i. The attached applicability determination has been pending for almost 2 years.
The regulation should be clear in how to calculate an emission increase at a flare
making this type of applicability determination un-necessary. The commenter
requests a response to the applicability determination in the promulgated BID.
This comment applies to J and Ja.
ii. In addition, it should be clear that adding a new line to the flare does not
increase the capacity of the flare and should not trigger Subpart J or Ja
iii. Since most streams routed to the flare occur during SSM events, it should be
clear how these SSM events trigger a modification, i.e. do you include these
emissions in the baseline emissions prior to the modification. This comment
applies to J and Ja.
iv. This comment applies to J and Ja. The affected facility should be well
defined. Is a knockout drum and flare gas compressor part of the affected
facility? It doesn't make sense for replacing a knockout drum to trigger NSPS on
a flare. Is the pilot gas system part of the affected facility.
v. It should be clear that flare tip replacements are considered routine
maintenance and repair and should be exempt from triggering a modification for J
and/or Ja. This should be true even if the flare tip is replaced with a flare tip of a
different geometry (potentially larger diameter) to reduce noise.
vi. There is an exemption for triggering a modification for an increase in production
rate of an existing facility, if that increase can be accomplished without a capital
expenditure on that facility? Does this exemption apply to flares? What is the
production rate for a flare, is it flare flow?
vii. Are turbines, cogens, welding machines, and IC engines fuel gas combustion
devices?
viii. The 50 ppm FCCU SO2 emission standard should be an option for Subpart J
even if there is no control device.
Comment submitted by B. Lane
This is comment on Notice
Standards of Performance for Petroleum Refineries
View Comment
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