutant 
    Emissions: Group I Polymers and Resins
    Sec.
    63.480  Applicability and designation of affected sources.
    63.481  Compliance schedule and relationship to existing applicable 
    rules.
    63.482  Definitions.
    63.483  Emission standards.
    63.484  Storage vessel provisions.
    63.485  Continuous front-end process vent provisions.
    63.486  Batch front-end process vent provisions.
    63.487  Batch front-end process vents--reference control technology.
    63.488  Methods and procedures for batch front-end process vent 
    group determination.
    63.489  Batch front-end process vents--monitoring requirements
    63.490  Batch front-end process vents--performance test methods and 
    procedures to determine compliance.
    63.491  Batch front-end process vents--recordkeeping requirements.
    63.492  Batch front-end process vents--reporting requirements.
    63.493  Standards for back-end processes.
    63.494  Back-end process provisions--residual organic HAP 
    limitations.
    63.495  Back-end process provisions--procedures to determine 
    compliance using stripping technology.
    63.496  Back-end process provisions--procedures to determine 
    compliance using control or recovery devices.
    63.497  Back-end process provisions--monitoring provisions for 
    control and recovery devices.
    63.498  Back-end process provisions--recordkeeping.
    63.499  Back-end process provisions--reporting.
    63.500  Back-end process provisions--carbon disulfide limitations 
    for styrene butadiene rubber by emulsion processes.
    63.501  Wastewater provisions.
    63.502  Equipment leak provisions.
    63.503  Emissions averaging provisions.
    63.504  Additional test methods and procedures.
    63.505  Parameter monitoring levels and excursions.
    63.506  General recordkeeping and reporting provisions.
    
    [[Page 46925]]
    
    Subpart U--National Emission Standards for Hazardous Air Pollutant 
    Emissions: Group I Polymers and Resins
    
    
    Sec. 63.480   Applicability and designation of affected sources.
    
        (a) Definition of affected source. The provisions of this subpart 
    apply to each affected source. An affected source is either an existing 
    affected source or a new affected source. Existing affected source is 
    defined in paragraph (a)(1) of this section, and new affected source is 
    defined in paragraph (a)(2) of this section. The affected source also 
    includes all wastewater streams and wastewater operations associated 
    with the elastomer product process unit(s) (EPPUs) included in the 
    affected source.
        (1) Except as specified in paragraphs (b) through (d) of this 
    section, an existing affected source is defined as each group of one or 
    more EPPUs that is not part of a new affected source, as defined in 
    paragraph (a)(2) of this section, and that is manufacturing the same 
    primary product and located at a plant site that is a major source.
        (2) Except as specified in paragraphs (b) through (d) of this 
    section, a new affected source is defined as a source meeting the 
    criteria of paragraph (a)(2)(i), (a)(2)(ii), or (a)(2)(iii) of this 
    section.
        (i) At a plant site previously without HAP emission points, each 
    group of one or more EPPUs manufacturing the same primary product that 
    is part of a major source on which construction commenced after June 
    12, 1995,
        (ii) An EPPU meeting the criteria in paragraph (i)(1)(i) of this 
    section, or
        (iii) A reconstructed affected source meeting the criteria in 
    paragraph (i)(2)(i) of this section.
        (b) EPPUs exempted from the affected source. EPPUs that do not use 
    any organic HAP may be excluded from the affected source, provided that 
    the owner or operator complies with the requirements of paragraphs 
    (b)(1) and (b)(2) of this section, if requested to do so by the 
    Administrator.
        (1) Retain information, data, and analyses used to document the 
    basis for the determination that the EPPU does not use any organic HAP. 
    Types of information that could document this determination include, 
    but are not limited to, records of chemicals purchased for the process, 
    analyses of process stream composition, or engineering calculations.
        (2) When requested by the Administrator, demonstrate that the EPPU 
    does not use any organic HAP.
        (c) Emission points exempted from the affected source. The affected 
    source does not include the emission points listed in paragraphs (c)(1) 
    through (c)(6) of this section:
        (1) Stormwater from segregated sewers;
        (2) Water from fire-fighting and deluge systems in segregated 
    sewers;
        (3) Spills;
        (4) Water from safety showers;
        (5) Vessels and equipment storing and/or handling material that 
    contains no organic HAP or organic HAP as impurities only; and
        (6) Equipment that is intended to operate in organic HAP service 
    for less than 300 hours during the calendar year.
        (d) Processes exempted from the affected source. The processes 
    specified in paragraphs (d)(1) through (d)(3) of this section are not 
    part of the affected source.
        (1) Research and development facilities;
        (2) Equipment that is located within an EPPU that is subject to 
    this subpart but does not contain organic HAP; and
        (3) Solvent reclamation, recovery, or recycling operations at 
    hazardous waste treatment, storage, and disposal facilities (TSDF) 
    requiring a permit under 40 CFR part 270 that are separate entities and 
    not part of an EPPU to which this subpart applies.
        (e) Applicability determination of elastomer equipment included in 
    a process unit producing a non-elastomer product. If an elastomer 
    product that is subject to this subpart is produced within a process 
    unit that is subject to subpart V of this part, and at least 50 percent 
    of the elastomer is used in the production of the product manufactured 
    by the subpart V process unit, the unit operations involved in the 
    production of the elastomer are considered part of the process unit 
    that is subject to subpart V, and not this subpart.
        (f) Primary product determination and applicability. The primary 
    product of a process unit shall be determined according to the 
    procedures specified in paragraphs (f)(1) and (f)(2) of this section. 
    Paragraphs (f)(3) through (f)(4) of this section describe whether or 
    not a process unit is subject to this subpart. Paragraphs (f)(5) 
    through (f)(7) of this section discuss compliance for those EPPUs 
    operated as flexible operation units, as specified in paragraph (f)(2) 
    of this section.
        (1) If a process unit only manufactures one product, then that 
    product shall represent the primary product of the process unit.
        (2) If a process unit is designed and operated as a flexible 
    operation unit, the primary product shall be determined as specified in 
    paragraphs (f)(2)(i) or (f)(2)(ii) of this section based on the 
    anticipated operations for the 5 years following September 5, 1996 for 
    existing affected sources and for the first 5 years after initial 
    startup for new affected sources.
        (i) If the flexible operation unit will manufacture one product for 
    the greatest operating time over the five-year period, then that 
    product shall represent the primary product of the flexible operation 
    unit.
        (ii) If the flexible operation unit will manufacture multiple 
    products equally based on operating time, then the product with the 
    greatest production on a mass basis over the five-year period shall 
    represent the primary product of the flexible operation unit.
        (3) If the primary product of a process unit is an elastomer 
    product, then that process unit is considered an EPPU. If that EPPU 
    meets all the criteria of paragraph (a) of this section, it is either 
    an affected source or is part of an affected source comprised of other 
    EPPU subject to this rule at the same plant site with the same primary 
    product. The status of a process unit as an EPPU, and as an affected 
    source or part of an affected source shall not change regardless of 
    what products are produced in the future by the EPPU, with the 
    exception noted in paragraph (f)(3)(i) of this section.
        (i) If a process unit terminates the production of all elastomer 
    products and does not anticipate the production of any elastomer 
    product in the future, the process unit is no longer an EPPU and is not 
    subject to the provisions of this subpart after notification is made as 
    specified in paragraph (f)(3)(ii) of this section.
        (ii) The owner or operator of a process unit that wishes to remove 
    the EPPU designation from the process unit, as specified in paragraph 
    (f)(3)(i) of this section, shall notify the Administrator. This 
    notification shall be accompanied by rationale for why it is 
    anticipated that no elastomer products will be produced in the process 
    unit in the future.
        (iii) If a process unit meeting the criteria of paragraph (f)(3)(i) 
    of this section begins the production of an elastomer product in the 
    future, the owner or operator shall use the procedures in paragraph 
    (f)(4)(i) of this section to determine if the process unit is re-
    designated as an EPPU.
        (4) If the primary product of a process unit is not an elastomer 
    product, then that process unit is not an affected source, nor is it 
    part of any affected source subject to this rule. The process unit is 
    not subject to this rule at any time, regardless of what product is 
    being produced. The status of the process unit
    
    [[Page 46926]]
    
    as not being an EPPU, and therefore not being an affected source or 
    part of an affected source subject to this subpart, shall not change 
    regardless of what products are produced in the future by the EPPU, 
    with the exception noted in paragraph (f)(4)(i) of this section.
        (i) If, at any time beginning September 5, 2001, the owner or 
    operator determines that an elastomer product is the primary product 
    for the process unit based on actual production data for any preceding 
    consecutive five-year period, then the process unit shall be classified 
    as an EPPU. If an EPPU meets all the criteria in paragraph (a) of this 
    section, it is either an affected source or part of an affected source 
    and shall be subject to this rule.
        (ii) If a process unit meets the criteria of paragraph (f)(4)(i) of 
    this section, the owner or operator shall notify the Administrator 
    within 6 months of making this determination. The EPPU, as the entire 
    affected source or part of an affected source, shall be in compliance 
    with the provisions of this rule within 3 years from the date of such 
    notification.
        (iii) If a process unit is re-designated as an EPPU but does not 
    meet all the criteria of paragraph (a) of this section, the owner or 
    operator shall notify the Administrator within 6 months of making this 
    determination. This notification shall include documentation justifying 
    the EPPU's status as not being an affected source or not being part of 
    an affected source.
        (5) Once the primary product of a process unit has been determined 
    to be an elastomer product and it has been determined that all the 
    criteria of paragraph (a) of this section are met for the EPPU, the 
    owner or operator of the affected source shall comply with the 
    standards for the primary product. Owners or operators of flexible 
    operation units shall comply with the standards for the primary product 
    as specified in either paragraph (f)(5)(i) or (f)(5)(ii) of this 
    section, except as specified in paragraph (f)(5)(iii) of this section.
        (i) Each owner or operator shall determine the group status of each 
    emission point that is part of that flexible operation unit based on 
    emission point characteristics when the primary product is being 
    manufactured. Based on this finding, the owner or operator shall comply 
    with the applicable standards for the primary product for each emission 
    point, as appropriate, at all times, regardless of what product is 
    being produced.
        (ii) Alternatively, each owner or operator shall determine the 
    group status of each emission point that is part of the flexible 
    operation unit based on the emission point characteristics when each 
    product produced by the flexible operation unit is manufactured, 
    regardless of whether the product is an elastomer product or not. Based 
    on these findings, the owner or operator shall comply with the 
    applicable standards, as appropriate, regardless of what product is 
    being produced.
    
        Note: Under this scenario, it is possible that the group status, 
    and therefore the requirement to achieve emission reductions, for an 
    emission point may change depending on the product being 
    manufactured.]
    
        (iii) Whenever a flexible operation unit manufactures a product 
    that meets the criteria of paragraph (b) of this section (i.e., does 
    not use or produce any organic HAP), all activities associated with the 
    manufacture of the product, including the operation and monitoring of 
    control or recovery devices, shall be exempt from the requirements of 
    this rule.
        (6) The determination of the primary product for a process unit, to 
    include the determination of applicability of this subpart to process 
    units that are designed and operated as flexible operation units, shall 
    be reported in the Notification of Compliance Status required by 
    Sec. 63.506(e)(5) when the primary product is determined to be an 
    elastomer product. The Notification of Compliance Status shall include 
    the information specified in either paragraph (e)(6)(i) or (e)(6)(ii) 
    of this section. If the primary product is determined to be something 
    other than an elastomer product, the owner or operator shall retain 
    information, data, and analysis used to document the basis for the 
    determination that the primary product is not an elastomer product.
        (i) If the EPPU manufactures only one elastomer product, 
    identification of that elastomer product.
        (ii) If the EPPU is designed and operated as a flexible operation 
    unit, the information specified in paragraphs (f)(6)(ii)(A) through 
    (f)(6)(ii)(C) of this section, as appropriate.
        (A) Identification of the primary product.
        (B) Information concerning operating time and/or production mass 
    for each product that was used to make the determination of the primary 
    product under paragraph (f)(2)(i) or (f)(2)(ii) of this section.
        (C) Identification of which compliance option, either paragraph 
    (f)(5)(i) or (f)(5)(ii) of this section, has been selected by the owner 
    or operator.
        (7) To demonstrate compliance with the rule during those periods 
    when a flexible operation unit that is subject to this subpart is 
    producing a product other than an elastomer product or is producing an 
    elastomer product that is not the primary product, the owner or 
    operator shall comply with either paragraphs (f)(7)(i) and (f)(7)(ii) 
    or paragraph (f)(7)(iii) of this section.
        (i) Establish parameter monitoring levels as specified in 
    Sec. 63.505, for those emission points designated as Group 1, as 
    appropriate.
        (ii) Submit the parameter monitoring levels developed under 
    paragraph (f)(7)(i) of this section and the basis for them in the 
    Notification of Compliance Status report, as specified in 
    Sec. 63.506(e)(5).
        (iii) Demonstrate that the parameter monitoring levels established 
    for the primary product are also appropriate for those periods when 
    products other than the primary product are being produced. Material 
    demonstrating this finding shall be submitted in the Notification of 
    Compliance Status report as specified in Sec. 63.506(e)(5).
        (g) Storage vessel ownership determination. The owner or operator 
    shall follow the procedures specified in paragraphs (g)(1) through 
    (g)(8) of this section to determine to which process unit a storage 
    vessel shall belong.
        (1) If a storage vessel is already subject to another subpart of 40 
    CFR part 63 on September 5, 1996, that storage vessel shall belong to 
    the process unit subject to the other subpart.
        (2) If a storage vessel is dedicated to a single process unit, the 
    storage vessel shall belong to that process unit.
        (3) If a storage vessel is shared among process units, then the 
    storage vessel shall belong to that process unit located on the same 
    plant site as the storage vessel that has the greatest input into or 
    output from the storage vessel (i.e., the process unit has the 
    predominant use of the storage vessel).
        (4) If predominant use cannot be determined for a storage vessel 
    that is shared among process units and if only one of those process 
    units is an EPPU subject to this subpart, the storage vessel shall 
    belong to that EPPU.
        (5) If predominant use cannot be determined for a storage vessel 
    that is shared among process units and if more than one of the process 
    units are EPPUs that have different primary products and that are 
    subject to this subpart, then the owner or operator shall assign the 
    storage vessel to any one of the EPPUs sharing the storage vessel.
        (6) If the predominant use of a storage vessel varies from year to 
    year, then predominant use shall be determined based on the utilization 
    that occurred during the year preceding September 5, 1996 or based on 
    the expected
    
    [[Page 46927]]
    
    utilization for the 5 years following September 5, 1996 for existing 
    affected sources, whichever is more representative of the expected 
    operations for that storage vessel, and based on the expected 
    utilization for the 5 years after initial startup for new affected 
    sources. The determination of predominant use shall be reported in the 
    Notification of Compliance Status required by Sec. 63.506(e)(5)(vii). 
    If the predominant use changes, the redetermination of predominant use 
    shall be reported in the next Periodic Report.
        (7) If the storage vessel begins receiving material from (or 
    sending material to) another process unit; ceases to receive material 
    from (or send material to) a process unit; or if the applicability of 
    this subpart to a storage vessel has been determined according to the 
    provisions of paragraphs (g)(1) through (g)(6) of this section and 
    there is a significant change in the use of the storage vessel that 
    could reasonably change the predominant use, the owner or operator 
    shall reevaluate the applicability of this subpart to the storage 
    vessel.
        (8) Where a storage vessel is located at a major source that 
    includes one or more process units which place material into, or 
    receive materials from the storage vessel, but the storage vessel is 
    located in a tank farm, the applicability of this subpart shall be 
    determined according to the provisions in paragraphs (g)(8)(i) through 
    (g)(8)(iv) of this section.
        (i) The storage vessel may only be assigned to a process unit that 
    utilizes the storage vessel and does not have an intervening storage 
    vessel for that product (or raw materials, as appropriate). With 
    respect to any process unit, an intervening storage vessel means a 
    storage vessel connected by hard-piping to the process unit and to the 
    storage vessel in the tank farm so that product or raw material 
    entering or leaving the process unit flows into (or from) the 
    intervening storage vessel and does not flow directly into (or from) 
    the storage vessel in the tank farm.
        (ii) If there is no process unit at the major source that meets the 
    criteria of paragraph (g)(8)(i) of this section with respect to a 
    storage vessel, this subpart does not apply to the storage vessel.
        (iii) If there is only one process unit at the major source that 
    meets the criteria of paragraph (g)(8)(i) of this section with respect 
    to a storage vessel, the storage vessel shall be assigned to that 
    process unit. Applicability of this subpart to the storage vessel shall 
    then be determined according to the provisions of paragraph (a) of this 
    section.
        (iv) If there are two or more process units at the major source 
    that meet the criteria of paragraph (g)(8)(i) of this section with 
    respect to a storage vessel, the storage vessel shall be assigned to 
    one of those process units according to the provisions of paragraph 
    (g)(6) of this section. The predominant use shall be determined among 
    only those process units that meet the criteria of paragraph (g)(8)(i) 
    of this section.
        (h) Recovery operation equipment ownership determination. The owner 
    or operator shall follow the procedures specified in paragraphs (h)(1) 
    through (h)(7) of this section to determine to which process unit 
    recovery operation equipment shall belong.
        (1) If recovery operation equipment is already subject to another 
    subpart of 40 CFR part 63 on September 5, 1996, that recovery operation 
    equipment shall belong to the process unit subject to the other 
    subpart.
        (2) If recovery operation equipment is used exclusively by a single 
    process unit, the recovery operation shall belong to that process unit.
        (3) If recovery operation equipment is shared among process units, 
    then the recovery operation equipment shall belong to that process unit 
    located on the same plant site as the recovery operation equipment that 
    has the greatest input into or output from the recovery operation 
    equipment (i.e., that process unit has the predominant use of the 
    recovery operation equipment).
        (4) If predominant use cannot be determined for recovery operation 
    equipment that is shared among process units and if one of those 
    process units is an EPPU subject to this subpart, the recovery 
    operation equipment shall belong to the EPPU subject to this subpart.
        (5) If predominant use cannot be determined for recovery operation 
    equipment that is shared among process units and if more than one of 
    the process units are EPPUs that have different primary products and 
    that are subject to this subpart, then the owner or operator shall 
    assign the recovery operation equipment to any one of those EPPUs.
        (6) If the predominant use of recovery operation equipment varies 
    from year to year, then the predominant use shall be determined based 
    on the utilization that occurred during the year preceding September 5, 
    1996 or based on the expected utilization for the 5 years following 
    September 5, 1996 for existing affected sources, whichever is the more 
    representative of the expected operations for the recovery operations 
    equipment, and based on the expected utilization for the first 5 years 
    after initial startup for new affected sources. This determination 
    shall be reported in the Notification of Compliance Status required by 
    Sec. 63.506(e)(5)(viii). If the predominant use changes, the 
    redetermination of predominant use shall be reported in the next 
    Periodic Report.
        (7) If there is an unexpected change in the utilization of recovery 
    operation equipment that could reasonably change the predominant use, 
    the owner or operator shall redetermine to which process unit the 
    recovery operation belongs by reperforming the procedures specified in 
    paragraphs (h)(2) through (h)(6) of this section.
        (i) Changes or additions to plant sites. The provisions of 
    paragraphs (i)(1) through (i)(4) of this section apply to owners or 
    operators that change or add to their plant site or affected source. 
    Paragraph (i)(5) provides examples of what are and are not considered 
    process changes for purposes of paragraph (i) of this section.
        (1) Adding an EPPU to a plant site. The provisions of paragraphs 
    (i)(1)(i) through (i)(1)(ii) of this section apply to owners or 
    operators that add EPPUs to a plant site.
        (i) If an EPPU is added to a plant site, the addition shall be a 
    new affected source and shall be subject to the requirements for a new 
    affected source in this subpart upon initial startup or by September 5, 
    1996, whichever is later, if the addition meets the criteria specified 
    in paragraphs (i)(1)(i)(A) through (i)(1)(i)(B) and either (i)(1)(i)(C) 
    or (i)(1)(i)(D) of this section:
        (A) It is an addition that meets the definition of construction in 
    Sec. 63.2 of subpart A;
        (B) Such construction commenced after June 12, 1995; and
        (C) The addition has the potential to emit 10 tons per year or more 
    of any HAP or 25 tons per year or more of any combination of HAP, and 
    the primary product of the addition is currently produced at the plant 
    site as the primary product of an affected source; or
        (D) The primary product of the addition is not currently produced 
    at the plant site as the primary product of an affected source, and the 
    plant site meets, or after the addition is constructed will meet, the 
    definition of a major source in Sec. 63.2 of subpart A.
        (ii) If an EPPU is added to a plant site, the addition shall be 
    subject to the requirements for an existing affected source in this 
    subpart upon initial startup or by 3 years after September 5, 1996, 
    whichever is later, if the addition does not meet the criteria 
    specified in
    
    [[Page 46928]]
    
    paragraph (i)(1)(i) of this section and the plant site meets, or after 
    the addition is completed will meet, the definition of major source.
        (2) Adding emission points or making process changes to existing 
    affected sources. The provisions of paragraphs (i)(2)(i) through 
    (i)(2)(ii) of this section apply to owners or operators that add 
    emission points or make process changes to an existing affected source.
        (i) If any process change is made or emission point is added to an 
    existing affected source, or if a process change creating one or more 
    additional Group 1 emission point(s) is made to an existing affected 
    source, the entire affected source shall be a new affected source and 
    shall be subject to the requirements for a new affected source in this 
    subpart upon initial startup or by September 5, 1996, whichever is 
    later, if the process change or addition meets the criteria specified 
    in paragraphs (i)(2)(i)(A) through (i)(2)(i)(B) of this section:
        (A) It is a process change or addition that meets the definition of 
    reconstruction in Sec. 63.2 of subpart A; and
        (B) Such reconstruction commenced after June 12, 1995.
        (ii) If any process change is made or emission point is added to an 
    existing affected source, or if a process change creating one or more 
    additional Group 1 emission point(s) is made to an existing affected 
    source and the process change or addition does not meet the criteria 
    specified in paragraphs (i)(2)(i)(A) and (i)(2)(i)(B) of this section, 
    the resulting emission point(s) shall be subject to the requirements 
    for an existing affected source in this subpart. The resulting emission 
    point(s) shall be in compliance upon initial startup or by 3 years 
    after September 5, 1996, whichever is later, unless the owner or 
    operator demonstrates to the Administrator that achieving compliance 
    will take longer than making the process change or addition. If this 
    demonstration is made to the Administrator's satisfaction, the owner or 
    operator shall follow the procedures in paragraphs (i)(2)(iii)(A) 
    through (i)(2)(iii)(C) of this section to establish a compliance date.
        (iii) To establish a compliance date for an emission point or 
    points specified in paragraph (i)(2)(ii) of this section, the 
    procedures specified in paragraphs (i)(2)(iii)(A) through 
    (i)(2)(iii)(C) of this section shall be followed.
        (A) The owner or operator shall submit to the Administrator for 
    approval a compliance schedule, along with a justification for the 
    schedule.
        (B) The compliance schedule shall be submitted within 180 days 
    after the process change or addition is made or the information 
    regarding the change or addition is known to the owner or operator, 
    unless the compliance schedule has been previously submitted to the 
    permitting authority. The compliance schedule may be submitted in the 
    next Periodic Report if the process change or addition is made after 
    the date the Notification of Compliance Status report is due.
        (C) The Administrator shall approve the compliance schedule or 
    request changes within 120 calendar days of receipt of the compliance 
    schedule and justification.
        (3) Existing source requirements for Group 2 emission points that 
    become Group 1 emission points. If a process change or addition that 
    does not meet the criteria in paragraph (i)(1) or (i)(2) of this 
    section is made to an existing plant site or existing affected source, 
    and the change causes a Group 2 emission point to become a Group 1 
    emission point, for that emission point the owner or operator shall 
    comply with the requirements of this subpart for existing Group 1 
    emission points. Compliance shall be achieved as expeditiously as 
    practicable, but in no event later than 3 years after the emission 
    point becomes a Group 1 emission point.
        (4) Existing source requirements for some emission points that 
    become subject to subpart H requirements. If a surge control vessel or 
    bottoms receiver becomes subject to Sec. 63.170 of subpart H, or if a 
    compressor becomes subject to Sec. 63.164 of subpart H, the owner or 
    operator shall be in compliance upon initial startup or by 3 years 
    after September 5, 1996, whichever is later, unless the owner or 
    operator demonstrates to the Administrator that achieving compliance 
    will take longer than making the change. If this demonstration is made 
    to the Administrator's satisfaction, the owner or operator shall follow 
    the procedures in paragraphs (i)(2)(iii)(A) through (i)(2)(iii)(C) of 
    this section to establish a compliance date.
        (5) Determining what are and are not process changes. For purposes 
    of paragraph (i) of this section, examples of process changes include, 
    but are not limited to, changes in production capacity, feedstock type, 
    or catalyst type, or whenever there is a replacement, removal, or 
    addition of recovery equipment. For purposes of paragraph (i) of this 
    section, process changes do not include: Process upsets, unintentional 
    temporary process changes, and changes that are within the equipment 
    configuration and operating conditions documented in the Notification 
    of Compliance Status report required by Sec. 63.506(e)(5).
        (j) Applicability of this subpart except during periods of startup, 
    shutdown, and malfunction. Each provision set forth in this subpart or 
    referred to in this subpart shall apply at all times except during 
    periods of startup, shutdown, and malfunction if the startup, shutdown, 
    or malfunction precludes the ability of a particular emission point at 
    an affected source to comply with one or more specific provisions to 
    which it is subject.
    
    
    Sec. 63.481  Compliance schedule and relationship to existing 
    applicable rules.
    
        (a) Affected sources are required to achieve compliance on or 
    before the dates specified in paragraphs (b) through (d) of this 
    section. Paragraph (e) of this section provides information on 
    requesting compliance extensions. Paragraphs (f) through (i) of this 
    section discuss the relationship of this subpart to subpart A and to 
    other applicable rules. Where an override of another authority of the 
    Act is indicated in this subpart, only compliance with the provisions 
    of this subpart is required. Paragraph (j) of this section specifies 
    the meaning of time periods.
        (b) New affected sources that commence construction or 
    reconstruction after June 12, 1995 shall be in compliance with this 
    subpart upon initial startup or September 5, 1996, whichever is later, 
    as provided in Sec. 63.6(b) of subpart A.
        (c) Existing affected sources shall be in compliance with this 
    subpart (except for Sec. 63.502 for which compliance is covered by 
    paragraph (d) of this section) no later than 3 years after September 5, 
    1996, as provided in Sec. 63.6(c) of subpart A, unless an extension has 
    been granted as specified in paragraph (e) of this section.
        (d) Except as provided for in paragraphs (d)(1) through (d)(4) of 
    this section, existing affected sources shall be in compliance with 
    Sec. 63.502 no later than March 5, 1997 unless a request for a 
    compliance extension is granted pursuant to section 112(i)(3)(B) of the 
    Act, as discussed in Sec. 63.182(a)(6) of subpart H.
        (1) Compliance with the compressor provisions of Sec. 63.164 of 
    subpart H shall occur no later than September 5, 1997 for any 
    compressor meeting one or more of the criteria in paragraphs (d)(1)(i) 
    through (d)(1)(iii) of this section, if the work can be accomplished 
    without a process unit shutdown, as defined in Sec. 63.161 of subpart 
    H.
        (i) The seal system will be replaced;
    
    [[Page 46929]]
    
        (ii) A barrier fluid system will be installed; or
        (iii) A new barrier fluid will be utilized which requires changes 
    to the existing barrier fluid system.
        (2) Compliance with the compressor provisions of Sec. 63.164 of 
    subpart H shall occur no later than March 5, 1998, for any compressor 
    meeting all the criteria in paragraphs (d)(2)(i) through (d)(2)(iv) of 
    this section.
        (i) The compressor meets one or more of the criteria specified in 
    paragraphs (d)(1)(i) through (d)(1)(iii) of this section;
        (ii) The work can be accomplished without a process unit shutdown 
    as defined in Sec. 63.161 of subpart H;
        (iii) The additional time is actually necessary, due to the 
    unavailability of parts beyond the control of the owner or operator; 
    and
        (iv) The owner or operator submits the request for a compliance 
    extension to the U.S. Environmental Protection Agency (EPA) Regional 
    Office at the addresses listed in Sec. 63.13 of subpart A no later than 
    45 days before March 5, 1997. The request for a compliance extension 
    shall contain the information specified in Sec. 63.6(i)(6)(i)(A), (B), 
    and (D) of subpart A. Unless the EPA Regional Office objects to the 
    request for a compliance extension within 30 calendar days after 
    receipt of the request, the request shall be deemed approved.
        (3) If compliance with the compressor provisions of Sec. 63.164 of 
    subpart H cannot reasonably be achieved without a process unit 
    shutdown, as defined in Sec. 63.161 of subpart H, the owner or operator 
    shall achieve compliance no later than September 8, 1998. The owner or 
    operator who elects to use this provision shall submit a request for an 
    extension of compliance in accordance with the requirements of 
    paragraph (d)(2)(iv) of this section.
        (4) Compliance with the compressor provisions of Sec. 63.164 of 
    subpart H shall occur not later than September 6, 1999 for any 
    compressor meeting one or more of the criteria in paragraphs (d)(4)(i) 
    through (d)(4)(iii) of this section. The owner or operator who elects 
    to use these provisions shall submit a request for an extension of 
    compliance in accordance with the requirements of paragraph (d)(2)(iv) 
    of this section.
        (i) Compliance cannot be achieved without replacing the compressor;
        (ii) Compliance cannot be achieved without recasting the distance 
    piece; or
        (iii) Design modifications are required to connect to a closed-vent 
    or recovery system.
        (5) Compliance with the surge control vessel and bottoms receiver 
    provisions of Sec. 63.170 of subpart H shall occur no later than 
    September 6, 1999.
        (e) Pursuant to section 112(i)(3)(B) of the Act, an owner or 
    operator may request an extension allowing the existing source up to 1 
    additional year to comply with section 112(d) standards. For purposes 
    of this subpart, a request for an extension shall be submitted to the 
    operating permit authority as part of the operating permit application 
    or to the Administrator as a separate submittal or as part of the 
    Precompliance Report. Requests for extensions shall be submitted no 
    later than the date on which the Precompliance Report is required to be 
    submitted in Sec. 63.506(e)(3)(i). The dates specified in Sec. 63.6(i) 
    of subpart A for submittal of requests for extensions shall not apply 
    to this subpart.
        (1) A request for an extension of compliance shall include the data 
    described in Sec. 63.6(i)(6)(i) (A), (B), and (D) of subpart A.
        (2) The requirements in Sec. 63.6(i)(8) through Sec. 63.6(i)(14) of 
    subpart A shall govern the review and approval of requests for 
    extensions of compliance with this subpart.
        (f) Table 1 of this subpart specifies the provisions of subpart A 
    that apply and those that do not apply to owners and operators of 
    affected sources subject to this subpart. For the purposes of this 
    subpart, Table 3 of subpart F is not applicable.
        (g) Table 2 of this subpart summarizes the provisions of subparts 
    F, G, and H that apply and those that do not apply to owners and 
    operators of affected sources subject to this subpart.
        (h)(1) After the compliance dates specified in this section, an 
    affected source subject to this subpart that is also subject to the 
    provisions of 40 CFR part 63, subpart I, is required to comply only 
    with the provisions of this subpart.
        (2) Sources subject to 40 CFR part 63, subpart I that have elected 
    to comply through a quality improvement program, as specified in 
    Sec. 63.175 or Sec. 63.176 or both of subpart H, may elect to continue 
    these programs without interruption as a means of complying with this 
    subpart. In other words, becoming subject to this subpart does not 
    restart or reset the ``compliance clock'' as it relates to reduced 
    burden earned through a quality improvement program.
        (i) After the compliance dates specified in this section, a storage 
    vessel that belongs to an affected source subject to this subpart that 
    is also subject to the provisions of 40 CFR part 60, subpart Kb is 
    required to comply only with the provisions of this subpart. After the 
    compliance dates specified in paragraph (d) of this section, that 
    storage vessel shall no longer be subject to 40 CFR part 60, subpart 
    Kb.
        (j) All terms in this subpart that define a period of time for 
    completion of required tasks (e.g., monthly, quarterly, annual), unless 
    specified otherwise in the section or subsection that imposes the 
    requirement, refer to the standard calendar periods.
        (1) Notwithstanding time periods specified in this subpart for 
    completion of required tasks, such time periods may be changed by 
    mutual agreement between the owner or operator and the Administrator, 
    as specified in subpart A of this part (e.g., a period could begin on 
    the compliance date or another date, rather than on the first day of 
    the standard calendar period). For each time period that is changed by 
    agreement, the revised period shall remain in effect until it is 
    changed. A new request is not necessary for each recurring period.
        (2) Where the period specified for compliance is a standard 
    calendar period, if the initial compliance date occurs after the 
    beginning of the period, compliance shall be required according to the 
    schedule specified in paragraphs (j)(2)(i) or (j)(2)(ii) of this 
    section, as appropriate.
        (i) Compliance shall be required before the end of the standard 
    calendar period within which the compliance deadline occurs, if there 
    remain at least 2 weeks for tasks that must be performed monthly, at 
    least 1 month for tasks that must be performed each quarter, or at 
    least 3 months for tasks that must be performed annually; or
        (ii) In all other cases, compliance shall be required before the 
    end of the first full standard calendar period after the period within 
    which the initial compliance deadline occurs.
        (3) In all instances where a provision of this subpart requires 
    completion of a task during each multiple successive period, an owner 
    or operator may perform the required task at any time during the 
    specified period, provided that the task is conducted at a reasonable 
    interval after completion of the task during the previous period.
    
    
    Sec. 63.482  Definitions.
    
        (a) The following terms used in this subpart shall have the meaning 
    given them in subparts A (Sec. 63.2), F (Sec. 63.101), G (Sec. 63.111), 
    and H (Sec. 63.161) as specified after each term:
    
    Act (subpart A)
    Administrator (subpart A)
    Automated monitoring and recording system (subpart G)
    Average concentration (subpart G)
    Boiler (subpart G)
    Bottoms receiver (subpart H)
    
    [[Page 46930]]
    
    By compound (subpart G)
    By-product (subpart F)
    Car-seal (subpart G)
    Chemical manufacturing process unit (subpart F)
    Closed-vent system (subpart G)
    Co-product (subpart F)
    Combustion device (subpart G)
    Commenced (subpart A)
    Compliance date (subpart A)
    Compliance schedule (subpart A)
    Connector (subpart H)
    Construction (subpart A)
    Continuous monitoring system (subpart A)
    Continuous record (subpart G)
    Continuous recorder (subpart G)
    Cover (subpart G)
    Distillation unit (subpart G)
    Emission standard (subpart A)
    Emissions averaging (subpart A)
    EPA (subpart A)
    Equipment (subpart H)
    Equipment leak (subpart F)
    Existing source (subpart A)
    External floating roof (subpart G)
    Fill (subpart G)
    Fixed roof (subpart G)
    Flame zone (subpart G)
    Flexible operation unit (subpart F)
    Floating roof (subpart G)
    Flow indicator (subpart G)
    Halogens and hydrogen halides (subpart G)
    Hazardous air pollutant (subpart A)
    Heat exchange system (subpart F)
    Impurity (subpart F)
    Incinerator (subpart G)
    In organic hazardous air pollutant service (subpart H)
    Instrumentation system (subpart H)
    Internal floating roof (subpart G)
    Lesser quantity (subpart A)
    Maintenance wastewater (subpart F)
    Major source (subpart A)
    Malfunction (subpart A)
    Mass flow rate (subpart G)
    Maximum true vapor pressure (subpart G)
    New source (subpart A)
    Open-ended valve or line (subpart H)
    Operating permit (subpart F)
    Organic HAP service (subpart H)
    Organic monitoring device (subpart G)
    Owner or operator (subpart A)
    Performance evaluation (subpart A)
    Performance test (subpart A)
    Permitting authority (subpart A)
    Plant site (subpart F)
    Point of generation (subpart G)
    Potential to emit (subpart A)
    Primary fuel (subpart G)
    Process heater (subpart G)
    Process unit shutdown (subpart H)
    Process wastewater (subpart F)
    Process wastewater stream (subpart G)
    Product separator (subpart F)
    Reactor (subpart G)
    Reconstruction (subpart A)
    Recovery device (subpart G)
    Reference control technology for process vents (subpart G)
    Reference control technology for storage vessels (subpart G)
    Reference control technology for wastewater (subpart G)
    Relief valve (subpart G)
    Research and development facility (subpart F)
    Residual (subpart G)
    Run (subpart A)
    Secondary fuel (subpart G)
    Sensor (subpart H)
    Shutdown (subpart A)
    Specific gravity monitoring device (subpart G)
    Startup (subpart A)
    Startup, shutdown, and malfunction plan (subpart F)
    State (subpart A)
    Surge control vessel (subpart H)
    Temperature monitoring device (subpart G)
    Test method (subpart A)
    Total resource effectiveness index value (subpart G)
    Treatment process (subpart G)
    Unit operation (subpart F)
    Vent stream (subpart G)
    Visible emission (subpart A)
    Waste management unit (subpart G)
    Wastewater (subpart F)
    Wastewater stream (subpart G)
        (b) All other terms used in this subpart shall have the meaning 
    given them in this section. If a term is defined in a subpart 
    referenced above and in this section, it shall have the meaning given 
    in this section for purposes of this subpart.
        Affected source is defined in Sec. 63.480(a).
        Aggregate batch vent stream means a gaseous emission stream 
    containing only the exhausts from two or more batch front-end process 
    vents that are ducted together before being routed to a control device 
    that is in continuous operation.
        Average flow rate, as used in conjunction with wastewater 
    provisions, is defined in and determined by the specifications in 
    Sec. 63.144(c) of subpart G; or, as used in conjunction with the batch 
    front-end process vent provisions, is defined in and determined by the 
    specifications in Sec. 63.488(e).
        Back-end refers to the unit operations in an EPPU following the 
    stripping operations. Back-end process operations include, but are not 
    limited to, filtering, coagulation, blending, concentration, drying, 
    separating, and other finishing operations, as well as latex and crumb 
    storage.
        Batch cycle means the operational step or steps, from start to 
    finish, that occur as part of a batch unit operation.
        Batch cycle limitation means an enforceable restriction on the 
    number of batch cycles that can be performed in a year for an 
    individual batch front-end process vent.
        Batch emission episode means a discrete emission venting episode 
    associated with a single batch unit operation. Multiple batch emission 
    episodes may occur from a single batch unit operation.
        Batch front-end process vent means a point of emission from a batch 
    unit operation having a gaseous emission stream with annual organic HAP 
    emissions greater than 225 kilograms per year and located in the front-
    end of a process unit. Batch front-end process vents exclude relief 
    valve discharges and leaks from equipment regulated under Sec. 63.502.
        Batch process means a discontinuous process involving the bulk 
    movement of material through sequential manufacturing steps. Mass, 
    temperature, concentration, and other properties of the process vary 
    with time. Addition of raw material and withdrawal of product do not 
    typically occur simultaneously in a batch process. For the purposes of 
    this subpart, a process producing polymers is characterized as 
    continuous or batch based on the operation of the polymerization 
    reactors.
        Batch unit operation means a unit operation operated in a batch 
    process mode.
        Butyl rubber means a copolymer of isobutylene and other monomers. 
    Typical other monomers include isoprene and methylstyrenes. A typical 
    composition of butyl rubber is approximately 85 to 99 percent 
    isobutylene and one to fifteen percent other monomers. Most butyl 
    rubber is produced by precipitation polymerization, although other 
    methods may be used.
        Compounding unit means a unit of operation which blends, melts, and 
    resolidifies solid polymers for the purpose of incorporating additives, 
    colorants, or stabilizers into the final elastomer product. A unit 
    operation whose primary purpose is to remove residual monomers from 
    polymers is not a compounding unit.
        Continuous front-end process vent means a point of emission from a 
    continuous process unit operation within an affected source having a 
    gaseous emission stream with a flow rate greater than or equal to 0.005 
    standard cubic meter per minute and with a total organic HAP 
    concentration greater than or equal to 50 parts per million by volume. 
    Continuous front-end process vents exclude relief valve
    
    [[Page 46931]]
    
    discharges and leaks from equipment regulated under Sec. 63.502.
        Continuous process means a process where the inputs and outputs 
    flow continuously through sequential manufacturing steps throughout the 
    duration of the process. Continuous processes typically approach 
    steady-state conditions. Continuous processes typically involve the 
    simultaneous addition of raw material and withdrawal of product. For 
    the purposes of this subpart, a process producing polymers is 
    characterized as continuous or batch based on the operation of the 
    polymerization reactors.
        Continuous unit operation means a unit operation operated in a 
    continuous process mode.
        Control device is defined in Sec. 63.111 of subpart G, except that 
    the term ``process vent'' shall be replaced with the term ``continuous 
    front-end process vent'' for the purpose of this subpart.
        Crumb rubber dry weight means the weight of the polymer, minus the 
    weight of water and residual organics.
        Drawing unit means a unit operation which converts polymer into a 
    different shape by melting or mixing the polymer and then pulling it 
    through an orifice to create a continuously extruded product.
        Elastomer means any polymer having a glass transition temperature 
    lower than -10 deg.C, or a glass transition temperature between 
    -10 deg.C and 25 deg.C that is capable of undergoing deformation 
    (stretching) of several hundred percent and recovering essentially when 
    the stress is removed. For the purposes of this subpart, resins are not 
    considered to be elastomers.
        Elastomer product means one of the following 12 types of products, 
    as they are defined in this section:
        (1) Butyl Rubber,
        (2) Halobutyl Rubber,
        (3) Epichlorohydrin Elastomers,
        (4) Ethylene Propylene Rubber,
        (5) HypalonTM,
        (6) Neoprene,
        (7) Nitrile Butadiene Rubber,
        (8) Nitrile Butadiene Latex,
        (9) Polybutadiene Rubber/Styrene Butadiene Rubber by Solution,
        (10) Polysulfide Rubber,
        (11) Styrene Butadiene Rubber by Emulsion, and
        (12) Styrene Butadiene Latex.
        Elastomer product process unit (EPPU) means a collection of 
    equipment assembled and connected by pipes or ducts used to process raw 
    materials and to manufacture an elastomer product as its primary 
    product. This collection of equipment includes process vents; storage 
    vessels, as determined in Sec. 63.480(g); and the equipment (i.e., 
    pumps, compressors, agitators, pressure relief devices, sampling 
    connection systems, open-ended valves or lines, valves, connectors, 
    instrumentation systems, surge control vessels, and bottoms receivers 
    that are associated with the elastomer product process unit) that are 
    subject to the equipment leak provisions as specified in Sec. 63.502. 
    Compounding units, spinning units, drawing units, extruding units, and 
    other finishing steps are not part of an EPPU. In addition, a solid 
    state polymerization unit is not part of an EPPU.
        Elastomer type means one of the elastomers defined under 
    ``elastomer product'' in this section. Each elastomer identified in 
    that definition represents a different elastomer type.
        Emission point means an individual continuous front-end process 
    vent, batch front-end process vent, back-end process vent, storage 
    vessel, wastewater stream, or equipment leak.
        Emulsion process means a process carried out with the reactants in 
    an emulsified form (e.g., polymerization reaction).
        Epichlorohydrin elastomer means an elastomer formed from the 
    polymerization or copolymerization of epichlorohydrin (EPI). The main 
    epichlorohydrin elastomers are polyepichlorohydrin, epi-ethylene oxide 
    (EO) copolymer, epi-allyl glycidyl ether (AGE) copolymer, and epi-EO-
    AGE terpolymer. Epoxy resins produced by the copolymerization of EPI 
    and bisphenol A are not epichlorohydrin elastomers.
        Ethylene-propylene rubber means an ethylene-propylene copolymer or 
    an ethylene-propylene terpolymer. Ethylene-propylene copolymers (EPM) 
    result from the polymerization of ethylene and propylene and contain a 
    saturated chain of the polymethylene type. Ethylene-propylene 
    terpolymers (EPDM) are produced in a similar manner as EPM, except that 
    a moderate amount of the third monomer is added to the reaction 
    sequence. Typical third monomers include ethylidene norbornene, 1,4-
    hexadiene, or dicyclopentadiene. Ethylidene norbornene is the most 
    commonly used. The production process includes, but is not limited to, 
    polymerization, recycle, recovery, and packaging operations. The 
    polymerization reaction may occur in either a solution process or a 
    suspension process.
        Extruding unit means a unit operation which converts polymer into a 
    different shape by melting or mixing the polymer and then forcing it 
    through an orifice to create a continuously extruded product.
        Front-end refers to the unit operations in an EPPU prior to, and 
    including, the stripping operations. The process front-end includes all 
    activity from raw material storage through the stripping operation, 
    including pre-polymerization blending, reactions, etc. For all gas-
    phased reaction processes, all unit operations are considered to be 
    front-end.
        Gas-phased reaction process means an elastomer production process 
    where the reaction occurs in a gas phase, fluidized bed.
        Grade means the subdivision of an elastomer product type by 
    different characteristics such as molecular weight, monomer 
    composition, significant mooney values, and the presence or absence of 
    extender oil and/or carbon black.
        Group 1 batch front-end process vent means a batch front-end 
    process vent releasing annual organic HAP emissions greater than or 
    equal to 11,800 kg/yr and with a cutoff flow rate, calculated in 
    accordance with Sec. 63.488(f), greater than or equal to the annual 
    average flow rate.
        Group 2 batch front-end process vent means a batch front-end 
    process vent that does not fall within the definition of a Group 1 
    batch front-end process vent.
        Group 1 continuous front-end process vent means a continuous front-
    end process vent releasing a gaseous emission stream that has a total 
    resource effectiveness index value, calculated according to Sec. 63.115 
    of subpart G, less than or equal to 1.0.
        Group 2 continuous front-end process vent means a continuous front-
    end process vent that does not fall within the definition of a Group 1 
    continuous front-end process vent.
        Group 1 storage vessel means a storage vessel at an existing 
    affected source that meets the applicability criteria specified in 
    Table 3 of this subpart, or a storage vessel at a new affected source 
    that meets the applicability criteria specified in Table 4 of this 
    subpart.
        Group 2 storage vessel means a storage vessel that does not fall 
    within the definition of a Group 1 storage vessel.
        Group 1 wastewater stream means a process wastewater stream from an 
    elastomer product process unit at an existing or new source with a 
    total volatile organic hazardous air pollutant average concentration 
    greater than or equal to 10,000 parts per million by weight of 
    compounds listed in table 9 of subpart G at any flowrate; or a process 
    wastewater stream from a process unit at an existing or new source that 
    has an average flow rate greater than or equal to 10 liters per minute 
    and a total volatile organic hazardous air pollutant
    
    [[Page 46932]]
    
    concentration greater than 1,000 parts per million by weight of 
    compounds listed in table 9 of subpart G.
        Group 2 wastewater stream means any process wastewater stream that 
    does not meet the definition of a Group 1 wastewater stream.
        Halobutyl rubber means a butyl rubber elastomer produced using 
    halogenated copolymers.
        Halogenated aggregate batch vent stream means an aggregate batch 
    vent stream determined to have a total mass emission rate of halogen 
    atoms contained in organic compounds of 3,750 kg/yr or greater 
    determined by the Procedures presented in Sec. 63.488(h).
        Halogenated batch front-end process vent means a batch front-end 
    process vent determined to have a mass emission rate of halogen atoms 
    contained in organic compounds of 3,750 kg/yr or greater determined by 
    the procedures presented in Sec. 63.488(h).
        Halogenated continuous front-end process vent means a continuous 
    front-end process vent determined to have a mass emission rate of 
    halogen atoms contained in organic compounds of 0.45 kg/hr or greater 
    determined by the procedures presented in Sec. 63.115(d)(2)(v) of 
    subpart G.
        High conversion latex means a latex where all monomers are reacted 
    to at least 95 percent conversion.
        Hypalon TM means a chlorosulfonated polyethylene that is a 
    synthetic rubber produced for uses such as wire and cable insulation, 
    shoe soles and heels, automotive components, and building products.
        Latex means a colloidal aqueous emulsion of elastomer. A latex may 
    be further processed into finished products by direct use as a coating 
    or as a foam, or it may be precipitated to separate the rubber 
    particles, which are then used in dry state to prepare finished 
    products.
        Latex weight includes the weight of the polymer and the weight of 
    the water solution.
        Mass process means a process carried out through the use of thermal 
    energy (e.g., polymerization reaction). Mass processes do not utilize 
    emulsifying or suspending agents, but can utilize catalysts or other 
    additives.
        Material recovery section means the equipment that recovers 
    unreacted or by-product materials from any process section for return 
    to the EPPU, off-site purification or treatment, or sale. Equipment 
    designed to separate unreacted or by-product material from the polymer 
    product is to be included in this process section, provided that at the 
    time of initial compliance some of the material is recovered for reuse 
    in the process, off-site purification or treatment, or sale. Otherwise, 
    such equipment is to be assigned to one of the other process sections, 
    as appropriate. If equipment is used to recover unreacted or by-product 
    material and return it directly to the same piece of process equipment 
    from which it was emitted, then the recovery equipment is considered to 
    be part of the process section that contains the process equipment. On 
    the other hand, if equipment is used to recover unreacted or by-product 
    material and return it to a different piece of process equipment in the 
    same process section, the recovery equipment is considered to be part 
    of a material recovery section. Equipment that treats recovered 
    materials is to be included in this process section, but equipment that 
    also treats raw materials is not to be included in this process 
    section. The latter equipment is to be included in the raw materials 
    preparation section.
        Month means either a calendar month or a repeating 30-day period. 
    For the purposes of compliance with the back-end limitations in 
    Sec. 63.506, a month can begin on any day of the month (i.e., starting 
    on the 15th and ending on the 14th of the following month), 
    as long as the month never contains more than 31 calendar days.
        Neoprene means a polymer of chloroprene (2-chloro-1,3-butadiene). 
    The free radical emulsion process is generally used to produce 
    neoprene, although other methods may be used.
        Nitrile butadiene latex means a polymer consisting primarily of 
    unsaturated nitriles and dienes, usually acrylonitrile and 1,3-
    butadiene, that is sold as a latex.
        Nitrile butadiene rubber means a polymer consisting primarily of 
    unsaturated nitriles and dienes, usually acrylonitrile and 1,3-
    butadiene, not including those facilities that produce nitrile 
    butadiene latex.
        Organic hazardous air pollutant(s) (organic HAP) means one or more 
    of the chemicals listed in Table 5 of this subpart or any other 
    chemical which:
        (1) Is knowingly introduced into the manufacturing process other 
    than as an impurity, or has been or will be reported under any Federal 
    or State program, such as EPCRA section 311, 312, or 313 or Title V; 
    and
        (2) Is listed in Table 2 of subpart F of this part.
        Polybutadiene rubber/styrene butadiene rubber by solution means a 
    polymer of 1,3-butadiene produced using a solution process, and/or a 
    polymer that consists primarily of styrene and butadiene monomer units 
    and is produced using a solution process.
        Polymerization reaction section means the equipment designed to 
    cause monomer(s) to react to form polymers, including equipment 
    designed primarily to cause the formation of short polymer chains 
    (e.g., oligomers or low polymers), but not including equipment designed 
    to prepare raw materials for polymerization (e.g., esterification 
    vessels). For the purposes of this subpart, the polymerization reaction 
    section begins with the equipment used to transfer the materials from 
    the raw materials preparation section and ends with the last vessel in 
    which polymerization occurs.
        Polysulfide rubber means a polymer produced by reacting sodium 
    polysulfide and chloroethyl formal. Polysulfide rubber may be produced 
    as latexes or solid product.
        Primary product is defined in and determined by the procedures 
    specified in Sec. 63.480(f).
        Process section means the equipment designed to accomplish a 
    general but well-defined task in polymers production. Process sections 
    include raw materials preparation, polymerization reaction, and 
    material recovery. A process section may be dedicated to a single EPPU 
    or may be common to more than one EPPU.
        Process unit means a collection of equipment assembled and 
    connected by pipes or ducts to process raw materials and to manufacture 
    a product.
        Process vent means a point of emission from a unit operation having 
    a gaseous emission stream. Typical process vents include condenser 
    vents, dryer vents, vacuum pumps, steam ejectors, and atmospheric vents 
    from reactors and other process vessels, but do not include pressure 
    relief valves.
        Product means a compound or material which is manufactured by a 
    process unit. By-products, isolated intermediates, impurities, wastes, 
    and trace contaminants are not considered products.
        Raw materials preparation section means the equipment at a polymer 
    manufacturing plant designed to prepare raw materials, such as monomers 
    and solvents, for polymerization. For the purposes of this standard, 
    this process section begins with the equipment used to transfer raw 
    materials from storage and/or the equipment used to transfer recovered 
    material from the material recovery process sections, and ends with the 
    last piece of equipment that prepares the material for polymerization. 
    The raw materials preparation section may include equipment that is 
    used to purify, dry, or otherwise treat raw materials or raw and 
    recovered
    
    [[Page 46933]]
    
    materials together; to activate catalysts; and to promote 
    esterification including the formation of some short polymer chains 
    (oligomers). The raw materials preparation section does not include 
    equipment that is designed primarily to accomplish the formation of 
    oligomers, the treatment of recovered materials alone, or the storage 
    of raw materials.
        Recovery operations equipment means the equipment used to separate 
    the components of process streams. Recovery operations equipment 
    includes distillation units, condensers, etc. Equipment used for 
    wastewater treatment shall not be considered recovery operations 
    equipment.
        Resin means a polymer that is not an elastomer. The following are 
    characteristics of resins and the production of resins:
        (1) The polymer is a block polymer;
        (2) The manufactured polymer does not require vulcanization to make 
    useful products;
        (3) The polymer production process is operated to achieve at least 
    99 percent monomer conversion; and
        (4) The polymer process unit does not recycle unreacted monomer 
    back to the process.
        Solid state polymerization unit means a unit operation which, 
    through the application of heat, furthers the polymerization (i.e., 
    increases the intrinsic viscosity) of polymer chips.
        Solution process means a process where both the monomers and the 
    resulting polymers are dissolved in an organic solvent.
        Steady-state conditions means that all variables (temperatures, 
    pressures, volumes, flow rates, etc.) in a process do not vary 
    significantly with time; minor fluctuations about constant mean values 
    can occur.
        Storage vessel means a tank or other vessel that is used to store 
    liquids that contain one or more organic HAP and that has been 
    assigned, according to the procedures in Sec. 63.480(g), to an EPPU 
    that is subject to this subpart. Storage vessels do not include:
        (1) Vessels permanently attached to motor vehicles such as trucks, 
    railcars, barges, or ships;
        (2) Pressure vessels designed to operate in excess of 204.9 
    kilopascals and without emissions to the atmosphere;
        (3) Vessels with capacities smaller than 38 cubic meters;
        (4) Vessels and equipment storing and/or handling material that 
    contains no organic HAP, or organic HAP as impurities only;
        (5) Surge control vessels and bottoms receiver tanks; and
        (6) Wastewater storage tanks.
        Stripping technology means the removal of organic compounds from a 
    raw elastomer product by the use of heat and/or vacuum. Stripping 
    technology includes steam stripping, direct volatilization, chemical 
    stripping, and other methods of devolatilization.
        Styrene butadiene latex means a polymer consisting primarily of 
    styrene and butadiene monomer units produced using an emulsion process 
    and sold as a latex.
        Styrene butadiene rubber by emulsion means a polymer consisting 
    primarily of styrene and butadiene monomer units produced using an 
    emulsion process. Styrene butadiene rubber by emulsion does not include 
    styrene butadiene latex.
        Suspension process means a process carried out with the reactants 
    in a state of suspension, typically achieved through the use of water 
    and/or suspending agents (e.g., polymerization reaction).
        Total organic compounds (TOC) means those compounds, excluding 
    methane and ethane, measured according to the procedures of Method 18 
    or Method 25A of 40 CFR part 60, appendix A.
        Year means any consecutive 12-month period or 365 rolling days. For 
    the purposes of emissions averaging, the term year applies to any 12-
    month period selected by the facility and defined in its Emissions 
    Averaging Plan. For the purposes of batch cycle limitations, the term 
    year applies to the 12-month period defined by the facility in its 
    Notification of Compliance Status.
    
    
    Sec. 63.483  Emission standards.
    
        (a) Except as allowed under paragraphs (b) and (c) of this section, 
    the owner or operator of an existing or new affected source shall 
    comply with the provisions in:
        (1) Section 63.484 for storage vessels;
        (2) Section 63.485 for continuous front-end process vents;
        (3) Sections 63.486 through 63.492 for batch front-end process 
    vents;
        (4) Sections 63.493 through 63.500 for back-end process operations;
        (5) Section 63.501 for wastewater;
        (6) Section 63.502 for equipment leaks;
        (7) Section 63.504 for additional test methods and procedures;
        (8) Section 63.505 for monitoring levels and excursions; and
        (9) Section 63.506 for general reporting and recordkeeping 
    requirements.
        (b) Instead of complying with Secs. 63.484, 63.485, 63.493, and 
    63.501, the owner or operator of an existing affected source may elect 
    to control any or all of the storage vessels, continuous front-end 
    process vents, batch front-end process vents, aggregate batch vent 
    streams, and back-end process emissions within the affected source, 
    plus any or all process wastewater streams associated with the affected 
    source, to different levels using an emissions averaging compliance 
    approach that uses the procedures specified in Sec. 63.503. An owner or 
    operator electing to use emissions averaging must still comply with the 
    provisions of Secs. 63.484, 63.485, 63.486, 63.493, and 63.501 for 
    affected source emission points not included in the emissions average.
        (c) A State may decide not to allow the use of the emissions 
    averaging compliance approach specified in paragraph (b) of this 
    section as a compliance option for an existing affected source.
    
    
    Sec. 63.484  Storage vessel provisions.
    
        (a) For each storage vessel located at an affected source, except 
    for those storage vessels exempted by paragraph (b) of this section, 
    the owner or operator shall comply with the requirements of 
    Secs. 63.119 through 63.123 and Sec. 63.148 of subpart G, with the 
    differences noted in paragraphs (c) through (q) of this section.
        (b) Storage vessels described in paragraphs (b)(1) through (b)(7) 
    of this section are exempt from the storage vessel requirements of this 
    section.
        (1) Storage vessels containing styrene-butadiene latex;
        (2) Storage vessels containing other latex products and located 
    downstream of the stripping operations;
        (3) Storage vessels containing high conversion latex products;
        (4) Storage vessels located downstream of the stripping operations 
    at affected sources subject to the back-end residual organic HAP 
    limitation located in Sec. 63.494, that are complying through the use 
    of stripping technology, as specified in Sec. 63.495;
        (5) Storage vessels containing styrene;
        (6) Storage vessels containing acrylamide; and
        (7) Storage vessels containing epichlorohydrin.
        (c) When the term ``storage vessel'' is used in Secs. 63.119 
    through 63.123 and 63.148 of subpart G, the definition of this term in 
    Sec. 63.482 shall apply for the purposes of this subpart.
        (d) When the term ``Group 1 storage vessel'' is used in 
    Secs. 63.119 through 63.123 and Sec. 63.148 of subpart G, the 
    definition of this term in Sec. 63.482 shall apply for the purposes of 
    this subpart.
        (e) When the term ``Group 2 storage vessel'' is used in 
    Secs. 63.119 through
    
    [[Page 46934]]
    
    63.123 and Sec. 63.148 of subpart G, the definition of this term in 
    Sec. 63.482 shall apply for the purposes of this subpart.
        (f) When the emissions averaging provisions of Sec. 63.150 of 
    subpart G are referred to in Sec. 63.119 and Sec. 63.123 of subpart G, 
    the emissions averaging provisions contained in Sec. 63.503 shall apply 
    for the purposes of this subpart.
        (g) When December 31, 1992 is referred to in Sec. 63.119 of subpart 
    G, it shall be replaced with June 12, 1995 for the purposes of this 
    subpart.
        (h) When April 22, 1994 is referred to in Sec. 63.119 of subpart G, 
    it shall be replaced with September 5, 1996 for the purposes of this 
    subpart.
        (i) Each owner or operator shall comply with this paragraph instead 
    of Sec. 63.120(d)(1)(ii) of subpart G for the purposes of this subpart. 
    If the control device used to comply with this section is also used to 
    comply with Secs. 63.485 through Sec. 63.501, the performance test 
    required for these sections is acceptable for demonstrating compliance 
    with Sec. 63.119(e) of subpart G for the purposes of this subpart. The 
    owner or operator will not be required to prepare a design evaluation 
    for the control device as described in Sec. 63.120(d)(1)(i) of subpart 
    G, if the performance test meets the criteria specified in paragraphs 
    (i)(1) and (i)(2) of this section.
        (1) The performance test demonstrates that the control device 
    achieves greater than or equal to the required control efficiency 
    specified in Sec. 63.119(e)(1) or Sec. 63.119(e)(2) of subpart G, as 
    applicable; and
        (2) The performance test is submitted as part of the Notification 
    of Compliance Status required by Sec. 63.506(e)(5).
        (j) When the term ``operating range'' is used in 
    Sec. 63.120(d)(3)(i) of subpart G, it shall be replaced with the term 
    ``level,'' for the purposes of this subpart. This level shall be 
    established using the procedures specified in Sec. 63.505.
        (k) When the Notification of Compliance Status requirements 
    contained in Sec. 63.152(b) of subpart G are referred to in 
    Secs. 63.120, 63.122, and 63.123 of subpart G, the Notification of 
    Compliance Status requirements contained in Sec. 63.506(e)(5) shall 
    apply for the purposes of this subpart.
        (l) When the Periodic Report requirements contained in 
    Sec. 63.152(c) of subpart G are referred to in Secs. 63.120, 63.122, 
    and 63.123 of subpart G, the Periodic Report requirements contained in 
    Sec. 63.506(e)(6) shall apply for the purposes of this subpart.
        (m) When other reports as required in Sec. 63.152(d) of subpart G 
    are referred to in Sec. 63.122 of subpart G, the reporting requirements 
    contained in Sec. 63.506(e)(7) shall apply for the purposes of this 
    subpart.
        (n) When the Implementation Plan requirements contained in 
    Sec. 63.151(c) of subpart G are referred to in Sec. 63.119 through 
    Sec. 63.123 of subpart G, for the purposes of this subpart the owner or 
    operator of an affected source need not comply.
        (o) When the Initial Notification Plan requirements contained in 
    Sec. 63.151(b) of subpart G are referred to in Sec. 63.119 through 
    Sec. 63.123 of subpart G, for the purposes of this subpart the owner or 
    operator of an affected source need not comply.
        (p) When the determination of equivalence criteria in 
    Sec. 63.102(b) of subpart F are referred to in Sec. 63.121(a) of 
    subpart G, the provisions in Sec. 63.6(g) of subpart A shall apply for 
    the purposes of this subpart.
        (q) The compliance date for storage vessels at affected sources 
    subject to the provisions of this section is specified in Sec. 63.481.
    
    
    Sec. 63.485  Continuous front-end process vent provisions.
    
        (a) For each continuous front-end process vent located at an 
    affected source, the owner or operator shall comply with the 
    requirements of Secs. 63.113 through 63.118 of subpart G, except as 
    provided for in paragraphs (b) through (s) of this section. Continuous 
    front-end process vents that are combined with one or more batch front-
    end process vents shall comply with paragraph (m) or (n) of this 
    section.
        (b) When the term ``process vent'' is used in Secs. 63.113 through 
    63.118 of subpart G, it shall be replaced with the term ``continuous 
    front-end process vent,'' and the definition of this term in 
    Sec. 63.482 shall apply for the purposes of this subpart.
        (c) When the term ``halogenated process vent'' is used in 
    Secs. 63.113 through 63.118 of subpart G, it shall be replaced with the 
    term ``halogenated continuous front-end process vent,'' and the 
    definition of this term in Sec. 63.482 shall apply for the purposes of 
    this subpart.
        (d) When the term ``Group 1 process vent'' is used in Secs. 63.113 
    through 63.118 of subpart G, it shall be replaced with the term ``Group 
    1 continuous front-end process vent,'' and the definition of this term 
    in Sec. 63.482 shall apply for the purposes of this subpart.
        (e) When the term ``Group 2 process vent'' is used in Secs. 63.113 
    through 63.118 of subpart G, it shall be replaced with the term ``Group 
    2 continuous front-end process vent,'' and the definition of this term 
    in Sec. 63.482 shall apply for the purposes of this subpart.
        (f) When December 31, 1992 is referred to in Sec. 63.113 of subpart 
    G, it shall be replaced with June 12, 1995 for the purposes of this 
    subpart.
        (g) When Secs. 63.151(f), alternative monitoring parameters, and 
    63.152(e), submission of an operating permit, of subpart G are referred 
    to in Secs. 63.114(c) and 63.117(e) of subpart G, Sec. 63.506(f), 
    alternative monitoring parameters, and Sec. 63.506(e)(8), submission of 
    an operating permit, respectively, shall apply for the purposes of this 
    subpart.
        (h) When the Notification of Compliance Status requirements 
    contained in Sec. 63.152(b) of subpart G are referred to in 
    Secs. 63.114, 63.117, and 63.118 of subpart G, the Notification of 
    Compliance Status requirements contained in Sec. 63.506(e)(5) shall 
    apply for the purposes of this subpart.
        (i) When the Periodic Report requirements contained in 
    Sec. 63.152(c) of subpart G are referred to in Secs. 63.117 and 63.118 
    of subpart G, the Periodic Report requirements contained in 
    Sec. 63.506(e)(6) shall apply for the purposes of this subpart.
        (j) When the definition of excursion in Sec. 63.152(c)(2)(ii)(A) of 
    subpart G is referred to in Sec. 63.118(f)(2) of subpart G, the 
    definition of excursion in Sec. 63.505(g) and (h) shall apply for the 
    purposes of this subpart.
        (k) For the purposes of this subpart, owners and operators shall 
    comply with Sec. 63.505, parameter monitoring levels and excursions, 
    instead of Sec. 63.114(e) of subpart G. When the term ``range'' is used 
    in Sec. 63.117(f), Sec. 63.118(a)(2)(iv), (b)(2)(iv), (f)(1), and 
    (f)(6) of subpart G, it shall be replaced with the term ``level.'' This 
    level is determined in accordance with Sec. 63.505.
        (l) When reports of process changes are required under Sec. 63.118 
    (g), (h), (i), and (j) of subpart G, paragraphs (l)(1) through (l)(4) 
    of this section shall apply for the purposes of this subpart.
        (1) Whenever a process change, as defined in Sec. 63.115(e) of 
    subpart G, is made that causes a Group 2 continuous front-end process 
    vent to become a Group 1 continuous front-end process vent, the owner 
    or operator shall submit the following information in the first 
    periodic report following the process change, as specified in 
    Sec. 63.506(e)(6)(iii)(D)(2):
        (i) A description of the process change; and
        (ii) A schedule for compliance with Sec. 63.113(a) of subpart G, as 
    required under Sec. 63.506(e)(6)(iii)(D)(2).
        (2) Whenever a process change, as defined in Sec. 63.115(e) of 
    subpart G, is made that causes a Group 2 continuous front-end process 
    vent with a TRE greater than 4.0 to become a Group 2
    
    [[Page 46935]]
    
    continuous front-end process vent with a TRE less than 4.0, the owner 
    or operator shall submit the following information in the first 
    periodic report following the process change, as specified in 
    Sec. 63.506(e)(6)(iii)(D)(2):
        (i) A description of the process change; and
        (ii) A schedule for compliance with the provisions of 
    Sec. 63.113(d) of subpart G, as required under 
    Sec. 63.506(e)(6)(iii)(D)(2).
        (3) Whenever a process change, as defined in Sec. 63.115(e) of 
    subpart G, is made that causes a Group 2 continuous front-end process 
    vent with a flow rate less than 0.005 standard cubic meter per minute 
    (scmm) to become a Group 2 continuous front-end process vent with a 
    flow rate of 0.005 scmm or greater and a TRE index value less than or 
    equal to 4.0, the owner or operator shall submit the following 
    information in the first periodic report following the process change, 
    as specified in Sec. 63.506(e)(6)(iii)(D)(2):
        (i) A description of the process change; and
        (ii) A schedule for compliance with two provisions of 
    Sec. 63.113(d) of subpart G, as required under 
    Sec. 63.506(e)(6)(iii)(D)(2).
        (4) Whenever a process change, as defined in Sec. 63.115(e) of 
    subpart G, is made that causes a Group 2 continuous front-end process 
    vent with an organic HAP concentration less than 50 parts per million 
    by volume (ppmv) to become a Group 2 continuous front-end process vent 
    with an organic HAP concentration of 50 ppmv or greater and a TRE index 
    value less than or equal to 4.0, the owner or operator shall submit the 
    following information in the first periodic report following the 
    process change, as specified in Sec. 63.506(e)(6)(iii)(D)(2):
        (i) A description of the process change; and
        (ii) A schedule for compliance with the provisions of 
    Sec. 63.113(d) of subpart G, as required under 
    Sec. 63.506(e)(6)(iii)(D)(2).
        (m) If a batch front-end process vent is combined with a continuous 
    front-end process vent prior to being routed to a control device, the 
    combined vent stream shall comply with either paragraph (m)(1) or 
    (m)(2) of this section, as appropriate.
        (1) If the continuous front-end process vent is a Group 1 
    continuous front-end process vent, the combined vent stream shall 
    comply with all requirements for a Group 1 continuous process vent 
    stream in Secs. 63.113 through 63.118 of subpart G, with the 
    differences noted in paragraphs (b) through (l) of this section.
        (2) If the continuous front-end process vent is a Group 2 
    continuous front-end process vent, the TRE index value shall be 
    calculated during maximum representative operating conditions. For 
    combined streams containing continuous front-end and batch front-end 
    process vents, the maximum representative operating conditions shall be 
    during periods when batch emission episodes are venting to the control 
    device resulting in the highest concentration of organic HAP in the 
    combined vent stream.
        (n) If a batch front-end process vent is combined with a continuous 
    front-end process vent prior to being routed to a recovery device, the 
    TRE index value shall be calculated at the exit of the recovery device 
    at maximum representative operating conditions. For combined vent 
    streams containing continuous front-end and batch front-end process 
    vents, the maximum representative operating conditions shall be during 
    periods when batch emission episodes are venting to the recovery device 
    resulting in the highest concentration of organic HAP in the combined 
    vent stream.
        (o) Group 1 halogenated continuous front-end process vents at 
    affected existing sources producing butyl rubber, halobutyl rubber, or 
    ethylene propylene rubber are exempt from the requirements to control 
    hydrogen halides and halogens from the outlet of combustion devices 
    contained in Sec. 63.113(c) of subpart G, if the conditions in 
    paragraphs (o)(1) and (o)(2) of this section are met. Affected new 
    sources are not exempt from these provisions.
        (1)(i) For affected sources producing butyl rubber, halobutyl 
    rubber, or ethylene propylene rubber using a solution process, if the 
    halogenated continuous front-end process vent stream was controlled by 
    a combustion device prior to June 12, 1995, or
        (ii) For affected sources producing ethylene propylene rubber using 
    a gas-phased reaction process, if the halogenated continuous front-end 
    process vent stream was controlled by a combustion device since 
    startup.
        (2) The combustion device meets the requirements of 
    Sec. 63.113(a)(1)(i), Sec. 63.113(a)(2), Sec. 63.113(a)(3), or 
    Sec. 63.113(b) of subpart G.
        (p) The compliance date for continuous front-end process vents 
    subject to the provisions of this section is specified in Sec. 63.481. 
    This replaces the reference to Sec. 63.100 of subpart F in 
    Sec. 63.115(e)(2) of subpart G.
        (q) Internal combustion engines. In addition to the three options 
    for the control of a Group 1 continuous front-end process vent listed 
    in Sec. 63.113(a) (1)-(3) of subpart G, an owner or operator can route 
    emissions of organic HAP to an internal combustion engine, provided the 
    conditions listed in paragraphs (q)(1) through (q)(3) of this section 
    are met.
        (1) The vent stream routed to the internal combustion engine shall 
    not be a halogenated continuous front-end process vent stream.
        (2) The organic HAP is introduced with the primary fuel.
        (3) The owner or operator continuously monitors the on/off status 
    of the internal combustion engine.
        (4) If an internal combustion engine meeting the requirements of 
    paragraphs (q) (1) through (3) of this section is used to comply with 
    the provisions of Sec. 63.113(a) of subpart G, the internal combustion 
    engine is exempt from the source testing requirements of Sec. 63.116 of 
    subpart G.
        (r) When the provisions of Sec. 63.116 (c)(3) and (c)(4) of subpart 
    G specify that Method 18 shall be used, Method 18 or Method 25A may be 
    used for the purposes of this subpart. The use of Method 25A shall 
    comply with paragraphs (r)(1) and (r)(2) of this section.
        (1) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (2) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (s) When the provisions of Sec. 63.116(b) identify conditions under 
    which a performance test is not required, for purposes of this subpart, 
    the exemption in paragraph (s)(1) of this section shall also apply. 
    Further, if a performance test meeting the conditions specified in 
    paragraph (s)(2) of this section has been conducted by the owner or 
    operator, the results of that performance test shall suffice, for the 
    purposes of this section.
        (1) An incinerator burning hazardous waste for which the owner or 
    operator complies with the requirements of 40 CFR part 264, subpart O.
        (2) Performance tests done for other subparts in part 60 or part 63 
    where total organic HAP or TOC was measured, provided that the owner or 
    operator can demonstrate that operating conditions for the process and 
    control or recovery device during the performance test are 
    representative of current operating conditions.
    
    [[Page 46936]]
    
    Sec. 63.486   Batch front-end process vent provisions.
    
        (a) Batch front-end process vents. Except as specified in paragraph 
    (b) of this section, owners and operators of new and existing affected 
    sources with batch front-end process vents shall comply with the 
    requirements in Secs. 63.487 through 63.492. The batch front-end 
    process vent group status shall be determined in accordance with 
    Sec. 63.488. Batch front-end process vents classified as Group 1 shall 
    comply with the reference control technology requirements for Group 1 
    batch front-end process vents in Sec. 63.487, the monitoring 
    requirements in Sec. 63.489, the performance test methods and 
    procedures to determine compliance requirements in Sec. 63.490, the 
    recordkeeping requirements in Sec. 63.491, and the reporting 
    requirements in Sec. 63.492. All Group 2 batch front-end process vents 
    shall comply with the applicable reference control technology 
    requirements in Sec. 63.487, the recordkeeping requirements in 
    Sec. 63.491, and the reporting requirements in Sec. 63.492.
        (b) Aggregate batch vent streams. Aggregate batch vent streams, as 
    defined in Sec. 63.482, are subject to the control requirements for 
    individual batch front-end process vents, as specified in 
    Sec. 63.487(b), as well as the monitoring, testing, recordkeeping, and 
    reporting requirements specified in Sec. 63.489 through Sec. 63.492.
    
    
    Sec. 63.487   Batch front-end process vents--reference control 
    technology.
    
        (a) Batch front-end process vents. The owner or operator of a Group 
    1 batch front-end process vent, as determined using the procedures in 
    Sec. 63.488, shall comply with the requirements of either paragraph 
    (a)(1) or (a)(2) of this section. Compliance can be based on either 
    organic HAP or TOC.
        (1) For each batch front-end process vent, reduce organic HAP 
    emissions using a flare.
        (i) The flare shall comply with the requirements of Sec. 63.11(b) 
    of subpart A.
        (ii) Halogenated batch front-end process vents, as defined in 
    Sec. 63.482, shall not be vented to a flare.
        (2) For each batch front-end process vent, reduce organic HAP 
    emissions for the batch cycle by 90 weight percent using a control 
    device. Owners or operators may achieve compliance with this paragraph 
    through the control of selected batch emission episodes or the control 
    of portions of selected batch emission episodes. Documentation 
    demonstrating how the 90 weight percent emission reduction is achieved 
    is required by Sec. 63.490(c)(2).
        (b) Aggregate batch vent streams. The owner or operator of an 
    aggregate batch vent stream that contains one or more Group 1 batch 
    front-end process vents shall comply with the requirements of either 
    paragraph (b)(1) or (b)(2) of this section. Compliance can be based on 
    either organic HAP or TOC.
        (1) For each aggregate batch vent stream, reduce organic HAP 
    emissions using a flare.
        (i) The flare shall comply with the requirements of Sec. 63.11(b) 
    of subpart A.
        (ii) Halogenated aggregate batch vent streams, as defined in 
    Sec. 63.482, shall not be vented to a flare.
        (2) For each aggregate batch vent stream, reduce organic HAP 
    emissions by 90 weight percent on a continuous basis using a control 
    device.
        (c) Halogenated emissions. Halogenated Group 1 batch front-end 
    process vents, halogenated aggregate batch vent streams, and 
    halogenated continuous front-end process vents that are combusted as 
    part of complying with paragraph (a)(2) or (b)(2) of this section, 
    shall be controlled according to either paragraph (c)(1) or (c)(2) of 
    this section.
        (1) If a combustion device is used to comply with paragraph (a)(2) 
    or (b)(2) of this section for a halogenated batch front-end process 
    vent or halogenated aggregate batch vent stream, the emissions shall be 
    ducted from the combustion device to an additional control device that 
    reduces overall emissions of hydrogen halides and halogens by 99 
    percent before those emissions are discharged to the atmosphere.
        (2) A control device may be used to reduce the halogen atom mass 
    emission rate to less than 3,750 kg/yr for batch front-end process 
    vents or aggregate batch vent streams and thus make the batch front-end 
    process vent or aggregate batch vent stream nonhalogenated. The 
    nonhalogenated batch front-end process vent or aggregate batch vent 
    stream must then comply with the requirements of either paragraph (a) 
    or (b) of this section, as appropriate.
        (d) If a boiler or process heater is used to comply with the 
    percent reduction requirement specified in paragraph (a)(2) or (b)(2) 
    of this section, the batch front-end process vent or aggregate batch 
    vent stream shall be introduced into the flame zone of such a device.
        (e) Combination of batch front-end process vents or aggregate batch 
    vent streams with continuous front-end process vents. A batch front-end 
    process vent or aggregate batch vent stream combined with a continuous 
    front-end process vent stream is not subject to the provisions of 
    Secs. 63.488 through 63.492, providing the requirements of paragraphs 
    (e)(1), (e)(2), and either (e)(3) or (e)(4) of this section are met.
        (1) The batch front-end process vent is combined with a continuous 
    front-end process vent prior to routing the continuous front-end 
    process vent to a control or recovery device. In this paragraph, the 
    definitions of control device and recovery device as they relate to 
    continuous front-end process vents shall be used.
        (2) The only emissions to the atmosphere from the batch front-end 
    process vent or aggregate batch vent stream prior to being combined 
    with the continuous front-end process vent are from equipment subject 
    to and in compliance with Sec. 63.502.
        (3) If the batch front-end vent stream or aggregate batch vent 
    stream is combined with a continuous front-end process vent stream 
    prior to being routed to a control device, the combined vent stream 
    shall comply with the requirements in Sec. 63.485(m). In this 
    paragraph, the definition of control device as it relates to continuous 
    front-end process vents shall be used.
        (4) If the batch front-end process vent or aggregate batch vent 
    stream is combined with a continuous front-end process vent stream 
    prior to being routed to a recovery device, the combined vent stream 
    shall comply with the requirements in Sec. 63.485(n). In this 
    paragraph, the definition of recovery device as it relates to 
    continuous front-end process vents shall be used.
        (f) Group 2 batch front-end process vents with annual emissions 
    greater than or equal to the level specified in Sec. 63.488(d). The 
    owner or operator of a Group 2 batch front-end process vent with annual 
    emissions greater than or equal to the level specified in 
    Sec. 63.488(d) shall comply with the provisions of paragraphs (f)(1) 
    and (f)(2) of this section.
        (1) Establish a batch cycle limitation that ensures that the Group 
    2 batch front-end process vent does not become a Group 1 batch front-
    end process vent, and
        (2) Comply with the recordkeeping requirements in 
    Sec. 63.491(d)(2), and the reporting requirements in Sec. 63.492(a)(3) 
    and (b).
        (g) Group 2 batch front-end process vents with annual emissions 
    less than the level specified in Sec. 63.488(d). The owner or operator 
    of a Group 2 batch front-end process vent with annual organic HAP 
    emissions less than the level specified in Sec. 63.488(d), shall comply 
    with either paragraphs (g)(1) and (g)(2) of this section or with
    
    [[Page 46937]]
    
    paragraphs (f)(1) and (f)(2) of this section.
        (1) Establish a batch cycle limitation that ensures emissions do 
    not exceed the appropriate level specified in Sec. 63.488(d), and
        (2) Comply with the recordkeeping requirements in 
    Sec. 63.491(d)(1), and the reporting requirements in Sec. 63.492(a)(2), 
    (b), and (c).
    
    
    Sec. 63.488   Methods and procedures for batch front-end process vent 
    group determination.
    
        (a) General requirements. Except as provided in paragraph (a)(3) of 
    this section, the owner or operator of batch front-end process vents at 
    affected sources shall determine the group status of each batch front-
    end process vent in accordance with the provisions of this section. 
    This determination may be based on either organic HAP or TOC emissions.
        (1) The procedures specified in paragraphs (b) through (i) shall be 
    followed for the expected mix of products for a given batch front-end 
    process vent, as specified in paragraph (a)(1)(i) of this section, or 
    for the worst-case HAP emitting batch unit operation, as specified in 
    paragraphs (a)(1)(ii) through (a)(1)(iv) of this section. ``Worst-case 
    HAP emitting product'' is defined in paragraph (a)(1)(iii) of this 
    section.
        (i) If an owner or operator chooses to follow the procedures 
    specified in paragraphs (b) through (i) of this section for the 
    expected mix of products, an identification of the different products 
    and the number of batch cycles accomplished for each is required as 
    part of the group determination documentation.
        (ii) If an owner or operator chooses to follow the procedures 
    specified in paragraphs (b) through (i) of this section for the worst-
    case HAP emitting product, documentation identifying the worst-case HAP 
    emitting product is required as part of the group determination 
    documentation.
        (iii) Except as specified in paragraph (a)(1)(iii)(B) of this 
    section, the worst-case HAP emitting product is as defined in paragraph 
    (a)(1)(iii)(A) of this section.
        (A) The worst-case HAP emitting product is the one with the highest 
    mass emission rate (kg organic HAP per hour) averaged over the entire 
    time period of the batch cycle.
        (B) Alternatively, when one product is produced more than 75 
    percent of the time, accounts for more than 75 percent of the annual 
    mass of product, and the owner or operator can show that the mass 
    emission rate (kg organic HAP per hour) averaged over the entire time 
    period of the batch cycle can reasonably be expected to be similar to 
    the mass emission rate for other products having emissions from the 
    same batch front-end process vent, that product may be considered the 
    worst-case HAP emitting product.
        (C) An owner or operator shall determine the worst-case HAP 
    emitting product for a batch front-end process vent as specified in 
    paragraphs (a)(1)(iii)(C)(1) through (a)(1)(iii)(C)(3) of this section.
        (1) The emissions per batch emission episode shall be determined 
    using any of the procedures specified in paragraph (b) of this section. 
    The mass emission rate (kg organic HAP per hour) averaged over the 
    entire time period of the batch cycle shall be determined by summing 
    the emissions for each batch emission episode making up a complete 
    batch cycle and dividing by the total duration in hours of the batch 
    cycle.
        (2) To determine the worst-case HAP emitting product as specified 
    under paragraph (a)(1)(iii)(A) of this section, the mass emission rate 
    for each product shall be determined and compared.
        (3) To determine the worst-case HAP emitting product as specified 
    under paragraph (a)(1)(iii)(B) of this section, the mass emission rate 
    for the product meeting the time and mass criteria of paragraph 
    (a)(1)(iii)(B) of this section shall be determined, and the owner or 
    operator shall provide adequate information to demonstrate that the 
    mass emission rate for said product is similar to the mass emission 
    rates for the other products having emissions from the same batch 
    process vent. In addition, the owner or operator shall provide 
    information demonstrating that the selected product meets the time and 
    mass criteria of paragraph (a)(1)(iii)(B) of this section.
        (iv) The annual production of the worst-case HAP emitting product 
    shall be determined by ratioing the production time of the worst-case 
    product up to a 12 month period of actual production. It is not 
    necessary to ratio up to a maximum production rate (i.e., 8,760 hours 
    per year at maximum design production).
        (2) The annual uncontrolled organic HAP or TOC emissions and 
    average flow rate shall be determined at the exit from the batch unit 
    operation. For the purposes of these determinations, the primary 
    condenser operating as a reflux condenser on a distillation column, the 
    primary condenser recovering monomer or solvent from a batch stripping 
    operation, and the primary condenser recovering monomer or solvent from 
    a batch distillation operation shall be considered part of the batch 
    unit operation. All other devices that recover or oxidize organic HAP 
    or TOC vapors shall be considered control devices as defined in 
    Sec. 63.482.
        (3) The owner or operator of a batch front-end process vent 
    complying with the flare provisions in Sec. 63.487(a)(1) or 
    Sec. 63.487(b)(1) or routing the batch front-end process vent to a 
    control device to comply with the requirements in Sec. 63.487(a)(2) or 
    Sec. 63.487(b)(2) is not required to perform the batch front-end 
    process vent group determination described in this section, but shall 
    comply with all requirements applicable to Group 1 batch front-end 
    process vents.
        (b) Determination of annual emissions. The owner or operator shall 
    calculate annual uncontrolled TOC or organic HAP emissions for each 
    batch front-end process vent using the methods described in paragraphs 
    (b)(1) through (b)(8) of this section. Paragraphs (b)(1) through (b)(4) 
    of this section present procedures that can be used to calculate the 
    emissions from individual batch emission episodes. Emissions from batch 
    front-end processes involving multicomponent systems are to be 
    calculated using the procedures in paragraphs (b)(1) through (b)(4) of 
    this section. Individual HAP partial pressures in multicomponent 
    systems shall be determined by the following methods: If the components 
    are miscible in one another, use Raoult's law to calculate the partial 
    pressures; if the solution is a dilute aqueous mixture, use Henry's law 
    constants to calculate partial pressures; if Raoult's law or Henry's 
    law are not appropriate or available, use experimentally obtained 
    activity coefficients, Henry's law constants, or solubility data; if 
    Raoult's law or Henry's law are not appropriate, use models, such as 
    the group-contribution models, to predict activity coefficients; and if 
    Raoult's law or Henry's law are not appropriate, assume the components 
    of the system behave independently and use the summation of all vapor 
    pressures from the HAP's as the total HAP partial pressure. Chemical 
    property data can be obtained from standard reference texts. Paragraph 
    (b)(5) of this section describes how direct measurement can be used to 
    estimate emissions. If the owner or operator can demonstrate that the 
    procedures in paragraphs (b)(1) through (b)(4) of this section are not 
    appropriate to estimate emissions from a batch front-end process 
    emission episode, emissions may be estimated using engineering 
    assessment, as described in paragraph (b)(6) of this section. Owners or 
    operators are not required to demonstrate that direct measurement is
    
    [[Page 46938]]
    
    not appropriate before utilizing engineering assessment. Paragraph 
    (b)(6)(ii) of this section describes how an owner or operator shall 
    demonstrate that the procedures in paragraphs (b)(1) through (b)(4) of 
    this section are not appropriate. Emissions from a batch cycle shall be 
    calculated in accordance with paragraph (b)(7) of this section, and 
    annual emissions from the batch front-end process vent shall be 
    calculated in accordance with paragraph (b)(8) of this section.
        (1) TOC or organic HAP emissions from the purging of an empty 
    vessel shall be calculated using Equation 1. This equation does not 
    take into account evaporation of any residual liquid in the vessel.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.000
    
    where:
    
    Eepisode=Emissions, kg/episode.
    Vves=Volume of vessel, m3.
    P=TOC or total organic HAP partial pressure, kPa.
    MWWAVG=Weighted average molecular weight of TOC or organic HAP in 
    vapor, determined in accordance with paragraph (b)(4)(iii) of this 
    section, kg/kmol.
    R=Ideal gas constant, 8.314 m3kPa/kmol deg.K.
    T=Temperature of vessel vapor space,  deg.K.
    m=Number of volumes of purge gas used.
    
        (2) TOC or organic HAP emissions from the purging of a filled 
    vessel shall be calculated using Equation 2.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.001
    
    where:
    
    Eepisode=Emissions, kg/episode.
    y=Saturated mole fraction of all TOC or organic HAP in vapor phase.
    Vdr=Volumetric gas displacement rate, m3/min.
    P=Pressure in vessel vapor space, kPa.
    MWWAVG=Weighted average molecular weight of TOC or organic HAP in 
    vapor, determined in accordance with paragraph (b)(4)(iii) of this 
    section, kg/kmol.
    R=Ideal gas constant, 8.314 m3kPa/kmol deg.K.
    T=Temperature of vessel vapor space,  deg.K.
    Pi=Vapor pressure of TOC or individual organic HAP i, kPa.
    xi=Mole fraction of TOC or organic HAP i in the liquid.
    n=Number of organic HAP in stream.
        Note: Summation not required if TOC emissions are being estimated.
    Tm=Minutes/episode.
    
        (3) Emissions from vapor displacement due to transfer of material 
    into or out of a vessel shall be calculated using Equation 3.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.002
    
    where:
    
    Eepisode=Emissions, kg/episode.
    y=Saturated mole fraction of all TOC or organic HAP in vapor phase.
    V=Volume of gas displaced from the vessel, m3.
    P=Pressure of vessel vapor space, kPa.
    MWWAVG=Weighted average molecular weight of TOC or organic HAP in 
    vapor, determined in accordance with paragraph (b)(4)(iii) of this 
    section, kg/kmol.
    R=Ideal gas constant, 8.314 m3kPa/kmol deg.K.
    T=Temperature of vessel vapor space,  deg.K.
        (4) Emissions caused by the heating of a vessel shall be calculated 
    using the procedures in either paragraph (b)(4)(i), (b)(4)(ii), or 
    (b)(4)(iii) of this section, as appropriate.
        (i) If the final temperature to which the vessel contents is heated 
    is lower than 50 K below the boiling point of the HAP in the vessel, 
    then emissions shall be calculated using the equations in paragraphs 
    (b)(4)(i)(A) through (b)(4)(i)(D) of this section.
        (A) Emissions caused by heating of a vessel shall be calculated 
    using Equation 4. The assumptions made for this calculation are 
    atmospheric pressure of 760 mm Hg and the displaced gas is always 
    saturated with VOC vapor in equilibrium with the liquid mixture.
    
    [[Page 46939]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.003
    
    
    where:
    
    Eepisode=Emissions, kg/episode.
    (Pi)T1, (Pi)T2=Partial pressure (kPa) TOC or each organic HAP 
    in the vessel headspace at initial (T1) and final (T2) temperature.
    n=Number of organic HAP in stream. Note: Summation not required if TOC 
    emissions are being estimated.
    =Number of kilogram-moles (kg-moles) of gas 
    displaced, determined in accordance with paragraph (b)(4)(i)(B) of this 
    section.
    101.325=Constant, kPa.
    (MWWAVG,T1), (MWWAVG,T2)=Weighted average molecular weight of 
    TOC or organic HAP in vapor, determined in accordance with paragraph 
    (b)(4)(iii) of this section.
    
        (B) The moles of gas displaced, , is calculated 
    using equation 5.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.004
    
    where:
    =Number of kg-moles of gas displaced.
    Vfs=Volume of free space in the vessel, m3.
    R=Ideal gas constant, 8.314 m3kPa/kmolK.
    Pa1=Initial noncondensible gas pressure in the vessel, kPa.
    Pa2=Final noncondensible gas pressure, kPa.
    T1=Initial temperature of vessel, K.
    T2=Final temperature of vessel, K.
        (C) The initial and final pressure of the noncondensible gas in the 
    vessel shall be calculated using equation 6.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.005
    
    where:
    
    Pa=Initial or final partial pressure of noncondensible gas in the 
    vessel headspace, kPa.
    101.325=Constant, kPa.
    (Pi)T=Partial pressure of TOC or each organic HAP i in the vessel 
    headspace, kPa, at the initial or final temperature (T1 or 
    T2).
    n=Number of organic HAP in stream. Note: Summation not required if TOC 
    emissions are being estimated.
    
        (D) The weighted average molecular weight of organic HAP in the 
    displaced gas, MWHAP, shall be calculated using equation 7:
    [GRAPHIC] [TIFF OMITTED] TR05SE96.006
    
    where:
    
    c=TOC or organic HAP component
    n=Number of TOC or organic HAP components in stream.
    
        (ii) If the vessel contents are heated to a temperature greater 
    than 50 K below the boiling point, then emissions from the heating of a 
    vessel shall be calculated as the sum of the emissions calculated in 
    accordance with paragraphs (b)(4)(ii)(A) and (b)(4)(ii)(B) of this 
    section.
        (A) For the interval from the initial temperature to the 
    temperature 50 K below the boiling point, emissions shall be calculated 
    using Equation 4, where T2 is the temperature 50 K below the 
    boiling point.
        (B) For the interval from the temperature 50 K below the boiling 
    point to the final temperature, emissions shall be calculated as the 
    summation of emissions for each 5 K increment, where the emissions for 
    each increment shall be calculated using Equation 4.
        (1) If the final temperature of the heatup is lower than 5 K below 
    the boiling point, the final temperature for the last increment shall 
    be the final temperature for the heatup, even if the last increment is 
    less than 5 K.
        (2) If the final temperature of the heatup is higher than 5 K below 
    the boiling point, the final temperature for the last increment shall 
    be the temperature 5 K below the boiling point, even if the last 
    increment is less than 5 K.
        (3) If the vessel contents are heated to the boiling point and the 
    vessel is not operating with a condenser, the final temperature for the 
    final increment shall be the temperature 5 K below the boiling point, 
    even if the last increment is less than 5 K.
        (iii) If the vessel is operating with a condenser, and the vessel 
    contents are heated to the boiling point, the primary condenser is 
    considered part of the process, as described in Sec. 63.488(a)(2). 
    Emissions shall be calculated as the sum of Equation 4, which 
    calculates emissions due to heating the vessel contents to the 
    temperature of the gas
    
    [[Page 46940]]
    
    exiting the condenser, and Equation 3, which calculates emissions due 
    to the displacement of the remaining saturated noncondensible gas in 
    the vessel. The final temperature in Equation 4 shall be set equal to 
    the exit gas temperature of the condenser. Equation 3 shall be used as 
    written below in Equation 3a, using free space volume, and T2 is 
    set equal to the condenser exit gas temperature.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.007
    
    where:
    
    Eepisode=Organic HAP emissions, kg/episode.
    yi=Saturated mole fraction of organic HAP in the vapor phase.
    Vfs=Volume of the free space in the vessel, m3.
    PT=Pressure of the vessel vapor space, kPa.
    MWHAP=Weighted average molecular weight of organic HAP in vapor, 
    determined in accordance with paragraph (b)(4)(iii) of this section.
    R=Ideal gas constant, 8.314 m3kPa/kmolK.
    T=Temperature of condenser exit stream K.
    n=Number of organic HAP in stream.
    
        (5) The owner or operator may estimate annual emissions for a batch 
    emission episode by direct measurement. If direct measurement is used, 
    the owner or operator shall either perform a test for the duration of a 
    representative batch emission episode or perform a test during only 
    those periods of the batch emission episode for which the emission rate 
    for the entire episode can be determined or for which the emissions are 
    greater than the average emission rate of the batch emission episode. 
    The owner or operator choosing either of these options must develop an 
    emission profile for the entire batch emission episode, based on either 
    process knowledge or test data collected, to demonstrate that test 
    periods are representative. Examples of information that could 
    constitute process knowledge include calculations based on material 
    balances and process stoichiometry. Previous test results may be used 
    provided the results are still relevant to the current batch process 
    vent conditions. Performance tests shall follow the procedures 
    specified in paragraphs (b)(5)(i) through (b)(5)(iii) of this section. 
    The procedures in either paragraph (b)(5)(iv) or (b)(5)(v) of this 
    section shall be used to calculate the emissions per batch emission 
    episode.
        (i) Method 1 or 1A, as appropriate, shall be used for selection of 
    the sampling sites if the flow measuring device is a pitot tube. No 
    traverse is necessary when Method 2A or 2D is used to determine gas 
    stream volumetric flow rate.
        (ii) Gas stream volumetric flow rate and/or average flow rate shall 
    be determined as specified in paragraph (e) of this section.
        (iii) Method 18 or Method 25A, of 40 CFR part 60, appendix A, shall 
    be used to determine the concentration of TOC or organic HAP, as 
    appropriate. The use of Method 25A shall comply with paragraphs 
    (b)(5)(iii)(A) and (b)(5)(iii)(B) of this section.
        (A) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (B) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (iv) If an integrated sample is taken over the entire batch 
    emission episode to determine TOC or average total organic HAP 
    concentration, emissions shall be calculated using Equation 8.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.008
    
    where:
    
    Eepisode=Emissions, kg/episode
    K=Constant, 2.494  x  10-6 (ppmv) -1 (gm-mole/scm) (kg/gm) 
    (min/hr), where standard temperature is 20 deg.C.
    Cj=Average concentration of TOC or sample organic HAP component j 
    of the gas stream for the batch emission episode, dry basis, ppmv.
    Mj=Molecular weight of TOC or sample component j of the gas 
    stream, dry basis, gm/gm-mole.
    AFR=Average flow rate of gas stream, dry basis, scmm.
    Th=Hours/episode
    n=Number of organic HAP in stream. Note: Summation not required if TOC 
    emissions are being estimated using a TOC concentration measured using 
    Method 25A.
    
        (v) If grab samples are taken to determine TOC or average total 
    organic HAP concentration, emissions shall be calculated according to 
    paragraphs (b)(5)(v)(A) and (b)(5)(v)(B) of this section.
        (A) For each measurement point, the emission rate shall be 
    calculated using Equation 9.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.009
    
    where:
    
    Epoint=Emission rate for individual measurement point, kg/hr.
    K=Constant, 2.494  x  10-6 (ppmv)-1 (gm-mole/scm) (kg/gm) 
    (min/hr), where standard temperature is 20 deg.C.
    Cj=Concentration of TOC or sample component j of the gas stream, 
    dry basis, ppmv.
    Mj=Molecular weight of TOC or sample component j of the gas 
    stream, gm/gm-mole.
    FR=Flow rate of gas stream for the measurement point, dry basis, scmm.
    n=Number of organic HAP in stream. Note: Summation not required if TOC 
    emissions are being estimated using a TOC concentration measured using 
    Method 25A.
    
        (B) The emissions per batch emission episode shall be calculated 
    using Equation 10.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.010
    
    where:
    
    Eepisode=Emissions, kg/episode.
    DUR=Duration of the batch emission episode, hr/episode.
    Ei=Emissions for measurement point i, kg/hr.
    n=Number of measurements.
        (6) If the owner or operator can demonstrate that the methods in 
    paragraphs (b)(1) through (b)(4) of this section are not appropriate to 
    estimate emissions for a batch emissions episode, the owner or operator 
    may use engineering assessment to estimate emissions as specified in 
    paragraphs (b)(6)(i) and (b)(6)(ii) of this section. All data, 
    assumptions, and procedures used in an engineering assessment shall be 
    documented.
        (i) Engineering assessment includes, but is not limited to, the 
    following:
        (A) Previous test results, provided the tests are representative of 
    current operating practices.
        (B) Bench-scale or pilot-scale test data representative of the 
    process under representative operating conditions.
        (C) Flow rate, TOC emission rate, or organic HAP emission rate 
    specified or implied within a permit limit applicable to the batch 
    front-end process vent.
        (D) Design analysis based on accepted chemical engineering 
    principles, measurable process parameters, or physical or chemical laws 
    or properties. Examples of analytical methods include, but are not 
    limited to:
    
    [[Page 46941]]
    
        (1) Use of material balances,
        (2) Estimation of flow rate based on physical equipment design, 
    such as pump or blower capacities, and
        (3) Estimation of TOC or organic HAP concentrations based on 
    saturation conditions.
        (ii) The emissions estimation equations in paragraphs (b)(1) 
    through (b)(4) of this section shall be considered inappropriate for 
    estimating emissions for a given batch emissions episode if one or more 
    of the criteria in paragraphs (b)(6)(ii)(A) through (b)(6)(ii)(B) of 
    this section are met.
        (A) Previous test data are available that show a greater than 20 
    percent discrepancy between the test value and the estimated value.
        (B) The owner or operator can demonstrate to the Administrator 
    through any other means that the emissions estimation equations are not 
    appropriate for a given batch emissions episode.
        (C) Data or other information supporting a finding that the 
    emissions estimation equations are inappropriate as specified under 
    paragraph (b)(6)(ii)(A) of this section shall be reported in the 
    Notification of Compliance Status, as required in Sec. 63.506(e)(5).
        (D) Data or other information supporting a finding that the 
    emissions estimation equations are inappropriate as specified under 
    paragraph (b)(6)(ii)(B) of this section shall be reported in the 
    Precompliance Report, as required in Sec. 63.506(e)(3).
        (7) For each batch front-end process vent, the TOC or organic HAP 
    emissions associated with a single batch cycle shall be calculated 
    using Equation 11.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.011
    
    where:
    
    Ecycle=Emissions for an individual batch cycle, kg/batch cycle.
    Eepisodei=Emissions from a batch emission episode i, kg/episode.
    n=Number of batch emission episodes for the batch cycle.
    
        (8) Annual TOC or organic HAP emissions from a batch front-end 
    process vent shall be calculated using Equation 12.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.012
    
    where:
    
    AE=Annual emissions from a batch front-end process vent, kg/yr.
    Ni=Number of type i batch cycles performed annually, cycles/year.
    Ecyclei=Emissions from the batch front-end process vent associated 
    with single type i batch cycle, as determined in paragraph (b)(7) of 
    this section, kg/batch cycle.
    n=Number of different types of batch cycles that cause the emission of 
    TOC or organic HAP from the batch front-end process vent.
    
        (c) [Reserved]
        (d) Minimum emission level exemption. A batch front-end process 
    vent with annual emissions less than 11,800 kg/yr is considered a Group 
    2 batch front-end process vent and the owner or operator of that batch 
    front-end process vent shall comply with the requirements in 
    Sec. 63.487 (f) or (g). The owner or operator of that batch front-end 
    process vent is not required to comply with the provisions in 
    paragraphs (e) through (g) of this section.
        (e) Determination of average flow rate. The owner or operator shall 
    determine the average flow rate for each batch emission episode in 
    accordance with one of the procedures provided in paragraphs (e)(1) 
    through (e)(2) of this section. The annual average flow rate for a 
    batch front-end process vent shall be calculated as specified in 
    paragraph (e)(3) of this section.
        (1) Determination of the average flow rate for a batch emission 
    episode by direct measurement shall be made using the procedures 
    specified in paragraphs (e)(1)(i) through (e)(1)(iii) of this section.
        (i) The vent stream volumetric flow rate (Qs) for a batch 
    emission episode, in scmm at 20  deg.C, shall be determined using 
    Method 2, 2A, 2C, or 2D of 40 CFR part 60, appendix A, as appropriate.
        (ii) The volumetric flow rate of a representative batch emission 
    episode shall be measured every 15 minutes.
        (iii) The average flow rate for a batch emission episode shall be 
    calculated using Equation 13.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.013
    
    where:
    
    AFRepisode=Average flow rate for the batch emission episode, scmm.
    FRi=Flow rate for individual measurement i, scmm.
    n=Number of flow rate measurements taken during the batch emission 
    episode.
    
        (2) The average flow rate for a batch emission episode may be 
    determined by engineering assessment, as defined in paragraph (b)(6)(i) 
    of this section. All data, assumptions, and procedures used shall be 
    documented.
        (3) The annual average flow rate for a batch front-end process vent 
    shall be calculated using Equation 14.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.014
    
    where:
    
    AFR=Annual average flow rate for the batch front-end process vent, 
    scmm.
    DURi=Duration of type i batch emission episodes annually, hr/yr.
    AFRepisode,i=Average flow rate for type i batch emission episode, 
    scmm.
    n=Number of types of batch emission episodes venting from the batch 
    front-end process vent.
    
        (f) Determination of cutoff flow rate. For each batch front-end 
    process vent, the owner or operator shall calculate the cutoff flow 
    rate using Equation 15.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.015
    
    where:
    
    CFR=Cutoff flow rate, scmm.
    AE=Annual TOC or organic HAP emissions, as determined in paragraph 
    (b)(8) of this section, kg/yr.
    
        (g) Group 1/Group 2 status determination. The owner or operator 
    shall compare the cutoff flow rate, calculated in accordance with 
    paragraph (f) of this section, with the annual average flow rate, 
    determined in accordance with paragraph (e)(3) of this section. The 
    group determination status for each batch front-end process vent shall 
    be made using the criteria specified in paragraphs (g)(1) and (g)(2) of 
    this section.
        (1) If the cutoff flow rate is greater than or equal to the annual 
    average flow rate of the stream, the batch front-end process vent is 
    classified as a Group 1 batch front-end process vent.
        (2) If the cutoff flow rate is less than the annual average flow 
    rate of the stream, the batch front-end process vent is classified as a 
    Group 2 batch front-end process vent.
        (h) Determination of halogenation status. To determine whether a 
    batch front-end process vent or an aggregate batch vent stream is 
    halogenated, the annual mass emission rate of halogen atoms contained 
    in organic compounds shall be calculated using the procedures specified 
    in paragraphs (h)(1) through (h)(3) of this section.
        (1) The concentration of each organic compound containing halogen 
    atoms (ppmv, by compound) for each batch emission episode shall be 
    determined based on the following procedures:
    
    [[Page 46942]]
    
        (i) Process knowledge that no halogens or hydrogen halides are 
    present in the process may be used to demonstrate that a batch emission 
    episode is nonhalogenated. Halogens or hydrogen halides that are 
    unintentionally introduced into the process shall not be considered in 
    making a finding that a batch emission episode is nonhalogenated.
        (ii) Engineering assessment as discussed in paragraph (b)(6)(i) of 
    this section.
        (iii) Concentration of organic compounds containing halogens and 
    hydrogen halides as measured by Method 26 or 26A of 40 CFR part 60, 
    appendix A.
        (iv) Any other method or data that has been validated according to 
    the applicable procedures in Method 301 of appendix A of this part.
        (2) The annual mass emissions of halogen atoms for a batch front-
    end process vent shall be calculated using Equation 16.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.016
    
    where:
    
    Ehalogen=Mass of halogen atoms, dry basis, kg/yr.
    K=Constant, 0.022 (ppmv)-1 (kg-mole per scm) (min/yr), where 
    standard temperature is 20 deg.C.
    AFR=Annual average flow rate of the batch front-end process vent, 
    determined according to paragraph (e) of this section, scmm.
    Mj,i=Molecular weight of halogen atom i in compound j, kg/kg-mole.
    Lj,i=Number of atoms of halogen i in compound j.
    n=Number of halogenated compounds j in the batch front-end process 
    vent.
    m=Number of different halogens i in each compound j of the batch front-
    end process vent.
    
    Cavgj=Average annual concentration of halogenated compound j in 
    the batch front-end process vent, as determined by using Equation 17, 
    dry basis, ppmv.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.017
    
    where:
    
    DURi=Duration of type i batch emission episodes annually, hr/yr.
    Ci=Average concentration of halogenated compound j in type i batch 
    emission episode, ppmv.
    n=Number of types of batch emission episodes venting from the batch 
    front-end process vent.
        (3) The annual mass emissions of halogen atoms for an aggregate 
    batch vent stream shall be the sum of the annual mass emissions of 
    halogen atoms for all batch front-end process vents included in the 
    aggregate batch vent stream.
        (i) Process changes affecting Group 2 batch front-end process 
    vents. Whenever process changes, as described in paragraph (i)(1) of 
    this section, are made that affect one or more Group 2 batch front-end 
    process vents, the owner or operator shall comply with paragraphs 
    (i)(2) and (i)(3) of this section.
        (1) Examples of process changes include, but are not limited to, 
    changes in production capacity, production rate, feedstock type, or 
    catalyst type; or whenever there is replacement, removal, or 
    modification of recovery equipment considered part of the batch unit 
    operation as specified in paragraph (a)(2) of this section. An increase 
    in the annual number of batch cycles beyond the batch cycle limitation 
    constitutes a process change. For purposes of this paragraph, process 
    changes do not include: Process upsets; unintentional, temporary 
    process changes; and changes that are within the margin of variation on 
    which the original group determination was based.
        (2) For each batch front-end process vent affected by a process 
    change, the owner or operator shall redetermine the group status by 
    repeating the procedures specified in paragraphs (b) through (g) of 
    this section, as applicable. Alternatively, engineering assessment, as 
    described in paragraph (b)(6)(i) of this section, can be used to 
    determine the effects of the process change.
        (3) Based on the results of paragraph (i)(2) of this section, 
    owners or operators shall comply with either paragraph (i)(3) (i), 
    (ii), or (iii) of this section.
        (i) If the redetermination described in paragraph (i)(2) of this 
    section indicates that a Group 2 batch front-end process vent has 
    become a Group 1 batch front-end process vent as a result of the 
    process change, the owner or operator shall submit a report as 
    specified in Sec. 63.492(b) and shall comply with the Group 1 
    provisions in Sec. 63.487 through Sec. 63.492 in accordance with the 
    compliance schedule described in Sec. 63.506(e)(6)(iii)(D)(2).
        (ii) If the redetermination described in paragraph (i)(2) of this 
    section indicates that a Group 2 batch front-end process vent with 
    annual emissions less than the applicable level specified in paragraph 
    (d) of this section, and that is in compliance with Sec. 63.487(g), now 
    has annual emissions greater than or equal to the applicable level 
    specified by paragraph (d) of this section but remains a Group 2 batch 
    front-end process vent, the owner or operator shall submit a report as 
    specified in Sec. 63.492(c) and shall comply with Sec. 63.487(f) in 
    accordance with the compliance schedule required by 
    Sec. 63.506(e)(6)(iii)(D)(2).
        (iii) If the redetermination described in paragraph (i)(2) of this 
    section indicates no change in group status or no change in the 
    relation of annual emissions to the levels specified in paragraph (d) 
    of this section, the owner or operator is not required to submit a 
    report, as described in Sec. 63.492(d).
    
    
    Sec. 63.489  Batch front-end process vents--monitoring requirements.
    
        (a) General requirements. Each owner or operator of a batch front-
    end process vent or aggregate batch vent stream that uses a control 
    device to comply with the
    
    [[Page 46943]]
    
    requirements in Sec. 63.487(a)(2) or Sec. 63.487(b)(2) shall install 
    the monitoring equipment specified in paragraph (b) of this section.
        (1) This monitoring equipment shall be in operation at all times 
    when batch emission episodes, or portions thereof, that the owner or 
    operator has selected to control are vented to the control device, or 
    at all times when an aggregate batch vent stream is vented to the 
    control device.
        (2) The owner or operator shall operate control devices such that 
    monitored parameters remain above the minimum level or below the 
    maximum level, as appropriate, established as specified in paragraph 
    (e) of this section.
        (b) Batch front-end process vent and aggregate batch vent stream 
    monitoring parameters. The monitoring equipment specified in paragraphs 
    (b)(1) through (b)(8) of this section shall be installed as specified 
    in paragraph (a) of this section. The parameters to be monitored are 
    specified in Table 6 of this subpart.
        (1) Where an incinerator is used, a temperature monitoring device 
    equipped with a continuous recorder is required.
        (i) Where an incinerator other than a catalytic incinerator is 
    used, the temperature monitoring device shall be installed in the 
    firebox or in the ductwork immediately downstream of the firebox in a 
    position before any substantial heat exchange occurs.
        (ii) Where a catalytic incinerator is used, temperature monitoring 
    devices shall be installed in the gas stream immediately before and 
    after the catalyst bed.
        (2) Where a flare is used, a device (including, but not limited to, 
    a thermocouple, ultra-violet beam sensor, or infrared sensor) capable 
    of continuously detecting the presence of a pilot flame is required.
        (3) Where a boiler or process heater of less than 44 megawatts 
    design heat input capacity is used, a temperature monitoring device in 
    the firebox equipped with a continuous recorder is required. Any boiler 
    or process heater in which all batch front-end process vents or 
    aggregate batch vent streams are introduced with the primary fuel or 
    are used as the primary fuel is exempt from this requirement.
        (4) Where a scrubber is used with an incinerator, boiler, or 
    process heater in concert with the combustion of halogenated batch 
    front-end process vents, the following monitoring equipment is required 
    for the scrubber:
        (i) A pH monitoring device equipped with a continuous recorder to 
    monitor the pH of the scrubber effluent; and
        (ii) A flow meter equipped with a continuous recorder shall be 
    located at the scrubber influent to monitor the scrubber liquid flow 
    rate.
        (5) Where an absorber is used, a scrubbing liquid temperature 
    monitoring device and a specific gravity monitoring device are 
    required, each equipped with a continuous recorder.
        (6) Where a condenser is used, a condenser exit temperature 
    (product side) monitoring device equipped with a continuous recorder is 
    required.
        (7) Where a carbon adsorber is used, an integrating regeneration 
    stream flow monitoring device having an accuracy of 10 
    percent, capable of recording the total regeneration stream mass flow 
    for each regeneration cycle; and a carbon bed temperature monitoring 
    device, capable of recording the carbon bed temperature after each 
    regeneration and within 15 minutes of completing any cooling cycle are 
    required.
        (8) As an alternate to paragraphs (b)(5) through (b)(7) of this 
    section, the owner or operator may install an organic monitoring device 
    equipped with a continuous recorder.
        (c) Alternative monitoring parameters. An owner or operator of a 
    batch front-end process vent or aggregate batch vent stream may request 
    approval to monitor parameters other than those required by paragraph 
    (b) of this section. The request shall be submitted according to the 
    procedures specified in Sec. 63.506(f). Approval shall be requested if 
    the owner or operator:
        (1) Uses a control device other than those included in paragraph 
    (b) of this section; or
        (2) Uses one of the control devices included in paragraph (b) of 
    this section, but seeks to monitor a parameter other than those 
    specified in Table 6 of this subpart and paragraph (b) of this section.
        (d) Monitoring of bypass lines. The owner or operator of a batch 
    front-end process vent or aggregate batch vent stream using a vent 
    system that contains bypass lines that could divert emissions away from 
    a control device used to comply with Sec. 63.487(a) or Sec. 63.487(b) 
    shall comply with either paragraph (d)(1), (d)(2), or (d)(3) of this 
    section. Equipment such as low leg drains, high point bleeds, analyzer 
    vents, open-ended valves or lines, and pressure relief valves needed 
    for safety purposes are not subject to this paragraph.
        (1) Properly install, maintain, and operate a flow indicator that 
    takes a reading at least once every 15 minutes. Records shall be 
    generated as specified in Sec. 63.491(e)(3). The flow indicator shall 
    be installed at the entrance to any bypass line that could divert 
    emissions away from the control device and to the atmosphere; or
        (2) Secure the bypass line valve in the non-diverting position with 
    a car-seal or a lock-and-key type configuration. A visual inspection of 
    the seal or closure mechanism shall be performed at least once every 
    month to ensure that the valve is maintained in the non-diverting 
    position and emissions are not diverted through the bypass line. 
    Records shall be generated as specified in Sec. 63.491(e)(4).
        (3) Continuously monitor the bypass line damper or valve position 
    using computer monitoring and record any periods when the position of 
    the bypass line damper or valve has changed as specified in 
    Sec. 63.491(e)(4).
        (e) Establishment of parameter monitoring levels. Parameter 
    monitoring levels for batch front-end process vents and aggregate batch 
    vent streams shall be established as specified in paragraphs (e)(1) 
    through (e)(3) of this section.
        (1) For each parameter monitored under paragraph (b) of this 
    section, the owner or operator shall establish a level, defined as 
    either a maximum or minimum operating parameter as denoted in Table 7 
    of this subpart, that indicates proper operation of the control device. 
    The level shall be established in accordance with the procedures 
    specified in Sec. 63.505.
        (i) For batch front-end process vents using a control device to 
    comply with Sec. 63.487(a)(2), the established level shall reflect the 
    control efficiency established as part of the initial compliance 
    demonstration specified in Sec. 63.490(c)(2).
        (ii) For aggregate batch vent streams using a control device to 
    comply with Sec. 63.487(b)(2), the established level shall reflect the 
    control efficiency requirement specified in Sec. 63.487(b)(2).
        (2) The established level, along with supporting documentation, 
    shall be submitted in the Notification of Compliance Status or the 
    operating permit application as required in Sec. 63.506(e)(5) or 
    Sec. 63.506(e)(8), respectively.
        (3) The operating day shall be defined as part of establishing the 
    parameter monitoring level and shall be submitted with the information 
    in paragraph (e)(2) of this section. The definition of operating day 
    shall specify the times at which an operating day begins and ends. The 
    operating day shall not exceed 24 hours.
    
    [[Page 46944]]
    
    Sec. 63.490  Batch front-end process vents--performance test methods 
    and procedures to determine compliance.
    
        (a) Use of a flare. When a flare is used to comply with 
    Sec. 63.487(a)(1) or Sec. 63.487(b)(1), the owner or operator shall 
    comply with the flare provisions in Sec. 63.11(b) of subpart A.
        (b) Exceptions to performance tests. An owner or operator is not 
    required to conduct a performance test when a control device specified 
    in paragraphs (b)(1) through (b)(4) of this section is used to comply 
    with Sec. 63.487(a)(2).
        (1) A boiler or process heater with a design heat input capacity of 
    44 megawatts or greater.
        (2) A boiler or process heater where the vent stream is introduced 
    with the primary fuel or is used as the primary fuel.
        (3) A control device for which a performance test was conducted for 
    determining compliance with a new source performance standard (NSPS) 
    and the test was conducted using the same procedures specified in this 
    section and no process changes have been made since the test.
        (4) A boiler or process heater burning hazardous waste for which 
    the owner or operator:
        (i) Has been issued a final permit under 40 CFR part 270 and 
    complies with the requirements of 40 CFR part 266, subpart H; or
        (ii) Has certified compliance with the interim status requirements 
    of 40 CFR part 266, subpart H.
        (5) An incinerator burning hazardous waste for which the owner or 
    operator complies with the requirements of 40 CFR part 264, subpart O.
        (6) Performance tests done for other subparts in part 60 or part 63 
    where total organic HAP or TOC was measured, provided that the owner or 
    operator can demonstrate that operating conditions for the process and 
    control device during the performance test are representative of 
    current operating conditions.
        (c) Batch front-end process vent testing and procedures for 
    compliance with Sec. 63.487(a)(2). Except as provided in paragraph (b) 
    of this section, an owner or operator using a control device to comply 
    with Sec. 63.487(a)(2) shall conduct a performance test using the 
    procedures specified in paragraph (c)(1) of this section in order to 
    determine the control efficiency of the control device. An owner or 
    operator shall determine the percent reduction for the batch cycle 
    using the control efficiency of the control device as specified in 
    paragraphs (c)(2)(i) through (c)(2)(iii) of this section and the 
    procedures specified in paragraph (c)(2) of this section. Compliance 
    may be based on either total organic HAP or TOC. For purposes of this 
    paragraph and all paragraphs that are part of paragraph (c) of this 
    section, the term ``batch emission episode'' shall have the meaning 
    ``period of the batch emission episode selected for control,'' which 
    may be the entire batch emission episode or may only be a portion of 
    the batch emission episode.
        (1) Performance tests shall be conducted as specified in paragraphs 
    (c)(1)(i) through (c)(1)(v) of this section.
        (i) Except as specified in paragraph (c)(1)(i)(A) of this section, 
    a test shall be performed for the entire period of each batch emission 
    episode in the batch cycle that the owner or operator selects to 
    control as part of achieving the required 90 percent emission reduction 
    for the batch cycle specified in Sec. 63.487(a)(2). Only one test is 
    required for each batch emission episode selected by the owner or 
    operator for control. The owner or operator shall follow the procedures 
    listed in paragraphs (c)(1)(i)(B) through (c)(1)(i)(D) of this section.
        (A) Alternatively, an owner or operator may choose to test only 
    those periods of the batch emission episode during which the emission 
    rate for the entire episode can be determined or during which the 
    emissions are greater than the average emission rate of the batch 
    emission episode. The owner or operator choosing either of these 
    options must develop an emission profile for the entire batch emission 
    episode, based on either process knowledge or test data collected, to 
    demonstrate that test periods are representative. Examples of 
    information that could constitute process knowledge include 
    calculations based on material balances and process stoichiometry. 
    Previous test results may be used, provided the results are still 
    relevant to the current batch front-end process vent conditions.
        (B) Method 1 or 1A, as appropriate, shall be used for selection of 
    the sampling sites if the flow measuring device is a pitot tube. No 
    traverse is necessary when Method 2A or 2D is used to determine gas 
    stream volumetric flow rate. Inlet sampling sites shall be located as 
    specified in paragraphs (c)(1)(i)(B)(1) and (c)(1)(i)(B)(2) of this 
    section. Outlet sampling sites shall be located at the outlet of the 
    final control device prior to release to the atmosphere.
        (1) The control device inlet sampling site shall be located at the 
    exit from the batch unit operation before any control device. Section 
    63.488(a)(2) describes those recovery devices considered part of the 
    unit operation. Inlet sampling sites would be after these specified 
    recovery devices.
        (2) If a batch process vent is introduced with the combustion air 
    or as a secondary fuel into a boiler or process heater with a design 
    capacity less than 44 megawatts, selection of the location of the inlet 
    sampling sites shall ensure the measurement of total organic HAP or TOC 
    (minus methane and ethane) concentrations in all batch front-end 
    process vents and primary and secondary fuels introduced into the 
    boiler or process heater.
        (C) Gas stream volumetric flow rate and/or average flow rate shall 
    be determined as specified in Sec. 63.488(e).
        (D) Method 18 or Method 25A of 40 CFR part 60, Appendix A, shall be 
    used to determine the concentration of organic HAP or TOC, as 
    appropriate. The use of Method 25A shall comply with paragraphs 
    (c)(1)(i)(D)(1) and (c)(1)(i)(D)(2) of this section.
        (1) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (2) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (ii) If an integrated sample is taken over the entire batch 
    emission episode to determine TOC or average total organic HAP 
    concentration, emissions per batch emission episode shall be calculated 
    using Equations 18 and 19.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.018
    
    
    [[Page 46945]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.019
    
    
    where:
    
    Eepisode=Inlet or outlet emissions, kg/episode.
    K=Constant, 2.494  x  10-6 (ppmv)-1 (gm-mole/scm) (kg/gm) 
    (min/hr), where standard temperature is 20 deg.C.
    Cj=Average inlet or outlet concentration of TOC or sample 
    component j of the gas stream for the batch emission episode, dry 
    basis, ppmv.
    Mj=Molecular weight of TOC or sample component j of the gas 
    stream, gm/gm-mole.
    AFR=Average inlet or outlet flow rate of gas stream for the batch 
    emission episode, dry basis, scmm.
    Th=Hours/episode.
    n=Number of organic HAP in stream. Note: Summation not required if TOC 
    emissions are being estimated using a TOC concentration measured using 
    Method 25A.
    
        (iii) If grab samples are taken to determine TOC or total organic 
    HAP concentration, emissions shall be calculated according to 
    paragraphs (c)(1)(iii)(A) and (c)(1)(iii)(B) of this section.
        (A) For each measurement point, the emission rates shall be 
    calculated using Equations 20 and 21.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.020
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.050
    
    where:
    
    Epoint=Inlet or outlet emission rate for the measurement point, 
    kg/hr.
    K=Constant, 2.494 x 10-6 (ppmv)-1 (gm-mole/scm) (kg/gm) (min/
    hr), where standard temperature is 20 deg.C.
    Cj=Inlet or outlet concentration of TOC or sample organic HAP 
    component j of the gas stream, dry basis, ppmv.
    Mj=Molecular weight of TOC or sample organic HAP component j of 
    the gas stream, gm/gm-mole.
    FR=Inlet or outlet flow rate of gas stream for the measurement point, 
    dry basis, scmm.
    n=Number of organic HAP in stream.
    
        Note: Summation not required if TOC emissions are being 
    estimated using a TOC concentration measured using Method 25A.
    
        (B) The emissions per batch emission episode shall be calculated 
    using Equations 22 and 23.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.021
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.022
    
    where:
    
    Eepisode=Inlet or outlet emissions, kg/episode.
    DUR=Duration of the batch emission episode, hr/episode.
    Epoint,i=Inlet or outlet emissions for measurement point i, kg/hr.
    n=Number of measurements.
    
        (iv) The control efficiency for the control device shall be 
    calculated using Equation 24.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.023
    
    Where:
    
    R=Control efficiency of control device, percent.
    Einleti=Mass rate of TOC or total organic HAP for batch emission 
    episode i at the inlet to the control device as calculated under 
    paragraph (c)(1)(ii) or (c)(1)(iii) of this section, kg/hr.
    Eoutleti=Mass rate of TOC or total organic HAP for batch emission 
    episode i at the outlet of the control device, as calculated under 
    paragraph (c)(1)(ii) or (c)(1)(iii) of this section, kg/hr.
    n=Number of batch emission episodes in the batch cycle selected to be 
    controlled.
    
        (v) If the batch front-end process vent entering a boiler or 
    process heater with a design capacity less than 44 megawatts is 
    introduced with the combustion air or as a secondary fuel, the weight-
    percent reduction of total organic HAP or TOC across the device shall 
    be determined by comparing the TOC or total organic HAP in all 
    combusted batch front-end process vents and primary and secondary fuels 
    with the TOC or total organic HAP exiting the combustion device, 
    respectively.
        (2) The percent reduction for the batch cycle shall be determined 
    using Equation 25 and the control device efficiencies specified in 
    paragraphs (c)(2)(i) through (c)(2)(iii) of this section. All 
    information used to calculate the batch cycle percent reduction, 
    including a definition of the batch cycle identifying all batch 
    emission episodes, must be recorded as specified in Sec. 63.491(b)(2). 
    This information shall include identification of those batch emission 
    episodes, or portions thereof, selected for control.
    
    [[Page 46946]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.024
    
    
    where:
    Eunc=Mass rate of TOC or total organic HAP for uncontrolled batch 
    emission episode i, kg/hr.
    Einletcon=Mass rate of TOC or total organic HAP for controlled 
    batch emission episode i at the inlet to the control device, kg/hr.
    R=Control efficiency of control device as specified in paragraphs 
    (c)(2)(i) through (c)(2)(iii) of this section.
    n=Number of uncontrolled batch emission episodes, controlled batch 
    emission episodes, and control devices. The value of n is not 
    necessarily the same for these three items.
        (i) If a performance test is required by paragraph (c) of this 
    section, the control efficiency of the control device shall be as 
    determined in paragraph (c)(1)(iv) of this section.
        (ii) If a performance test is not required by paragraph (c) of this 
    section for a combustion control device, as specified in paragraph (b) 
    of this section, the control efficiency of the control device shall be 
    98 percent. The control efficiency for a flare shall be 98 percent.
        (iii) If a performance test is not required by paragraph (c) of 
    this section for a noncombustion control device, the control efficiency 
    shall be determined by the owner or operator based on engineering 
    assessment.
        (d) Batch process vent and aggregate batch vent stream testing for 
    compliance with Sec. 63.487(c) [halogenated emission streams]. An owner 
    or operator controlling halogenated emissions in compliance with 
    Sec. 63.487(c) shall conduct a performance test to determine compliance 
    with the control efficiency specified in Sec. 63.487(c)(1) or the 
    emission limit specified in Sec. 63.487(c)(2) for hydrogen halides and 
    halogens.
        (1) Sampling sites shall be located at the inlet and outlet of the 
    scrubber or other control device used to reduce halogen emissions in 
    complying with Sec. 63.487(c)(1) or at the outlet of the control device 
    used to reduce halogen emissions in complying with Sec. 63.487(c)(2).
        (2) The mass emissions of each hydrogen halide and halogen compound 
    for the batch cycle or aggregate batch vent stream shall be calculated 
    from the measured concentrations and the gas stream flow rate(s) 
    determined by the procedures specified in paragraphs (d)(2)(i) and 
    (d)(2)(ii) of this section, except as specified in paragraph (d)(5) of 
    this section.
        (i) Method 26 or Method 26A of 40 CFR part 60, appendix A, shall be 
    used to determine the concentration, in Mg per dry scm, of total 
    hydrogen halides and halogens present in the emissions stream.
        (ii) Gas stream volumetric flow rate and/or average flow rate shall 
    be determined as specified in Sec. 63.488(e).
        (3) To determine compliance with the percent reduction specified in 
    Sec. 63.487(c)(1), the mass emissions for any hydrogen halides and 
    halogens present at the inlet of the scrubber or other control device 
    shall be summed together. The mass emissions of any hydrogen halides or 
    halogens present at the outlet of the scrubber or other control device 
    shall be summed together. Percent reduction shall be determined by 
    subtracting the outlet mass emissions from the inlet mass emissions and 
    then dividing the result by the inlet mass emissions.
        (4) To determine compliance with the emission limit specified in 
    Sec. 63.487(c)(2), the annual mass emissions for any hydrogen halides 
    and halogens present at the outlet of the control device and prior to 
    any combustion device shall be summed together and compared to the 
    emission limit specified in Sec. 63.487(c)(2).
        (5) The owner or operator may use any other method to demonstrate 
    compliance if the method or data has been validated according to the 
    applicable procedures of Method 301 of appendix A.
        (e) Aggregate batch vent stream testing for compliance with 
    Sec. 63.487(b)(2). Owners or operators of aggregate batch vent streams 
    complying with Sec. 63.487(b)(2) shall conduct a performance test using 
    the performance testing procedures for continuous front-end process 
    vents in Sec. 63.116(c) of subpart G. For the purposes of this subpart, 
    when the provisions of Sec. 63.116(c) specify that Method 18 shall be 
    used, Method 18 or Method 25A may be used. The use of Method 25A shall 
    comply with paragraphs (e)(1) and (e)(2) of this section.
        (1) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (2) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (f) Batch cycle limitation. The batch cycle limitation required by 
    Sec. 63.487(f)(1) and Sec. 63.487(g)(1) shall be established as 
    specified in paragraph (f)(1) of this section and shall include the 
    elements specified in paragraph (f)(2) of this section.
        (1) The batch cycle limitation shall be determined by the owner or 
    operator such that annual emissions for the batch front-end process 
    vent remain less than the level specified in Sec. 63.488(d) when 
    complying with Sec. 63.487(g). Alternatively, when complying with 
    Sec. 63.487(f), the batch cycle limitation shall ensure that annual 
    emissions remain at a level such that the batch front-end process vent 
    remains a Group 2 batch front-end process vent, given the actual annual 
    flow rate for that batch front-end process vent determined according to 
    Sec. 63.488(e)(3). The batch cycle limitation shall be determined using 
    the same basis, as described in Sec. 63.488(a)(1), used to make the 
    group determination (i.e., expected mix of products or worst-case HAP 
    emitting product). The establishment of the batch cycle limitation is 
    not dependent upon any past production or activity level.
        (i) If the expected mix of products serves as the basis for the 
    batch cycle limitation, the batch cycle limitation shall be determined 
    such that any foreseeable combination of products which the owner or 
    operator desires the flexibility to manufacture shall be allowed. 
    Combinations of products not accounted for in the documentation 
    required by paragraph (f)(2)(iv) of this section shall not be allowed 
    within the restrictions of the batch cycle limitation.
        (ii) If, for a batch front-end process vent with more than one 
    product, a single worst-case HAP emitting product serves as the basis 
    for the batch cycle limitation, the batch cycle limitation shall be 
    determined such that the maximum number of batch cycles the owner or 
    operator desires the flexibility to accomplish, using the worst-case
    
    [[Page 46947]]
    
    HAP emitting product and ensuring that the batch front-end process vent 
    remains a Group 2 batch front-end process vent or that emissions remain 
    less than the level specified in Sec. 63.488(d), shall be allowed. This 
    value shall be the total number of batch cycles allowed within the 
    restrictions of the batch cycle limitation regardless of which products 
    are manufactured.
        (2) Documentation supporting the establishment of the batch cycle 
    limitation shall include the information specified in paragraphs 
    (f)(2)(i) through (f)(2)(v) of this section, as appropriate.
        (i) Identification that the purpose of the batch cycle limitation 
    is to comply with Sec. 63.487(f)(1) or (g)(1).
        (ii) Identification that the batch cycle limitation is based on a 
    single worst-case HAP emitting product or on the expected mix of 
    products for the batch front-end process vent as allowed under 
    Sec. 63.488(a)(1).
        (iii) Definition of the operating year, for the purposes of 
    determining compliance with the batch cycle limitation.
        (iv) If the batch cycle limitation is based on a single worst-case 
    HAP emitting product, documentation specified in Sec. 63.488(a)(1)(ii) 
    describing how the single product meets the requirements for worst-case 
    HAP emitting product, as specified in Sec. 63.488(a)(1) and the number 
    of batch cycles allowed under the batch cycle limitation for each 
    product associated with the batch front-end process vent are required.
        (v) If the batch cycle limitation is based on the expected mix of 
    products, the owner or operator shall provide documentation that 
    describes as many scenarios for differing mixes of products (i.e., how 
    many of each type of product) that the owner or operator desires the 
    flexibility to accomplish. Alternatively, the owner or operator shall 
    provide a description of the relationship among the mix of products 
    that will allow a determination of compliance with the batch cycle 
    limitation under an infinite number of scenarios. For example, if a 
    batch process vent has two products, each product has the same flow 
    rate and emits for the same amount of time, and product No. 1 has twice 
    the emissions as product No. 2, the relationship describing an infinite 
    number of scenarios would be that the owner or operator can accomplish 
    two batch cycles of product No. 2 for each batch cycle of product No. 1 
    within the restriction of the batch cycle limitation.
    
    
    Sec. 63.491  Batch front-end process vents--recordkeeping requirements.
    
        (a) Group determination records for batch front-end process vents. 
    Except as provided in paragraphs (a)(7) through (a)(9) of this section, 
    each owner or operator of an affected source shall maintain the records 
    specified in paragraphs (a)(1) through (a)(6) of this section for each 
    batch front-end process vent subject to the group determination 
    procedures of Sec. 63.488. Except for paragraph (a)(1) of this section, 
    the records required to be maintained by this paragraph are limited to 
    the information developed and used to make the group determination 
    under Sec. 63.488(b) through Sec. 63.488(g), as appropriate. The 
    information required by paragraph (a)(1) of this section is required 
    for all batch front-end process vents subject to the group 
    determination procedures of Sec. 63.488. If an owner or operator did 
    not need to develop certain information (e.g., annual average flow 
    rate) to determine the group status, this paragraph does not require 
    that additional information be developed.
        (1) An identification of each unique product that has emissions 
    from one or more batch emission episodes venting from the batch front-
    end process vent.
        (2) A description of, and an emission estimate for, each batch 
    emission episode, and the total emissions associated with one batch 
    cycle for each unique product identified in paragraph (a)(1) of this 
    section that was considered in making the group determination under 
    Sec. 63.488.
        (3) Total annual uncontrolled TOC or organic HAP emissions, 
    determined at the exit from the batch unit operation before any 
    emission control, as determined in accordance with Sec. 63.488(b).
        (i) For Group 2 batch front-end process vents, emissions shall be 
    determined at the batch cycle limitation.
        (ii) For Group 1 batch front-end process vents, emissions shall be 
    those used to determine the group status of the batch front-end process 
    vent.
        (4) The annual average flow rate for the batch front-end process 
    vent as determined in accordance with Sec. 63.488(e).
        (5) The cutoff flow rate, determined in accordance with 
    Sec. 63.488(f).
        (6) The results of the batch front-end process vent group 
    determination, conducted in accordance with Sec. 63.488(g).
        (7) If a batch front-end process vent is in compliance with 
    Sec. 63.487(a) or Sec. 63.487(b), and the control device is operating 
    at all times when batch emission episodes are venting from the batch 
    front-end process vent, none of the records in paragraphs (a)(1) 
    through (a)(6) of this section are required.
        (8) If a batch front-end process vent is in compliance with 
    Sec. 63.487(a) or Sec. 63.487(b), but the control device is operated 
    only during selected batch emission episodes, only the records in 
    paragraphs (a)(1) through (a)(3) of this section are required.
        (9) If the total annual emissions from the batch front-end process 
    vent are less than the appropriate level specified in Sec. 63.488(d), 
    only the records in paragraphs (a)(1) through (a)(3) of this section 
    are required.
        (b) Compliance demonstration records. Each owner or operator of a 
    batch front-end process vent or aggregate batch vent stream complying 
    with Sec. 63.487(a) or (b), shall keep the following records, as 
    applicable, up-to-date and readily accessible:
        (1) The annual mass emissions of halogen atoms in the batch front-
    end process vent or aggregate batch vent stream determined according to 
    the procedures specified in Sec. 63.488(h)(2).
        (2) If a batch front-end process vent is in compliance with 
    Sec. 63.487(a)(2), records documenting the batch cycle percent 
    reduction as specified in Sec. 62.486-4(c)(2).
        (3) When using a flare to comply with Sec. 63.487(a)(1):
        (i) The flare design (i.e., steam-assisted, air-assisted, or non-
    assisted);
        (ii) All visible emission readings, heat content determinations, 
    flow rate measurements, and exit velocity determinations made during 
    the compliance determination required by Sec. 63.11(b) of subpart A; 
    and
        (iii) All periods during the compliance determination required by 
    Sec. 63.11(b) of subpart A when the pilot flame is absent.
        (4) The following information when using a control device to 
    achieve compliance with Sec. 63.487(a)(2) or (b)(2):
        (i) For an incinerator or non-combustion control device, the 
    percent reduction of organic HAP or TOC achieved, as determined using 
    the procedures specified in Sec. 63.490(c) for batch front-end process 
    vents and Sec. 63.490(e) for aggregate batch vent streams;
        (ii) For a boiler or process heater, a description of the location 
    at which the vent stream is introduced into the boiler or process 
    heater;
        (iii) For a boiler or process heater with a design heat input 
    capacity of less than 44 megawatts and where the process vent stream is 
    introduced with combustion air or is used as a secondary fuel and is 
    not mixed with the primary fuel, the percent reduction of organic HAP 
    or TOC achieved, as determined
    
    [[Page 46948]]
    
    using the procedures specified in Sec. 63.490(c) for batch front-end 
    process vents and Sec. 63.490(e) for aggregate batch vent streams; and
        (iv) For a scrubber or other control device following a combustion 
    device to control a halogenated batch front-end process vent or 
    halogenated aggregate batch vent stream, the percent reduction of total 
    hydrogen halides and halogens, as determined under Sec. 63.490(d)(3) or 
    the emission limit determined under Sec. 63.490(d)(4).
        (c) Establishment of parameter monitoring level records. For each 
    parameter monitored according to Sec. 63.489(b) and Table 6 of this 
    subpart, or for alternate parameters and/or parameters for alternate 
    control devices monitored according to Sec. 63.492(e) as allowed under 
    Sec. 63.489(c), maintain documentation showing the establishment of the 
    level that indicates proper operation of the control device as required 
    by Sec. 63.489(e) for parameters specified in Sec. 63.489(b) and as 
    required by Sec. 63.506(f) for alternate parameters. This documentation 
    shall include the parameter monitoring data used to establish the 
    level.
        (d) Group 2 batch front-end process vent continuous compliance 
    records. The owner or operator of a Group 2 batch front-end process 
    vent shall comply with either paragraph (d)(1) or (d)(2) of this 
    section, as appropriate.
        (1) The owner or operator of a Group 2 batch front-end process vent 
    complying with Sec. 63.487(g) shall keep the following records up-to-
    date and readily accessible:
        (i) Records designating the established batch cycle limitation 
    required by Sec. 63.487(g)(1) and specified in Sec. 63.490(f).
        (ii) Records specifying the number and type of batch cycles 
    accomplished.
        (2) The owner or operator of a Group 2 batch front-end process vent 
    complying with Sec. 63.487(f) shall keep the following records up-to-
    date and readily accessible:
        (i) Records designating the established batch cycle limitation 
    required by Sec. 63.487(f)(1) and specified in Sec. 63.490(f).
        (ii) Records specifying the number and type of batch cycles 
    accomplished for each three month period.
        (e) Controlled batch front-end process vent continuous compliance 
    records. Each owner or operator of a batch front-end process vent that 
    uses a control device to comply with Sec. 63.487(a) shall keep the 
    following records up-to-date and readily accessible:
        (1) Continuous records of the equipment operating parameters 
    specified to be monitored under Sec. 63.489(b) as applicable, and 
    listed in Table 6 of this subpart, or specified by the Administrator in 
    accordance with Sec. 63.492(e) as allowed under Sec. 63.489(c). These 
    records shall be kept as specified under Sec. 63.506(d), except as 
    specified in paragraphs (e)(1)(i) and (e)(1)(ii) of this section.
        (i) For flares, the records specified in Table 6 of this subpart 
    shall be kept rather than averages.
        (ii) For carbon adsorbers, the records specified in Table 6 of this 
    subpart shall be kept rather than averages.
        (2) Records of the batch cycle daily average value of each 
    continuously monitored parameter, except as provided in paragraphs 
    (e)(2)(iii) of this section, as calculated using the procedures 
    specified in paragraphs (e)(2)(i) through (e)(2)(ii) of this section.
        (i) The batch cycle daily average shall be calculated as the 
    average of all parameter values measured during those batch emission 
    episodes, or portions thereof, in the batch cycle that the owner or 
    operator has selected to control.
        (ii) Monitoring data recorded during periods of monitoring system 
    breakdowns, repairs, calibration checks, and zero (low-level) and high-
    level adjustments shall not be included in computing the batch cycle 
    daily averages.
        (iii) If all recorded values for a monitored parameter during an 
    operating day are above the minimum or below the maximum level 
    established in accordance with Sec. 63.489(e), the owner or operator 
    may record that all values were above the minimum or below the maximum 
    level established, rather than calculating and recording a batch cycle 
    daily average for that operating day.
        (3) Hourly records of whether the flow indicator for bypass lines 
    specified under Sec. 63.489(d)(1) was operating and whether flow was 
    detected at any time during the hour. Also, records of the times and 
    durations of all periods when the vent is diverted from the control 
    device, or the flow indicator specified in Sec. 63.489(d)(1) is not 
    operating.
        (4) Where a seal or closure mechanism is used to comply with 
    Sec. 63.489(d)(2) or where computer monitoring of the position of the 
    bypass damper or valve is used to comply with Sec. 63.489(d)(3), hourly 
    records of flow are not required.
        (i) For compliance with Sec. 63.489(d)(2), the owner or operator 
    shall record whether the monthly visual inspection of the seals or 
    closure mechanism has been done, and shall record the occurrence of all 
    periods when the seal mechanism is broken, the bypass line valve 
    position has changed, or the key for a lock-and-key type configuration 
    has been checked out, and records of any car-seal that has been broken.
        (ii) For compliance with Sec. 63.489(d)(3), the owner or operator 
    shall record the times of all periods when the bypass line valve 
    position has changed.
        (5) Records specifying the times and duration of periods of 
    monitoring system breakdowns, repairs, calibration checks, and zero 
    (low-level) and high level adjustments. In addition, records specifying 
    any other periods of process or control device operation when monitors 
    are not operating.
        (f) Aggregate batch vent stream continuous compliance records. In 
    addition to the records specified in paragraphs (b) and (c) of this 
    section, each owner or operator of an aggregate batch vent stream using 
    a control device to comply with Sec. 63.487(b) shall keep records in 
    accordance with the requirements for continuous process vents in 
    Sec. 63.118(a) and Sec. 63.118(b) of subpart G, as applicable and 
    appropriate, except that when complying with Sec. 63.118(b), owners or 
    operators shall disregard statements concerning TRE index values for 
    the purposes of this subpart.
    
    
    Sec. 63.492   Batch front-end process vents--reporting requirements.
    
        (a) The owner or operator of a batch front-end process vent at an 
    affected source shall submit the information specified in paragraphs 
    (a)(1) through (a)(4) of this section, as appropriate, as part of the 
    Notification of Compliance Status specified in Sec. 63.506(e)(5).
        (1) For each batch front-end process vent complying with 
    Sec. 63.487(a) and each aggregate batch vent stream complying with 
    Sec. 63.487(b), the information specified in Sec. 63.491(b) and 
    Sec. 63.491(c), as applicable.
        (2) For each Group 2 batch front-end process vent with annual 
    emissions less than the level specified in Sec. 63.488(d), the 
    information specified in Sec. 63.491(d)(1)(i).
        (3) For each Group 2 batch front-end process vent with annual 
    emissions greater than or equal to the level specified in 
    Sec. 63.488(d), the information specified in Sec. 63.491(d)(2)(i).
        (4) For each batch process vent subject to the group determination 
    procedures, the information specified in Sec. 63.491(a), as 
    appropriate.
        (b) Whenever a process change, as defined in Sec. 63.488(i)(1), is 
    made that causes a Group 2 batch front-end process vent to become a 
    Group 1 batch front-end process vent, the owner or operator shall 
    submit a report within 180 operating days after the process
    
    [[Page 46949]]
    
    change is made or the information regarding the process change is known 
    to the owner or operator. This report may be included in the next 
    Periodic Report, as specified in Sec. 63.506(e)(6)(iii)(D)(2). The 
    following information shall be submitted:
        (1) A description of the process change; and
        (2) A schedule for compliance with the provisions of Sec. 63.487(a) 
    or Sec. 63.487(b), as appropriate, as required under 
    Sec. 63.506(e)(6)(iii)(D)(2).
        (c) Whenever a process change, as defined in Sec. 63.488(i)(1), is 
    made that causes a Group 2 batch front-end process vent with annual 
    emissions less than the level specified in Sec. 63.488(d) that is in 
    compliance with Sec. 63.487(g) to have annual emissions greater than or 
    equal to the levels specified in Sec. 63.488(d) but remains a Group 2 
    batch front-end process vent, the owner or operator shall submit a 
    report within 180 operating days after the process change is made or 
    the information regarding the process change is known to the owner or 
    operator. This report may be included in the next Periodic Report, as 
    specified in Sec. 63.506(e)(6)(iii)(D)(2). The following information 
    shall be submitted:
        (1) A description of the process change;
        (2) The results of the redetermination of the annual emissions, 
    average flow rate, and cutoff flow rate required under Sec. 63.488(f) 
    and recorded under Sec. 63.491 (a)(3) through (a)(5); and
        (3) The batch cycle limitation determined in accordance with 
    Sec. 63.487(f)(1).
        (d) The owner or operator is not required to submit a report of a 
    process change if one of the conditions specified in paragraphs (d)(1) 
    and (d)(2) of this section is met.
        (1) The process change does not meet the description of a process 
    change in Sec. 63.488(i).
        (2) The redetermined group status remains Group 2 for an individual 
    batch front-end process vent with annual emissions greater than or 
    equal to the level specified in Sec. 63.488(d), or a Group 2 batch 
    front-end process vent with annual emissions less than the level 
    specified in Sec. 63.488(d) complying with Sec. 63.487(g) continues to 
    have emissions less than the level specified in Sec. 63.488(d).
        (e) If an owner or operator uses a control device other than those 
    specified in Sec. 63.489(b) and listed in Table 6 of this subpart or 
    requests approval to monitor a parameter other than those specified in 
    Sec. 63.489(c) and listed in Table 6 of this subpart, the owner or 
    operator shall submit a description of planned reporting and 
    recordkeeping procedures, as specified in Sec. 63.506(f), as part of 
    the Precompliance Report as required under Sec. 63.506(e)(3). The 
    Administrator will specify appropriate reporting and recordkeeping 
    requirements as part of the review of the Precompliance Report.
        (f) Owners or operators complying with Sec. 63.489(d), shall comply 
    with paragraph (f)(1) or (f)(2) of this section, as appropriate.
        (1) Reports of the times of all periods recorded under 
    Sec. 63.491(e)(3) when the batch front-end process vent is diverted 
    away from the control device through a bypass line.
        (2) Reports of all occurrences recorded under Sec. 63.491(e)(4) in 
    which the seal mechanism is broken, the bypass line valve position has 
    changed, or the key to unlock the bypass line valve was checked out.
    
    
    Sec. 63.493   Back-end process provisions.
    
        Owners and operators of new and existing affected sources shall 
    comply with the requirements in Sec. 63.494 through Sec. 63.500. Owners 
    and operators of affected sources that produce only latex products, 
    liquid rubber products, or products in a gas-phased polymerization 
    reaction are not subject to the provisions of these sections. Section 
    63.494 contains residual organic HAP limitations. Compliance with these 
    residual organic HAP limitations may be achieved by using either 
    stripping technology, or by using control or recovery devices. If 
    compliance with these limitations is achieved using stripping 
    technology, the procedures to determine compliance are specified in 
    Sec. 63.495. If compliance with these limitations is achieved using 
    control or recovery devices, the procedures to determine compliance are 
    specified in Sec. 63.496, and associated monitoring requirements are 
    specified in Sec. 63.497. Recordkeeping requirements are contained in 
    Sec. 63.498, and reporting requirements in Sec. 63.499. Section 63.500 
    contains a limitation on carbon disulfide emissions from affected 
    sources that produce styrene butadiene rubber using an emulsion 
    process. Table 8 contains a summary of compliance alternative 
    requirements for these sections.
    
    
    Sec. 63.494   Back-end process provisions--residual organic HAP 
    limitations.
    
        (a) The monthly weighted average residual organic HAP content of 
    all grades of elastomer processed, measured immediately after the 
    stripping operation [or the reactor(s) if the plant has no stripper(s)] 
    is completed, shall not exceed the limits provided in paragraphs (a)(1) 
    through (a)(4) of this section, as applicable. Owners or operators 
    shall comply with the requirements of this paragraph using either 
    stripping technology or control/recovery devices.
        (1) For styrene butadiene rubber produced by the emulsion process:
        (i) A monthly weighted average of 0.40 kg styrene per megagram (Mg) 
    latex for existing sources; and
        (ii) A monthly weighted average of 0.23 kg styrene per Mg latex for 
    new sources;
        (2) For polybutadiene rubber and styrene butadiene rubber produced 
    by the solution process:
        (i) A monthly weighted average of 10 kg total organic HAP per Mg 
    crumb rubber (dry weight) for existing sources; and
        (ii) A monthly weighted average of 6 kg total organic HAP per Mg 
    crumb rubber (dry weight) for new sources.
        (3) For ethylene-propylene rubber produced by the solution process:
        (i) A monthly weighted average of 8 kg total organic HAP per Mg 
    crumb rubber (dry weight) for existing sources; and
        (ii) A monthly weighted average of 5 kg total organic HAP per Mg 
    crumb rubber (dry weight) for new sources.
        (4) There are no back-end process operation residual organic HAP 
    limitations for neoprene, Hypalon TM, nitrile butadiene rubber, 
    butyl rubber, halobutyl rubber, epichlorohydrin elastomer, and 
    polysulfide rubber.
        (5) For EPPU that produce both an elastomer product with a residual 
    organic HAP limitation listed in this section, and a product listed in 
    paragraphs (a)(5) (i) through (iv) of this section, only the residual 
    HAP content of the elastomer product with a residual organic HAP 
    limitation shall be used in determining the monthly average residual 
    organic HAP content.
        (i) Resins;
        (ii) Liquid rubber products;
        (iii) Latexes from which crumb rubber is not coagulated; or
        (iii) Elastomer products listed in paragraph (a)(4) of this 
    section.
        (b) If an owner or operator complies with the residual organic HAP 
    limitations in paragraph (a) of this section using stripping 
    technology, compliance shall be demonstrated in accordance with 
    Sec. 63.495. The owner or operator shall also comply with the 
    recordkeeping provisions in Sec. 63.498, and the reporting provisions 
    in Sec. 63.499.
        (c) If an owner or operator complies with the residual organic HAP 
    limitations in paragraph (a) of this section using control or recovery 
    devices, compliance shall be
    
    [[Page 46950]]
    
    demonstrated using the procedures in Sec. 63.496. The owner or operator 
    shall also comply with the monitoring provisions in Sec. 63.497, the 
    recordkeeping provisions in Sec. 63.498, and the reporting provisions 
    in Sec. 63.499.
    
    
    Sec. 63.495  Back-end process provisions--procedures to determine 
    compliance using stripping technology.
    
        (a) If an owner or operator complies with the residual organic HAP 
    limitations in Sec. 63.494(a) using stripping technology, compliance 
    shall be demonstrated using the periodic sampling procedures in 
    paragraph (b) of this section, or using the stripper parameter 
    monitoring procedures in paragraph (c) of this section. The owner or 
    operator shall determine the monthly weighted average residual organic 
    HAP content for each month in which any portion of the back-end of an 
    elastomer production process is in operation. A single monthly weighted 
    average shall be determined for all back-end process operations at the 
    affected source.
        (b) If the owner or operator is demonstrating compliance using 
    periodic sampling, this demonstration shall be in accordance with 
    paragraphs (b)(1) through (b)(5) of this section,
        (1) The location of the sampling shall be in accordance with 
    paragraph (d) of this section.
        (2) The frequency of the sampling shall be in accordance with 
    paragraphs (b)(2)(i) or (b)(2)(ii) of this section.
        (i) If batch stripping is used, at least one representative sample 
    is to be taken from every batch of elastomer produced, at the location 
    specified in paragraph (d) of this section, and identified by elastomer 
    type and by the date and time the batch is completed.
        (ii) If continuous stripping is used, at least one representative 
    sample is to be taken each operating day. The sample is to be taken at 
    the location specified in paragraph (d) of this section, and identified 
    by elastomer type and by the date and time the sample was taken.
        (3) The residual organic HAP content in each sample is to be 
    determined using specified methods.
        (4) The quantity of material (weight of latex or dry crumb rubber) 
    represented by each sample shall be recorded. Acceptable methods of 
    determining this quantity are production records, measurement of stream 
    characteristics, and engineering calculations.
        (5) The monthly weighted average shall be determined using the 
    equation in paragraph (f) of this section. All samples taken and 
    analyzed during the month shall be used in the determination of the 
    monthly weighted average.
        (c) If the owner or operator is demonstrating compliance using 
    stripper parameter monitoring, this demonstration shall be in 
    accordance with paragraphs (c)(1) through (c)(4) of this section.
        (1) The owner or operator shall establish stripper operating 
    parameter levels for each grade in accordance with Sec. 63.505(e).
        (2) The owner or operator shall monitor the stripper operating 
    parameters at all times the stripper is in operation. Readings of each 
    parameter shall be made at intervals no greater than 15 minutes.
        (3) The residual organic HAP content for each grade shall be 
    determined in accordance with either paragraph (c)(3)(i) or (c)(3)(ii) 
    of this section.
        (i) If during the processing of a grade in the stripper, all hourly 
    average parameter values are in accordance with operating parameter 
    levels established in paragraph (c)(1) of this section, the owner or 
    operator shall use the residual organic HAP content determined in 
    accordance with Sec. 63.505(e)(1).
        (ii) If during the processing of a grade in the stripper, the 
    hourly average of any stripper monitoring parameter is not in 
    accordance with an established operating parameter level, the residual 
    organic HAP content shall be determined using the procedures in 
    paragraphs (b)(1) and (b)(3) of this section.
        (4) The monthly weighted average shall be determined using the 
    equation in paragraph (f) of this section.
        (d) The location of the sampling shall be in accordance with 
    paragraph (d)(1) or (d)(2) of this section.
        (1) For styrene butadiene rubber produced by the emulsion process, 
    the sample shall be a sample of the latex taken at the location 
    specified in either paragraph (d)(1)(i), (d)(1)(ii), or (d)(1)(iii) of 
    this section.
        (i) When the latex is not blended with other materials or latexes, 
    the sample shall be taken at a location meeting all of the following 
    criteria:
        (A) After the stripping operation,
        (B) Prior to entering the coagulation operations, and
        (C) Before the addition of carbon black or oil extenders.
        (ii) When two or more latexes subject to this subpart are blended, 
    samples may be taken in accordance with either paragraph (d)(1)(ii) (A) 
    or (B) of this section, at a location meeting the requirements of 
    paragraphs (d)(1)(i) (A) through (C) of this section.
        (A) Individual samples may be taken of each latex prior to 
    blending, or
        (B) A sample of the blended latex may be taken.
        (iii) When a latex subject to this subpart is blended with a latex 
    or material not subject to this subpart, a sample shall be taken of the 
    latex prior to blending at a location meeting the requirements of 
    paragraphs (d)(1)(i) (A) through (C) of this section.
        (2) For styrene butadiene rubber produced by the solution process, 
    polybutadiene rubber produced by the solution process, and ethylene-
    propylene rubber produced by the solution process, the sample shall be 
    a sample of crumb rubber taken as soon as safe and feasible after the 
    stripping operation, but no later than the entry point for the first 
    unit operation following the stripper (e.g., the dewatering screen).
        (e) Reserved.
        (f) The monthly weighted average residual organic HAP content shall 
    be calculated using Equation 26.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.025
    
    where:
    HAPCONTavg,wk = Monthly weighted average organic HAP content for 
    all rubber processed at the affected source, kg organic HAP per Mg 
    latex or dry crumb rubber.
    n = Number of samples in the month.
    Ci = Residual organic HAP content of sample i, determined in 
    accordance with (b)(3) or (c)(3) of this section, kg organic HAP per Mg 
    latex or dry crumb rubber.
    Pi = Weight of latex or dry crumb rubber represented by sample i.
    Pwk = Weight of latex or dry crumb rubber (Mg) processed in the 
    month.
    
    
    Sec. 63.496  Back-end process provisions--procedures to determine 
    compliance using control or recovery devices.
    
        (a) If an owner or operator complies with the residual organic HAP 
    limitations in Sec. 63.494(a) using control or recovery devices, 
    compliance shall be demonstrated using the procedures in paragraphs (b) 
    and (c) of this section. Previous test results conducted in accordance 
    with paragraphs (b)(1) through (b)(6) of this section may be used to 
    determine compliance in accordance with paragraph (c) of this section.
        (b) Compliance shall be demonstrated using the provisions in 
    paragraphs (b)(1) through (b)(10) of this section, as applicable.
        (1) A test shall be conducted, the duration of which shall be in 
    accordance with either paragraph
    
    [[Page 46951]]
    
    (b)(1)(i) or (b)(1)(ii) of this section, as appropriate.
        (i) If the back-end process operations are continuous, the test 
    shall consist of three separate one hour runs.
        (ii) If the back-end process operations are batch, the test shall 
    consist of three separate one-hour runs, unless the duration of the 
    batch cycle is less than one-hour, in which case the run length shall 
    equal the complete duration of the back-end process batch cycle.
        (2) The test shall be conducted when the grade of elastomer product 
    with the highest residual organic HAP content leaving the stripper is 
    processed in the back-end operations.
        (3) The uncontrolled residual organic HAP content in the latex or 
    dry crumb rubber shall be determined in accordance with 
    Sec. 63.495(b)(1) and (b)(3). A separate sample shall be taken and 
    analyzed for each test run. The sample shall be representative of the 
    material being processed in the back-end operation during the test, and 
    does not need to be taken during the test.
        (4) The quantity of material (weight of latex or dry crumb rubber) 
    processed during the test run shall be recorded. Acceptable methods of 
    determining this quantity are production records, measurement of stream 
    characteristics, and engineering calculations.
        (5) The inlet and outlet emissions from the control or recovery 
    device shall be determined using the procedures in paragraphs (b)(5)(i) 
    through (b)(5)(v) of this section, with the exceptions noted in 
    paragraphs (b)(6) and (b)(7) of this section. The inlet and outlet 
    emissions shall be determined when the material for which the 
    uncontrolled residual organic HAP content is determined in accordance 
    with paragraph (b)(3) of this section, is being processed in the 
    equipment controlled by the control or recovery device.
        (i) Method 1 or 1A of 40 CFR part 60, appendix A, as appropriate, 
    shall be used for selection of the sampling sites. Sampling sites shall 
    be located at the inlet of the control or recovery device as specified 
    in paragraphs (b)(5)(i)(A) or (b)(5)(i)(B) of this section, and at the 
    outlet of the control or recovery device.
        (A) The inlet sampling site shall be located at the exit of the 
    back-end process unit operation before any opportunity for emission to 
    the atmosphere, and before any control or recovery device.
        (B) If back-end process vent streams are combined prior to being 
    routed to control or recovery devices, the inlet sampling site may be 
    for the combined stream, as long as there is no opportunity for 
    emission to the atmosphere from any of the streams prior to being 
    combined.
        (ii) The gas volumetric flow rate shall be determined using Method 
    2, 2A, 2C, or 2D of 40 CFR part 60, appendix A, as appropriate.
        (iii) To determine the inlet and outlet total organic HAP 
    concentrations, the owner or operator shall use Method 18 or Method 25A 
    of 40 CFR part 60, appendix A. Alternatively, any other method or data 
    that has been validated according to the applicable procedures in 
    Method 301 of appendix A may be used. The minimum sampling time for 
    each run shall be in accordance with paragraph (b)(1) of this section, 
    during which either an integrated sample or grab samples shall be 
    taken. If grab sampling is used, then the samples shall be taken at 
    approximately equal intervals during the run, with the time between 
    samples no greater than 15 minutes.
        (iv) The mass rate of total organic HAP shall be computed using 
    Equations 27 and 28.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.026
    
    where:
    Cij, Coj=Concentration of sample component j of the gas 
    stream at the inlet and outlet of the control or recovery device, 
    respectively, dry basis, ppmv.
    Ei, Eo=Mass rate of total organic HAP at the inlet and outlet 
    of the control or recovery device, respectively, dry basis, kg per hour 
    (kg/hr).
    Mij, Moj=Molecular weight of sample component j of the gas 
    stream at the inlet and outlet of the control or recovery device, 
    respectively, gm/gm-mole.
    Qi, Qo=Flow rate of gas stream at the inlet and outlet of the 
    control or recovery device, respectively, dry standard m\3\/min.
    K2=Constant, 2.494  x  10-6 (ppmv)-1 (gm-mole/scm) (kg/
    gm) (min/hr), where standard temperature is 20 deg.C.
        (v) Inlet and outlet organic HAP emissions for the run shall be 
    calculated by multiplying the mass rate total inlet and outlet 
    emissions determined in accordance with paragraph (b)(5)(iv) of this 
    section by the duration of the run (in hours).
        (6) If a back-end process vent stream is introduced with the 
    combustion air, or as a secondary fuel into a boiler or process heater 
    with a design capacity less than 44 megawatts, the inlet and outlet 
    emissions shall be determined in accordance with paragraphs (b)(6)(i) 
    through (b)(6)(iv) of this section.
        (i) The inlet organic HAP emissions for the back-end process unit 
    operation shall be determined in accordance with paragraph (b)(5) of 
    this section.
        (ii) The owner or operator shall also measure total organic HAP (or 
    TOC, minus methane and ethane) emissions in all process vent streams 
    and primary and secondary fuels introduced into the boiler or process 
    heater, using the procedures in paragraph (b)(5) of this section, with 
    the exceptions noted in paragraphs (b)(6)(ii)(A) through (b)(6)(ii)(C) 
    of this section.
        (A) Selection of the location of the inlet sampling sites shall 
    ensure the measurement of total organic HAP concentrations in all 
    process vent streams and primary and secondary fuels introduced into 
    the boiler or process heater.
        (B) Paragraph (b)(5)(iii) of this section is applicable, except 
    that TOC (minus methane and ethane) may be measured instead of total 
    organic HAP.
        (C) The mass rates shall be calculated in accordance with paragraph 
    (b)(5)(iv) of this section, except that Cj at the inlet and outlet 
    of the control device shall be the sum of all total organic HAP (or 
    TOC, minus methane and ethane) concentrations for all process vent 
    streams and primary and secondary fuels introduced into the boiler or 
    process heater.
        (iii) The control efficiency of the boiler or process heater shall 
    be calculated using Equation 29.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.027
    
    
    [[Page 46952]]
    
    
    where:
    
    R=Control efficiency of boiler or process heater, percent.
    Einlet=Mass rate of total organic HAP or TOC (minus methane and 
    ethane) for all process vent streams and primary and secondary fuels at 
    the inlet to the boiler or process heater, kg organic HAP/hr or kg TOC/
    hr.
    Eoutlet=Mass rate of total organic HAP or TOC (minus methane and 
    ethane) for all process vent streams and primary and secondary fuels at 
    the outlet to the boiler or process heater, kg organic HAP/hr or kg 
    TOC/hr.
    
        (iv) The outlet total organic HAP emissions associated with the 
    back-end process unit operation shall be calculated using the equation 
    in paragraph (b)(8) of this section.
        (7) An owner or operator is not required to conduct a source test 
    to determine the outlet organic HAP emissions if any control device 
    specified in paragraphs (b)(7)(i) through (b)(7)(v) of this section is 
    used. For these devices, the inlet emissions associated with the back-
    end process unit operation shall be determined in accordance with 
    paragraph (b)(5) of this section, and the outlet emissions shall be 
    calculated using the equation in paragraph (b)(8) of this section.
        (i) A flare, provided the owner or operator complies with the flare 
    provisions in Sec. 63.11(b) of subpart A. The compliance determination 
    required by Sec. 63.6(h) of subpart A shall be conducted using Method 
    22 of 40 CFR part 60, appendix A, to determine visible emissions. 
    Compliance determinations are not necessary for flares already deemed 
    to be in compliance with the flare provisions in Sec. 63.11(b) of 
    subpart A.
        (ii) A boiler or process heater with a design heat input capacity 
    of 44 megawatts or greater.
        (iii) A boiler or process heater into which the process vent stream 
    is introduced with the primary fuel or is used as the primary fuel.
        (iv) A control device for which a performance test was conducted 
    for determining compliance with an NSPS and the test was conducted 
    using the same procedures specified in this section and no process 
    changes have been made since the test.
        (v) A boiler or process heater burning hazardous waste for which 
    the owner or operator:
        (A) Has been issued a final permit under 40 CFR part 270 and 
    complies with the requirements of 40 CFR part 266, subpart H, or
        (B) Has certified compliance with the interim status requirements 
    of 40 CFR part 266, subpart H.
        (8) If one of the control devices listed in paragraph (b)(6) or 
    (b)(7) of this section is used, the outlet emissions shall be 
    calculated using Equation 30.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.028
    
    where:
    
    Eo=Mass rate of total organic HAP at the outlet of the control or 
    recovery device, respectively, dry basis, kg/hr.
    Ei=Mass rate of total organic HAP at the inlet of the control or 
    recovery device, respectively, dry basis, kg/hr, determined using the 
    procedures in paragraph (b)(5)(iv) of this section.
    R=Control efficiency of control device, as specified in paragraph 
    (b)(8) (i), (ii), or (iii) of this section.
    
        (i) If a back-end process vent stream is introduced with the 
    combustion air, or as a secondary fuel into a boiler or process heater 
    with a design capacity less than 44 megawatts, the control efficiency 
    of the boiler or process heater shall be determined using the 
    procedures in paragraph (b)(6)(iii) of this section.
        (ii) If a back-end process vent is controlled using a control 
    device specified in paragraph (b)(7) (i), (ii), (iii), or (v) of this 
    section, the control device efficiency shall be assumed to be 98 
    percent.
        (iii) If a back-end process vent is controlled using a control 
    device specified in paragraph (b)(7)(iv) of this section, the control 
    device efficiency shall be the efficiency determined in the previous 
    performance test.
        (c) Compliance shall be determined using the procedures in this 
    paragraph.
        (1) For each test run, the residual organic HAP content, adjusted 
    for the control or recovery device emission reduction, shall be 
    calculated using Equation 31.
    Where:
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.029
    
    HAPCONTrun=Factor, kg organic HAP per kg elastomer (latex or dry 
    crumb rubber).
    C=Total uncontrolled organic HAP content, determined in accordance with 
    paragraph (b)(3) of this section, kg organic HAP per kg latex or dry 
    crumb rubber.
    P=Weight of latex or dry crumb rubber processed during test run.
    Ei,run=Mass rate of total organic HAP at the inlet of the control 
    or recovery device, respectively, dry basis, kg per test run.
    Eo,run=Mass rate of total organic HAP at the outlet of the control 
    or recovery device, respectively, dry basis, kg per test run.
    
        (2) A facility is in compliance if the average of the organic HAP 
    contents calculated for all three test runs is below the residual 
    organic HAP limitations in Sec. 63.494(a).
        (d) An owner or operator complying with the residual organic HAP 
    limitations in Sec. 63.494(a) using a control or recovery device, shall 
    redetermine the compliance status through the requirements described in 
    paragraph (b) of this section whenever process changes are made. The 
    owner or operator shall report the results of the redetermination in 
    accordance with Sec. 63.499(d). For the purposes of this section, a 
    process change is any action that would reasonably be expected to 
    impair the performance of the control or recovery device. For the 
    purposes of this section, the production of an elastomer with a 
    residual organic HAP content greater than the residual organic HAP 
    content of the elastomer used in the compliance demonstration 
    constitutes a process change, unless the overall effect of the change 
    is to reduce organic HAP emissions from the source as a whole. Other 
    examples of process changes may include changes in production capacity 
    or production rate, or removal or addition of equipment. For the 
    purposes of this paragraph, process changes do not include: Process 
    upsets; unintentional, temporary process changes; or changes that 
    reduce the residual organic HAP content of the elastomer.
    
    
    Sec. 63.497  Back-end process provisions--monitoring provisions for 
    control and recovery devices.
    
        (a) An owner or operator complying with the residual organic HAP 
    limitations in Sec. 63.494(a) using control
    
    [[Page 46953]]
    
    or recovery devices, or a combination of stripper technology and 
    control or recovery devices, shall install the monitoring equipment 
    specified in paragraphs (a)(1) through (a)(6) of this section, as 
    appropriate.
        (1) Where an incinerator is used, a temperature monitoring device 
    equipped with a continuous recorder is required.
        (i) Where an incinerator other than a catalytic incinerator is 
    used, the temperature monitoring device shall be installed in the 
    firebox or in the ductwork immediately downstream of the firebox in a 
    position before any substantial heat exchange occurs.
        (ii) Where a catalytic incinerator is used, the temperature 
    monitoring devices shall be installed in the gas stream immediately 
    before and after the catalyst bed.
        (2) Where a flare is used, a device (including, but not limited to, 
    a thermocouple, ultra-violet beam sensor, or infrared sensor) capable 
    of continuously detecting the presence of a pilot flame is required.
        (3) Where a boiler or process heater of less than 44 megawatts 
    design heat input capacity is used, a temperature monitoring device in 
    the firebox equipped with a continuous recorder is required. Any boiler 
    or process heater in which all vent streams are introduced with primary 
    fuel or are used as the primary fuel is exempt from this requirement.
        (4) For an absorber, a scrubbing liquid temperature monitoring 
    device and a specific gravity monitoring device are required, each 
    equipped with a continuous recorder.
        (5) For a condenser, a condenser exit (product side) temperature 
    monitoring device equipped with a continuous recorder is required.
        (6) For a carbon adsorber, an integrating regeneration stream flow 
    monitoring device having an accuracy of at least plus-minus10 
    percent, capable of recording the total regeneration stream flow for 
    each regeneration cycle; and a carbon bed temperature monitoring 
    device, capable of recording the carbon bed temperature after each 
    regeneration and within 15 minutes of completing any cooling cycle are 
    required.
        (b) An owner or operator may request approval to monitor parameters 
    other than those required by paragraph (a) of this section. The request 
    shall be submitted according to the procedures specified in 
    Sec. 63.506(f) or (g). Approval shall be requested if the owner or 
    operator:
        (1) Uses a control or recovery device other than those listed in 
    paragraph (a) of this section; or
        (2) Uses one of the control or recovery devices listed in paragraph 
    (a) of this section, but seeks to monitor a parameter other than those 
    specified in paragraph (a) of this section.
        (c) The owner or operator shall establish a level, defined as 
    either a maximum or minimum operating parameter, that indicates proper 
    operation of the control or recovery device for each parameter 
    monitored under paragraphs (a)(1) through (a)(6) of this section. This 
    level is determined in accordance with Sec. 63.505. The established 
    level, along with supporting documentation, shall be submitted in the 
    Notification of Compliance Status or the operating permit application, 
    as required in Sec. 63.506 (e)(5) or (e)(8), respectively. The owner or 
    operator shall operate control and recovery devices above or below the 
    established level, as required, to ensure continued compliance with the 
    standard.
        (d) The owner or operator of a controlled back-end process vent 
    using a vent system that contains bypass lines that could divert a vent 
    stream away from the control or recovery device used to comply with 
    Sec. 63.494(a) shall comply with paragraph (d)(1), (d)(2), or (d)(3) of 
    this section. Equipment such as low leg drains, high point bleeds, 
    analyzer vents, open-ended valves or lines, and pressure relief valves 
    needed for safety purposes are not subject to this paragraph.
        (1) Properly install, maintain, and operate a flow indicator that 
    takes a reading at least once every 15 minutes. Records shall be 
    generated as specified in Sec. 63.498(d)(5)(iii). The flow indicator 
    shall be installed at the entrance to any bypass line that could divert 
    the vent stream away from the control device to the atmosphere; or
        (2) Secure the bypass line valve in the non-diverting position with 
    a car-seal or a lock-and-key type configuration. A visual inspection of 
    the seal or closure mechanism shall be performed at least once every 
    month to ensure that the valve is maintained in the non-diverting 
    position and the vent stream is not diverted through the bypass line.
        (3) Continuously monitor the bypass line damper or valve position 
    using computer monitoring and record any periods when the position of 
    the bypass line valve has changes as specified in 
    Sec. 63.498(d)(5)(iv).
    
    
    Sec. 63.498  Back-end process provisions--recordkeeping.
    
        (a) Each owner or operator shall maintain the records specified in 
    paragraphs (a)(1) through (a)(3) of this section for each back-end 
    process operation at an affected source.
        (1) The type of elastomer product processed in the back-end 
    operation.
        (2) The type of process (solution process, emulsion process, etc.)
        (3) If the back-end process operation is subject to an emission 
    limitation in Sec. 63.494(a), whether compliance will be achieved by 
    stripping technology, or by control or recovery devices.
        (b) Each owner or operator of a back-end process operation using 
    stripping technology to comply with an emission limitation in 
    Sec. 63.494(a), and demonstrating compliance using the periodic 
    sampling procedures in Sec. 63.495(b), shall maintain the records 
    specified in paragraph (b)(1), and in paragraph (b)(2) or (b)(3) of 
    this section, as appropriate.
        (1) Records associated with each sample taken in accordance with 
    Sec. 63.495(b). These records shall include the following for each 
    sample:
        (i) Elastomer type,
        (ii) The date and time the sample was collected,
        (iii) The corresponding quantity of elastomer processed over the 
    time period represented by the sample. Acceptable methods of 
    determining this quantity are production records, measurement of stream 
    characteristics, and engineering calculations.
        (A) For emulsion processes, this quantity shall be the weight of 
    the latex leaving the stripper.
        (B) For solution processes, this quantity shall be the crumb rubber 
    dry weight of the rubber leaving the stripper.
        (iv) The organic HAP content of each sample.
        (2) The monthly weighted average organic HAP content, calculated in 
    accordance with Sec. 63.495(f).
        (3) If the organic HAP contents for all samples analyzed during a 
    month are below the appropriate level in Sec. 63.494(a), the owner or 
    operator may record that all samples were in accordance with the 
    residual organic HAP limitations in Sec. 63.494(a), rather than 
    calculating and recording a monthly weighted average.
        (c) Each owner or operator of a back-end process operation using 
    stripping technology to comply with an emission limitation in 
    Sec. 63.494(a), and demonstrating compliance using the stripper 
    parameter monitoring procedures in Sec. 63.495(c), shall maintain the 
    records specified in paragraphs (c)(1) through (c)(3) of this section.
        (1) Records associated with the initial, and subsequent, 
    determinations of the organic HAP content of each grade of elastomer 
    produced. These records shall include the following:
    
    [[Page 46954]]
    
        (i) An identification of the elastomer type and grade;
        (ii) The results of the residual organic HAP analyses, conducted in 
    accordance with Sec. 63.505(e)(1);
        (iii) The stripper monitoring parameters required to be established 
    in Sec. 63.495(c)(1).
        (iv) If re-determinations are made of the organic HAP content, and 
    re-establishment of the stripper monitoring parameters, records of the 
    initial determination are no longer required to be maintained.
        (2) Records associated with each grade or batch. These records 
    shall include the following for each grade or batch:
        (i) Elastomer type and grade;
        (ii) The quantity of elastomer processed;
        (A) For emulsion processes, this quantity shall be the weight of 
    the latex leaving the stripper.
        (B) For solution processes, this quantity shall be the crumb rubber 
    dry weight of the crumb rubber leaving the stripper.
        (iii) The hourly average of all stripper parameter results;
        (iv) If one or more hourly average stripper monitoring parameters 
    is not in accordance with the established levels, the results of the 
    residual organic HAP analysis.
        (3) The monthly weighted average organic HAP content, calculated in 
    accordance with Sec. 63.495(f).
        (d) Each owner or operator of a back-end process operation using 
    control or recovery devices to comply with an organic HAP emission 
    limitation in Sec. 63.494(a) shall maintain the records specified in 
    paragraphs (d)(1) through (d)(5) of this section.
        (1) Results of the testing required by Sec. 63.496(b). These 
    results shall include the following, for each of the three required 
    test runs:
        (i) The uncontrolled residual organic HAP content in the latex or 
    dry crumb rubber, as required to be determined by Sec. 63.496(b)(3), 
    including the test results of the analysis;
        (ii) The total quantity of material (weight of latex or dry crumb 
    rubber) processed during the test run, recorded in accordance with 
    Sec. 63.496(b)(4),
        (iii) The organic HAP emissions at the inlet and outlet of the 
    control or recovery device, determined in accordance with Sec. 63.496 
    (b)(5) through (b)(8), including all test results and calculations,
        (iv) The residual organic HAP content, adjusted for the control or 
    recovery device emission reduction, determined in accordance with 
    Sec. 63.496(c)(1).
        (2) The operating parameter level established in accordance with 
    Sec. 63.497(c), along with supporting documentation.
        (3) The following information when using a flare:
        (i) The flare design (i.e., steam-assisted, air-assisted, or non-
    assisted);
        (ii) All visible emission readings, heat content determinations, 
    flow rate measurements, and exit velocity determinations made during 
    the compliance determination; and
        (iii) All periods during the compliance determination when the 
    pilot flame is absent.
        (4) When using a boiler or process heater, a description of the 
    location at which the vent stream is introduced into the boiler or 
    process heater.
        (5) Each owner or operator using a control or recovery device shall 
    keep the following records up-to-date and readily accessible:
        (i) Continuous records of the equipment operating parameters 
    specified to be monitored under Sec. 63.497(a) or specified by the 
    Administrator in accordance with Sec. 63.497(b). For flares, the hourly 
    records and records of pilot flame outages shall be maintained in place 
    of continuous records.
        (ii) Records of the daily average value of each continuously 
    monitored parameter for each operating day, except as provided in 
    paragraphs (d)(5)(ii)(D) and (d)(5)(ii)(E) of this section.
        (A) The daily average shall be calculated as the average of all 
    values for a monitored parameter recorded during the operating day, 
    except as provided in paragraph (d)(5)(ii)(B) of this section. The 
    average shall cover a 24-hour period if operation is continuous, or the 
    number of hours of operation per operating day if operation is not 
    continuous.
        (B) Monitoring data recorded during periods of monitoring system 
    breakdowns, repairs, calibration checks, and zero (low-level) and high-
    level adjustments shall not be included in computing the hourly or 
    daily averages. Records shall be kept of the times and durations of all 
    such periods and any other periods of process or control device 
    operation when monitors are not operating.
        (C) The operating day shall be the period defined in the operating 
    permit or the Notification of Compliance Status in Sec. 63.506(e)(8) or 
    (e)(5). It may be from midnight to midnight or another 24-hour period.
        (D) If all recorded values for a monitored parameter during an 
    operating day are below the maximum, or above the minimum, level 
    established in the Notification of Compliance Status in 
    Sec. 63.506(e)(5) or in the operating permit, the owner or operator may 
    record that all values were below the maximum or above the minimum 
    level, rather than calculating and recording a daily average for that 
    operating day.
        (E) For flares, records of the times and duration of all periods 
    during which the pilot flame is absent shall be kept rather than daily 
    averages. The records specified in this paragraph are not required 
    during periods when emissions are not routed to the flare, or during 
    startups, shutdowns, or malfunctions when the owner or operator 
    complies with the applicable requirements of subpart A of this part, as 
    directed by Sec. 63.506(b)(1).
        (iii) Hourly records of whether the flow indicator specified under 
    Sec. 63.497(d)(1) was operating and whether a diversion was detected at 
    any time during the hour, as well as records of the times of all 
    periods when the vent stream is diverted from the control device or the 
    flow indicator is not operating.
        (iv) Where a seal mechanism is used to comply with 
    Sec. 63.497(d)(2), or where computer monitoring of the position of the 
    bypass damper or valve is used to comply with Sec. 63.497(d)(3), hourly 
    records of flow are not required.
        (A) For compliance with Sec. 63.497(d)(2), the owner or operator 
    shall record whether the monthly visual inspection of the seals or 
    closure mechanisms has been done, and shall record instances when the 
    seal mechanism is broken, the bypass line valve position has changed, 
    or the key for a lock-and-key type configuration has been checked out, 
    and records of any car-seal that has broken.
        (B) For compliance with Sec. 63.497(d)(3), the owner or operator 
    shall record the times of all periods when the bypass line damper or 
    valve position has changed.
    
    
    Sec. 63.499   Back-end process provisions--reporting.
    
        (a) The owner or operator of an affected source with back-end 
    process operations shall submit the information required in 
    Sec. 63.498(a) as part of the Notification of Compliance Status 
    specified in Sec. 63.506(e)(5).
        (b) Each owner or operator of a back-end process operation using 
    stripping to comply with an emission limitation in Sec. 63.494(a), and 
    demonstrating compliance by stripper parameter monitoring, shall submit 
    reports as specified in paragraphs (b)(1) and (b)(2) of this section.
        (1) As part of the Notification of Compliance Status specified in
    
    [[Page 46955]]
    
    Sec. 63.506(e)(5), the owner or operator shall submit the information 
    specified in Sec. 63.498(c)(1).
        (2) For organic HAP content/stripping monitoring parameter re-
    determinations, and the addition of new grades, the information 
    specified in Sec. 63.498(c)(1) shall be submitted in the next periodic 
    report specified in Sec. 63.506(e)(6).
        (c) Each owner or operator of a back-end process operation control 
    or recovery devices that must comply with an emission limitation in 
    Sec. 63.494(a) shall submit the information specified in paragraphs 
    (c)(1) through (c)(3) of this section as part of the Notification of 
    Compliance Status specified in Sec. 63.506(e)(5).
        (1) The residual organic HAP content, adjusted for the control or 
    recovery device emission reduction, determined in accordance with 
    Sec. 63.496(c)(1), for each test run in the compliance determination.
        (2) The operating parameter level established in accordance with 
    Sec. 63.497(c), along with supporting documentation.
        (3) The information specified in Sec. 63.498(d)(3) regarding flares 
    and Sec. 63.498(d)(4) regarding boilers and process heaters, if 
    applicable.
        (d) Whenever a process change, as defined in Sec. 63.496(d), is 
    made that causes the redetermination of the compliance status for the 
    back-end process operations, the owner or operator shall submit a 
    report within 180 calendar days after the process change as specified 
    in Sec. 63.506(e)(7)(iii). The report shall include:
        (1) A description of the process change;
        (2) The results of the redetermination of the compliance status, 
    determined in accordance with Sec. 63.496(b), and recorded in 
    accordance with Sec. 63.498(d)(1), and
        (3) Documentation of the re-establishment of a parameter level for 
    the control or recovery device, defined as either a maximum or minimum 
    operating parameter, that indicates proper operation of the control or 
    recovery device, in accordance with Sec. 63.497(c) and recorded in 
    accordance with Sec. 63.498(d)(2).
        (e) If an owner or operator uses a control or recovery device other 
    than those listed in Sec. 63.497(a) or requests approval to monitor a 
    parameter other than those specified in Sec. 63.497(a), the owner or 
    operator shall submit a description of planned reporting and 
    recordkeeping procedures as required under Sec. 63.506(e)(3) or (e)(8). 
    The Administrator will specify appropriate reporting and recordkeeping 
    requirements as part of the review of the Precompliance Report or 
    Operating Permit application.
    
    
    Sec. 63.500   Back-end process provisions--carbon disulfide limitations 
    for styrene butadiene rubber by emulsion processes.
    
        (a) Owners or operators of sources subject to this subpart 
    producing styrene butadiene rubber using an emulsion process shall 
    operate the process such that the carbon disulfide concentration in 
    each crumb dryer exhausts shall not exceed 45 ppmv.
        (1) The owner or operator shall develop standard operating 
    procedures for the addition of sulfur containing shortstop agents to 
    ensure that the limitation in paragraph (a) of this section is 
    maintained. There shall be a standard operating procedure representing 
    the production of every grade of styrene butadiene rubber produced at 
    the affected source using a sulfur containing shortstop agent.
        (2) A validation of each standard operating procedure shall be 
    conducted in accordance with paragraph (c) of this section, except as 
    provided in paragraph (b) of this section, to demonstrate compliance 
    with the limitation in paragraph (a) of this section.
        (3) The owner or operator shall operate the process in accordance 
    with a validated standard operating procedure at all times when styrene 
    butadiene rubber is being produced using a sulfur containing shortstop 
    agent. If a standard operating procedure is changed, it must be re-
    validated.
        (4) Records specified in paragraph (d) of this section shall be 
    maintained.
        (5) Reports shall be submitted in accordance with paragraph (e) of 
    this section.
        (b) Crumb dryers that are vented to a combustion device are not 
    subject to the provisions in this section.
        (c) The owner or operator shall validate each standard operating 
    procedure to determine compliance with the limitation in paragraph (a) 
    of this section using the testing procedures in paragraph (c)(1) of 
    this section or engineering assessment, as described in paragraph 
    (c)(2) of this section.
        (1) The owner or operator shall conduct a performance test using 
    the procedures in paragraphs (c)(1)(i) through (c)(1)(iii) of this 
    section to demonstrate compliance with the carbon disulfide 
    concentration limitation in paragraph (a) of this section. One test 
    shall be conducted for each standard operating procedure.
        (i) Method 1 or 1A of 40 CFR part 60, appendix A, as required, 
    shall be used for selection of the sampling sites.
        (ii) The gas volumetric flow rate shall be determined using Method 
    2, 2A, 2C, or 2D of 40 CFR part 60, appendix A, as required.
        (iii) To determine compliance with the carbon disulfide 
    concentration limit in paragraph (a) of this section, the owner or 
    operator shall use Method 18 or Method 25A of 40 CFR part 60, appendix 
    A, to measure carbon disulfide. Alternatively, any other method or data 
    that has been validated according to the applicable procedures in 
    Method 301 of appendix A of this part may be used. The following 
    procedures shall be used to calculate carbon disulfide concentration:
        (A) The minimum sampling time for each run shall be 1 hour, in 
    which either an integrated sample or a minimum of four grab samples 
    shall be taken. If grab sampling is used, then the samples shall be 
    taken at approximately equal intervals in time, such as 15 minute 
    intervals during the run.
        (B) The concentration of carbon disulfide shall be calculated using 
    Equation 32.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.030
    
    where:
    
    CCS2=Concentration of carbon disulfide, dry basis, ppmv.
    CCS2i=Concentration of carbon disulfide of sample i, dry basis, 
    ppmv.
    n=Number of samples in the sample run.
    
        (2) The owner or operator shall use engineering assessment to 
    demonstrate compliance with the carbon disulfide concentration 
    limitation in paragraph (a) of this section. Engineering assessment 
    includes, but is not limited to, the following:
        (i) Previous test results, provided the tests are representative of 
    current operating practices at the process unit.
        (ii) Bench-scale or pilot-scale test data representative of the 
    process under representative operating conditions.
        (iii) Flow rate and/or carbon disulfide emission rate specified or 
    implied within an applicable permit limit.
        (iv) Design analysis based on accepted chemical engineering 
    principles, measurable process parameters, or physical or chemical laws 
    or properties. Examples of analytical methods include, but are not 
    limited to:
        (A) Use of material balances,
        (B) Estimation of flow rate based on physical equipment design such 
    as pump or blower capacities, and
        (C) Estimation of carbon disulfide concentrations based on 
    saturation conditions.
    
    [[Page 46956]]
    
        (v) All data, assumptions, and procedures used in the engineering 
    assessment shall be documented.
        (d) Owners and operators of sources subject to this section shall 
    maintain the records specified in paragraphs (d)(1) and (d)(2) of this 
    section.
        (1) Documentation of the results of the testing required by 
    paragraph (c) of this section.
        (2) A description of the standard operating procedure used during 
    the testing. This description shall include, at a minimum, an 
    identification of the sulfur containing shortstop added to the styrene 
    butadiene rubber prior to the dryers, an identification of the point 
    and time in the process where the sulfur containing shortstop is added, 
    and an identification of the amount of sulfur containing shortstop 
    added per unit of latex.
        (e) Owners and operators shall submit the reports as specified in 
    paragraphs (e)(1) and (e)(2) of this section.
        (1) As part of the Notification of Compliance Status specified in 
    Sec. 63.506(e)(5), documentation of the results of the testing required 
    by paragraph (c) of this section.
        (2) If changes are made in the standard operating procedure used 
    during the compliance test and recorded in accordance with paragraph 
    (d)(2) of this section, and if those changes have the potential for 
    increasing the concentration of carbon disulfide in the crumb dryer 
    exhaust to above the 45 ppmv limit, the owner or operator shall:
        (i) Redetermine compliance using the test procedures in paragraph 
    (c) of this section, and
        (ii) Submit documentation of the testing results in the next 
    periodic report required by Sec. 63.506(e)(6).
    
    
    Sec. 63.501  Wastewater provisions.
    
        (a) For each process wastewater stream originating at an affected 
    source, except those wastewater streams exempted by paragraph (c) of 
    this section, the owner or operator shall comply with the requirements 
    of Secs. 63.131 through 63.148 of subpart G, with the differences noted 
    in paragraphs (a)(1) through (a)(11) of this section, for the purposes 
    of this subpart.
        (1) When the determination of equivalence criteria in 
    Sec. 63.102(b) of subpart F is referred to in Secs. 63.132, 63.133, and 
    63.137 of subpart G, the provisions in Sec. 63.6(g) of subpart A shall 
    apply for the purposes of this subpart.
        (2) When the storage tank requirements contained in Secs. 63.119 
    through 63.123 of subpart G are referred to in Secs. 63.132 through 
    63.148 of subpart G, Secs. 63.119 through 63.123 of subpart G are 
    applicable, with the exception of the differences referred to in 
    Sec. 63.484, for the purposes of this subpart.
        (3) When the Implementation Plan requirements contained in 
    Sec. 63.151 in subpart G are referred to in Sec. 63.146 of subpart G, 
    the owner or operator of an affected source subject to this subpart 
    need not comply.
        (4) When the Initial Notification Plan requirements in 
    Sec. 63.151(b) of subpart G are referred to in Sec. 63.146 of subpart 
    G, the owner or operator of an affected source subject to this subpart 
    need not comply.
        (5) When the owner or operator requests to use alternatives to the 
    continuous operating parameter monitoring and recordkeeping provisions 
    referred to in Sec. 63.151(g) of subpart G, or the owner or operator 
    submits an operating permit application instead of an Implementation 
    Plan as specified in Sec. 63.152(e) of subpart G, as referred to in 
    Sec. 63.146(a)(3) of subpart G, Sec. 63.506(f) and Sec. 63.506(e)(8), 
    respectively, shall apply for the purposes of this subpart.
        (6) When the Notification of Compliance Status requirements 
    contained in Sec. 63.152(b) of subpart G are referred to in 
    Secs. 63.146 and 63.147 of subpart G, the Notification of Compliance 
    Status requirements contained in Sec. 63.506(e)(5) shall apply for the 
    purposes of this subpart.
        (7) When the Periodic Report requirements contained in 
    Sec. 63.152(c) of subpart G are referred to in Secs. 63.146 and 63.147 
    of subpart G, the Periodic Report requirements contained in 
    Sec. 63.506(e)(6) shall apply for the purposes of this subpart.
        (8) When the term ``range'' is used in Sec. 63.143(f) of subpart G, 
    the term ``level'' shall be used instead, for the purposes of this 
    subpart. This level shall be determined using the procedures specified 
    in Sec. 63.505.
        (9) For the purposes of this subpart, owners or operators are not 
    required to comply with the provisions of Sec. 63.138(e)(2) of subpart 
    G which specify that owners or operators shall demonstrate that 95 
    percent of the mass of HAP, as listed in Table 9 of subpart G, is 
    removed from the wastewater stream or combination of wastewater streams 
    by the procedure specified in Sec. 63.145(i) of subpart G for a 
    biological treatment unit.
        (10) For the purposes of this subpart, owners or operators are not 
    required to comply with the provisions of Sec. 63.138(j)(3) of subpart 
    G which specify that owners or operators shall use the procedures 
    specified in Appendix C of subpart G to demonstrate compliance when 
    using a biological treatment unit.
        (11) When the provisions of Sec. 63.139(c)(1)(ii) of subpart G or 
    the provisions of Sec. 63.145(e)(2)(ii)(B) specify that Method 18 shall 
    be used, Method 18 or Method 25A may be used for the purposes of this 
    subpart. The use of Method 25A shall comply with paragraphs (a)(11)(i) 
    and (a)(11)(ii) of this section.
        (i) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (ii) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (b) Except for those streams exempted by paragraph (c) of this 
    section, the owner or operator of each affected source shall comply 
    with the requirements for maintenance wastewater in Sec. 63.105 of 
    subpart F, except that when Sec. 63.105(a) refers to ``organic HAPs,'' 
    the definition of organic HAP in Sec. 63.482 shall apply for the 
    purposes of this subpart.
        (c) The following wastewater streams are exempt from the 
    requirements of paragraphs (a) and (b) of this section:
        (1) Back-end wastewater streams originating from equipment that 
    only produces latex products.
        (2) Back-end wastewater streams at affected sources that are 
    subject to a residual organic HAP limitation in Sec. 63.494(a), and 
    that are complying with these limitations through the use of stripping 
    technology.
        (d) The compliance date for the affected source subject to the 
    provisions of this section is specified in Sec. 63.481.
    
    
    Sec. 63.502  Equipment leak provisions.
    
        (a) The owner or operator of each affected source, shall comply 
    with the requirements of subpart H of this part for all equipment in 
    organic HAP service, with the exception noted in paragraphs (b) through 
    (h) of this section.
        (b) Surge control vessels and bottoms receivers described in 
    paragraphs (b)(1) through (b)(6) of this section are exempt from the 
    requirements contained in Sec. 63.170 of subpart H.
        (1) Surge control vessels and bottoms receivers containing styrene-
    butadiene latex;
        (2) Surge control vessels and bottoms receivers containing other 
    latex products and located downstream of the stripping operations;
    
    [[Page 46957]]
    
        (3) Surge control vessels and bottoms receivers containing high 
    conversion latex products;
        (4) Surge control vessels and bottoms receivers located downstream 
    of the stripping operations at affected sources subject to the back-end 
    residual organic HAP limitation located in Sec. 63.494, that are 
    complying through the use of stripping technology, as specified in 
    Sec. 63.495;
        (5) Surge control vessels and bottoms receivers containing styrene;
        (6) Surge control vessels and bottoms receivers containing 
    acrylamide; and
        (7) Surge control vessels and bottoms receivers containing 
    epichlorohydrin.
        (c) The compliance date for the equipment leak provisions in this 
    section is provided in Sec. 63.481.
        (d) For an affected source producing polybutadiene rubber and 
    styrene butadiene rubber by solution, the indications of liquids 
    dripping, as defined in subpart H of this part, from bleed ports in 
    pumps and agitator seals in light liquid service, shall not be 
    considered a leak. For the purposes of this subpart, a ``bleed port'' 
    is a technologically-required feature of the pump or seal whereby 
    polymer fluid used to provide lubrication and/or cooling of the pump or 
    agitator shaft exits the pump, thereby resulting in a visible dripping 
    of fluid.
        (e) Affected sources subject to subpart I of this part shall 
    continue to comply with subpart I until the compliance date specified 
    in Sec. 63.481. After the compliance date for this section, the source 
    shall be subject to subpart H of this part and shall no longer be 
    subject to subpart I.
        (f) The owner or operator of each affected source shall comply with 
    the requirements of Sec. 63.104 of subpart F for heat exchange systems.
        (g) Owners and operators of an affected source subject to this 
    subpart are not required to submit the Initial Notification required by 
    Sec. 63.182(a)(1) and Sec. 63.182(b) of subpart H.
        (h) The Notification of Compliance Status required by 
    Sec. 63.182(a)(2) and Sec. 63.182(c) of subpart H shall be submitted 
    within 150 days (rather than 90 days) of the applicable compliance date 
    specified in Sec. 63.481 for the equipment leak provisions. The 
    notification can be submitted as part of the Notification of Compliance 
    Status required by Sec. 63.506(e)(5).
        (i) The Periodic Reports required by Sec. 63.182(a)(3) and 
    Sec. 63.182(d) of subpart H shall be submitted as part of the Periodic 
    Reports required by Sec. 63.506(e)(6).
    
    
    Sec. 63.503  Emissions averaging provisions.
    
        (a) This section applies to owners or operators of existing 
    affected sources who seek to comply with Sec. 63.483(b) by using 
    emissions averaging rather than following the provisions of 
    Secs. 63.484, 63.485, 63.486, 63.494, and 64.488.
        (1) The following emission point limitations apply to the use of 
    these provisions:
        (i) All emission points included in an emissions average shall be 
    from the same affected source. There may be an emissions average for 
    each individual affected source located at a plant site.
        (ii)(A) If a plant site has only one affected source for which 
    emissions averaging is being used to demonstrate compliance, the number 
    of emission points allowed to be included in the emission average is 
    limited to twenty. This number may be increased by up to five 
    additional points if pollution prevention measures are used to control 
    five or more of the emission points included in the emissions average.
        (B) If a plant site has two or more affected sources for which 
    emissions averaging is being used to demonstrate compliance, the number 
    of emission points allowed in the emissions average for those affected 
    sources is limited to twenty. This number may be increased by up to 
    five additional emission points if pollution prevention measures are 
    used to control five or more of the emission points included in the 
    emissions averages.
        (2) Compliance with the provisions of this section can be based on 
    either organic HAP or TOC.
        (3) For the purposes of these provisions, whenever Method 18 is 
    specified within the paragraphs of this section or is specified by 
    reference through provisions outside this section, Method 18 or Method 
    25A may be used. The use of Method 25A shall comply with paragraphs 
    (a)(3)(i) and (a)(3)(ii) of this section.
        (i) The organic HAP used as the calibration gas for Method 25A 
    shall be the single organic HAP representing the largest percent by 
    volume of the emissions.
        (ii) The use of Method 25A is acceptable if the response from the 
    high-level calibration gas is at least 20 times the standard deviation 
    of the response from the zero calibration gas when the instrument is 
    zeroed on the most sensitive scale.
        (b) Unless an operating permit application has been submitted, the 
    owner or operator shall develop and submit for approval an Emissions 
    Averaging Plan containing all of the information required in 
    Sec. 63.506(e)(4) for all emission points to be included in an 
    emissions average.
        (c) Paragraphs (c)(1) through (c)(4) of this section describe the 
    emission points that can be used to generate emissions averaging 
    credits if control was applied after November 15, 1990 and if 
    sufficient information is available to determine the appropriate value 
    of credits for the emission point. Paragraph (c)(5) of this section 
    discusses the use of pollution prevention in generating emissions 
    averaging credits.
        (1) Storage vessels, batch front-end process vents, aggregate batch 
    vent streams, continuous front-end process vents, and process 
    wastewater streams that are determined to be Group 2 emission points.
        (2) Storage vessels, continuous front-end process vents, and 
    process wastewater steams that are determined to be Group 1 emission 
    points and that are controlled by a technology that the Administrator 
    or permitting authority agrees has a higher nominal efficiency than the 
    reference control technology. Information on the nominal efficiencies 
    for such technologies must be submitted and approved as provided in 
    paragraph (i) of this section.
        (3) Batch front-end process vents and aggregate batch vent streams 
    that are determined to be Group 1 emission points and that are 
    controlled to a level more stringent than the applicable standard.
        (4) Back-end process operations that are controlled such that 
    organic HAP emissions from the back-end process operation are less than 
    would be achieved by meeting the residual organic HAP limits in 
    Sec. 63.494. For the purposes of the emission averaging provisions in 
    this section, all back-end process operations at an affected facility 
    shall be considered a single emission point.
        (5) The percent reduction for any storage vessel, batch front-end 
    process vent, aggregate batch vent stream, continuous front-end process 
    vent, and process wastewater stream shall be determined using the 
    procedures specified in paragraph (j) of this section.
        (i) For a Group 1 storage vessel, batch front-end process vent, 
    aggregate batch vent stream, continuous front-end process vent, or 
    process wastewater stream, the pollution prevention measure must reduce 
    emissions more than if the reference control technology or standard had 
    been applied to the emission point instead of the pollution prevention 
    measure, except as provided in paragraph (c)(5)(ii) of this section.
        (ii) If a pollution prevention measure is used in conjunction with 
    other controls for a Group 1 storage vessel,
    
    [[Page 46958]]
    
    batch front-end process vent, aggregate batch vent stream, continuous 
    front-end process vent, or process wastewater stream, the pollution 
    prevention measure alone does not have to reduce emissions more than 
    the reference control technology or standard, but the combination of 
    the pollution prevention measure and other controls must reduce 
    emissions more than if the applicable reference control technology or 
    standard had been applied instead of the pollution prevention measure.
        (d) The following emission points cannot be used to generate 
    emissions averaging credits:
        (1) Emission points already controlled on or before November 15, 
    1990 cannot be used to generate credits unless the level of control was 
    increased after November 15, 1990. In this case, credit will be allowed 
    only for the increase in control after November 15, 1990.
        (2) Group 1 emission points, identified in paragraph (c)(2) of this 
    section, that are controlled by a reference control technology cannot 
    be used to generate credits unless the reference control technology has 
    been approved for use in a different manner and a higher nominal 
    efficiency has been assigned according to the procedures in paragraph 
    (i) of this section.
        (3) Emission points on nonoperating EPPU cannot be used to generate 
    credits. EPPU that are shutdown cannot be used to generate credits or 
    debits.
        (4) Maintenance wastewater cannot be used to generate credits. 
    Wastewater streams treated in biological treatment units cannot be used 
    to generate credits. These two types of wastewater cannot be used to 
    generate credits or debits. For the purposes of this section, the terms 
    wastewater and wastewater stream are used to mean process wastewater.
        (5) Emission points controlled to comply with a State or Federal 
    rule other than this subpart cannot be used to generate credits, unless 
    the level of control has been increased after November 15, 1990 to a 
    level above what is required by the other State or Federal rule. Only 
    the control above what is required by the other State or Federal rule 
    will be credited. However, if an emission point has been used to 
    generate emissions averaging credit in an approved emissions average, 
    and the emission point is subsequently made subject to a State or 
    Federal rule other than this subpart, the emission point can continue 
    to generate emissions averaging credit for the purpose of complying 
    with the previously approved emissions average.
        (e) For all emission points included in an emissions average, the 
    owner or operator shall perform the following tasks:
        (1) Calculate and record monthly debits for all Group 1 emission 
    points that are controlled to a level less stringent than the reference 
    control technology or standard for those emission points. The Group 1 
    emission points are identified in paragraphs (c)(2) through (c)(4) of 
    this section. Equations in paragraph (g) of this section shall be used 
    to calculate debits.
        (2) Calculate and record monthly credits for all Group 1 and Group 
    2 emission points that are overcontrolled to compensate for the debits. 
    Equations in paragraph (h) of this section shall be used to calculate 
    credits. Emission points and controls that meet the criteria of 
    paragraph (c) of this section may be included in the credit 
    calculation, whereas those described in paragraph (d) of this section 
    shall not be included.
        (3) Demonstrate that annual credits calculated according to 
    paragraph (h) of this section are greater than or equal to debits 
    calculated for the same annual compliance period according to paragraph 
    (g) of this section.
        (i) The owner or operator may choose to include more than the 
    required number of credit-generating emission points in an emissions 
    average in order to increase the likelihood of being in compliance.
        (ii) The initial demonstration in the Emissions Averaging Plan or 
    operating permit application that credit-generating emission points 
    will be capable of generating sufficient credits to offset the debits 
    from the debit-generating emission points must be made under 
    representative operating conditions. After the compliance date, actual 
    operating data will be used for all debit and credit calculations.
        (4) Demonstrate that debits calculated for a quarterly (3-month) 
    period according to paragraph (g) of this section are not more than 
    1.30 times the credits for the same period calculated according to 
    paragraph (h) of this section. Compliance for the quarter shall be 
    determined based on the ratio of credits and debits from that quarter, 
    with 30 percent more debits than credits allowed on a quarterly basis.
        (5) Record and report quarterly and annual credits and debits in 
    the Periodic Reports as specified in Sec. 63.506(e)(6). Every fourth 
    Periodic Report shall include a certification of compliance with the 
    emissions averaging provisions as required by 
    Sec. 63.506(e)(6)(vi)(D)(2).
        (f) Debits and credits shall be calculated in accordance with the 
    methods and procedures specified in paragraphs (g) and (h) of this 
    section, respectively, and shall not include emissions during the 
    following periods:
        (1) Emissions during periods of startup, shutdown, and malfunction 
    as described in the Startup, Shutdown, and Malfunction Plan.
        (2) Emissions during periods of monitoring excursions, as defined 
    in Sec. 63.505 (g) or (h). For these periods, the calculation of 
    monthly credits and debits shall be adjusted as specified in paragraphs 
    (f)(2)(i) through (f)(2)(iii) of this section.
        (i) No credits would be assigned to the credit-generating emission 
    point.
        (ii) Maximum debits would be assigned to the debit-generating 
    emission point.
        (iii) The owner or operator may demonstrate to the Administrator 
    that full or partial credits or debits should be assigned using the 
    procedures in paragraph (l) of this section.
        (g) Debits are generated by the difference between the actual 
    emissions from a Group 1 emission point that is uncontrolled or is 
    controlled to a level less stringent than the applicable reference 
    control technology or standard and the emissions allowed for the Group 
    1 emission point. Debits shall be calculated as follows:
        (1) Source-wide debits shall be calculated using Equation 33. 
    Debits and all terms of the equation are in units of megagrams per 
    month (Mg/month).
    
    [[Page 46959]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.031
    
    
    where:
    ECFEPViACTUAL=Emissions from each Group 1 continuous front-end 
    process vent i that is uncontrolled or is controlled to a level less 
    stringent than the applicable reference control technology. 
    ECFEPViACTUAL is calculated according to paragraph (g)(2)(iii) of 
    this section.
    (0.02)ECFEPViu=Emissions from each Group 1 continuous front-end 
    process vent i if the applicable reference control technology had been 
    applied to the uncontrolled emissions. ECFEPViu is calculated 
    according to paragraph (g)(2)(ii) of this section.
    ESiACTUAL=Emissions from each Group 1 storage vessel i that is 
    uncontrolled or is controlled to a level less stringent than the 
    applicable reference control technology or standard. ESiACTUAL is 
    calculated according to paragraph (g)(3) of this section.
    (0.05)ESiu=Emissions from each Group 1 storage vessel i if the 
    applicable reference control technology or standard had been applied to 
    the uncontrolled emissions. ESiu is calculated according to 
    paragraph (g)(3) of this section.
    EBEPACTUAL=Emissions from back-end process operations that do not 
    meet the residual organic HAP limits in Sec. 63.494. EBEPACTUAL is 
    calculated according to paragraph (g)(4)(i) of this section.
    EBEPc=Emissions from back-end process operations if the residual 
    organic HAP limits in Sec. 63.494(a) were met. EBEPc is calculated 
    according to paragraph (g)(4)(ii) of this section.
    EWWiACTUAL=Emissions from each Group 1 wastewater stream i that is 
    uncontrolled or is controlled to a level less stringent than the 
    applicable reference control technology. EWW2iACTUAL is calculated 
    according to paragraph (g)(5) of this section.
    EWWic=Emissions from each Group 1 wastewater stream i if the 
    reference control technology had been applied to the uncontrolled 
    emissions. EWWic is calculated according to paragraph (g)(5) of 
    this section.
    EBFEPViACTUAL=Emissions from each Group 1 batch front-end process 
    vent stream i that is uncontrolled or is controlled to a level less 
    stringent than the reference control technology. EBFEPViACTUAL is 
    calculated according to paragraph (g)(6)(ii) of this section.
    (0.1)EBFEPViu=Emissions from each Group 1 batch front-end process 
    vent i if the applicable reference control technology or standard had 
    been applied to the uncontrolled emissions. EBFEPViu is calculated 
    according to paragraph (g)(6)(i) of this section.
    EABViACTUAL=Emissions from each Group 1 aggregate batch vent 
    stream i that is uncontrolled or is controlled to a level less 
    stringent than the applicable reference control technology. 
    EABViACTUAL is calculated according to paragraph (g)(7)(iii) of 
    this section.
    (0.1)EABViu=Emissions from each Group 1 aggregate batch vent 
    stream i if the applicable reference control technology had been 
    applied to the uncontrolled emissions. EABViu is calculated 
    according to paragraph (g)(7)(ii) of this section.
    n=The number of emission points being included in the emissions 
    average.
    
        (2) Emissions from continuous front-end process vents shall be 
    calculated as follows:
        (i) For purposes of determining continuous front-end process vent 
    stream flow rate, organic HAP concentrations, and temperature, the 
    sampling site shall be after the final product recovery device, if any 
    recovery devices are present; before any control device (for continuous 
    front-end process vents, recovery devices shall not be considered 
    control devices); and before discharge to the atmosphere. Method 1 or 
    1A of 40 CFR part 60, appendix A, shall be used for selection of the 
    sampling site.
        (ii) ECFEPViu for each continuous front-end process vent i 
    shall be calculated using Equation 34.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.032
    
    where:
    ECFEPViu=Uncontrolled continuous front-end process vent emission 
    rate from continuous front-end process vent i, Mg/month.
    Q=Vent stream flow rate, dry standard m3/min, measured using 
    Method 2, 2A, 2C, or 2D of 40 CFR part 60, appendix A, as appropriate.
    h=Monthly hours of operation during which positive flow is present in 
    the continuous front-end process vent, hr/month.
    Cj=Concentration, ppmv, dry basis, of organic HAP j as measured by 
    Method 18 or Method 25A of 40 CFR part 60, appendix A.
    
    [[Page 46960]]
    
    Mj=Molecular weight of organic HAP j, gram per gram-mole.
    n=Number of organic HAP in stream.
    
        (A) The values of Q and Cj shall be determined during a 
    performance test conducted under representative operating conditions. 
    The values of Q and Cj shall be established in the Notification of 
    Compliance Status and must be updated as provided in paragraph 
    (g)(2)(ii)(B) of this section.
        (B) If there is a change in capacity utilization other than a 
    change in monthly operating hours, or if any other change is made to 
    the process or product recovery equipment or operation such that the 
    previously measured values of Q and Cj are no longer 
    representative, a new performance test shall be conducted to determine 
    new representative values of Q and Cj. These new values shall be 
    used to calculate debits and credits from the time of the change 
    forward, and the new values shall be reported in the next Periodic 
    Report.
        (iii) The following procedures and equations shall be used to 
    calculate ECFEPViACTUAL:
        (A) If the continuous front-end process vent is not controlled by a 
    control device or pollution prevention measure, ECFEPViACTUAL = 
    ECFEPViu, where ECFEPViu is calculated according to the 
    procedures contained in paragraphs (g)(2)(i) and (g)(2)(ii) of this 
    section.
        (B) If the continuous front-end process vent is controlled using a 
    control device or a pollution prevention measure achieving less than 
    98-percent reduction, ECFEPViACTUAL is calculated using Equation 
    35.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.033
    
    Where:
    
    ECFEPViACTUAL = Emissions from each Group 1 continuous front-end 
    process vent i that is uncontrolled or is controlled to a level less 
    stringent than the reference control technology.
    ECFEPViu = Uncontrolled continuous front-end process vent emission 
    rate from continuous front-end process vent i, Mg/month.
        (1) The percent reduction shall be measured according to the 
    procedures in Sec. 63.116 of subpart G if a combustion control device 
    is used. For a flare meeting the criteria in Sec. 63.116(a) of subpart 
    G, or a boiler or process heater meeting the criteria in Sec. 63.116(b) 
    of subpart G, the percent reduction shall be 98 percent. If a 
    noncombustion control device is used, percent reduction shall be 
    demonstrated by a performance test at the inlet and outlet of the 
    device, or, if testing is not feasible, by a control design evaluation 
    and documented engineering calculations.
        (2) For determining debits from Group 1 continuous front-end 
    process vents, product recovery devices shall not be considered control 
    devices and cannot be assigned a percent reduction in calculating 
    ECFEPViACTUAL. The sampling site for measurement of uncontrolled 
    emissions is after the final product recovery device. However, as 
    provided in Sec. 63.113(a)(3) of subpart G, a Group 1 continuous front-
    end process vent may add sufficient product recovery to raise the TRE 
    index value above 1.0, thereby becoming a Group 2 continuous front-end 
    process vent. Such a continuous front-end process vent would not be a 
    Group 1 continuous front-end process vent and would, therefore, not be 
    included in determining debits under this paragraph.
        (3) Procedures for calculating the percent reduction of pollution 
    prevention measures are specified in paragraph (j) of this section.
        (3) Emissions from storage vessels shall be calculated using the 
    procedures specified in Sec. 63.150(g)(3) of subpart G.
        (4) Emissions from back-end process operations shall be calculated 
    as follows:
        (i) Equation 36 shall be used to calculate EBEPACTUAL:
        [GRAPHIC] [TIFF OMITTED] TR05SE96.034
        
    where:
    
    EBEPACTUAL = Actual emissions from back-end process operations, 
    Mg/month.
    Ci = Residual organic HAP content of sample i, kg organic HAP per 
    Mg latex or dry crumb rubber.
    Pi = Weight of latex or dry crumb rubber leaving the stripper 
    represented by sample i, Mg.
        (ii) Equation 37 shall be used to calculate EBEPc:
        [GRAPHIC] [TIFF OMITTED] TR05SE96.051
        
    where:
    
    EBEPc = Emissions from back-end process operations if the residual 
    organic HAP limits in Sec. 63.494(a) were met, Mg/month.
    HAPlimit = Residual organic HAP limits in Sec. 63.494 of this 
    subpart, kg organic HAP per Mg latex or dry crumb rubber.
    Pmonth=Weight of latex or dry crumb rubber leaving the stripper in 
    the month, Mg.
    
        (5) Emissions from wastewater shall be calculated using the 
    procedures specified in Sec. 63.150(g)(5) of subpart G.
        (6) Emissions from batch front-end process vents shall be 
    calculated as follows:
        (i) EBFEPViu for each batch front-end process vent i shall be 
    calculated using the procedures specified in Sec. 63.488(b).
        (ii) The following procedures and equations shall be used to 
    determine EBFEPViACTUAL:
        (A) If the batch front-end process vent is not controlled by a 
    control device or pollution prevention measure,
    
    [[Page 46961]]
    
    EBFEPViACTUAL=EBFEPViu, where EBFEPViu is calculated 
    according to the procedures in Sec. 63.488(b).
        (B) If the batch front-end process vent is controlled using a 
    control device or a pollution prevention measure achieving less than 90 
    percent reduction for the batch cycle, calculate EBFEPViACTUAL 
    using Equation 38, where percent reduction is for the batch cycle.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.035
    
        (1) The percent reduction for the batch cycle shall be measured 
    according to the procedures in Sec. 63.490(c)(2).
        (2) The percent reduction for control devices shall be calculated 
    according to the procedures in Sec. 63.490 (c)(2)(i) through 
    (c)(2)(iii).
        (3) The percent reduction of pollution prevention measures shall be 
    calculated using the procedures specified in paragraph (j) of this 
    section.
        (7) Emissions from aggregate batch vents shall be calculated as 
    follows:
        (i) For purposes of determining aggregate batch vent stream flow 
    rate, organic HAP concentrations, and temperature, the sampling site 
    shall be before any control device and before discharge to the 
    atmosphere. Method 1 or 1A of 40 CFR part 60, appendix A, shall be used 
    for selection of the sampling site.
        (ii) EABViu for each aggregate batch vent i shall be 
    calculated using Equation 39.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.036
    
    where:
    
    EABViu=Uncontrolled aggregate batch vent emission rate from 
    aggregate batch vent i, Mg/month.
    Q=Vent stream flow rate, dry standard cubic meters per minute, measured 
    using Method 2, 2A, 2C, or 2D of 40 CFR part 60, appendix A, as 
    appropriate.
    h=Monthly hours of operation during which positive flow is present from 
    the aggregate batch vent stream, hr/month.
    Cj=Concentration, ppmv, dry basis, of organic HAP j as measured by 
    Method 18 of 40 CFR part 60, appendix A.
    Mj=Molecular weight of organic HAP j, gram per gram-mole.
    n=Number of organic HAP in the stream.
    
        (A) The values of Q and Cj shall be determined during a 
    performance test conducted under representative operating conditions. 
    The values of Q and Cj shall be established in the Notification of 
    Compliance Status and must be updated as provided in paragraph 
    (g)(7)(ii)(B) of this section.
        (B) If there is a change in capacity utilization other than a 
    change in monthly operating hours, or if any other change is made to 
    the process or product recovery equipment or operation such that the 
    previously measured values of Q and Cj are no longer 
    representative, a new performance test shall be conducted to determine 
    new representative values of Q and Cj. These new values shall be 
    used to calculate debits and credits from the time of the change 
    forward, and the new values shall be reported in the next Periodic 
    Report.
        (iii) The following procedures and equations shall be used to 
    calculate EABViACTUAL:
        (A) If the aggregate batch vent is not controlled by a control 
    device or pollution prevention measure, EABViACTUAL = EABViu, 
    where EABViu is calculated according to the procedures in 
    paragraphs (g)(7)(i) and (g)(7)(ii) of this section.
        (B) If the aggregate batch vent stream is controlled using a 
    control device or a pollution prevention measure achieving less than 90 
    percent reduction, calculate EABViACTUAL using Equation 40.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.037
    
        (1) The percent reduction for control devices shall be determined 
    according to the procedures in Sec. 63.490(e).
        (2) The percent reduction of pollution prevention measures shall be 
    calculated according to the procedures specified in paragraph (j) of 
    this section.
        (h) Credits are generated by the difference between emissions that 
    are allowed for each Group 1 and Group 2 emission point and the actual 
    emissions from that Group 1 or Group 2 emission point that has been 
    controlled after November 15, 1990 to a level more stringent than what 
    is required by this subpart or any other State or Federal rule or 
    statute. Credits shall be calculated as follows:
        (1) Source-wide credits shall be calculated using Equation 41. 
    Credits and all terms of the equation are in units of Mg/month, and the 
    baseline date is November 15, 1990.
    
    [[Page 46962]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.038
    
    
    where:
    D = Discount factor = 0.9 for all credit generating emission points, 
    except those controlled by a pollution prevention measure; discount 
    factor = 1.0 for each credit generating emission point controlled by a 
    pollution prevention measure (i.e., no discount provided).
    ECFEPV1iACTUAL = Emissions for each Group 1 continuous front-end 
    process vent i that is controlled to a level more stringent than the 
    reference control technology. ECFEPV1iACTUAL is calculated 
    according to paragraph (h)(2)(ii) of this section.
    (0.02)ECFEPV1iu = Emissions from each Group 1 continuous front-end 
    process vent i if the reference control technology had been applied to 
    the uncontrolled emissions. ECFEPV1iu is calculated according to 
    paragraph (h)(2)(i) of this section.
    ECFEPV2iACTUAL = Emissions from each Group 2 continuous front-end 
    process vent i that is controlled. ECFEPV2iACTUAL is calculated 
    according to paragraph (h)(2)(iii) of this section.
    ECFEPV2iBASE = Emissions from each Group 2 continuous front-end 
    process vent i at the baseline date. ECFEPV1iBASE is calculated in 
    paragraph (h)(2)(iv) of this section.
    ES1iACTUAL = Emissions from each Group 1 storage vessel i that is 
    controlled to a level more stringent than the reference control 
    technology or standard. ES1iACTUAL is calculated according to 
    paragraph (h)(3) of this section.
    (0.05) ES1iu = Emissions from each Group 1 storage vessel i if the 
    reference control technology had been applied to the uncontrolled 
    emissions. ES1iu is calculated according to paragraph (h)(3) of 
    this section.
    ES2iACTUAL = Emissions from each Group 2 storage vessel i that is 
    controlled. ES2iACTUAL is calculated according to paragraph (h)(3) 
    of this section.
    ES2iBASE = Emissions from each Group 2 storage vessel i at the 
    baseline date. ES2iBASE is calculated in paragraph (h)(3) of this 
    section.
    EBEPACTUAL = Actual emissions from back-end process operations, 
    Mg/month. EBEPACTUAL is calculated in paragraph (h)(4)(i) of this 
    section.
    EBEPc = Emissions from back-end process operations if the residual 
    organic HAP limits in Sec. 63.494(a) were met, Mg/month. EBEPc is 
    calculated in paragraph (h)(4)(ii) of this section.
    EWW1iACTUAL = Emissions from each Group 1 wastewater stream i that 
    is controlled to a level more stringent than the reference control 
    technology. EWW1iACTUAL is calculated according to paragraph 
    (h)(5) of this section.
    EWW1ic = Emissions from each Group 1 wastewater stream i if the 
    reference control technology had been applied to the uncontrolled 
    emissions. EWW1ic is calculated according to paragraph (h)(5) of 
    this section.
    EWW2iACTUAL = Emissions from each Group 2 wastewater stream i that 
    is controlled. EWW2iACTUAL is calculated according to paragraph 
    (h)(5) of this section.
    EWW2iBASE = Emissions from each Group 2 wastewater stream i at the 
    baseline date. EWW2iBASE is calculated according to paragraph 
    (h)(5) of this section.
    (0.1) EBFEPV1iu = Emissions from each Group 1 batch front-end 
    process vent i if the applicable reference control technology had been 
    applied to the uncontrolled emissions. EBFEPViu is calculated 
    according to paragraph (h)(6)(i) of this section.
    EBFEPV1iACTUAL = Emissions from each Group 1 batch front-end 
    process vent i that is controlled to a level more stringent than the 
    reference control technology. EBFEPV1iACTUAL is calculated 
    according to paragraph (h)(6)(ii) of this section.
    (0.1)EABV1iu = Emissions from each Group 1 aggregate batch vent 
    stream i if the applicable reference control technology had been 
    applied to the uncontrolled emissions. EABV1iu is calculated 
    according to paragraph (h)(7)(i) of this section.
    EABV1iACTUAL = Emissions from each Group 1 aggregate batch vent 
    stream i that is controlled to a level more stringent than the 
    reference control technology or standard. EABV1iACTUAL is 
    calculated according to paragraph (h)(7)(ii) of this section.
    EBFEPV2iBASE = Emissions from each Group 2 batch front-end process 
    vent i at the baseline date. EBFEPV2iBASE is calculated according 
    to paragraph (h)(6)(iv) of this section.
    EBFEPV2iACTUAL = Emissions from each Group 2 batch front-end 
    process vent i that is controlled. EBFEPV2iACTUAL is calculated 
    according to paragraph (h)(6)(iii) of this section.
    EABV2iBASE = Emissions from each Group 2 aggregate batch vent 
    stream i at the baseline date. EABV2iBASE is calculated according 
    to paragraph (g)(7)(iv) of this section.
    EABV2iACTUAL = Emissions from each Group 2 aggregate batch vent 
    stream i that is controlled. EABV2iACTUAL is calculated according 
    to paragraph (g)(7)(iii) of this section.
    
    [[Page 46963]]
    
    n = Number of Group 1 emission points included in the emissions 
    average. The value of n is not necessarily the same for continuous 
    front-end process vents, batch front-end process vents, aggregate batch 
    vent streams, storage vessels, wastewater streams, or the collection of 
    process sections within the affected source.
    m = Number of Group 2 emission points included in the emissions 
    average. The value of m is not necessarily the same for continuous 
    front-end process vents, batch front-end process vents, aggregate batch 
    vent streams, storage vessels, wastewater streams, or the collection of 
    process sections within the affected source.
        (i) Except as specified in paragraph (h)(1)(iv) of this section, 
    for an emission point controlled using a reference control technology, 
    the percent reduction for calculating credits shall be no greater than 
    the nominal efficiency associated with the reference control 
    technology, unless a higher nominal efficiency is assigned as specified 
    in paragraph (h)(1)(ii) of this section.
        (ii) For an emission point controlled to a level more stringent 
    than the reference control technology, the nominal efficiency for 
    calculating credits shall be assigned as described in paragraph (i) of 
    this section. A reference control technology may be approved for use in 
    a different manner and assigned a higher nominal efficiency according 
    to the procedures in paragraph (i) of this section. A reference control 
    technology may be approved for use in a different manner and assigned a 
    higher nominal efficiency according to the procedure in paragraph (i) 
    of this section.
        (iii) For an emission point controlled using a pollution prevention 
    measure, except for back-end process operation emissions, the nominal 
    efficiency for calculating credits shall be as determined as described 
    in paragraph (j) of this section. Emissions for back-end process 
    operations shall be determined as described in paragraph (h)(4) of this 
    section.
        (iv) For Group 1 and Group 2 batch front-end process vents and 
    Group 1 and Group 2 aggregate batch vent streams, the percent reduction 
    for calculating credits shall be the percent reduction determined 
    according to the procedures in paragraphs (h)(6)(ii) and (h)(6)(iii) of 
    this section for batch front-end process vents and paragraphs 
    (h)(7)(ii) and (h)(7)(iii) of this section for aggregate batch vent 
    streams.
        (2) Emissions from continuous front-end process vents shall be 
    determined as follows:
        (i) Uncontrolled emissions from Group 1 continuous front-end 
    process vents, ECFEPV1iu, shall be calculated according to the 
    procedures and equation for ECFEPViu in paragraphs (g)(2)(i) and 
    (g)(2)(ii) of this section.
        (ii) Actual emissions from Group 1 continuous front-end process 
    vents controlled using a technology with an approved nominal efficiency 
    greater than 98 percent or a pollution prevention measure achieving 
    greater than 98 percent emission reduction, ECFEPV1iACTUAL, shall 
    be calculated using Equation 42.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.039
    
    Where:
    ECFEPV1iACTUAL = Emissions for each Group 1 continuous front-end 
    process vent i that is controlled to a level more stringent than the 
    reference control technology.
    ECFEPV1iu = Emissions from each Group 1 continuous front-end 
    process vent i if the reference control technology had been applied to 
    the uncontrolled emissions.
        (iii) The following procedures shall be used to calculate actual 
    emissions from Group 2 continuous front-end process vents, 
    ECFEPV2iACTUAL:
        (A) For a Group 2 continuous front-end process vent controlled by a 
    control device, a recovery device applied as a pollution prevention 
    project, or a pollution prevention measure, where the control achieves 
    a percent reduction less than or equal to 98 percent reduction, 
    Equation 43 shall be used.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.040
    
        Where:
    ECFEPV2iACTUAL=Emissions from each Group 2 continuous
    front-end process vent i that is controlled.
    ECFEPV2iu=Emissions from each Group 2 continuous front-end process 
    vent i if the reference control technology had been applied to the 
    uncontrolled emissions.
        (1) ECFEPV2iu shall be calculated according to the equations 
    and procedures for ECFEPViu in paragraphs (g)(2)(i) and 
    (g)(2)(ii) of this section, except as provided in paragraph 
    (h)(2)(iii)(A)(3) of this section.
        (2) The percent reduction shall be calculated according to the 
    procedures in paragraphs (g)(2)(iii)(B)(1) through (g)(2)(iii)(B)(3) of 
    this section, except as provided in paragraph (h)(2)(iii)(A)(4) of this 
    section.
        (3) If a recovery device was added as part of a pollution 
    prevention project, ECFEPV2iu shall be calculated prior to that 
    recovery device. The equation for ECFEPViu in paragraph (g)(2)(ii) 
    of this section shall be used to calculate ECFEPV2iu; however, the 
    sampling site for measurement of vent stream flow rate and organic HAP 
    concentration shall be at the inlet of the recovery device.
        (4) If a recovery device was added as part of a pollution 
    prevention project, the percent reduction shall be demonstrated by 
    conducting a performance test at the inlet and outlet of that recovery 
    device.
        (B) For a Group 2 continuous front-end process vent controlled 
    using a technology with an approved nominal efficiency greater than 98 
    percent or a pollution prevention measure achieving greater than 98 
    percent reduction, Equation 44 shall be used.
    
    [[Page 46964]]
    
    [GRAPHIC] [TIFF OMITTED] TR05SE96.041
    
    
    Where:
    ECFEPV2iACTUAL=Emissions from each Group 2 continuous
    front-end process vent i that is controlled.
    ECFEPV2iu=Emissions from each Group 2 continuous front-end process 
    vent i if the reference control technology had been applied to the 
    uncontrolled emissions.
        (iv) Emissions from Group 2 continuous front-end process vents at 
    baseline, ECFEPV2iBASE, shall be calculated as follows:
        (A) If the continuous front-end process vent was uncontrolled on 
    November 15, 1990, ECFEPV2iBASE=ECFEPV2iu and shall be 
    calculated according to the procedures and equation for ECFEPViu 
    in paragraphs (g)(2)(i) and (g)(2)(ii) of this section.
        (B) If the continuous front-end process vent was controlled on 
    November 15, 1990, Equation 45 shall be used.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.042
    
        (1) ECFEPV2iu is calculated according to the procedures and 
    equation for ECFEPViu in paragraphs (g)(2)(i) and (g)(2)(ii) of 
    this section.
        (2) The percent reduction shall be calculated according to the 
    procedures specified in paragraphs (g)(2)(iii)(B)(1) through 
    (g)(2)(iii)(B)(3) of this section.
        (C) If a recovery device was added as part of a pollution 
    prevention project initiated after November 15, 1990, 
    ECFEPV2iBASE=ECFEPV2iu, where ECFEPV2iu is calculated 
    according to paragraph (h)(2)(iii)(A)(3) of this section.
        (3) Emissions from storage vessels shall be calculated using the 
    procedures specified in Sec. 63.150(h)(3) of subpart G.
        (4) Emissions from back-end process operations shall be calculated 
    as follows:
        (i) EBEPACTUAL shall be calculated according to the equation 
    for EBEPACTUAL contained in paragraph (g)(4)(i) of this section.
        (ii) EBEPc shall be calculated according to the equation for 
    EBEPc contained in paragraph (g)(4)(ii) of this section.
        (5) Emissions from wastewater streams shall be calculated using the 
    procedures specified in Sec. 63.150(h)(5) of subpart G.
        (6) Emissions from batch front-end process vents shall be 
    determined as follows:
        (i) Uncontrolled emissions from Group 1 batch front-end process 
    vents (EBFEPV1iu) shall be calculated according using the 
    procedures specified in Sec. 63.488(b).
        (ii) Actual emissions from Group 1 batch front-end process vents 
    controlled to a level more stringent than the reference control 
    technology (EBFEPV1iACTUAL) shall be calculated using Equation 46, 
    where percent reduction is for the batch cycle.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.043
    
        (A) The percent reduction for the batch cycle shall be calculated 
    according to the procedures in Sec. 63.490(c)(2).
        (B) The percent reduction for control devices shall be determined 
    according to the procedures in Sec. 63.490(c)(2)(i) through 
    (c)(2)(iii).
        (C) The percent reduction of pollution prevention measures shall be 
    calculated using the procedures specified in paragraph (j) of this 
    section.
        (iii) Actual emissions from Group 2 batch front-end process vents 
    (EBFEPV2iACTUAL) shall be calculated using Equation 47 and the 
    procedures in paragraphs (h)(6)(ii)(A) through (h)(6)(ii)(C) of this 
    section. EBFEPV2iu shall be calculated using the procedures 
    specified in Sec. 63.488(b).
    [GRAPHIC] [TIFF OMITTED] TR05SE96.044
    
        (iv) Emissions from Group 2 batch front-end process vents at 
    baseline shall be calculated as follows:
        (A) If the batch front-end process vent was uncontrolled on 
    November 15, 1990, EBFEPV2iBASE=EBFEPV2iu and shall be 
    calculated according to the procedures using the procedures specified 
    in Sec. 63.488(b).
        (B) If the batch front-end process vent was controlled on November 
    15, 1990, use Equation 48 and the procedures in paragraphs 
    (h)(6)(ii)(A) through (h)(6)(ii)(C) of this section. EBFEPV2iu 
    shall be calculated using the procedures specified in Sec. 63.488(b).
    [GRAPHIC] [TIFF OMITTED] TR05SE96.045
    
    
    [[Page 46965]]
    
    
        (7) Emissions from aggregate batch vent streams shall be determined 
    as follows:
        (i) Uncontrolled emissions from Group 1 aggregate batch vent 
    streams (EABV1iu) shall be calculated according to the procedures 
    and equation for EABViu in paragraphs (g)(7)(i) and (g)(7)(ii) of 
    this section.
        (ii) Actual emissions from Group 1 aggregate batch vent streams 
    controlled to a level more stringent than the reference control 
    technology (EABV1iACTUAL) shall be calculated using Equation 49.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.046
    
        (A) The percent reduction for control devices shall be determined 
    according to the procedures in Sec. 63.490(e).
        (B) The percent reduction of pollution prevention measures shall be 
    calculated using the procedures specified in paragraph (j) of this 
    section.
        (iii) Actual emissions from Group 2 aggregate batch vents streams 
    (EABV2iACTUAL) shall be calculated using Equation 50 and the 
    procedures in paragraphs (h)(7)(ii)(A) through (h)(7)(ii)(B) of this 
    section. EABV2iu shall be calculated according to the equations 
    and procedures for EABViu in paragraphs (g)(7)(i) and (g)(7)(ii) 
    of this section.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.047
    
        (iv) Emissions from Group 2 aggregate batch vent streams at 
    baseline shall be calculated as follows:
        (A) If the aggregate batch vent stream was uncontrolled on November 
    15, 1990, EABV2iBASE=EABV2iu and shall be calculated 
    according to the procedures and equation for EABViu in paragraph 
    (g)(7)(i) and (g)(7)(ii) of this section.
        (B) If the aggregate batch vent stream was controlled on November 
    15, 1990, use Equation 51 and the procedures in paragraphs 
    (h)(7)(ii)(A) through (h)(7)(ii)(B) of this section. EABV2iu shall 
    be calculated according to the equations and procedures for EABViu 
    in paragraphs (g)(7)(i) and (g)(7)(ii) of this section.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.048
    
        (i) The following procedures shall be followed to establish nominal 
    efficiencies for emission controls for storage vessels, continuous 
    front-end process vents, and process wastewater streams. The procedures 
    in paragraphs (i)(1) through (i)(6) of this section shall be followed 
    for control technologies that are different in use or design from the 
    reference control technologies and achieve greater percent reductions 
    than the percent efficiencies assigned to the reference control 
    technologies in Sec. 63.111 of subpart G.
        (1) In those cases where the owner or operator is seeking 
    permission to take credit for use of a control technology that is 
    different in use or design from the reference control technology, and 
    the different control technology will be used in more than three 
    applications at a single plant-site, the owner or operator shall submit 
    the information specified in paragraphs (i)(1)(i) through (i)(1)(iv) of 
    this section to the Director of the EPA Office of Air Quality Planning 
    and Standards, in writing.
        (i) Emission stream characteristics of each emission point to which 
    the control technology is or will be applied, including the kind of 
    emission point, flow, organic HAP concentration, and all other stream 
    characteristics necessary to design the control technology or determine 
    its performance.
        (ii) Description of the control technology, including design 
    specifications.
        (iii) Documentation demonstrating to the Administrator's 
    satisfaction the control efficiency of the control technology. This may 
    include performance test data collected using an appropriate EPA Method 
    or any other method validated according to Method 301 of appendix A. If 
    it is infeasible to obtain test data, documentation may include a 
    design evaluation and calculations. The engineering basis of the 
    calculation procedures and all inputs and assumptions made in the 
    calculations shall be documented.
        (iv) A description of the parameter or parameters to be monitored 
    to ensure that the control technology will be operated in conformance 
    with its design and an explanation of the criteria used for selection 
    of that parameter (or parameters).
        (2) The Administrator shall determine within 120 operating days 
    whether an application presents sufficient information to determine 
    nominal efficiency. The Administrator reserves the right to request 
    specific data in addition to the items listed in paragraph (i)(1) of 
    this section.
        (3) The Administrator shall determine within 120 operating days of 
    the submittal of sufficient data whether a control technology shall 
    have a nominal efficiency and the level of that nominal efficiency. If, 
    in the Administrator's judgment, the control technology achieves a 
    level of emission reduction greater than the reference control 
    technology for a particular kind of emission point, the Administrator 
    will publish a Federal Register notice establishing a nominal 
    efficiency for the control technology.
    
    [[Page 46966]]
    
        (4) The Administrator may grant permission to take emission credits 
    for use of the control technology. The Administrator may also impose 
    requirements that may be necessary to ensure operation and maintenance 
    to achieve the specified nominal efficiency.
        (5) In those cases where the owner or operator is seeking 
    permission to take credit for use of a control technology that is 
    different in use or design from the reference control technology and 
    the different control technology will be used in no more than three 
    applications at a single plant site, the information listed in 
    paragraph (i)(1)(i) can be submitted to the permitting authority for 
    the affected source for approval instead of the Administrator.
        (i) In these instances, use and conditions for use of the control 
    technology can be approved by the permitting authority as part of an 
    operating permit application or modification. The permitting authority 
    shall follow the procedures specified in paragraphs (i)(2) through 
    (i)(4) of this section except that, in these instances, a Federal 
    Register notice is not required to establish the nominal efficiency for 
    the different technology.
        (ii) If, in reviewing the application, the permitting authority 
    believes the control technology has broad applicability for use by 
    other sources, the permitting authority shall submit the information 
    provided in the application to the Director of the EPA Office of Air 
    Quality Planning and Standards. The Administrator shall review the 
    technology for broad applicability and may publish a Federal Register 
    notice; however, this review shall not affect the permitting 
    authority's approval of the nominal efficiency of the control 
    technology for the specific application.
        (6) If, in reviewing an application for a control technology for an 
    emission point, the Administrator or permitting authority determines 
    that the control technology is not different in use or design from the 
    reference control technology, the Administrator or permitting authority 
    shall deny the application.
        (j) The following procedures shall be used for calculating the 
    efficiency (percent reduction) of pollution prevention measures for 
    storage vessels, continuous front-end process vents, batch front-end 
    process vents, aggregate batch vent streams, and wastewater streams:
        (1) A pollution prevention measure is any practice which meets the 
    criteria of paragraphs (j)(1)(i) and (j)(1)(ii) of this section.
        (i) A pollution prevention measure is any practice that results in 
    a lesser quantity of organic HAP emissions per unit of product released 
    to the atmosphere prior to out-of-process recycling, treatment, or 
    control of emissions, while the same product is produced.
        (ii) Pollution prevention measures may include substitution of 
    feedstocks that reduce organic HAP emissions; alterations to the 
    production process to reduce the volume of materials released to the 
    environment; equipment modifications; housekeeping measures; and in-
    process recycling that returns waste materials directly to production 
    as raw materials. Production cutbacks do not qualify as pollution 
    prevention.
        (2) The emission reduction efficiency of pollution prevention 
    measures implemented after November 15, 1990, can be used in 
    calculating the actual emissions from an emission point in the debit 
    and credit equations in paragraphs (g) and (h) of this section.
        (i) For pollution prevention measures, the percent reduction is 
    used in the equations in paragraphs (g)(2) through (g)(7) of this 
    section and paragraphs (h)(2) through (h)(7) of this section is the 
    percent difference between the monthly organic HAP emissions for each 
    emission point after the pollution prevention measure for the most 
    recent month versus monthly emissions from the same emission point 
    before the pollution prevention measure, adjusted by the volume of 
    product produced during the two monthly periods.
        (ii) Equation 52 shall be used to calculate the percent reduction 
    of a pollution prevention measure for each emission point.
    [GRAPHIC] [TIFF OMITTED] TR05SE96.049
    
    where:
    
    Percent reduction=Efficiency of pollution prevention measure (percent 
    organic HAP reduction).
    EB=Monthly emissions before the pollution prevention measure, Mg/
    month, determined as specified in paragraphs (j)(2)(ii)(A), 
    (j)(2)(ii)(B), and (j)(2)(ii)(C) of this section.
    Epp=Monthly emissions after the pollution prevention measure, Mg/
    month, as determined for the most recent month, determined as specified 
    in either paragraphs (j)(2)(ii)(D) or (j)(2)(ii)(E) of this section.
    PB=Monthly production before the pollution prevention measure, Mg/
    month, during the same period over which EB is calculated.
    Ppp=Monthly production after the pollution prevention measure, Mg/
    month, as determined for the most recent month.
    
        (A) The monthly emissions before the pollution prevention measure, 
    EB, shall be determined in a manner consistent with the equations 
    and procedures in paragraph (g)(2) of this section for continuous 
    front-end process vents, paragraph (g)(3) of this section for storage 
    vessels, paragraph (g)(6) of this section for batch front-end process 
    vents, and paragraph (g)(7) of this section for aggregate batch vent 
    streams.
        (B) For wastewater, E B shall be calculated according to 
    Sec. 63.150(j)(2)(ii)(B) of subpart G.
        (C) If the pollution prevention measure was implemented prior to 
    September 5, 1996, records may be used to determine E B.
        (D) The monthly emissions after the pollution prevention measure, E 
    pp, may be determined during a performance test or by a design 
    evaluation and documented engineering calculations. Once an emissions-
    to-production ratio has been established, the ratio can be used to 
    estimate monthly emissions from monthly production records.
        (E) For wastewater, E pp shall be calculated according to 
    Sec. 63.150(j)(2)(ii)(E) of subpart G.
        (iii) All equations, calculations, test procedures, test results, 
    and other information used to determine the percent reduction achieved 
    by a pollution prevention measure for each emission point shall be 
    fully documented.
    
    [[Page 46967]]
    
        (iv) The same pollution prevention measure may reduce emissions 
    from multiple emission points. In such cases, the percent reduction in 
    emissions for each emission point must be calculated.
        (v) For the purposes of the equations in paragraphs (h)(2) through 
    (h)(7) of this section, used to calculate credits for emission points 
    controlled more stringently than the reference control technology, the 
    nominal efficiency of a pollution prevention measure is equivalent to 
    the percent reduction of the pollution prevention measure. When a 
    pollution prevention measure is used, the owner or operator of an 
    affected source is not required to apply to the Administrator for a 
    nominal efficiency and is not subject to paragraph (i) of this section.
        (k) The owner or operator must demonstrate that the emissions from 
    the emission points proposed to be included in the emissions average 
    will not result in greater hazard, or at the option of the 
    Administrator, greater risk to human health or the environment than if 
    the emission points were controlled according to the provisions in 
    Secs. 63.484, 63.485, 63.486, 63.493, and 63.501.
        (1) This demonstration of hazard or risk equivalency shall be made 
    to the satisfaction of the Administrator.
        (i) The Administrator may require owners and operators to use 
    specific methodologies and procedures for making a hazard or risk 
    determination.
        (ii) The demonstration and approval of hazard or risk equivalency 
    shall be made according to any guidance that the Administrator makes 
    available for use.
        (2) Owners and operators shall provide documentation demonstrating 
    the hazard or risk equivalency of their proposed emissions average in 
    their operating permit application or in their Emissions Averaging Plan 
    if an operating permit application has not yet been submitted.
        (3) An Emissions Averaging Plan that does not demonstrate hazard or 
    risk equivalency to the satisfaction of the Administrator shall not be 
    approved. The Administrator may require such adjustments to the 
    Emissions Averaging Plan as are necessary in order to ensure that the 
    emissions average will not result in greater hazard or risk to human 
    health or the environment than would result if the emission points were 
    controlled according to Secs. 63.484, 63.485, 63.486, 63.493, and 
    63.501.
        (4) A hazard or risk equivalency demonstration must:
        (i) Be a quantitative, bona fide chemical hazard or risk 
    assessment;
        (ii) Account for differences in chemical hazard or risk to human 
    health or the environment; and
        (iii) Meet any requirements set by the Administrator for such 
    demonstrations.
        (l) For periods of monitoring excursions, an owner or operator may 
    request that the provisions of paragraphs (l)(1) through (l)(4) of this 
    section be followed instead of the procedures in paragraphs (f)(2)(i) 
    and (f)(2)(ii) of this section.
        (1) The owner or operator shall notify the Administrator of 
    monitoring excursions in the Periodic Reports as required in 
    Sec. 63.506(e)(6).
        (2) The owner or operator shall demonstrate that other types of 
    monitoring data or engineering calculations are appropriate to 
    establish that the control device for the emission point was operating 
    in such a fashion to warrant assigning full or partial credits and 
    debits. This demonstration shall be made to the Administrator's 
    satisfaction, and the Administrator may establish procedures for 
    demonstrating compliance that are acceptable.
        (3) The owner or operator shall provide documentation of the 
    excursion and the other types of monitoring data or engineering 
    calculations to be used to demonstrate that the control device for the 
    emission point was operating in such a fashion to warrant assigning 
    full or partial credits and debits.
        (4) The Administrator may assign full or partial credit and debits 
    upon review of the information provided.
        (m) For each emission point included in an emissions average, the 
    owner or operator shall perform testing, monitoring, recordkeeping, and 
    reporting equivalent to that required for Group 1 emission points 
    complying with Secs. 63.484, 63.485, 63.486, 63.493, and 63.501, as 
    applicable. If back-end process operations are included in an emissions 
    average, the owner or operator shall perform testing, monitoring, 
    recordkeeping, and reporting equivalent to that required for back-end 
    process operations complying with Sec. 63.493. The specific 
    requirements for continuous front-end process vents, batch front-end 
    process vents, aggregate batch vent streams, storage vessels, back-end 
    process operations, and wastewater are identified in paragraphs (m)(1) 
    through (m)(6) of this section.
        (1) For each continuous front-end process vent equipped with a 
    flare, incinerator, boiler, or process heater, as appropriate to the 
    control technique:
        (i) Determine whether the continuous front-end process vent is 
    Group 1 or Group 2 according to the procedures specified in Sec. 63.115 
    of subpart G and as required by Sec. 63.485;
        (ii) Conduct initial performance tests to determine percent 
    reduction as specified in Sec. 63.116 of subpart G and as required by 
    Sec. 63.485; and
        (iii) Monitor the operating parameters, keep records, and submit 
    reports as specified in Sec. 63.114, Sec. 63.117(a), and 
    Sec. 63.118(a), (f), and (g) of subpart G, as required, for the 
    specific control device as required by Sec. 63.485.
        (2) For each continuous front-end process vent equipped with a 
    carbon adsorber, absorber, or condenser but not equipped with a control 
    device, as appropriate to the control technique:
        (i) Determine the flow rate, organic HAP concentration, and TRE 
    index value according to the procedures specified in Sec. 63.115 of 
    subpart G; and
        (ii) Monitor the operating parameters, keep records, and submit 
    reports according to the procedures specified in Sec. 63.114, 
    Sec. 63.117(a), and Sec. 63.118 (b), (f), and (g) of subpart G, as 
    required, for the specific recovery device, and as required by 
    Sec. 63.485.
        (3) For each storage vessel controlled with an internal floating 
    roof, external roof, or a closed vent system with a control device, as 
    appropriate to the control technique:
        (i) Perform the monitoring or inspection procedures according to 
    the procedures specified in Sec. 63.120 of subpart G, and as required 
    by Sec. 63.484;
        (ii) Perform the reporting and recordkeeping procedures according 
    to the procedures specified in Secs. 63.122 and 63.123 of subpart G, 
    and as required by Sec. 63.484; and
        (iii) For closed vent systems with control devices, conduct an 
    initial design evaluation and submit an operating plan according to the 
    procedures specified in Sec. 63.120(d) and Sec. 63.122(a)(2) and (b) of 
    subpart G, and as required by Sec. 63.484.
        (4) For back-end process operations included in an emissions 
    average:
        (i) If stripping technology, and no control or recovery device, is 
    used to reduce back-end process operation emissions, the owner or 
    operator shall implement the following portions of this subpart:
        (A) Paragraphs (b)(1), (b)(2), and (b)(3) of Sec. 63.495, paragraph 
    (b) of Sec. 63.498, and the applicable provisions of Sec. 63.499, or
        (B) Paragraphs (c) (1), (2), and (3) of Sec. 63.495, paragraph (c) 
    of Sec. 63.498, and the applicable provisions of Sec. 63.499;
        (ii) If a control or recovery device is used to reduce back-end 
    process operation emissions, the owner or operator shall comply with 
    Secs. 63.496, 63.497, 63.498(d), and the applicable provisions of 
    63.499, and shall
    
    [[Page 46968]]
    
    implement the provisions of these sections.
        (5) For wastewater emission points, as appropriate to the control 
    techniques:
        (i) For wastewater treatment processes, conduct tests according to 
    the procedures specified in Sec. 63.138(i) and (j) of subpart G, and as 
    required by Sec. 63.501;
        (ii) Conduct inspections and monitoring according to the procedures 
    specified in Sec. 63.143 of subpart G, and as required by Sec. 63.501;
        (iii) Implement a recordkeeping program according to the procedures 
    specified in Sec. 63.147 of subpart G, and as required by Sec. 63.501; 
    and
        (iv) Implement a reporting program according to the procedures 
    specified in Sec. 63.146 of subpart G, and as required by Sec. 63.501.
        (6) For each batch front-end process vent and aggregate batch vent 
    stream equipped with a control device, as appropriate to the control 
    technique:
        (i) Determine whether the batch front-end process vent or aggregate 
    batch vent stream is Group 1 or Group 2 according to the procedures 
    specified in Sec. 63.488;
        (ii) Conduct performance tests according to the procedures 
    specified in Sec. 63.490;
        (iii) Conduct monitoring according to the procedures specified in 
    Sec. 63.489; and
        (iv) Perform the recordkeeping and reporting procedures according 
    to the procedures specified in Secs. 63.491 and 63.492.
        (7) If an emission point in an emissions average is controlled 
    using a pollution prevention measure or a device or technique for which 
    no monitoring parameters or inspection procedures are required by 
    Secs. 63.484, 63.485, 63.486, 63.493, or Sec. 63.501, the owner or 
    operator shall submit the information specified in Sec. 63.506(f) for 
    alternate monitoring parameters or inspection procedures in the 
    Emissions Averaging Plan or operating permit application.
        (n) Records of all information required to calculate emission 
    debits and credits shall be retained for 5 years.
        (o) Precompliance Reports, Emission Averaging Plans, Notifications 
    of Compliance Status, Periodic Reports, and other reports shall be 
    submitted as required by Sec. 63.506.
    
    
    Sec. 63.504  Additional test methods and procedures.
    
        (a) Performance testing shall be conducted in accordance with 
    Sec. 63.7 (a)(3), (d), (e), (g), and (h) of subpart A, with the 
    exceptions specified in paragraphs (a)(1) through (a)(4) of this 
    section and the additions specified in paragraph (b) of this section. 
    Sections 63.484 through 63.501 also contain specific testing 
    requirements.
        (1) Performance tests shall be conducted according to the 
    provisions of Sec. 63.7(e) of subpart A, except that performance tests 
    shall be conducted at maximum representative operating conditions for 
    the process.
        (2) References in Sec. 63.7(g) of subpart A to the Notification of 
    Compliance Status requirements in Sec. 63.9(h) shall refer to the 
    requirements in Sec. 63.506(e)(5).
        (3) Because the site-specific test plans in Sec. 63.7(c)(3) of 
    subpart A are not required, Sec. 63.7(h)(4)(ii) is not applicable.
        (4) The owner or operator shall notify the Administrator of the 
    intention to conduct a performance test at least 30 calendar days 
    before the performance test is scheduled, to allow the Administrator 
    the opportunity to have an observer present during the test.
        (b) Data shall be reduced in accordance with the EPA approved 
    methods specified in the applicable subpart or, if other test methods 
    are used, the data and methods shall be validated according to the 
    protocol in Method 301 of appendix A of this part.
    
    
    Sec. 63.505  Parameter monitoring levels and excursions.
    
        (a) Establishment of parameter monitoring levels. The owner or 
    operator of a control or recovery device that has one or more parameter 
    monitoring level requirements specified under this subpart shall 
    establish a maximum or minimum level for each measured parameter using 
    the procedures specified in paragraph (b), (c), or (d) of this section. 
    The procedures specified in paragraph (b) have been approved by the 
    Administrator. The procedures in paragraphs (c) and (d) of this section 
    have not been approved by the Administrator, and determination of the 
    parameter monitoring level using the procedures in paragraphs (c) or 
    (d) of this section and is subject to review and approval by the 
    Administrator. The determination and supporting documentation shall be 
    included in the Precompliance Report.
        (1) The owner or operator shall operate control and recovery 
    devices such that monitored parameters remain above the minimum 
    established level or below the maximum established level.
        (2) As specified in Sec. 63.506(e)(5) and Sec. 63.506(e)(8), all 
    established levels, along with their supporting documentation and the 
    definition of an operating day, shall be approved as part of and 
    incorporated into the Notification of Compliance Status or operating 
    permit, respectively.
        (3) Nothing in this section shall be construed to allow a 
    monitoring parameter excursion caused by an activity that violates 
    other applicable provisions of subparts A, F, or G of this part.
        (b) Establishment of parameter monitoring levels based on 
    performance tests. The procedures specified in paragraphs (b)(1) 
    through (b)(3) of this section shall be used, as applicable, in 
    establishing parameter monitoring levels. Level(s) established under 
    this paragraph shall be based on the parameter values measured during 
    the performance test.
        (1) Storage tanks and wastewater. The maximum and/or minimum 
    monitoring levels shall be based on the parameter values measured 
    during the performance test, supplemented, if desired, by engineering 
    assessments and/or manufacturer's recommendations.
        (2) Continuous front-end process vents and back-end process 
    operations complying using control or recovery devices. During initial 
    compliance testing, the appropriate parameter shall be continuously 
    monitored during the required 1-hour runs. The monitoring level(s) 
    shall then be established as the average of the maximum (or minimum) 
    point values from the three test runs. The average of the maximum 
    values shall be used when establishing a maximum level, and the average 
    of the minimum values shall be used when establishing a minimum level.
        (3) Batch front-end process vents. The monitoring level(s) shall be 
    established using the procedures specified in paragraphs (b)(3)(i) 
    through (b)(3)(iii) of this section, as appropriate. The procedures 
    specified in this paragraph may only be used if the batch emission 
    episodes, or portions thereof, selected to be controlled were tested, 
    and monitoring data were collected, during the entire period in which 
    emissions were vented to the control device, as specified in 
    Sec. 63.490(c)(1)(i). If the owner or operator chose to test only a 
    portion of the batch emission episode, or portion thereof, selected to 
    be controlled, as specified in Sec. 63.490(c)(1)(i)(A), the procedures 
    in paragraph (c) of this section must be used.
        (i) If more than one batch emission episode or more than one 
    portion of a batch emission episode has been selected to be controlled, 
    a single level for the batch cycle shall be calculated as follows:
        (A) During initial compliance testing, the appropriate parameter 
    shall be
    
    [[Page 46969]]
    
    monitored continuously at all times when batch emission episodes, or 
    portions thereof, selected to be controlled are vented to the control 
    device.
        (B) The average monitored parameter value shall be calculated for 
    each batch emission episode, or portion thereof, in the batch cycle 
    selected to be controlled. The average shall be based on all values 
    measured during the required performance test.
        (C) If the level to be established is a maximum operating 
    parameter, the level shall be defined as the minimum of the average 
    parameter values of the batch emission episodes, or portions thereof, 
    in the batch cycle selected to be controlled.
        (D) If the level to be established is a minimum operating 
    parameter, the level shall be defined as the maximum of the average 
    parameter values of the batch emission episodes, or portions thereof, 
    in the batch cycle selected to be controlled.
        (E) Alternatively, an average monitored parameter value shall be 
    calculated for the entire batch cycle based on all values measured 
    during each batch emission episode, or portion thereof, selected to be 
    controlled.
        (ii) Instead of establishing a single level for the batch cycle, as 
    described in paragraph (b)(3)(i) of this section, an owner or operator 
    may establish separate levels for each batch emission episode, or 
    portion thereof, selected to be controlled. Each level shall be 
    determined as specified in paragraphs (b)(3)(i)(A) and (b)(3)(i)(B) of 
    this section.
        (iii) The batch cycle shall be defined in the Notification of 
    Compliance Status, as specified in Sec. 63.506(e)(5). The definition 
    shall include an identification of each batch emission episode and the 
    information required to determine parameter monitoring compliance for 
    partial batch cycles (i.e., when part of a batch cycle is accomplished 
    during two different operating days).
        (4) Aggregate batch vent streams. For aggregate batch vent streams, 
    the monitoring level shall be established in accordance with paragraph 
    (b)(2) of this section.
        (c) Establishment of parameter monitoring levels based on 
    performance tests, engineering assessments, and/or manufacturer's 
    recommendations. As required in paragraph (a) of this section, the 
    information specified in paragraphs (c)(2) and (c)(3) of this section 
    shall be provided in the Precompliance Report.
        (1) Parameter monitoring levels established under this paragraph 
    shall be based on the parameter values measured during the performance 
    test supplemented by engineering assessments and manufacturer's 
    recommendations. Performance testing is not required to be conducted 
    over the entire range of expected parameter values.
        (2) The specific level of the monitored parameter(s) for each 
    emission point.
        (3) The rationale for the specific level for each parameter for 
    each emission point, including any data and calculations used to 
    develop the level and a description of why the level indicates proper 
    operation of the control or recovery device.
        (d) Establishment of parameter monitoring based on engineering 
    assessments and/or manufacturer's recommendations. If a performance 
    test is not required by this subpart for a control or recovery device, 
    the maximum or minimum level may be based solely on engineering 
    assessments and/or manufacturer's recommendations. As required in 
    paragraph (a) of this section, the determined level and all supporting 
    documentation shall be provided in the Precompliance Report.
        (e) Demonstration of compliance with back-end process provisions 
    using stripper parameter monitoring. If the owner or operator is 
    demonstrating compliance with Sec. 63.495 using stripper parameter 
    monitoring, stripper parameter levels shall be established for each 
    grade in accordance with paragraphs (e)(1) and (e)(2) of this section. 
    A single set of stripper parameter levels can be representative of 
    multiple grades.
        (1) For each grade, the owner or operator shall calculate the 
    residual organic HAP content using the procedures in paragraphs 
    (e)(1)(i) and (e)(1)(ii) of this section.
        (i) The location of the sampling shall be in accordance with 
    Sec. 63.495(d).
        (ii) The residual organic HAP content in each sample is to be 
    determined using specified methods.
        (2) For each grade, the owner or operator shall establish stripper 
    operating parameter levels that represent stripper operation during the 
    residual organic HAP content determination in paragraph (e)(1) of this 
    section. The stripper operating parameters shall include, at a minimum, 
    temperature, pressure, steaming rates (for steam strippers), and some 
    parameter that is indicative of residence time.
        (3) After the initial determinations, an owner or operator can add 
    a grade, with corresponding stripper parameter levels, using the 
    procedures in paragraphs (e)(1) and (e)(2) of this section. The results 
    of this determination shall be submitted in the next periodic report.
        (4) An owner or operator complying with the residual organic HAP 
    limitations in paragraph (a) of Sec. 63.494 using stripping, and 
    demonstrating compliance by stripper parameter monitoring, shall 
    redetermine the residual organic HAP content for all affected grades 
    whenever process changes are made. For the purposes of this section, a 
    process change is any action that would reasonably be expected to 
    impair the performance of the stripping operation. For the purposes of 
    this section, examples of process changes may include changes in 
    production capacity or production rate, or removal or addition of 
    equipment. For purposes of this paragraph, process changes do not 
    include: Process upsets; unintentional, temporary process changes; or 
    changes that reduce the residual organic HAP content of the elastomer.
        (f) Compliance determinations. The provisions of this paragraph 
    apply only to emission points and control or recovery devices for which 
    continuous monitoring is required under this subpart.
        (1) The parameter monitoring data for storage vessels, front-end 
    process vents, back-end process operations complying through the use of 
    control or recovery devices, process wastewater streams, and emission 
    points included in emissions averages that are required to perform 
    continuous monitoring shall be used to determine compliance for the 
    monitored control or recovery devices.
        (2) Except as provided in paragraph (f)(3) and (i) of this section, 
    for each excursion, as defined in paragraphs (g) and (h) of this 
    section, the owner or operator shall be deemed out of compliance with 
    the provisions of this subpart.
        (3) If the daily average value of a monitored parameter is above 
    the maximum level or below the minimum level established, or if 
    monitoring data cannot be collected during monitoring device 
    calibration check or monitoring device malfunction, but the affected 
    source is operated during the periods of startup, shutdown, or 
    malfunction in accordance with the affected source's Startup, Shutdown, 
    and Malfunction Plan, then the event shall not be considered a 
    monitoring parameter excursion.
        (g) Parameter monitoring excursion definitions. (1) For storage 
    vessels, continuous front-end process vents, aggregate batch vent 
    streams, back-end process operations complying through the use of 
    control or recovery devices, and wastewater streams, an excursion
    
    [[Page 46970]]
    
    means any of the three cases listed in paragraphs (g)(1)(i) through 
    (g)(1)(iii) of this section. For a control or recovery device where 
    multiple parameters are monitored, if one or more of the parameters 
    meets the excursion criteria in paragraphs (g)(1)(i) through 
    (g)(1)(iii) of this section, this is considered a single excursion for 
    the control or recovery device.
        (i) When the daily average value of one or more monitored 
    parameters is above the maximum level or below the minimum level 
    established for the given parameters.
        (ii) When the period of control or recovery device operation is 4 
    hours or greater in an operating day and monitoring data are 
    insufficient, as defined in paragraph (g)(1)(iv) of this section, to 
    constitute a valid hour of data for at least 75 percent of the 
    operating hours.
        (iii) When the period of control or recovery device operation is 
    less than 4 hours in an operating day and more than two of the hours 
    during the period of operation do not constitute a valid hour of data 
    due to insufficient monitoring data, as defined in paragraph (g)(1)(iv) 
    of this section.
        (iv) Monitoring data are insufficient to constitute a valid hour of 
    data, as used in paragraphs (g)(1)(ii) and (g)(1)(iii) of this section, 
    if measured values are unavailable for any of the 15-minute periods 
    within the hour. For data compression systems approved under 
    Sec. 63.506(g)(3), monitoring data are insufficient to calculate a 
    valid hour of data if there are less than four data measurements made 
    during the hour.
        (2) For batch front-end process vents, an excursion means one of 
    the two cases listed in paragraphs (g)(2)(i) and (g)(2)(ii) of this 
    section. For a control device where multiple parameters are monitored, 
    if one or more of the parameters meets the excursion criteria in either 
    paragraph (g)(2)(i) or (g)(2)(ii) of this section, this is considered a 
    single excursion for the control device.
        (i) When the batch cycle daily average value of one or more 
    monitored parameters is above the maximum or below the minimum 
    established level for the given parameters.
        (ii) When monitoring data are insufficient. Monitoring data shall 
    be considered insufficient when measured values are not available for 
    at least 75 percent of the 15-minute periods when batch emission 
    episodes, or portions thereof, selected to be controlled are being 
    vented to the control device during the operating day.
        (h) Excursion definitions for back-end operations complying through 
    stripping. (1) For back-end process operations complying through the 
    use of stripping technology, and demonstrating compliance by sampling, 
    an excursion means one of the two cases listed in paragraphs (h)(1)(i) 
    and (h)(1)(ii) of this section.
        (i) When the monthly weighted average residual organic HAP content 
    is above the applicable residual organic HAP limitation in Sec. 63.494; 
    or
        (ii) When less than 75 percent of the samples required in 1 month 
    are taken and analyzed in accordance with the provisions of 
    Sec. 63.495(b).
        (2) For back-end process operations complying through the use of 
    stripping technology, and demonstrating compliance by stripper 
    parameter monitoring, an excursion means one of the three cases listed 
    in paragraphs (h)(2)(i), (h)(2)(ii), and (h)(2)(iii) of this section.
        (i) When the monthly weighted average residual organic HAP content 
    is above the applicable residual organic HAP limitation in Sec. 63.494;
        (ii) When an owner or operator fails to sample and analyze the 
    organic HAP content of a sample for a grade with an hourly average 
    stripper operating parameter value not in accordance with the 
    established monitoring parameter levels for that parameter; or
        (iii) When an owner or operator does not collect sufficient 
    monitoring data for at least 75 percent of the grades or batches 
    processed during a month. Stripper monitoring data are considered 
    insufficient if monitoring parameters are obtained for less than 75 
    percent of the 15-minute periods during the processing of a grade, and 
    a sample of that grade or batch is not taken and analyzed to determine 
    the residual organic HAP content.
        (i) Excused excursions. A number of excused excursions shall be 
    allowed for each control or recovery device for each semiannual period. 
    The number of excused excursions for each semiannual period is 
    specified in paragraphs (i)(1) through (i)(6) of this section. This 
    paragraph applies to affected sources required to submit Periodic 
    Reports semiannually or quarterly. The first semiannual period is the 
    6-month period starting the date the Notification of Compliance Status 
    is due.
        (1) For the first semiannual period--six excused excursions.
        (2) For the second semiannual period--five excused excursions.
        (3) For the third semiannual period--four excused excursions.
        (4) For the fourth semiannual period--three excused excursions.
        (5) For the fifth semiannual period--two excused excursions.
        (6) For the sixth and all subsequent semiannual periods--one 
    excused excursion.
    
    
    Sec. 63.506   General recordkeeping and reporting provisions.
    
        (a) Data retention. Each owner or operator of an affected source 
    shall keep copies of all applicable records and reports required by 
    this subpart for at least 5 years, unless otherwise specified in this 
    subpart.
        (b) Subpart A requirements. The owner or operator of an affected 
    source shall comply with the applicable recordkeeping and reporting 
    requirements in 40 CFR part 63, subpart A as specified in Table 1 of 
    this subpart. These requirements include, but are not limited to, the 
    requirements specified in paragraphs (b)(1) and (b)(2) of this section.
        (1) Startup, shutdown, and malfunction plan. The owner or operator 
    of an affected source shall develop and implement a written startup, 
    shutdown, and malfunction plan as specified in Sec. 63.6(e)(3) of 
    subpart A. This plan shall describe, in detail, procedures for 
    operating and maintaining the affected source during periods of 
    startup, shutdown, and malfunction and a program for corrective action 
    for malfunctioning process and air pollution control equipment used to 
    comply with this subpart. The affected source shall keep this plan 
    onsite and shall incorporate it by reference into their operating 
    permit. Records associated with the plan shall be kept as specified in 
    paragraphs (b)(1)(i)(A) through (b)(1)(i)(D) of this section. Reports 
    related to the plan shall be submitted as specified in paragraph 
    (b)(1)(ii) of this section.
        (i) Records of startup, shutdown, and malfunction. The owner or 
    operator shall keep the records specified in paragraphs (b)(1)(i)(A) 
    through (b)(1)(i)(D) of this section.
        (A) Records of the occurrence and duration of each malfunction of 
    air pollution control equipment or continuous monitoring systems used 
    to comply with this subpart.
        (B) For each startup, shutdown, or malfunction, a statement that 
    the procedures specified in the affected source's startup, shutdown, 
    and malfunction plan were followed; alternatively, documentation of any 
    actions taken that are not consistent with the plan.
        (C) For continuous monitoring systems used to comply with this 
    subpart, records documenting the completion of calibration checks and 
    maintenance of continuous monitoring
    
    [[Page 46971]]
    
    systems that are specified in the manufacturer's instructions.
        (D) Records specified in paragraphs (b)(1)(i)(B) and (b)(1)(i)(C) 
    of this section are not required if they pertain solely to Group 2 
    emission points that are not included in an emissions average.
        (ii) Reports of startup, shutdown, and malfunction. For the 
    purposes of this subpart, the semiannual startup, shutdown, and 
    malfunction reports shall be submitted on the same schedule as the 
    Periodic Reports required under paragraph (e)(6) of this section 
    instead of the schedule specified in Sec. 63.10(d)(5)(i) of subpart A. 
    The reports shall include the information specified in paragraphs 
    (b)(1)(i)(A) through (b)(1)(i)(C) of this section and shall contain the 
    name, title, and signature of the owner or operator or other 
    responsible official who is certifying its accuracy.
        (2) Application for approval of construction or reconstruction. For 
    new affected sources, each owner or operator shall comply with the 
    provisions in Sec. 63.5 of subpart A regarding construction and 
    reconstruction, excluding the provisions specified in 
    Sec. 63.5(d)(1)(ii)(H), (d)(1)(iii), (d)(2), and (d)(3)(ii) of subpart 
    A.
        (c) Subpart H requirements. Owners or operators of affected sources 
    shall comply with the reporting and recordkeeping requirements in 
    subpart H, except as specified in Sec. 63.502(g) through 
    Sec. 63.502(i).
        (d) Recordkeeping and documentation. Owners or operators required 
    to keep continuous records shall keep records as specified in 
    paragraphs (d)(1) through (d)(8) of this section, unless an alternative 
    recordkeeping system has been requested and approved as specified in 
    paragraph (f), (g), or (h) of this section. Documentation requirements 
    are specified in paragraphs (d)(9) and (d)(10) of this section.
        (1) The monitoring system shall measure data values at least once 
    every 15 minutes.
        (2) The owner or operator shall record either:
        (i) Each measured data value; or
        (ii) Block average values for 1 hour or shorter periods calculated 
    from all measured data values during each period. If values are 
    measured more frequently than once per minute, a single value for each 
    minute may be used to calculate the hourly (or shorter period) block 
    average instead of all measured values; or
        (iii) For batch front-end process vents, each batch cycle average 
    or batch emission episode average, as appropriate, in addition to each 
    measured data value recorded as required in paragraph (d)(2)(i) of this 
    section.
        (3) Daily average (or batch cycle daily average) values of each 
    continuously monitored parameter shall be calculated for each operating 
    day as specified in paragraphs (d)(3)(i) through (d)(3)(ii) of this 
    section, except as specified in paragraph (d)(6) of this section.
        (i) The daily average value or batch cycle daily average shall be 
    calculated as the average of all parameter values recorded during the 
    operating day. As specified in Sec. 63.491(e)(2)(i), only parameter 
    values measured during those batch emission episodes, or portions 
    thereof, in the batch cycle that the owner or operator has chosen to 
    control shall be used to calculate the average. The calculated average 
    shall cover a 24-hour period if operation is continuous, or the number 
    of hours of operation per operating day if operation is not continuous.
        (ii) The operating day shall be the period that the owner or 
    operator specifies in the operating permit or the Notification of 
    Compliance Status. It may be from midnight to midnight or another 24-
    hour period.
        (4) Records required when out of compliance. If the daily average 
    (or batch cycle daily average) value of a monitored parameter for a 
    given operating day is below the minimum level or above the maximum 
    level established in the Notification of Compliance Status or operating 
    permit, the owner or operator shall retain the data recorded that 
    operating day under paragraph (d)(2) of this section.
        (5) Records required when in compliance for daily average value or 
    batch cycle daily average value. If the daily average (or batch cycle 
    daily average) value of a monitored parameter for a given operating day 
    is above the minimum level or below the maximum level established in 
    the Notification of Compliance Status or operating permit, the owner or 
    operator shall either:
        (i) Retain block average values for 1 hour or shorter periods for 
    that operating day; or
        (ii) Retain the data recorded in paragraphs (d)(2)(i) and 
    (d)(2)(iii) of this section.
        (6) Records required when all recorded values are in compliance. If 
    all recorded values for a monitored parameter during an operating day 
    are above the minimum level or below the maximum level established in 
    the Notification of Compliance Status or operating permit, the owner or 
    operator may record that all values were above the minimum level or 
    below the maximum level rather than calculating and recording a daily 
    average (or batch cycle daily average) for that operating day. For 
    these operating days, the records required in paragraph (d)(5) of this 
    section are required.
        (7) Monitoring data recorded during periods of monitoring system 
    breakdowns, repairs, calibration checks, and zero (low-level) and high-
    level adjustments shall not be included in any average computed under 
    this subpart. Records shall be kept of the times and durations of all 
    such periods.
        (8) In addition to the periods specified in paragraph (d)(7) of 
    this section, records shall be kept of the times and durations of any 
    other periods during process operation or control device operation when 
    monitors are not operating. For batch front-end process vents, this 
    paragraph only applies during batch emission episodes, or portions 
    thereof, that the owner or operator has selected for control.
        (9) For each EPPU that is not part of the affected source because 
    it does not use any organic HAP, the owner or operator shall maintain 
    the documentation specified in Sec. 63.480(b)(1).
        (10) For each flexible operation unit in which the primary product 
    is determined to be something other than an elastomer product, the 
    owner or operator shall maintain the documentation specified in 
    Sec. 63.480(f)(6).
        (e) Reporting and notification. (1) In addition to the reports and 
    notifications required by subparts A and H, as specified in this 
    subpart, the owner or operator of an affected source shall prepare and 
    submit the reports listed in paragraphs (e)(3) through (e)(8) of this 
    section, as applicable.
        (2) All reports required under this subpart shall be sent to the 
    Administrator at the addresses listed in Sec. 63.13 of subpart A of 
    this part. If acceptable to both the Administrator and the owner or 
    operator of a source, reports may be submitted on electronic media.
        (3) Precompliance Report. Affected sources requesting an extension 
    for compliance, or requesting approval to use alternative monitoring 
    parameters, alternative continuous monitoring and recordkeeping, or 
    alternative controls, shall submit a Precompliance Report according to 
    the schedule described in paragraph (e)(3)(i) of this section. The 
    Precompliance Report shall contain the information specified in 
    paragraphs (e)(3)(ii) through (e)(3)(vi) of this section, as 
    appropriate.
        (i) Submittal dates. The Precompliance Report shall be submitted to 
    the Administrator no later
    
    [[Page 46972]]
    
    than 12 months prior to the compliance date. For new sources, the 
    Precompliance Report shall be submitted to the Administrator with the 
    application for approval of construction or reconstruction required in 
    paragraph (b)(2) of this section.
        (ii) A request for an extension for compliance must be submitted in 
    the Precompliance Report, if it has not been submitted to the operating 
    permit authority as part of the operating permit application. The 
    request for a compliance extension will include the data outlined in 
    Sec. 63.6(i)(6)(i)(A), (B), and (D) of subpart A, as required in 
    Sec. 63.481(e)(1).
        (iii) The alternative monitoring parameter information required in 
    paragraph (f) of this section shall be submitted if, for any emission 
    point, the owner or operator of an affected source seeks to comply 
    through the use of a control technique other than those for which 
    monitoring parameters are specified in this subpart or in subpart G of 
    this part, or seeks to comply by monitoring a different parameter than 
    those specified in this subpart or in subpart G of this part.
        (iv) If the affected source seeks to comply using alternative 
    continuous monitoring and recordkeeping as specified in paragraph (g) 
    of this section, the information requested in paragraph (e)(3)(iv)(A) 
    or (e)(3)(iv)(B) of this section must be submitted in the Precompliance 
    Report.
        (A) The owner or operator must submit notification of the intent to 
    use the provisions specified in paragraph (h) of this section; or
        (B) The owner or operator must submit a request for approval to use 
    alternative continuous monitoring and recordkeeping provisions as 
    specified in paragraph (g) of this section.
        (v) The owner or operator shall report the intent to use 
    alternative controls to comply with the provisions of this subpart. 
    Alternative controls must be deemed by the Administrator to be 
    equivalent to the controls required by the standard, under the 
    procedures outlined in Sec. 63.6(g) of subpart A.
        (4) Emissions Averaging Plan. For all existing affected sources 
    using emissions averaging, an Emissions Averaging Plan shall be 
    submitted for approval according to the schedule and procedures 
    described in paragraph (e)(4)(i) of this section. The Emissions 
    Averaging Plan shall contain the information specified in paragraph 
    (e)(4)(ii) of this section, unless the information required in 
    paragraph (e)(4)(ii) of this section is submitted with an operating 
    permit application. An owner or operator of an affected source who 
    submits an operating permit application instead of an Emissions 
    Averaging Plan shall submit the information specified in paragraph 
    (e)(8) of this section. In addition, a supplement to the Emissions 
    Averaging Plan, as required under paragraph (e)(4)(iii) of this 
    section, is to be submitted whenever alternative controls or operating 
    scenarios may be used to comply with this subpart. Updates to the 
    Emissions Averaging Plan shall be submitted in accordance with 
    paragraph (e)(4)(iv) of this section.
        (i) Submittal and approval. The Emissions Averaging Plan shall be 
    submitted no later than 18 months prior to the compliance date, and is 
    subject to Administrator approval. The Administrator shall determine 
    within 120 operating days whether the Emissions Averaging Plan 
    submitted presents sufficient information. The Administrator shall 
    either approve the Emissions Averaging Plan, request changes, or 
    request that the owner or operator submit additional information. Once 
    the Administrator receives sufficient information, the Administrator 
    shall approve, disapprove, or request changes to the plan within 120 
    operating days.
        (ii) Information required. The Emissions Averaging Plan shall 
    contain the information listed in paragraphs (e)(4)(ii)(A) through 
    (e)(4)(ii)(M) of this section for all emission points included in an 
    emissions average.
        (A) The required information shall include the identification of 
    all emission points and process back-end operations in the planned 
    emissions average and, where applicable, notation of whether each 
    storage vessel, continuous front-end process vent, batch front-end 
    process vent, aggregate batch vents stream, and process wastewater 
    stream is a Group 1 or Group 2 emission point, as defined in 
    Sec. 63.482 or as designated under Sec. 63.503(c)(2).
        (B) The required information shall include the projected emission 
    debits and credits for each emission point and the sum for the emission 
    points involved in the average calculated according to Sec. 63.503. The 
    projected credits must be greater than or equal to the projected 
    debits, as required under Sec. 63.503(e)(3).
        (C) The required information shall include the specific control 
    technology or pollution prevention measure that will be used for each 
    emission point included in the average and date of application or 
    expected date of application.
        (D) The required information shall include the specific 
    identification of each emission point affected by a pollution 
    prevention measure. To be considered a pollution prevention measure, 
    the criteria in Sec. 63.503(j)(1) must be met. If the same pollution 
    prevention measure reduces or eliminates emissions from multiple 
    emission points in the average, the owner or operator must identify 
    each of these emission points.
        (E) The required information shall include a statement that the 
    compliance demonstration, monitoring, inspection, recordkeeping, and 
    reporting provisions in Sec. 63.503(m), (n), and (o) that are 
    applicable to each emission point in the emissions average will be 
    implemented beginning on or before the date of compliance.
        (F) The required information shall include documentation of the 
    data listed in paragraphs (e)(4)(ii)(F)(1) through (e)(4)(ii)(F)(5) of 
    this section for each storage vessel and continuous front-end process 
    vent included in the average.
        (1) The required documentation shall include the values of the 
    parameters used to determine whether the emission point is Group 1 or 
    Group 2. Where a TRE index value is used for continuous front-end 
    process vent group determination, the estimated or measured values of 
    the parameters used in the TRE equation in Sec. 63.115(d) of subpart G 
    and the resulting TRE index value shall be submitted.
        (2) The required documentation shall include the estimated values 
    of all parameters needed for input to the emission debit and credit 
    calculations in Sec. 63.503 (g) and (h). These parameter values shall 
    be specified in the affected source's Emissions Averaging Plan (or 
    operating permit) as enforceable operating conditions. Changes to these 
    parameters must be reported in an update to the Emissions Averaging 
    Plan, as required by paragraph (e)(4)(iv)(B)(2) of this section.
        (3) The required documentation shall include the estimated percent 
    reduction if a control technology achieving a lower percent reduction 
    than the efficiency of the applicable reference control technology or 
    standard is or will be applied to the emission point.
        (4) The required documentation shall include the anticipated 
    nominal efficiency if a control technology achieving a greater percent 
    emission reduction than the efficiency of the reference control 
    technology is or will be applied to the emission point. The procedures 
    in Sec. 63.503(i) shall be followed to apply for a nominal efficiency.
        (5) The required documentation shall include the information 
    specified in Sec. 63.120(d)(2)(i) and in either
    
    [[Page 46973]]
    
    Sec. 63.120(d)(2)(ii) or (d)(2)(iii) of subpart G for each storage 
    vessel controlled with a closed-vent system using a control device 
    other than a flare.
        (G) The information specified in paragraph (f) of this section 
    shall be included in the Emissions Averaging Plan for:
        (1) Each continuous front-end process vent controlled by a 
    pollution prevention measure or control technique for which monitoring 
    parameters or inspection procedures are not specified in Sec. 63.114 of 
    subpart G, and
        (2) Each storage vessel controlled by pollution prevention or a 
    control technique other than an internal or external floating roof or a 
    closed vent system with a control device.
        (H) The required information shall include documentation of the 
    data listed in paragraphs (e)(4)(ii)(H)(1) through (e)(4)(ii)(H)(4) of 
    this section for each process wastewater stream included in the 
    average.
        (1) The required documentation shall include the data used to 
    determine whether the wastewater stream is a Group 1 or Group 2 
    wastewater stream and the information specified in table 14b of subpart 
    G of this part for wastewater streams at new and existing sources.
        (2) The required documentation shall include the estimated values 
    of all parameters needed for input to the wastewater emission credit 
    and debit calculations in Sec. 63.503(g)(5) and (h)(5). These parameter 
    values shall be specified in the affected source's Emissions Averaging 
    Plan (or operating permit) as enforceable operating conditions. Changes 
    to these parameters must be reported as required by paragraph 
    (e)(4)(iv)(B)(2) of this section.
        (3) The required documentation shall include the estimated percent 
    reduction if:
        (i) A control technology that achieves an emission reduction less 
    than or equal to the emission reduction that would otherwise have been 
    achieved by a steam stripper designed to the specifications found in 
    Sec. 63.138(g) of subpart G is or will be applied to the wastewater 
    stream, or external floating roof or a closed vent system with a 
    control device.
        (ii) A control technology achieving less than or equal to 95 
    percent emission reduction is or will be applied to the vapor stream(s) 
    vented and collected from the treatment processes, or
        (iii) A pollution prevention measure is or will be applied.
        (4) The required documentation shall include the anticipated 
    nominal efficiency if the owner or operator plans to apply for a 
    nominal efficiency under Sec. 63.503(i). A nominal efficiency shall be 
    applied for if:
        (i) A control technology that achieves an emission reduction 
    greater than the emission reduction that would have been achieved by a 
    steam stripper designed to the specifications found in Sec. 63.138(g) 
    of subpart G, is or will be applied to the wastewater stream; or
        (ii) A control technology achieving greater than 95 percent 
    emission reduction is or will be applied to the vapor stream(s) vented 
    and collected from the treatment processes.
        (I) For each pollution prevention measure, treatment process, or 
    control device used to reduce air emissions of organic HAP from 
    wastewater and for which no monitoring parameters or inspection 
    procedures are specified in Sec. 63.143 of subpart G, the information 
    specified in paragraph (f) of this section (Alternative Monitoring 
    Parameters) shall be included in the Emissions Averaging Plan.
        (J) The required information shall include documentation of the 
    data required by estimated values of all parameters needed for input to 
    the emission debit and credit calculations in Sec. 63.503 (g) and (h) 
    for each process back-end operation included in an emissions average. 
    These values shall be specified in the affected source's Emissions 
    Averaging Plan (or operating permit) as enforceable operating 
    conditions. Changes to these parameters must be reported as required by 
    paragraph (e)(4)(iv)(B)(2) of this section.
        (K) The required information shall include documentation of the 
    information required by Sec. 63.503(k). The documentation must 
    demonstrate that the emissions from the emission points proposed to be 
    included in the average will not result in greater hazard or, at the 
    option of the Administrator, greater risk to human health or the 
    environment than if the emission points were not included in an 
    emissions average.
        (L) The required information shall include documentation of the 
    data listed in paragraphs (e)(4)(ii)(L)(1) through (e)(4)(ii)(L)(3) of 
    this section for each batch front-end process vent and aggregate batch 
    vent stream included in the average.
        (1) The required documentation shall include the values of the 
    parameters used to determine whether the emission point is Group 1 or 
    Group 2.
        (2) The required information shall include the estimated values of 
    all parameters needed for input to the emission debit and credit 
    calculations in Sec. 63.503(g) and (h). These parameter values shall be 
    specified in the affected source's Emissions Averaging Plan (or 
    operating permit) as enforceable operating conditions. Changes to these 
    parameters must be reported as required by paragraph (e)(4)(iv) of this 
    section.
        (3) For batch front-end process vents, the required documentation 
    shall include the estimated percent reduction for the batch cycle. For 
    aggregate batch vent streams, the required documentation shall include 
    the estimated percent reduction achieved on a continuous basis.
        (M) For each pollution prevention measure or control device used to 
    reduce air emissions of organic HAP from batch front-end process vents 
    or batch vent streams and for which no monitoring parameters or 
    inspection procedures are specified in Sec. 63.489, the information 
    specified in paragraph (f) of this section, Alternative Monitoring 
    Parameters, shall be included in the Emissions Averaging Plan.
        (iii) Supplement to Emissions Averaging Plan. The owner or operator 
    required to prepare an Emissions Averaging Plan under paragraph (e)(4) 
    of this section shall also prepare a supplement to the Emissions 
    Averaging Plan for any alternative controls or operating scenarios that 
    may be used to achieve compliance.
        (iv) Updates to Emissions Averaging Plan. The owner or operator of 
    an affected source required to submit an Emissions Averaging Plan under 
    paragraph (e)(4) of this section shall also submit written updates of 
    the Emissions Averaging Plan to the Administrator for approval under 
    the circumstances described in paragraphs (e)(4)(iv)(A) and 
    (e)(4)(iv)(B) of this section unless the relevant information has been 
    included and submitted in an operating permit application or amendment.
        (A) The owner or operator who plans to make a change listed in 
    either paragraph (e)(4)(iv)(A)(1) or (e)(4)(iv)(A)(2) of this section 
    shall submit an Emissions Averaging Plan update at least 120 operating 
    days prior to making the change.
        (1) An Emissions Averaging Plan update shall be submitted whenever 
    an owner or operator elects to achieve compliance with the emissions 
    averaging provisions in Sec. 63.503 by using a control technique other 
    than that specified in the Emissions Averaging Plan, or plans to 
    monitor a different parameter or operate a control device in a manner 
    other than that specified in the Emissions Averaging Plan.
        (2) An Emissions Averaging Plan update shall be submitted whenever 
    an emission point or an EPPU is added to an existing affected source 
    and is
    
    [[Page 46974]]
    
    planned to be included in an emissions average, or whenever an emission 
    point not included in the emissions average described in the Emissions 
    Averaging Plan is to be added to an emissions average. The information 
    in paragraph (e)(4) of this section shall be updated to include the 
    additional emission point.
        (B) The owner or operator who has made a change as defined in 
    paragraph (e)(4)(iv)(B)(1) or (e)(4)(iv)(B)(2) of this section shall 
    submit an Emissions Averaging Plan update within 90 operating days 
    after the information regarding the change is known to the affected 
    source. The update may be submitted in the next quarterly periodic 
    report if the change is made after the date the Notification of 
    Compliance Status is due.
        (1) An Emissions Averaging Plan update shall be submitted whenever 
    a process change is made such that the group status of any emission 
    point in an emissions average changes.
        (2) An Emissions Averaging Plan update shall be submitted whenever 
    a value of a parameter in the emission credit or debit equations in 
    Sec. 63.503(g) or (h) changes such that it is below the minimum or 
    above the maximum established level specified in the Emissions 
    Averaging Plan and causes a decrease in the projected credits or an 
    increase in the projected debits.
        (C) The Administrator shall approve or request changes to the 
    Emissions Averaging Plan update within 120 operating days of receipt of 
    sufficient information regarding the change for emission points 
    included in emissions averages.
        (5) Notification of Compliance Status. For existing and new 
    affected sources, a Notification of Compliance Status shall be 
    submitted within 150 operating days after the compliance dates 
    specified in Sec. 63.481. The notification shall contain the 
    information listed in paragraphs (e)(5)(i) through (e)(5)(vii) of this 
    section.
        (i) The results of any emission point group determinations, process 
    section applicability determinations, performance tests, inspections, 
    continuous monitoring system performance evaluations, any other 
    information used to demonstrate compliance, values of monitored 
    parameters established during performance tests, and any other 
    information required to be included in the Notification of Compliance 
    Status under Sec. 63.122 of subpart G for storage vessels, Sec. 63.117 
    of subpart G for continuous front-end process vents, Sec. 63.492 for 
    batch front-end process vents, Sec. 63.499 for back-end process 
    operations, Sec. 63.146 of subpart G for process wastewater, and 
    Sec. 63.503 for emission points included in an emissions average. In 
    addition, each owner or operator shall comply with paragraphs 
    (e)(5)(i)(A) and (e)(5)(i)(B) of this section.
        (A) For performance tests, and group determinations, and process 
    section applicability determinations that are based on measurements, 
    the Notification of Compliance Status shall include one complete test 
    report, as described in paragraph (e)(5)(i)(B) of this section, for 
    each test method used for a particular kind of emission point. For 
    additional tests performed for the same kind of emission point using 
    the same method, the results and any other required information shall 
    be submitted, but a complete test report is not required.
        (B) A complete test report shall include a brief process 
    description, sampling site description, description of sampling and 
    analysis procedures and any modifications to standard procedures, 
    quality assurance procedures, record of operating conditions during the 
    test, record of preparation of standards, record of calibrations, raw 
    data sheets for field sampling, raw data sheets for field and 
    laboratory analyses, documentation of calculations, and any other 
    information required by the test method.
        (ii) For each monitored parameter for which a maximum or minimum 
    level is required to be established under Sec. 63.120(d)(3) of subpart 
    G for storage vessels, Sec. 63.485(k) for continuous front-end process 
    vents, Sec. 63.489 for batch front-end process vents and aggregate 
    batch vent streams, Sec. 63.497 for back-end process operations, 
    Sec. 63.143(f) of subpart G for process wastewater, Sec. 63.503(m) for 
    emission points in emissions averages, paragraph (e)(8) of this 
    section, or paragraph (f) of this section, the information specified in 
    paragraphs (e)(5)(ii)(A) through (e)(5)(ii)(E) of this section, unless 
    this information has been established and provided in the operating 
    permit.
        (A) The required information shall include the specific maximum or 
    minimum level of the monitored parameter(s) for each emission point.
        (B) The required information shall include the rationale for the 
    specific maximum or minimum level for each parameter for each emission 
    point, including any data and calculations used to develop the level 
    and a description of why the level indicates proper operation of the 
    control device.
        (C) The required information shall include a definition of the 
    affected source's operating day, as specified in paragraph (d)(3)(ii) 
    of this section, for purposes of determining daily average values of 
    monitored parameters.
        (D) For batch front-end process vents, the required information 
    shall include a definition of each batch cycle that requires the 
    control of one or more batch emission episodes during the cycle, as 
    specified in Sec. 63.490(c)(2) and 63.505(b)(3)(ii).
        (E) The required information shall include a definition of the 
    affected source's operating month for the purposes of determining 
    monthly average values of residual organic HAP.
        (iii) For emission points included in an emissions average, the 
    values of all parameters needed for input to the emission credit and 
    debit equations in Sec. 63.503 (g) and (h), calculated or measured 
    according to the procedures in Sec. 63.503 (g) and (h), and the 
    resulting calculation of credits and debits for the first quarter of 
    the year. The first quarter begins on the compliance date specified.
        (iv) For batch front-end process vents required to establish a 
    batch cycle limitation under Sec. 63.490(f), the owner or operator must 
    define the 12-month period over which that source's ``year'' will be 
    said to occur, as required by the definition of ``year'' in 
    Sec. 63.482.
        (v) The determination of applicability for flexible operation units 
    as specified in Sec. 63.480(f)(6).
        (vi) The parameter monitoring levels for flexible operation units, 
    and the basis on which these levels were selected, or a demonstration 
    that these levels are appropriate at all times, as specified in 
    Sec. 63.480(f)(7).
        (vii) The results for each predominant use determination for 
    storage vessels belonging to an affected source subject to this subpart 
    that is made under Sec. 63.480(g)(6).
        (viii) The results for each predominant use determination for 
    recovery operation equipment belonging to an affected source subject to 
    this subpart that is made under Sec. 63.480(h)(6).
        (ix) For owners and operators of Group 2 batch front-end process 
    vents establishing a batch cycle limitation, as specified in 
    Sec. 63.490(f), the affected source's operating year for purposes of 
    determining compliance with the batch cycle limitation.
        (6) Periodic Reports. For existing and new affected sources, each 
    owner or operator shall submit Periodic Reports as specified in 
    paragraphs (e)(6)(i) through (e)(6)(xi) of this section.
        (i) Except as specified in paragraphs (e)(6)(x) and (e)(6)(xi) of 
    this section, a report containing the information in paragraph 
    (e)(6)(ii) of this section or paragraphs (e)(6)(iii) through (e)(6)(ix) 
    of this section, as appropriate, shall be
    
    [[Page 46975]]
    
    submitted semiannually no later than 60 operating days after the end of 
    each 180 day period. The first report shall be submitted no later than 
    240 days after the date the Notification of Compliance Status is due 
    and shall cover the 6-month period beginning on the date the 
    Notification of Compliance Status is due. Subsequent reports shall 
    cover each preceding 6-month period.
        (ii) If none of the compliance exceptions in paragraphs (e)(6)(iii) 
    through (e)(6)(ix) of this section occurred during the 6-month period, 
    the Periodic Report required by paragraph (e)(6)(i) of this section 
    shall be a statement that the affected source was in compliance for the 
    preceding 6-month period and that none of the activities specified in 
    paragraphs (e)(6)(iii) through (e)(6)(ix) of this section occurred.
        (iii) For an owner or operator of an affected source complying with 
    the provisions of Secs. 63.484 through 63.501 for any emission point, 
    Periodic Reports shall include:
        (A) All information specified in Sec. 63.122(a)(4) of subpart G for 
    storage vessels, Secs. 63.117(a)(3) and 63.118(f) of subpart G for 
    continuous front-end process vents, Sec. 63.492 for batch front-end 
    process vents and aggregate batch vent streams, Sec. 63.499 for back-
    end process operations, Sec. 63.104(b)(4) of subpart F for heat 
    exchange systems, and Sec. 63.146(c) through Sec. 63.146(f) of subpart 
    G for process wastewater.
        (B) The daily average values or batch cycle daily average values of 
    monitored parameters for all excursions, as defined in Sec. 63.505(g) 
    and Sec. 63.505(h).
        (C) The periods when monitoring data were not collected shall be 
    specified; and
        (D) The information in paragraphs (e)(6)(iii)(D)(1) through 
    (e)(6)(iii)(D)(3) of this section, as applicable:
        (1) Any supplements to the Emissions Averaging Plan, as required in 
    paragraph (e)(4)(iii) of this section;
        (2) Notification if a process change is made such that the group 
    status of any emission point changes. The information submitted shall 
    include a compliance schedule, as specified in paragraphs 
    (e)(6)(iii)(D)(2)(i) and (e)(6)(iii)(D)(2)(ii) of this section, for 
    emission points that change from Group 2 to Group 1, or for continuous 
    front-end process vents under the conditions listed in 
    Sec. 63.485(l)(1) through Sec. 63.485(l)(4), or for batch front-end 
    process vents under the conditions listed in Sec. 63.492 (b) or (c).
        (i) The owner of operator shall submit to the Administrator for 
    approval a compliance schedule and a justification for the schedule.
        (ii) The Administrator shall approve the compliance schedule or 
    request changes within 120 operating days of receipt of the compliance 
    schedule and justification.
        (3) Notification if one or more emission points or one or more EPPU 
    is added to an affected source. The owner or operator shall submit the 
    information contained in paragraphs (e)(6)(iii)(D)(3)(i) through 
    (e)(6)(iii)(D)(3)(iii) of this section.
        (i) A description of the addition to the affected source;
        (ii) Notification of the group status of the additional emission 
    point or all emission points in the EPPU;
        (iii) A compliance schedule, as required under paragraph 
    (e)(6)(iii)(D)(2) of this section.
        (4) Notification if a standard operating procedure, as defined in 
    Sec. 63.500(l), is changed. This shall also include test results of the 
    carbon disulfide concentration resulting from the new standard 
    operating procedure.
        (E) The information in paragraph (b)(1)(ii) of this section for 
    reports of startup, shutdown, and malfunction.
        (iv) For each batch front-end process vent with a batch cycle 
    limitation, the owner or operator shall include the number of batch 
    cycles accomplished during the preceding 12-month period once per year 
    in a Periodic Report.
        (v) If any performance tests are reported in a Periodic Report, the 
    following information shall be included:
        (A) One complete test report shall be submitted for each test 
    method used for a particular kind of emission point tested. A complete 
    test report shall contain the information specified in paragraph 
    (e)(5)(i)(B) of this section.
        (B) For additional tests performed for the same kind of emission 
    point using the same method, results and any other information required 
    shall be submitted, but a complete test report is not required.
        (vi) The results for each change made to a primary product 
    determination for an elastomer product made under Sec. 63.480(f)(6).
        (vii) The results for each change made to a predominant use 
    determination for a storage vessel belonging to an affected source 
    subject to this subpart that is made under Sec. 63.480(g)(6).
        (viii) The results for each change made to a predominant use 
    determination for recovery operation equipment belonging to an affected 
    source subject to this subpart that is made under Sec. 63.480(h)(6).
        (ix) The Periodic Report required by Sec. 63.502(i) shall be 
    submitted as part of the Periodic Report required by paragraph (e)(6) 
    of this section.
        (x) The owner or operator of an affected source shall submit 
    quarterly reports for all emission points included in an emissions 
    average.
        (A) The quarterly reports shall be submitted no later than 60 
    operating days after the end of each quarter. The first report shall be 
    submitted with the Notification of Compliance Status no later than 150 
    days after the compliance date.
        (B) The quarterly reports shall include the information specified 
    in paragraphs (e)(6)(x)(B)(1) through (e)(6)(x)(B)(7) of this section 
    for all emission points included in an emissions average.
        (1) The credits and debits calculated each month during the 
    quarter;
        (2) A demonstration that debits calculated for the quarter are not 
    more than 1.30 times the credits calculated for the quarter, as 
    required under Sec. 63.503(e)(4);
        (3) The values of any inputs to the debit and credit equations in 
    Sec. 63.503(g) and (h) that change from month to month during the 
    quarter or that have changed since the previous quarter;
        (4) Results of any performance tests conducted during the reporting 
    period including one complete report for each test method used for a 
    particular kind of emission point as described in paragraph (e)(6)(v) 
    of this section;
        (5) Reports of daily average values or batch cycle daily averages 
    of monitored parameters for excursions as defined in Sec. 63.505(g) or 
    (h);
        (6) For excursions caused by lack of monitoring data, the duration 
    of periods when monitoring data were not collected shall be specified; 
    and
        (7) Any other information the affected source is required to report 
    under the operating permit or Emissions Averaging Plan for the affected 
    source.
        (C) Sec. 63.505 shall govern the use of monitoring data to 
    determine compliance for Group 1 and Group 2 emission points included 
    in emissions averages.
        (D) Every fourth quarterly report shall include the following:
        (1) A demonstration that annual credits are greater than or equal 
    to annual debits as required by Sec. 63.503(e)(3); and
        (2) A certification of compliance with all the emissions averaging 
    provisions in Sec. 63.503.
        (xi) The owner or operator of an affected source shall submit 
    quarterly reports for particular emission points and process sections 
    not included in an emissions average as specified in paragraphs 
    (e)(6)(xi)(A) through (e)(6)(xi)(E) of this section.
        (A) If requested by the Administrator, the owner or operator of an 
    affected
    
    [[Page 46976]]
    
    source shall submit quarterly reports for a period of 1 year for an 
    emission point or process section that is not included in an emissions 
    average if either the conditions in paragraph (e)(6)(xi)(A)(1) or 
    (e)(6)(xi)(A)(2) of this section are met.
        (1) An emission point has any excursions, as defined in 
    Sec. 63.505(g) or Sec. 63.505(h) for a semiannual reporting period.
        (2) The process section is out of compliance with its applicable 
    standard.
        (B) The quarterly reports shall include all information specified 
    in paragraphs (e)(6)(iii) and (e)(6)(ix) of this section, as applicable 
    to the emission point or process section for which quarterly reporting 
    is required under paragraph (e)(6)(ix)(A) of this section. Information 
    applicable to other emission points within the affected source shall be 
    submitted in the semiannual reports required under paragraph (e)(6)(i) 
    of this section.
        (C) Quarterly reports shall be submitted no later than 60 operating 
    days after the end of each quarter.
        (D) After quarterly reports have been submitted for an emission 
    point for 1 year, the owner or operator may return to semiannual 
    reporting for the emission point or process section unless the 
    Administrator requests the owner or operator to continue to submit 
    quarterly reports.
        (E) Sec. 63.505 shall govern the use of monitoring data to 
    determine compliance for Group 1 emission points.
        (7) Other reports. Other reports shall be submitted as specified in 
    paragraphs (e)(7)(i) and (e)(7)(ii) of this section.
        (i) For storage vessels, the notifications of inspections required 
    by Sec. 63.484 shall be submitted, as specified in Sec. 63.122(h)(1) 
    and (h)(2) of subpart G.
        (ii) For owners or operators of affected sources required to 
    request approval for a nominal control efficiency for use in 
    calculating credits for an emissions average, the information specified 
    in Sec. 63.503(i) shall be submitted.
        (iii) For back-end process operations complying using control or 
    recovery devices, the recompliance determination report required by 
    Sec. 63.499(d) shall be submitted within 180 days after the process 
    change.
        (8) Operating Permit. An owner or operator who submits an operating 
    permit application instead of an Emissions Averaging Plan or a 
    Precompliance Report shall submit the following information with the 
    operating permit application:
        (i) The information specified in paragraph (e)(4) of this section 
    for points included in an emissions average; and
        (ii) The information specified in paragraph (e)(3) of this section, 
    Precompliance Report, as applicable.
        (f) Alternative monitoring parameters. The owner or operator who 
    has been directed by any section of this subpart to set unique 
    monitoring parameters, or who requests approval to monitor a different 
    parameter than those listed in Sec. 63.484 for storage vessels, 
    Sec. 63.114 of subpart G for continuous front-end process vents, 
    Sec. 63.489 for batch front-end process vents and aggregate batch vent 
    streams, Sec. 63.497 for back-end process operations, or Sec. 63.143 of 
    subpart G for process wastewater shall submit the information specified 
    in paragraphs (f)(1) through (f)(3) of this section in the 
    Precompliance Report, as required by paragraph (e)(3) of this section. 
    The owner or operator shall retain for a period of 5 years each record 
    required by paragraphs (f)(1) through (f)(3) of this section.
        (1) The required information shall include a description of the 
    parameter(s) to be monitored to ensure the recovery device, control 
    device, or pollution prevention measure is operated in conformance with 
    its design and achieves the specified emission limit, percent 
    reduction, or nominal efficiency, and an explanation of the criteria 
    used to select the parameter(s).
        (2) The required information shall include a description of the 
    methods and procedures that will be used to demonstrate that the 
    parameter indicates proper operation, the schedule for this 
    demonstration, and a statement that the owner or operator will 
    establish a level for the monitored parameter as part of the 
    Notification of Compliance Status report required in paragraph (e)(5) 
    of this section, unless this information has already been included in 
    the operating permit application.
        (3) The required information shall include a description of the 
    proposed monitoring, recordkeeping, and recording system, to include 
    the frequency and content of monitoring, recordkeeping, and reporting. 
    Further, the rationale for the proposed monitoring, recordkeeping, and 
    reporting system shall be included if either condition in paragraph 
    (f)(3)(i) or (f)(3)(ii) of this section are met:
        (i) If monitoring and recordkeeping is not continuous, or
        (ii) If reports of daily average values will not be included in 
    Periodic Reports when the monitored parameter value is above the 
    maximum level or below the minimum level as established in the 
    operating permit or the Notification of Compliance Status.
        (g) Alternative continuous monitoring and recordkeeping. An owner 
    or operator choosing not to implement the continuous parameter 
    operating and recordkeeping provisions listed in Sec. 63.485 for 
    continuous front-end process vents, Sec. 63.486 for batch front-end 
    process vents and aggregate batch vent streams, Sec. 63.493 for back-
    end process operations, and Sec. 63.501 for wastewater, may instead 
    request approval to use alternative continuous monitoring and 
    recordkeeping provisions according to the procedures specified in 
    paragraphs (g)(1) through (g)(4) of this section. Requests shall be 
    submitted in the Precompliance Report as specified in paragraph 
    (e)(3)(iv) of this section, if not already included in the operating 
    permit application, and shall contain the information specified in 
    paragraphs (g)(2)(ii) and (g)(3)(ii) of this section, as applicable.
        (1) The provisions in Sec. 63.8(f)(5)(i) of subpart A shall govern 
    the review and approval of requests.
        (2) An owner or operator of an affected source that does not have 
    an automated monitoring and recording system capable of measuring 
    parameter values at least once every 15 minutes and that does not 
    generate continuous records may request approval to use a nonautomated 
    system with less frequent monitoring, in accordance with paragraphs 
    (g)(2)(i) and (g)(2)(ii) of this section.
        (i) The requested system shall include manual reading and recording 
    of the value of the relevant operating parameter no less frequently 
    than once per hour. Daily average or batch cycle daily average values 
    shall be calculated from these hourly values and recorded.
        (ii) The request shall contain:
        (A) A description of the planned monitoring and recordkeeping 
    system;
        (B) Documentation that the affected source does not have an 
    automated monitoring and recording system;
        (C) Justification for requesting an alternative monitoring and 
    recordkeeping system; and
        (D) Demonstration to the Administrator's satisfaction that the 
    proposed monitoring frequency is sufficient to represent control device 
    operating conditions, considering typical variability of the specific 
    process and control device operating parameter being monitored.
        (3) An owner or operator may request approval to use an automated 
    data compression recording system that does not record monitored 
    operating parameter values at a set frequency (for example, once every 
    15 minutes), but that records all values that meet set criteria for 
    variation from previously
    
    [[Page 46977]]
    
    recorded values, in accordance with paragraphs (g)(3)(i) and (g)(3)(ii) 
    of this section.
        (i) The requested system shall be designed to:
        (A) Measure the operating parameter value at least once every 15 
    minutes;
        (B) Except for the monitoring of batch front-end process vents, 
    record at least four values each hour during periods of operation;
        (C) Record the date and time when monitors are turned off or on;
        (D) Recognize unchanging data that may indicate the monitor is not 
    functioning properly, alert the operator, and record the incident;
        (E) Calculate daily average or batch cycle daily average values of 
    the monitored operating parameter based on all measured data; and
        (F) If the daily average is not an excursion, as defined in 
    Sec. 63.505 (g) or (h), the data for that operating day may be 
    converted to hourly average values and the four or more individual 
    records for each hour in the operating day may be discarded.
        (ii) The request shall contain:
        (A) A description of the monitoring system and data compression 
    recording system, including the criteria used to determine which 
    monitored values are recorded and retained;
        (B) The method for calculating daily averages and batch cycle daily 
    averages; and
        (C) A demonstration that the system meets all criteria in paragraph 
    (g)(3)(i) of this section.
        (4) An owner or operator may request approval to use other 
    alternative monitoring systems according to the procedures specified in 
    Sec. 63.8(f)(4) of subpart A.
        (h) Reduced recordkeeping program. For any parameter with respect 
    to any item of equipment, the owner or operator may implement the 
    recordkeeping requirements in paragraph (h)(1) or (h)(2) of this 
    section as alternatives to the continuous operating parameter 
    monitoring and recordkeeping provisions listed in Sec. 63.484 for 
    storage vessels, Sec. 63.485 for continuous front-end process vents, 
    Sec. 63.486 for batch front-end process vents and aggregate batch vent 
    streams, Sec. 63.493 for back-end processes, and Sec. 63.501 for 
    wastewater. The owner or operator shall retain for a period of 5 years 
    each record required by paragraph (h)(1) or (h)(2) of this section.
        (1) The owner or operator may retain only the daily average or the 
    batch cycle daily average value, and is not required to retain more 
    frequent monitored operating parameter values, for a monitored 
    parameter with respect to an item of equipment, if the requirements of 
    paragraphs (h)(1)(i) through (h)(1)(iv) of this section are met. An 
    owner or operator electing to comply with the requirements of paragraph 
    (h)(1) of this section shall notify the Administrator in the 
    Notification of Compliance Status or, if the Notification of Compliance 
    Status has already been submitted, in the Periodic Report immediately 
    preceding implementation of the requirements of paragraph (h)(1) of 
    this section.
        (i) The monitoring system is capable of detecting unrealistic or 
    impossible data during periods of operation other than startups, 
    shutdowns or malfunctions (e.g., a temperature reading of -200 deg.C on 
    a boiler), and will alert the operator by alarm or other means. The 
    owner or operator shall record the occurrence. All instances of the 
    alarm or other alert in an operating day constitute a single 
    occurrence.
        (ii) The monitoring system generates, updated at least hourly 
    throughout each operating day, a running average of the monitoring 
    values that have been obtained during that operating day, and the 
    capability to observe this running average is readily available to the 
    Administrator on-site during the operating day. The owner or operator 
    shall record the occurrence of any period meeting the criteria in 
    paragraphs (h)(1)(ii)(A) through (h)(1)(ii)(C) of this section. All 
    instances in an operating day constitute a single occurrence.
        (A) The running average is above the maximum or below the minimum 
    established limits;
        (B) The running average is based on at least six one-hour periods; 
    and
        (C) The running average reflects a period of operation other than a 
    startup, shutdown, or malfunction.
        (iii) The monitoring system is capable of detecting unchanging data 
    during periods of operation other than startups, shutdowns or 
    malfunctions, except in circumstances where the presence of unchanging 
    data is the expected operating condition based on past experience 
    (e.g., pH in some scrubbers), and will alert the operator by alarm or 
    other means. The owner or operator shall record the occurrence. All 
    instances of the alarm or other alert in an operating day constitute a 
    single occurrence.
        (iv) The monitoring system will alert the owner or operator by an 
    alarm, if the running average parameter value calculated under 
    paragraph (h)(1)(ii) of this section reaches a set point that is 
    appropriately related to the established limit for the parameter that 
    is being monitored.
        (v) The owner or operator shall verify the proper functioning of 
    the monitoring system, including its ability to comply with the 
    requirements of paragraph (h)(1) of this section, at the times 
    specified in paragraphs (h)(1)(v)(A) through (h)(1)(v)(C) of this 
    section. The owner or operator shall document that the required 
    verifications occurred.
        (A) Upon initial installation.
        (B) Annually after initial installation.
        (C) After any change to the programming or equipment constituting 
    the monitoring system, which might reasonably be expected to alter the 
    monitoring system's ability to comply with the requirements of this 
    section.
        (vi) The owner or operator shall retain the records identified in 
    paragraphs (h)(1)(vi)(A) through (h)(1)(vi)(C) of this section.
        (A) Identification of each parameter, for each item of equipment, 
    for which the owner or operator has elected to comply with the 
    requirements of paragraph (h) of this section.
        (B) A description of the applicable monitoring system(s), and how 
    compliance will be achieved with each requirement of paragraphs 
    (h)(1)(i) through (h)(1)(v) of this section. The description shall 
    identify the location and format (e.g., on-line storage, log entries) 
    for each required record. If the description changes, the owner or 
    operator shall retain both the current and the most recent superseded 
    description.
        (C) A description, and the date, of any change to the monitoring 
    system that would reasonably be expected to affect its ability to 
    comply with the requirements of paragraph (h)(1) of this section.
        (2) If an owner or operator has elected to implement the 
    requirements of paragraph (h)(1) of this section for a monitored 
    parameter with respect to an item of equipment and a period of 6 
    consecutive months has passed without an excursion as defined in 
    paragraph (h)(2)(iv) of this section, the owner or operator is no 
    longer required to record the daily average or batch cycle daily 
    average value, for any operating day when the daily average or batch 
    cycle daily average value is less than the maximum, or greater than the 
    minimum established limit. With approval by the Administrator, 
    monitoring data generated prior to the compliance date of this subpart 
    shall be credited toward the period of 6 consecutive months, if the 
    parameter limit and the monitoring accomplished during the period prior 
    to the compliance date was required and/or approved by the 
    Administrator.
        (i) If the owner or operator elects not to retain the daily average 
    or batch cycle
    
    [[Page 46978]]
    
    daily average values, the owner or operator shall notify the 
    Administrator in the next Periodic Report. The notification shall 
    identify the parameter and unit of equipment.
        (ii) If, on any operating day after the owner or operator has 
    ceased recording daily average or batch cycle daily average values as 
    provided in paragraph (h)(2) of this section, there is an excursion as 
    defined in paragraph (h)(2)(iv) of this section, the owner or operator 
    shall immediately resume retaining the daily average or batch cycle 
    daily average value for each operating day and shall notify the 
    Administrator in the next Periodic Report. The owner or operator shall 
    continue to retain each daily average or batch cycle daily average 
    value until another period of 6 consecutive months has passed without 
    an excursion as defined in paragraph (h)(2)(iv) of this section.
        (iii) The owner or operator shall retain the records specified in 
    paragraphs (h)(1)(i), (h)(1)(ii), and (h)(1)(iv) of this section, for 
    the duration specified in paragraph (h) of this section. For any 
    calendar month, if compliance with paragraphs (h)(1)(i) through 
    (h)(1)(iv) of this section does not result in retention of a record of 
    at least one occurrence or measured parameter value, the owner or 
    operator shall record and retain at least one parameter value during a 
    period of operation other than a startup, shutdown, or malfunction.
        (iv) For the purposes of paragraph (h) of this section, an 
    excursion means that the daily average or batch cycle daily average 
    value of monitoring data for a parameter is greater than the maximum, 
    or less than the minimum established value, except as provided in 
    paragraphs (h)(2)(iv)(A) and (h)(2)(iv)(B) of this section.
        (A) The daily average or batch cycle daily average value during any 
    startup, shutdown, or malfunction shall not be considered an excursion 
    for purposes of paragraph (h)(2) of this section, if the owner or 
    operator follows the applicable provisions of the startup, shutdown, 
    and malfunction plan required by Sec. 63.6(e)(3) of subpart A.
        (B) An excused excursion, as described in Sec. 63.505(i), shall not 
    be considered an excursion for the purposes of paragraph (h)(2) of this 
    section.
    
                       Table 1.--Applicability of General Provisions to Subpart U Affected Sources                  
    ----------------------------------------------------------------------------------------------------------------
                  Reference                 Applies to subpart U                        Comment                     
    ----------------------------------------------------------------------------------------------------------------
    63.1(a)(1)...........................  Yes...................  Sec.  63.482 of Subpart U specifies definitions  
                                                                    in addition to or that supersede definitions in 
                                                                    Sec.  63.2.                                     
    63.1(a)(2)-63.1(a)(3)................  Yes                                                                      
    63.1(a)(4)...........................  Yes...................  Subpart U (this table) specifies the             
                                                                    applicability of each paragraph in subpart A to 
                                                                    subpart U.                                      
    63.1(a)(5)...........................  No....................  Reserved.                                        
    63.1(a)(6)-63.1(a)(8)................  Yes                                                                      
    63.1(a)(9)...........................  No....................  Reserved.                                        
    63.1(a)(10)..........................  No....................  Subpart U and other cross-referenced subparts    
                                                                    specify calendar or operating day.              
    63.1(a)(11)..........................  Yes                                                                      
    63.1(a)(12)-63.1(a)(14)..............  Yes                                                                      
    63.1(b)(1)...........................  Yes...................  Sec.  63.480(a) contains specific applicability  
                                                                    criteria.                                       
    63.1(b)(2)...........................  Yes                                                                      
    63.1(b)(3)...........................  No....................  Sec.  63.480(b) of subpart U provides            
                                                                    documentation requirements for EPPUs not        
                                                                    considered affected sources.                    
    63.1(c)(1)...........................  Yes...................  Subpart U (this table) specifies the             
                                                                    applicability of each paragraph in subpart A to 
                                                                    subpart U.                                      
    63.1(c)(2)...........................  No....................  Area sources are not subject to subpart U.       
    63.1(c)(3)...........................  No....................  Reserved.                                        
    63.1(c)(4)...........................  Yes                                                                      
    63.1(c)(5)...........................  Yes...................  Except that affected sources are not required to 
                                                                    submit notifications overridden by this table.  
    63.1(d)..............................  No....................  Reserved.                                        
    63.1(e)..............................  Yes                                                                      
    63.2.................................  Yes...................  Sec.  63.482 of subpart U specifies those subpart
                                                                    A definitions that apply to subpart U.          
    63.3.................................  Yes                                                                      
    63.4(a)(1)-63.4(a)(3)................  Yes                                                                      
    63.4(a)(4)...........................  No....................  Reserved.                                        
    63.4(a)(5)...........................  Yes                                                                      
    63.4(b)..............................  Yes                                                                      
    63.4(c)..............................  Yes                                                                      
    63.5(a)..............................  Yes                                                                      
    63.5(b)(1)...........................  Yes                                                                      
    63.5(b)(2)...........................  No....................  Reserved.                                        
    63.5(b)(3)...........................  Yes                                                                      
    63.5(b)(4)...........................  Yes                                                                      
    63.5(b)(5)...........................  Yes                                                                      
    63.5(b)(6)...........................  No....................  Sec.  63.480(i) of subpart U specifies           
                                                                    requirements.                                   
    63.5(c)..............................  No....................  Reserved.                                        
    63.5(d)(1)(i)........................  Yes                                                                      
    63.5(d)(1)(ii).......................  Yes...................  Except that for affected sources subject to      
                                                                    subpart U, emission estimates specified in Sec. 
                                                                    63.5(d)(1)(ii)(H) are not required.             
    63.5(d)(1)(iii)......................  No....................  Sec.  63.506(e)(5) of subpart U specifies        
                                                                    Notification of Compliance Status requirements. 
    63.5(d)(2)...........................  xlNo..................                                                   
    63.5(d)(3)...........................  Yes...................  Except Sec.  63.5(d)(3)(ii) does not apply.      
    63.5(d)(4)...........................  Yes                                                                      
    63.5(e)..............................  Yes                                                                      
    63.5(f)(1)...........................  Yes                                                                      
    63.5(f)(2)...........................  Yes...................  Except that where Sec.  63.5(d)(1) is referred   
                                                                    to, Sec.  63.5(d)(1)(i) does not apply.         
    63.6(a)..............................  Yes                                                                      
    63.6(b)(1)...........................  Yes                                                                      
    
    [[Page 46979]]
    
                                                                                                                    
    63.6(b)(2)...........................  Yes                                                                      
    63.6(b)(3)...........................  Yes                                                                      
    63.6(b)(4)...........................  Yes                                                                      
    63.6(b)(5)...........................  Yes                                                                      
    63.6(b)(6)...........................  No....................  Reserved.                                        
    63.6(b)(7)...........................  Yes                                                                      
    63.6(c)(1)...........................  Yes...................  Sec.  63.481 of subpart U specifies the          
                                                                    compliance date.                                
    63.6(c)(2)...........................  Yes                                                                      
    63.6(c)(3)...........................  No....................  Reserved.                                        
    63.6(c)(4)...........................  No....................  Reserved.                                        
    63.6(c)(5)...........................  Yes                                                                      
    63.6(d)..............................  No....................  Reserved.                                        
    63.6(e)..............................  Yes...................  Except the plan, and any records or reports of   
                                                                    startup, shutdown and malfunction do not apply  
                                                                    to Group 2 emission points, unless they are     
                                                                    included in an emissions average.               
    63.6(f)(1)...........................  Yes                                                                      
    63.6(f)(2)...........................  Yes...................  Except that in Sec.  63.6(f)(2)(iii)(D),         
                                                                    paragraph 63.7(c) does not apply.               
    63.6(f)(3)...........................  Yes...................  Except that Sec.  63.6(f)(2)(iii)(D) is not      
                                                                    applicable.                                     
    63.6(g)..............................  Yes                                                                      
    63.6(h)..............................  No....................  Subpart U does not require opacity and visible   
                                                                    emission standards.                             
    63.6(i)..............................  Yes...................  Except for Sec.  63.6(i)(15), which is reserved, 
                                                                    and except that the requests for extension shall
                                                                    be submitted no later than the date on which the
                                                                    Precompliance Report is required to be submitted
                                                                    in Sec.  63.506(e)(3)(i).                       
    63.6(j)..............................  Yes                                                                      
    63.7(a)(1)...........................  Yes                                                                      
    63.7(a)(2)...........................  No....................  Sec.  63.506(e)(5) of subpart U specifies        
                                                                    submittal dates.                                
    63.7(a)(3)...........................  Yes                                                                      
    63.7(b)..............................  No....................  Sec.  63.504(a)(4) of subpart U specifies        
                                                                    notification requirements.                      
    63.7(c)..............................  No....................  Except if the owner or operator chooses to submit
                                                                    an alternative nonopacity emission standard for 
                                                                    approval under Sec.  63.6(g).                   
    63.7(d)..............................  Yes                                                                      
    63.7(e)..............................  Yes...................  Except that performance tests must be conducted  
                                                                    at maximum representative operating conditions. 
                                                                    In addition, some of the testing requirements   
                                                                    specified in subpart U are not consistent with  
                                                                    Sec.  63.7(e)(3).                               
    63.7(f)..............................  No....................  Subpart U specifies applicable test methods and  
                                                                    provides alternatives.                          
    63.7(g)..............................  Yes...................  Except that references to the Notification of    
                                                                    Compliance Status report in 63.9(h) of subpart A
                                                                    are replaced with the requirements in Sec.      
                                                                    63.506(e)(5) of subpart U.                      
    63.7(h)..............................  Yes...................  Except Sec.  63.7(h)(4)(ii) is not applicable,   
                                                                    since the site-specific test plans in Sec.      
                                                                    63.7(c)(3) are not required.                    
    63.8(a)(1)...........................  Yes                                                                      
    63.8(a)(2)...........................  No                                                                       
    63.8(a)(3)...........................  No....................  Reserved.                                        
    63.8(a)(4)...........................  Yes                                                                      
    63.8(b)(1)...........................  Yes                                                                      
    63.8(b)(2)...........................  No....................  Subpart U specifies locations to conduct         
                                                                    monitoring.                                     
    63.8(b)(3)                                                                                                      
    63.8(c)(1)(i)........................  Yes                                                                      
    63.8(c)(1)(ii).......................  No                                                                       
    63.8(c)(1)(iii)......................  Yes                                                                      
    63.8(c)(2)...........................  Yes                                                                      
    63.8(c)(3)...........................  Yes                                                                      
    63.8(c)(4)...........................  No....................  Sec.  63.505 of subpart U specifies monitoring   
                                                                    frequency.                                      
    63.8(c)(5)-63.8(c)(8)................  No                                                                       
    63.8(d)..............................  No                                                                       
    63.8(e)..............................  No                                                                       
    63.8(f)(1)-63.8(f)(3)................  Yes                                                                      
    63.8(f)(4)(i)........................  No....................  Timeframe for submitting request is specified in 
                                                                    Sec.  63.506(f) of subpart U.                   
    63.8(f)(4)(ii).......................  No                                                                       
    63.8(f)(4)(iii)......................  No                                                                       
    63.8(f)(5)(i)........................  Yes                                                                      
    63.8(f)(5)(ii).......................  No                                                                       
    63.8(f)(5)(iii)......................  Yes                                                                      
    63.8(f)(6)...........................  No....................  Subpart U does not require CEM's.                
    63.8(g)..............................  No....................  Data reduction procedures specified in Sec.      
                                                                    63.506(d) of subpart U.                         
    63.9(a)..............................  Yes                                                                      
    63.9(b)..............................  No....................  Subpart U does not require an initial            
                                                                    notification.                                   
    63.9(c)..............................  Yes                                                                      
    63.9(d)..............................  Yes                                                                      
    63.9(e)..............................  No                                                                       
    63.9(f)..............................  No....................  Subpart U does not require opacity and visible   
                                                                    emission standards.                             
    63.9(g)..............................  No                                                                       
    63.9(h)..............................  No....................  Sec.  63.506(e)(5) of subpart U specifies        
                                                                    Notification of Compliance Status requirements. 
    
    [[Page 46980]]
    
                                                                                                                    
    63.9(i)..............................  Yes                                                                      
    63.9(j)..............................  No                                                                       
    63.10(a).............................  Yes                                                                      
    63.10(b)(1)..........................  Yes                                                                      
    63.10(b)(2)..........................  Yes                                                                      
    63.10(b)(3)..........................  No....................  Sec.  63.480(b) of subpart U requires            
                                                                    documentation of sources that are not affected  
                                                                    sources.                                        
    63.10(c).............................  No....................  Sec.  63.506 of subpart U specifies recordkeeping
                                                                    requirements.                                   
    63.10(d)(1)..........................  Yes                                                                      
    63.10(d)(2)..........................  No                                                                       
    63.10(d)(3)..........................  No....................  Subpart U does not require opacity and visible   
                                                                    emission standards.                             
    63.10(d)(4)..........................  Yes                                                                      
    63.10(d)(5)..........................  Yes...................  Except that reports required by Sec.             
                                                                    63.10(d)(5)(i) shall be submitted at the same   
                                                                    time as Periodic Reports specified in Sec.      
                                                                    63.506(e)(6) of subpart U. The startup,         
                                                                    shutdown, and malfunction plan, and any records 
                                                                    or reports of startup, shutdown, and malfunction
                                                                    do not apply to Group 2 emission points unless  
                                                                    they are included in an emissions average.      
    63.10(e).............................  No                                                                       
    63.10(f).............................  Yes                                                                      
    63.10(d)(4)..........................  Yes                                                                      
    63.11................................  Yes                                                                      
    63.12................................  Yes                                                                      
    63.13................................  Yes                                                                      
    63.14................................  Yes                                                                      
    63.15................................  Yes                                                                      
    ----------------------------------------------------------------------------------------------------------------
    
    
                       Table 2. Applicability of Subparts F, G, & H to Subpart U Affected Sources                   
    ----------------------------------------------------------------------------------------------------------------
                                     Applies To                                               Applicable section of 
              Reference              subpart U                     Comment                          subpart U       
    ----------------------------------------------------------------------------------------------------------------
                                                        Subpart F                                                   
    ----------------------------------------------------------------------------------------------------------------
    63.100.......................  No                                                                               
    63.101.......................  Yes..........  Several definitions from 63.101 are       63.482                  
                                                   incorporated by reference into 63.482.                           
    63.102-63.109................  No                                                                               
    ----------------------------------------------------------------------------------------------------------------
                                                        Subpart G                                                   
    ----------------------------------------------------------------------------------------------------------------
    63.110.......................  No                                                                               
    63.111.......................  Yes..........  Several definitions from 63.111 are       63.482                  
                                                   incorporated by reference into 63.482.                           
    63.112.......................  No                                                                               
    63.113-63.118................  Yes..........  With the differences noted in 63.485(b)   63.485                  
                                                   through 63.485(k).                                               
    63.119-63.123................  Yes..........  With the differences noted in 63.484(c)   63.484                  
                                                   through 63.484(q).                                               
    63.124-63.125................  No...........  Reserved                                                          
    63.126-63.130................  No                                                                               
    63.131-63.147................  Yes..........  With the differences noted in             63.501                  
                                                   63.501(a)(1) through 63.501(a)(8).                               
    63.148.......................  Yes..........  With the differences noted in 63.484(c)   63.484 and 63.501       
                                                   through 63.484(q) and 63.501(a)(1)                               
                                                   through 63.501(a)(8).                                            
    63.149.......................  No...........  Reserved                                                          
    63.150(a) through 63.150(f)..  No                                                                               
    63.150(g)(1) and 63.150(g)(2)  No                                                                               
    63.150(g)(3).................  Yes..........  ........................................  63.503(g)(3)            
    63.150(g)(4).................  No                                                                               
    63.150(g)(5).................  Yes..........  ........................................  63.503(g)(5)            
    63.150(h)(1) and 63.150(h)(2)  No                                                                               
    63.150(h)(3).................  Yes..........  ........................................  63.503(h)(3)            
    63.150(h)(4).................  No                                                                               
    63.150(h)(5).................  Yes..........  ........................................  63.503(h)(5)            
    63.150(i) through 63.150(o)..  No                                                                               
    63.151-63.152................  No                                                                               
    ----------------------------------------------------------------------------------------------------------------
                                                        Subpart H                                                   
    ----------------------------------------------------------------------------------------------------------------
    63.160-63.193................  Yes..........  Subpart U affected sources must comply    63.502                  
                                                   with all requirements of subpart H.                              
    ----------------------------------------------------------------------------------------------------------------
    
    
    [[Page 46981]]
    
    
    
         Table 3.--Group 1 Storage Vessels at Existing Affected Sources     
    ------------------------------------------------------------------------
                                                       Vapor pressure a     
           Vessel capacity  (cubic meters)               (kilopascals)      
    ------------------------------------------------------------------------
    75  capacity < 151...............="">13.1           
    151  capacity....................  5.2            
    ------------------------------------------------------------------------
    a Maximum true vapor pressure of total organic HAP at storage           
      temperature.                                                          
    
    
                Table 4.--Group 1 Storage Vessels at New Sources            
    ------------------------------------------------------------------------
                                                       Vapor Pressure a     
           Vessel capacity (cubic meters)                (kilopascals)      
    ------------------------------------------------------------------------
    38  capacity < 151...............=""> 13.1          
    151  capacity....................   0.7           
    ------------------------------------------------------------------------
    a Maximum true vapor pressure of total organic HAP at storage           
      temperature.                                                          
    
    
                                                       Table 5.--Known Organic HAP From Elastomer Products                                                  
    --------------------------------------------------------------------------------------------------------------------------------------------------------
                                                                                 Elastomer Product/Subcategory                                              
      Organic HAP/chemical name   --------------------------------------------------------------------------------------------------------------------------
              (CAS No.)                                                                                                 PBR/                                
                                       BR        EPI        EPR        HBR       HYP       NEO       NBL       NBR      SBRS       PSR       SBL      SBRE  
    --------------------------------------------------------------------------------------------------------------------------------------------------------
    Acrylonitrile (107131).......  .........  .........  .........  ........  ........  ........                                              
     1,3 Butadiene (106990)......  .........  .........  .........  ........  ........  ........           ........      
    Carbon Tetrachloride (56235).  .........  .........  .........  ........                                                                         
    Chlorobenzene (108907).......  .........  .........  .........  ........                                                                         
    Chloroform (67663)...........  .........  .........  .........  ........                                                                         
    Chloroprene (126998).........  .........  .........  .........  ........  ........                                                               
    Epichlorohydrin (106898).....  .........                                                                                                         
    Ethylbenzene (100414)........      .........  .........  ........  ........  ........  ........  ........  ........  ........             
    Ethylene Dichloride (75343)..  .........  .........  .........  ........  ........  ........  ........  ........  ........  ........  ........          
    Ethylene Oxide (75218).......  .........      .........  ........  ........  ........  ........  ........  ........                       
    Formaldehyde (50000).........  .........  .........  .........  ........  ........  ........  ........  ........  ........                       
    Hexane (100543)..............      .........      ........  ........  ........  ........  ........     ........      
    Methanol (67561).............      .........  .........  ........  ........  ........  ........  ........                                 
    Methyl Chloride (74873)......      .........  .........  ........                                                                         
    Propylene Oxide (75569)......  .........                                                                                                         
    Styrene (100425).............  .........  .........  .........  ........  ........  ........  ........  ........     ........      
    Toluene (108883).............  .........          ........  ........     ........  ........     ........      
    Xylenes (1330207)............      .........  .........  ........  ........  ........  ........  ........  ........  ........             
    --------------------------------------------------------------------------------------------------------------------------------------------------------
     AAAACAS No. = Chemical Abstract Service Number.                                                                                                        
     BR = Butyl Rubber.                                                                                                                                     
     EPI = Epichlorohydrin Rubber.                                                                                                                          
     EPR = Ethylene Propylene Rubber.                                                                                                                       
     HBR = Halobutyl Rubber.                                                                                                                                
     HYP = Hypalon TM.                                                                                                                                      
     NEO = Neoprene.                                                                                                                                        
     NBL = Nitrile Butadiene Latex.                                                                                                                         
     NBR = Nitrile Butadiene Rubber.                                                                                                                        
     PBR/SBRS = Polybutadiene and Styrene Butadiene Rubber by Solution.                                                                                     
     PSR = Polysulfide Rubber.                                                                                                                              
     SBL = Styrene Butadiene Latex.                                                                                                                         
     SBR = Styrene Butadiene Rubber by Emulsion or Solution.                                                                                                
    a Includes mono- and di-ethers of ethylene glycol, diethylene glycol, and triethylene glycol R-(OCH2 CH2)n -OR' where:                                  
     n=1,2, or 3;                                                                                                                                           
     R=alkyl or aryl groups; and                                                                                                                            
     R'=R, H, or groups which, when removed, yield glycol ethers with the structure:                                                                        
     R-(OCH2 CH2)n-OH                                                                                                                                       
    
    
          Table 6.--Group 1 Batch Front-End Process Vents--Monitoring,      
                    Recordkeeping, and Reporting Requirements               
    ------------------------------------------------------------------------
                                                          Recordkeeping and 
                                     Parameter to be          reporting     
       Control/recovery device          monitored         requirements for  
                                                        monitored parameters
    ------------------------------------------------------------------------
    Thermal Incinerator.........  Firebox temperature   1. Continuous       
                                   a.                    records as         
                                                         specified in Sec.  
                                                         63.491(e)(1) b.    
                                                        2. Record and report
                                                         the average firebox
                                                         temperature        
                                                         measured during the
                                                         performance test-- 
                                                         NCS.c              
    
    [[Page 46982]]
    
                                                                            
                                                        3. Record the batch 
                                                         cycle daily average
                                                         firebox temperature
                                                         as specified in    
                                                         Sec.  63.491(e)(2).
                                                        4. Report all batch 
                                                         cycle daily average
                                                         temperatures that  
                                                         are below the      
                                                         minimum operating  
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         monitoring data are
                                                         not collected--    
                                                         PR.d,e             
    Catalytic Incinerator.......  Temperature upstream  1. Continuous       
                                   and downstream of     records as         
                                   the catalyst bed.     specified in Sec.  
                                                         63.491(e)(1).b     
                                                        2. Record and report
                                                         the average        
                                                         upstream and       
                                                         downstream         
                                                         temperatures and   
                                                         the average        
                                                         temperature        
                                                         difference across  
                                                         the catalyst bed   
                                                         measured during the
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Record the batch 
                                                         cycle daily average
                                                         upstream           
                                                         temperature and    
                                                         temperature        
                                                         difference across  
                                                         catalyst bed as    
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         upstream           
                                                         temperatures that  
                                                         are below the      
                                                         minimum upstream   
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit--PR.d,e     
                                                        5. Report all batch 
                                                         cycle daily average
                                                         temperature        
                                                         differences across 
                                                         the catalyst bed   
                                                         that are below the 
                                                         minimum difference 
                                                         established in the 
                                                         NCS or operating   
                                                         permit--PR.d,e     
                                                        6. Report all       
                                                         instances when     
                                                         monitoring data are
                                                         not collected.e    
    Boiler or Process Heater      Firebox temperature   1. Continuous       
     with a design heat input      a.                    records as         
     capacity less than 44                               specified in Sec.  
     megawatts and where the                             63.491(e)(1).b     
     batch front-end process                            2. Record and report
     vents or aggregate batch                            the average firebox
     vent streams are not                                temperature        
     introduced with or used as                          measured during the
     the primary fuel.                                   performance test-- 
                                                         NCS.c              
                                                        3. Record the batch 
                                                         cycle daily average
                                                         firebox temperature
                                                         as specified in    
                                                         Sec.  63.491(e)(2).
                                                         d                  
                                                        4. Report all batch 
                                                         cycle daily average
                                                         temperatures that  
                                                         are below the      
                                                         minimum operating  
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         monitoring data are
                                                         not collected--    
                                                         PR.d,e             
    Flare.......................  Presence of a flame   1. Hourly records of
                                   at the pilot light.   whether the monitor
                                                         was continuously   
                                                         operating during   
                                                         batch emission     
                                                         episodes selected  
                                                         for control and    
                                                         whether the pilot  
                                                         flame was          
                                                         continuously       
                                                         present during each
                                                         hour.              
                                                        2. Record and report
                                                         the presence of a  
                                                         flame at the pilot 
                                                         light over the full
                                                         period of the      
                                                         compliance         
                                                         determination--NCS.
                                                         c                  
                                                        3. Record the times 
                                                         and durations of   
                                                         all periods during 
                                                         batch emission     
                                                         episodes when a    
                                                         pilot flame is     
                                                         absent or the      
                                                         monitor is not     
                                                         operating.         
                                                        4. Report the times 
                                                         and durations of   
                                                         all periods during 
                                                         batch emission     
                                                         episodes selected  
                                                         for control when   
                                                         all pilot flames of
                                                         a flare are absent--
                                                         PR.d               
    
    [[Page 46983]]
    
                                                                            
    Scrubber for halogenated      pH of scrubber        1. Continuous       
     batch front-end process       effluent, and.        records as         
     vents or aggregate batch                            specified in Sec.  
     vent streams (Note:                                 63.491(e)(1).b     
     Controlled by a combustion                         2. Record and report
     device other than a flare).                         the average pH of  
                                                         the scrubber       
                                                         effluent measured  
                                                         during the         
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Record the batch 
                                                         cycle daily average
                                                         pH of the scrubber 
                                                         effluent as        
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         pH values of the   
                                                         scrubber effluent  
                                                         that are below the 
                                                         minimum operating  
                                                         pH established in  
                                                         the NCS or         
                                                         operating permit   
                                                         and all instances  
                                                         when insufficient  
                                                         monitoring data are
                                                         collected--PR.d e  
                                  Scrubber liquid flow  1. Continuous       
                                   rate.                 records as         
                                                         specified in Sec.  
                                                         63.491(e)(1).b     
                                                        2. Record and report
                                                         the scrubber liquid
                                                         flow rate measured 
                                                         during the         
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Record the batch 
                                                         cycle daily average
                                                         scrubber liquid    
                                                         flow rate as       
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         scrubber liquid    
                                                         flow rates that are
                                                         below the minimum  
                                                         flow rate          
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         insufficient       
                                                         monitoring data are
                                                         collected--PR.d e  
    Absorber g..................  Exit temperature of   1. Continuous       
                                   the absorbing         records as         
                                   liquid, and.          specified in Sec.  
                                                         63.491(e)(1).b     
                                                        2. Record and report
                                                         the average exit   
                                                         temperature of the 
                                                         absorbing liquid   
                                                         measured during the
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Record the batch 
                                                         cycle daily average
                                                         exit temperature of
                                                         the absorbing      
                                                         liquid as specified
                                                         in Sec.            
                                                         63.491(e)(2) for   
                                                         each batch cycle.  
                                                        4. Report all the   
                                                         batch cycle daily  
                                                         average exit       
                                                         temperatures of the
                                                         absorbing liquid   
                                                         that are below the 
                                                         minimum operating  
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         monitoring data are
                                                         not collected--PR.d
                                                         e                  
    Absorber f..................  Exit specific         1. Continuous       
                                   gravity for the       records as         
                                   absorbing liquid.     specified in Sec.  
                                                         63.491(e)(1).b     
                                                        2. Record and report
                                                         the average exit   
                                                         specific gravity   
                                                         measured during the
                                                         performance test-- 
                                                         NCS.               
                                                        3. Record the batch 
                                                         cycle daily average
                                                         exit specific      
                                                         gravity as         
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         exit specific      
                                                         gravity values that
                                                         are below the      
                                                         minimum operating  
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         monitoring data are
                                                         not collected--PR.d
                                                         e                  
    Condenser f.................  Exit (product side)   1. Continuous       
                                   temperature.          records as         
                                                         specified in Sec.  
                                                         63.491(e)(1).b     
                                                        2. Record and report
                                                         the average exit   
                                                         temperature        
                                                         measured during the
                                                         performance test-- 
                                                         NCS.               
                                                        3. Record the batch 
                                                         cycle daily average
                                                         exit temperature as
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         exit temperatures  
                                                         that are above the 
                                                         maximum operating  
                                                         temperature        
                                                         established in the 
                                                         NCS or operating   
                                                         permit and all     
                                                         instances when     
                                                         monitoring data are
                                                         not collected--    
                                                         PR.d,e             
    
    [[Page 46984]]
    
                                                                            
    Carbon Adsorber f...........  Total regeneration    1. Record of total  
                                   stream mass flow      regeneration stream
                                   during carbon bed     mass flow for each 
                                   regeneration          carbon bed         
                                   cycle(s), and.        regeneration cycle.
                                                        2. Record and report
                                                         the total          
                                                         regeneration stream
                                                         mass flow during   
                                                         each carbon bed    
                                                         regeneration cycle 
                                                         during the         
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Report all carbon
                                                         bed regeneration   
                                                         cycles when the    
                                                         total regeneration 
                                                         stream mass flow is
                                                         above the maximum  
                                                         mass flow rate     
                                                         established in the 
                                                         NCS or operating   
                                                         permit--PR.d e     
    Carbon Adsorber g...........  Temperature of the    1. Record the       
                                   carbon bed after      temperature of the 
                                   regeneration and      carbon bed after   
                                   within 15 minutes     each regeneration  
                                   of completing any     and within 15      
                                   cooling cycle(s).     minutes of         
                                                         completing any     
                                                         cooling cycle(s).  
                                                        2. Record and report
                                                         the temperature of 
                                                         the carbon bed     
                                                         after each         
                                                         regeneration and   
                                                         within 15 minutes  
                                                         of completing any  
                                                         cooling cycle(s)   
                                                         measured during the
                                                         performance test-- 
                                                         NCS.c              
                                                        3. Report all carbon
                                                         bed regeneration   
                                                         cycles when the    
                                                         temperature of the 
                                                         carbon bed after   
                                                         regeneration, or   
                                                         within 15 minutes  
                                                         of completing any  
                                                         cooling cycle(s),  
                                                         is above the       
                                                         maximum temperature
                                                         established in the 
                                                         NCS or operating   
                                                         permit--PR.d,e     
    All Control Devices.........  Presence of flow      1. Hourly records of
                                   diverted to the       whether the flow   
                                   atmosphere from the   indicator was      
                                   control device or.    operating during   
                                                         batch emission     
                                                         episodes selected  
                                                         for control and    
                                                         whether flow was   
                                                         detected at any    
                                                         time during the    
                                                         hour, as specified 
                                                         in Sec.            
                                                         63.491(e)(3).      
                                                        2. Record and report
                                                         the times and      
                                                         durations of all   
                                                         periods during     
                                                         batch emission     
                                                         episodes selected  
                                                         for control when   
                                                         emissions are      
                                                         diverted through a 
                                                         bypass line or the 
                                                         flow indicator is  
                                                         not operating--PD.d
    All Control Devices.........  Monthly inspections   1. Records that     
                                   of sealed valves.     monthly inspections
                                                         were performed as  
                                                         specified in Sec.  
                                                         63.491(e)(4)(i).   
                                                        2. Record and report
                                                         all monthly        
                                                         inspections that   
                                                         show the valves are
                                                         not closed or the  
                                                         seal has been      
                                                         changed--PR.d      
    Absorber, Condenser, and      Concentration level   1. Continuous       
     Carbon Adsorber (as an        or reading            records as         
     alternative to the above).    indicated by an       specified in Sec.  
                                   organic monitoring    63.491(e)(1).b     
                                   device at the        2. Record and report
                                   outlet of the         the average        
                                   recovery device.      concentration level
                                                         or reading measured
                                                         during the         
                                                         performance test-- 
                                                         NCS.               
                                                        3. Record the batch 
                                                         cycle daily average
                                                         concentration level
                                                         or reading as      
                                                         specified in Sec.  
                                                         63.491(e)(2).      
                                                        4. Report all batch 
                                                         cycle daily average
                                                         concentration      
                                                         levels or readings 
                                                         that are above the 
                                                         maximum            
                                                         concentration or   
                                                         reading established
                                                         in the NCS or      
                                                         operating permit   
                                                         and all instances  
                                                         when monitoring    
                                                         data are not       
                                                         collected--PR.d,e  
    ------------------------------------------------------------------------
    a Monitor may be installed in the firebox or in the ductwork immediately
      downstream of the firebox before any substantial heat exchange is     
      encountered.                                                          
    b ``Continuous records'' is defined in Sec.  63.111 of subpart G.       
    c NCS = Notification of Compliance Status described in Sec.             
      63.506(e)(5).                                                         
    d PR = Periodic Reports described in Sec.  63.506(e)(6) of this subpart.
                                                                            
    e The periodic reports shall include the duration of periods when       
      monitoring data are not collected as specified in Sec.                
      63.506(e)(6)(iii)(C) of this subpart.                                 
    f Alternatively, these devices may comply with the organic monitoring   
      device provisions listed at the end of this table.                    
    
    
     Table 7.--Operating Parameters for Which Monitoring Levels Are Required
     To Be Established for Continuous and Batch Front-End Process Vents and 
                          Aggregate Batch Vent Streams                      
    ------------------------------------------------------------------------
                                                             Established    
       Control/Recovery device      Parameters to be          operating     
                                        monitored           parameter(s)    
    ------------------------------------------------------------------------
    Thermal incinerator.........  Firebox temperature.  Minimum temperature.
    
    [[Page 46985]]
    
                                                                            
    Catalytic incinerator.......  Temperature upstream  Minimum upstream    
                                   and downstream of     temperature; and   
                                   the catalyst bed.     minimum temperature
                                                         difference across  
                                                         the catalyst bed.  
    Boiler or process heater....  Firebox temperature.  Minimum temperature.
    Scrubber for halogenated      Ph of scrubber        Minimum pH; and     
     vents.                        effluent; and         minimum flow rate. 
                                   scrubber liquid                          
                                   flow rate.                               
    Absorber....................  Exit temperature of   Minimum temperature;
                                   the absorbing         and minimum        
                                   liquid; and exit      specific gravity.  
                                   specific gravity of                      
                                   the absorbing                            
                                   liquid.                                  
    Condenser...................  Exit temperature....  Maximum temperature.
    Carbon absorber.............  Total regeneration    Maximum mass flow;  
                                   stream mass flow      and maximum        
                                   during carbon bed     temperature.       
                                   regeneration cycle;                      
                                   and temperature of                       
                                   the carbon bed                           
                                   after regeneration                       
                                   (and within 15                           
                                   minutes of                               
                                   completing any                           
                                   cooling cycle(s)).                       
    Other devices (or as an       HAP concentration     Maximum HAP         
     alternate to the above) a.    level or reading at   concentration or   
                                   outlet of device.     reading.           
    ------------------------------------------------------------------------
    a Concentration is measured instead of an operating parameter.          
    
    
     Table 8.--Summary of Compliance Alternative Requirements for the Back- 
                             End Process Provisions                         
    ------------------------------------------------------------------------
                                     Parameter to be                        
       Compliance alternative           monitored           Requirements    
    ------------------------------------------------------------------------
    Compliance Using Stripping    Residual organic HAP  (1) If batch        
     Technology, Demonstrated      content in each       stripping is used, 
     through Periodic Sampling     sample of crumb or    at least one       
     [Sec.  63.495(b)].            latex.                representative     
                                                         sample is to be    
                                                         taken from every   
                                                         batch.             
                                                        (2) If continuous   
                                                         stripping is used, 
                                                         at least one       
                                                         representative     
                                                         sample is to be    
                                                         taken each         
                                                         operating day.     
                                  Quantity of Material  (1) Acceptable      
                                   (weight of latex or   methods of         
                                   dry crumb rubber)     determining this   
                                   represented by each   quantity are       
                                   sample.               production records,
                                                         measurement of     
                                                         stream             
                                                         characteristics,   
                                                         and engineering    
                                                         calculations.      
    Compliance Using Stripping    At a minimum,         (1) Establish       
     Technology, Demonstrated      temperature,          stripper operating 
     through Stripper Parameter    pressure, steaming    parameter levels   
     Monitoring [Sec.              rates (for steam      for each grade in  
     63.495(c)].                   strippers), and       accordance with    
                                   some parameter that   Sec.  63.505(e).   
                                   is indicative of     (2) Continuously    
                                   residence time..      monitor stripper   
                                                         operating          
                                                         parameters.        
                                                        (3) If hourly       
                                                         average parameters 
                                                         are outside of the 
                                                         established        
                                                         operating parameter
                                                         levels, a crumb or 
                                                         latex sample shall 
                                                         be taken in        
                                                         accordance with    
                                                         Sec.  63.495(c)(3)(
                                                         ii).               
    Determining Compliance Using  Parameters to be      Comply with         
     Control or Recovery Devices   monitored are         requirements listed
     [Sec.  63.496].               described in Table    in Table 3 of      
                                   3 of subpart G..      subpart G, except  
                                                         for the            
                                                         requirements for   
                                                         halogenated vent   
                                                         stream scrubbers.  
    ------------------------------------------------------------------------
    
    [FR Doc. 96-21941 Filed 9-4-96; 8:45 am]
    BILLING CODE 6560-50-P
    
    
    

Document Information

Published:
09/05/1996
Department:
Environmental Protection Agency
Entry Type:
Rule
Action:
Final rule.
Document Number:
96-21941
Dates:
September 5, 1996. See the Supplementary Information section concerning judicial review.
Pages:
46906-46985 (80 pages)
Docket Numbers:
AD-FRL-5543-1
RINs:
2060-AE37: NESHAP: Polymers and Resins, Group IV
RIN Links:
https://www.federalregister.gov/regulations/2060-AE37/neshap-polymers-and-resins-group-iv
PDF File:
96-21941.pdf
CFR: (280)
40 CFR 63.487(a)(1)
40 CFR 63.488(a)(2)
40 CFR 63.488(a)(1)
40 CFR 63.487(a)
40 CFR 63.487(a)(2)
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