Federal Implementation Plan for the Billings/Laurel, MT, Sulfur Dioxide Area, 21418-21465 [E8-7868]
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Federal Register / Vol. 73, No. 77 / Monday, April 21, 2008 / Rules and Regulations
[EPA–R08–OAR–2006–0098; FRL–8551–2]
Program, Environmental Protection
Agency (EPA), Region 8, 1595 Wynkoop
Street, Denver, Colorado 80202–1129,
(303) 312–6437, ostrand.laurie@epa.gov.
SUPPLEMENTARY INFORMATION:
RIN 2008–AA01
Table of Contents
ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Part 52
Federal Implementation Plan for the
Billings/Laurel, MT, Sulfur Dioxide
Area
Environmental Protection
Agency (EPA).
ACTION: Final rule.
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AGENCY:
SUMMARY: The Environmental Protection
Agency (EPA) is promulgating a Federal
Implementation Plan (FIP) containing
emission limits and compliance
determining methods for several sources
located in Billings and Laurel, Montana.
EPA is promulgating a FIP because of
our previous partial and limited
disapprovals of the Billings/Laurel
Sulfur Dioxide (SO2) State
Implementation Plan (SIP). The
intended effect of this action is to assure
attainment of the SO2 National Ambient
Air Quality Standards (NAAQS) in the
Billings/Laurel, Montana area. EPA is
taking this action under sections 110,
301, and 307 of the Clean Air Act (Act).
DATES: Effective Date: This final rule is
effective May 21, 2008. The
incorporation by reference of certain
publications listed in this regulation is
approved by the Director of the Federal
Register as of May 21, 2008.
ADDRESSES: EPA has established a
docket for this action under Docket ID
No. EPA–R08–OAR–2006–0098. All
documents in the docket are listed on
the https://www.regulations.gov Web
site. Although listed in the index, some
information is not publicly available,
e.g., Confidential Business Information
(CBI) or other information whose
disclosure is restricted by statute.
Certain other material, such as
copyrighted material, is not placed on
the Internet and will be publicly
available only in hard copy form.
Publicly available docket materials are
available either electronically through
https://www.regulations.gov or in hard
copy at the Air and Radiation Program,
Environmental Protection Agency
(EPA), Region 8, 1595 Wynkoop Street,
Denver, Colorado 80202–1129. EPA
requests that if at all possible, you
contact the individual listed in the FOR
FURTHER INFORMATION CONTACT section to
view the hard copy of the docket. You
may view the hard copy of the docket
Monday through Friday, 8 a.m. to 4
p.m., excluding Federal holidays.
FOR FURTHER INFORMATION CONTACT:
Laurie Ostrand, Air and Radiation
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Definitions
I. Background of the Final Rules
II. Issues Raised by Commenters and EPA’s
Response
A. FIP Not Necessary
B. EPA Exceeded Its Authority in
Proposing a FIP
C. Flare Monitoring
D. Flare Limits
E. Concerns With Dispersion Modeling
F. Miscellaneous Comments
G. MSCC Specific Issues
H. ConocoPhillips Specific Issues
I. ExxonMobil Specific Issues
J. CHS Inc. Specific Issues
III. Summary of the Final Rules and Changes
From the July 12, 2006, Proposal
A. Flare Requirements Applicable to All
Sources
B. CHS Inc.
C. ConocoPhillips
D. ExxonMobil
E. Montana Sulphur & Chemical Company
(MSCC)
F. Modeling to Support Emission Limits
IV. Statutory and Executive Order Reviews
A. Executive Order 12866, Regulatory
Planning Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132, Federalism
F. Executive Order 13175, Coordination
With Indian Tribal Governments
G. Executive Order 13045, Protection of
Children From Environmental Health
Risks and Safety Risks
H. Executive Order 13211, Actions That
Significantly Affect Energy Supply,
Distribution, or Use
I. National Technology Transfer and
Advancement Act
J. Executive Order 12898: Federal Actions
To Address Environmental Justice in
Minority Populations and Low-Income
Populations
K. Congressional Review Act
L. Petitions for Judicial Review
Definitions
For the purpose of this document, we
are giving meaning to certain words or
initials as follows:
(i) The words or initials Act or CAA
mean or refer to the Clean Air Act,
unless the context indicates otherwise.
(ii) The initials API mean or refer to
the American Petroleum Institute.
(iii) The initials BAAQMD mean or
refer to the Bay Area Air Quality
Management District.
(iv) The initials CEMS mean or refer
to continuous emission monitoring
system.
(v) The initials CO mean or refer to
carbon monoxide.
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(vi) The initials COPC mean or refer
to ConocoPhillips.
(vii) The words EPA, we, us or our
mean or refer to the United States
Environmental Protection Agency.
(viii) The initials FIP mean or refer to
Federal Implementation Plan.
(ix) The initials H2S mean or refer to
hydrogen sulfide.
(x) The initials MBER mean or refer to
the Montana Board of Environmental
Review.
(xi) The initials MDEQ mean or refer
to the Montana Department of
Environmental Quality.
(xii) The initials MPA mean or refer to
the Montana Petroleum Association.
(xiii) The initials MSCC mean or refer
to the Montana Sulphur & Chemical
Company.
(xiv) The initials NAAQS mean or
refer to National Ambient Air Quality
Standards
(xv) The initials NEDA/CAP mean or
refer to the National Environmental
Development Association’s Clean Air
Project.
(xvi) The initials NPRA mean or refer
to the National Petrochemical & Refiners
Association.
(xvii) The initials SCAQMD mean or
refer to the South Coast Air Quality
Management District.
(xviii) The initials SIP mean or refer
to State Implementation Plan.
(xix) The initials SO2 mean or refer to
sulfur dioxide.
(xx) The words State or Montana
mean the State of Montana, unless the
context indicates otherwise.
(xxi) The initials SRU mean or refer
to sulfur recovery unit.
(xxii) The initials SWS mean or refer
to sour water stripper.
(xxiii) The initials WETA mean or
refer to the Western Environmental
Trade Association.
(xxiv) The initials WSPA mean or
refer to the Western States Petroleum
Association.
(xxv) The initials YCC mean or refer
to the Yellowstone County
Commissioners.
(xxvi) The initials YVAS mean or
refer to the Yellowstone Valley
Audubon Society.
I. Background of the Final Rules
The Clean Air Act (Act) requires EPA
to establish national ambient air quality
standards (NAAQS) that protect public
health and welfare. NAAQS have been
established for SO2 as follows: 0.030
parts per million (ppm) annual
standard, not to be exceeded in a
calendar year; 0.14 ppm 24-hour
standard, not to be exceeded more than
once per calendar year; and 0.5 ppm 3hour standard, not to be exceeded more
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than once per calendar year. See 40 CFR
50.4 and 50.5. The Act also requires
states to prepare and gain EPA approval
of a plan, termed a State
Implementation Plan (SIP), to assure
that the NAAQS are attained and
maintained.
Dispersion modeling completed in
1991 and 1993 for the Billings/Laurel
area of Montana predicted that the SO2
NAAQS were not being attained. As a
result, in March 1993 EPA (pursuant to
sections 110(a)(2)(H) and 110(k)(5) of
the Act, 42 U.S.C. 7410(a)(2)(H) and
7410(k)(5)) requested the State of
Montana to revise its previously
approved SO2 SIP for the Billings/Laurel
area. See 58 FR 41450, August 4, 1993.
In response, the State submitted
revisions to the SO2 SIP on September
6, 1995, August 27, 1996, April 2, 1997,
July 29, 1998, and May 4, 2000.
On May 2, 2002 (67 FR 22168) and
May 22, 2003 (68 FR 27908), we
partially approved, partially
disapproved, limitedly approved, and
limitedly disapproved the Billings/
Laurel SO2 SIP. In those actions we
disapproved the following:
• The attainment demonstration due
to issues with various emission limits,
inappropriate stack height credit, and
lack of emission limits on flares.
• The emission limits for Montana
Sulphur & Chemical Company’s
(MSCC’s) sulfur recovery unit (SRU)
100-meter stack and the stack height
credit on which those limits were based.
• The emission limits for MSCC’s
auxiliary vent stacks due to lack of an
adequate limit on fuel burned in the
associated heaters and boilers and lack
of a reliable compliance determining
method.
• The emission limits for MSCC’s 30meter stack due to lack of an adequate
limit on fuel burned in the associated
heaters and boilers, and lack of a
reliable compliance determining
method.
• Provisions that allowed sour water
stripper overheads to be burned in the
flares at CHS Inc. and ExxonMobil.
• ExxonMobil’s refinery fuel gas
combustion device emission limits and
associated compliance determining
methods.
• ExxonMobil’s Coker CO Boiler stack
emission limits and associated
compliance determining methods.
• CHS Inc.’s combustion source
emission limits and certain associated
compliance determining methods.
On June 10, 2002, MSCC petitioned
the United States Court of Appeals for
the Ninth Circuit for review of EPA’s
May 2, 2002, final SIP action.
Subsequently, MSCC and EPA agreed to
a stay of the litigation pending EPA’s
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final action on this FIP. The case is
captioned Montana Sulphur & Chemical
Company v. United States
Environmental Protection Agency, No.
02–71657. No petitions for judicial
review were filed regarding EPA’s May
22, 2003, SIP action.
On July 12, 2006 (71 FR 39259), EPA
proposed Federal Implementation Plan
(FIP) provisions for the Billings/Laurel,
Montana area because of our
disapproval of portions of Montana’s
Billings/Laurel SO2 SIP. In our proposal,
we indicated that our FIP would not
replace the SIP entirely, but instead
would only replace elements of, or fill
gaps in, the SIP.
In promulgating today’s rules, EPA is
fulfilling its mandatory duty under
section 110(c) of the Act. Under section
110(c), whenever we disapprove a SIP,
in whole or in part, we are required to
promulgate a FIP. Specifically, section
110(c) provides:
‘‘(1) The Administrator shall promulgate a
Federal implementation plan at any time
within 2 years after the Administrator—
(A) Finds that a State has failed to make
a required submission or finds that the plan
or plan revision submitted by the State does
not satisfy the minimum criteria established
under [section 110(k)(1)(A)],1 or
(B) Disapproves a State implementation
plan submission in whole or in part, unless
the State corrects the deficiency, and the
Administrator approves the plan or plan
revision, before the Administrator
promulgates such Federal implementation
plan.’’
Thus, because we disapproved
portions of the Billings/Laurel SO2 SIP,
and the attainment demonstration, we
are required to promulgate a FIP.
Section 302(y) defines the term
‘‘Federal implementation plan’’ in
pertinent part, as:
‘‘[A] plan (or portion thereof) promulgated
by the Administrator to fill all or a portion
of a gap or otherwise correct all or a portion
of an inadequacy in a State implementation
plan, and which includes enforceable
emission limitations or other control
measures, means or techniques (including
economic incentives, such as marketable
permits or auctions or emissions allowances)
* * *.’’
More simply, a FIP is ‘‘a set of
enforceable federal regulations that
stand in the place of deficient portions
of a SIP.’’ McCarthy v. Thomas, 27 F.3d
1363, 1365 (9th Cir. 1994). As the Court
of Appeals for the D.C. Circuit noted in
a 1995 case, FIPs are powerful tools to
remedy deficient state action:
1 Section 110(k)(1) requires the Administrator to
promulgate minimum criteria that any plan
submission must meet before EPA is required to act
on the submission. These completeness criteria are
set forth at 40 CFR 51, Appendix V.
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The FIP provides an additional incentive
for state compliance because it rescinds state
authority to make the many sensitive
technical and political choices that a
pollution control regime demands. The FIP
provision also ensures that progress toward
NAAQS attainment will proceed
notwithstanding inadequate action at the
state level.
Natural Resources Defense Council,
Inc. v. Browner, 57 F.3d 1122, 1124
(D.C. Cir. 1995).
When EPA promulgates a FIP, courts
have not required EPA to demonstrate
explicit authority for specific measures:
‘‘We are inclined to construe Congress’
broad grant of power to the EPA as
including all enforcement devices
reasonably necessary to the achievement
and maintenance of the goals
established by the legislation.’’ South
Terminal Corp. v. EPA, 504 F.2d 646,
669 (1st Cir. 1974). As the Ninth Circuit
stated in a case involving a FIP with farreaching consequences in Los Angeles:
‘‘The authority to regulate pollution
carries with it the power to do so in a
manner reasonably calculated to reach
that end.’’ City of Santa Rosa v. EPA,
534 F.2d 150, 155 (9th Cir. 1976),
vacated and remanded on other grounds
sub nom. Pacific Legal Foundation v.
EPA, 429 U.S. 990 (1976).
In addition to giving EPA remedial
authority, section 110(c) enables EPA to
assume the powers that the state would
have to protect air quality, when the
state fails to adequately discharge its
planning responsibility. As the Ninth
Circuit held, when EPA acts to fill in the
gaps in an inadequate state plan under
section 110(c), EPA ‘‘ ‘stands in the
shoes of the defaulting State, and all of
the rights and duties that would
otherwise fall to the State accrue instead
to EPA.’ ’’ Central Arizona Water
Conservation District v. EPA, 990 F.2d
1531, 1541 (9th Cir. 1993). As the First
Circuit held in an early case:
‘‘[T]he Administrator must promulgate
promptly regulations setting forth ‘an
implementation plan for a State’ should the
state itself fail to propose a satisfactory one
* * * The statutory scheme would be
unworkable were it read as giving to EPA,
when promulgating an implementation plan
for a state, less than those necessary
measures allowed by Congress to a state to
accomplish federal clean air goals. We do not
adopt any such crippling interpretation.’’
South Terminal Corp. v. EPA, supra,
at 668 (citing previous version of section
110(c)).
The Billings/Laurel SO2 FIP
establishes emission limits and
compliance determining methods for
four sources located in Billings/Laurel,
Montana, to replace/fill gaps in portions
of the SIP we disapproved, and to
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support our attainment demonstration.
Three of the sources are petroleum
refineries: CHS Inc., ConocoPhillips
(including the Jupiter Sulfur facility),
and ExxonMobil. The fourth source is
Montana Sulphur & Chemical Company,
which provides sulfur recovery for the
ExxonMobil refinery.
The following is a summary of the
major components of our FIP rule:
(1) The FIP establishes flare emission
limits at all four sources (150 lbs SO2/
3-hour period at all but the Jupiter
Sulfur flare, 75 lbs SO2/3-hour period
shared limit for the Jupiter Sulfur flare
and the Jupiter Sulfur SRU/ATS stack)
and monitoring methods to determine
compliance with those limits. The FIP
includes an affirmative defense to
penalties for violations of the flare
limits that occur during malfunction,
startup, and shutdown periods. To
determine flare emissions, the FIP
requires concentration monitoring
(which can consist of continuous
monitoring, grab sampling, or integrated
sampling) and continuous flow
monitoring.
(2) The FIP prohibits the burning of
sour water stripper overheads in CHS
Inc.’s main crude heater and requires
CHS Inc. to keep the valve between the
old sour water stripper and the main
crude heater closed, chained, and
locked.
(3) The FIP provides that emission
limits for identified ExxonMobil
refinery fuel gas combustion units are
contained in the SIP, and establishes
compliance determining methods for
instances in which the H2S
concentration in the refinery fuel gas
stream exceeds 1200 ppmv. These
methods involve the use of length-ofstain detector tubes on a once-per-hour
frequency.
(4) The FIP provides that emission
limits for ExxonMobil’s Coker CO Boiler
stack, when ExxonMobil’s Coker unit is
operating and Coker unit flue gases are
burned in the Coker CO Boiler, are
contained in the SIP. The FIP
establishes compliance determining
methods for these emission limits that
require measurement of the SO2
concentration and flow rate in the Coker
CO Boiler stack using CEMS.
(5) The FIP establishes emission
limits on MSCC’s SRU 100-meter stack,
based on good engineering practice
(GEP) stack height credit of 65 meters,
with compliance with these limits to be
determined using methods already
approved in the SIP. The FIP does not
provide variable emission limits for this
stack.
(6) The FIP establishes emission
limits and compliance determining
methods for MSCC’s auxiliary vent
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stacks and SRU 30-meter stack. In
addition to mass limits, the FIP
establishes concentration limits on fuel
burned in the units that vent to the
auxiliary vent stacks and SRU 30-meter
stack. These concentration limits are
160 ppm H2S per 3-hour period and 100
ppm H2S per calendar day. When trigger
events specified in the rule occur,
MSCC must measure the H2S
concentration in the fuel using lengthof-stain detector tubes on a once-per-3hour period.
(7) The FIP establishes various
recordkeeping and reporting
requirements.
It is important to note that, in cases
where the provisions of the FIP address
emissions activities differently or
establish different requirements than
provisions of the SIP, the provisions of
the FIP take precedence. We also
caution that if any of the four sources
are subject to requirements under other
provisions of the Act (e.g., section 111
or 112, part C of title I, or SIP-approved
permit programs under part A of title I),
our promulgation of the FIP does not
excuse any of the sources from meeting
such requirements. Finally, our
promulgation of the FIP does not imply
any sort of applicability determination
under other provisions of the Act (e.g.,
section 111 or 112, part C of title I, or
SIP-approved permit programs under
part A of title I).
II. Issues Raised by Commenters and
EPA’s Response
A. FIP Not Necessary
1. Ambient Data and Historical
Modeling Show Attainment
(a) Comment (CHS Inc., COPC,
ExxonMobil, NPRA, MPA, MDEQ,
MSCC, WETA): The FIP is not necessary
for attainment of the NAAQS because
ambient data show that the Billings/
Laurel area has been for many years and
continues to be in attainment with both
the Federal and State SO2 ambient air
quality standards for all averaging
periods.
Response: EPA does not agree that a
FIP is not necessary because ambient
data show attainment of the SO2
NAAQS. Ambient monitoring is limited
in time and in space. Ambient
monitoring can measure pollutant
concentrations only as they occur; it
cannot predict future concentrations
when emission levels and
meteorological conditions may differ
from present conditions.
EPA has long held that ambient
monitoring data alone generally are not
adequate for SO2 attainment
demonstrations. Additionally, a small
number of ambient SO2 monitors
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usually are not representative of the air
quality for an area. (See reference
document GGGGG, April 21, 1983,
memorandum from Sheldon Meyers,
Director, Office of Air Quality Planning
and Standards (OAQPS), to Regional Air
and Waste Division Directors, titled
‘‘Section 107 Designation Policy
Summary,’’ and reference document
HHHHH, September 4, 1992,
memorandum from John Calcagni,
Director, Air Quality Management
Division, OAQPS, to Regional Air
Division Directors, titled ‘‘Procedures
for Processing Requests to Redesignate
Areas to Attainment.’’)
Typically, modeling estimates of
maximum ambient concentrations are
based on a fairly infrequent combination
of meteorological and source operating
conditions. To capture such results on
an ambient monitor would normally
require a prohibitively large and
expensive network. Therefore,
dispersion modeling is generally
necessary to comprehensively evaluate
sources’ impacts and to determine the
areas of expected high concentrations.
(Id.) Air quality modeling results would
be especially important if sources were
not emitting at their maximum level
during the monitoring period or if the
monitoring period did not coincide with
potentially worst-case meteorological
conditions. Further, ambient monitoring
data are not adequate if sources are
using stacks with actual heights greater
than good engineering practice stack
height (which indeed is the case with
MSCC and ConocoPhillips) or other
dispersion techniques for which SIP/FIP
modeling credit is not allowed. (See also
our discussion of related issues in our
final action on the Billings/Laurel SO2
SIP (67 FR 22168, 22185–22187, May 2,
2002.))
Ambient monitoring data and air
quality modeling data for a particular
area can sometimes appear to conflict.
This is primarily due to the fact that
modeling results may predict maximum
SO2 concentration at receptors where no
monitors are located.
Moreover, our SIP Call for the
Billings/Laurel area was based on
modeled violations of the SO2 NAAQS,
not monitored violations. (See reference
documents Y and Z.) We took final
action on the SIP Call in our May 2,
2002, action on the Billings/Laurel SIP
(67 FR 22168, 22173), and we are not
revisiting it in this FIP action. It would
be inconsistent and inappropriate to
now rely solely on monitoring to
determine necessary measures and
demonstrate attainment.
It is especially important to recognize
that, as a result of our partial and
limited disapproval of the Billings/
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Laurel SO2 SIP, we are legally obligated
to promulgate a FIP for the area. See
section 110(c)(1) of the CAA, 42 U.S.C.
7410(c)(1). However, the SIP
deficiencies that triggered our partial
and limited disapproval were varied
and were not necessarily associated
with problems that could be measured
at an ambient monitor. For example, one
basis for disapproval of the SIP was the
State’s use of improper (too tall) stack
height credit for MSCC in modeling
attainment of the NAAQS. In the real
world, emissions at the actual (100
meter) height of the stack create less
impact on monitored ambient
concentrations in the Billings/Laurel
area than if the emissions were emitted
from a lower stack. Nonetheless, we had
to partially disapprove the SIP due to
the State’s inappropriate grant of stack
height credit, and section 110(c) of the
CAA requires that we correct the
deficiency. Since the State did not
model attainment at the proper stack
height credit for MSCC’s stack, it was
necessary that we do so and set
emission limits for the stack consistent
with our attainment demonstration. We
believe MSCC has consistently been
meeting the emission limits we are
adopting, so there may be no reduction
in actual emissions from the stack, but
that does not mean the CAA allows us
to forego this aspect of the FIP.
Likewise, CAA sections 110(a)(2)(A)
and (C) require that SIP control
measures be enforceable. We
disapproved several source monitoring
methods because they were not
adequate to determine compliance
under all operating conditions. It may
be impossible to measure the impact
these SIP deficiencies may have on
ambient SO2 concentrations in the area,
but the CAA still requires that we
correct the deficiencies. Regarding the
emission limits and compliance
determining methods for the flares, the
State-only flare limits, which the State
relied on to demonstrate attainment,
may have positively impacted flare
emissions in the past few years.
However, the State did not include the
State-only flare limits or adequate
compliance determining methods in the
SIP. Thus, the SIP remains deficient. We
now have the responsibility to ensure
that emission limits relied on to
demonstrate attainment are included in
the SIP and are practically enforceable,
consistent with the requirements of
section 110 of the Act.
(b) Comment (MSCC, MDEQ): The
State’s SIP modeling, along with
appropriate emission limits, show
attainment of the NAAQS.
Response: EPA addressed this issue in
its actions on Montana’s SIP
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submissions. As explained in those
actions, EPA does not agree that the
State’s SIP modeling, along with
appropriate emission limits, show
attainment of the NAAQS. EPA’s formal
determinations regarding the attainment
demonstration and emission limits were
made in final actions on May 2, 2002
(67 FR 22168) and May 22, 2003 (68 FR
27908). The FIP fills the gaps for the
provisions we disapproved.
We note that we have not reopened
our SIP actions as part of this action.
Thus, to the extent the commenters are
expressing their disagreement with
EPA’s actions on the SIP, their
comments are not relevant to this
action, and EPA is not re-considering
them here.
(c) Comment (ExxonMobil): EPA’s
proposed FIP ignores the substantial
improvement in air quality in the
Billings/Laurel area and instead predicts
exceedances of NAAQS based upon
modeling performed as long as 15 years
ago. EPA’s FIP proposal must be further
examined in light of subsequent
developments, including correct
modeling and consideration of currently
available information indicating
compliance.
Response: See response to comment
II.A.1.(a), above, regarding ambient data
and response to comments in section
II.E., below, regarding modeling.
2. Existing Controls Sufficient
(a) Comment (MDEQ, MSCC, COPC,
ExxonMobil, MPA, NPRA, WETA): The
FIP offers questionable improvements
because the existing control plan
provisions submitted by the state are
adequate and contain sufficient SO2
emission controls and strategies and
provide for the implementation,
maintenance, and enforcement of the
SO2 NAAQS.
Response: EPA addressed the
adequacy of Montana’s SIP submissions
in its final actions on the SIP. As
explained in those actions, EPA does
not agree that the State’s SIP control
plan provisions are adequate and
contain sufficient SO2 emission controls
to show attainment of the NAAQS.
EPA’s formal determinations regarding
the attainment demonstration and
emission control plan were made in
final actions on May 2, 2002 (67 FR
22168) and May 22, 2003 (68 FR 27908).
In our May 2002 and May 2003 actions
we disapproved various control plan
provisions. The FIP fills the gaps for the
provisions we disapproved. The FIP
offers necessary improvements to the
SIP by imposing new emission limits
and reliable compliance determining
methods to ensure attainment of the SO2
NAAQS.
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We note that we have not reopened
our SIP actions as part of this action.
Thus, to the extent the commenters are
expressing their disagreement with
EPA’s actions on the SIP, their
comments are not relevant to this
action, and EPA is not re-considering
them here.
(b) Comment (CHS Inc., WETA,
COPC, MDEQ, ExxonMobil, NPRA): In
addition to the SIP, SO2 emissions in
the Billings/Laurel area have decreased
as a result of Consent Decrees and
Montana Air Quality Permit changes.
These limits are all federally enforceable
because there are Title V operating
permit conditions (CHS Inc.). EPA did
not consider these emission reductions
in making its determination that the FIP
was necessary. The FIP proposal does
not otherwise acknowledge the practical
effects of the recent consent decrees
between the primary refinery parties
subject to regulation as well as other
permitting actions that have occurred
over the past eight years (MSCC, COPC).
Response: EPA did not consider the
emission reductions that resulted, or
will result, from the consent decrees
and/or State permit revisions to
determine that the FIP was necessary or
include the emission reductions in our
modeling for several reasons.
First, the FIP is required because we
disapproved the SIP, and the State has
not made revisions to the SIP to address
the SIP’s flaws. As noted in other
responses, because we disapproved the
SIP, we have a legal obligation to
promulgate a FIP. See CAA section
110(c), 42 U.S.C. 7410(c).
Second, even though permits and
consent decrees are federally
enforceable, some permits can be
revised without EPA approval and
consent decrees have a limited
lifespan.2 To protect the integrity of the
attainment demonstration, and our
statutory role in assessing SIP/FIP
adequacy, we believe that stationary
source emission limits necessary to
demonstrate attainment must be
included in the FIP (or approved SIP).
See, e.g., CAA sections 110(a)(2)(A),
110(i), 110(k)(3)–(6), and 110(l), 42
U.S.C. 7410(a)(2)(A), (i), (k)(3)–(6), and
(l). This ensures that changes to those
limits will only be made with EPA’s
approval as a SIP or FIP revision,
2 The State can revise construction permits
without EPA approval, and, while EPA has
authority to object to Title V permits, that authority
is only available to ensure that underlying
applicable requirements are included in the Title V
permits. Thus, if those underlying requirements
change, EPA may have no recourse at the Title V
stage.
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following notice and comment
rulemaking.
Third, the consent decrees and
permitting actions, for some emission
points, do not contain SO2 emission
limits that are consistent with the
averaging times of the SO2 NAAQS,
specifically, the 3-hour and calendar
day averaging periods. For example, the
SIP establishes 3-hour, calendar day,
and calendar year emission limits for
CHS Inc.’s FCC regenerator/CO boiler
stack. The January 17, 2007, final State
construction permit (reference
document IIIII) and the consent decree
(reference document JJJJJ) indicate that
the FCC regenerator stack SO2 emissions
shall not exceed 50 ppm by volume
(corrected to 0% O2) for a 7-day rolling
average [or a fresh feed of 0.3 percent by
weight] and 25 ppm by volume
(corrected to 0% O2) for a 365-day
rolling average. None of the commenters
has suggested these limits be converted
to FIP mass limits that would apply over
a 3-hour averaging period, and the State
has not submitted a SIP revision with
such limits.
It should be noted that EPA did solicit
comment on whether we should limit
the main flares to 500 pounds of SO2 per
calendar day. This value is consistent
with the trigger point for certain
analyses contained in settlements (i.e.,
consent decrees) between the United
States and CHS Inc., ConocoPhillips,
and ExxonMobil. We received limited
comments on this proposal and have
decided to keep the limit at 150 pounds
of SO2 per 3-hour period to maintain
consistency with the State’s State-only
limit.
jlentini on PROD1PC65 with RULES2
B. EPA Exceeded Its Authority in
Proposing a FIP
1. State’s Responsibility
(a) Comment (WETA, MPA,
ExxonMobil): EPA’s role is limited to
determining whether or not a SIP is
attaining and maintaining the NAAQS.
Selecting the source mix and various
control measures to achieve these ends
has been determined by courts to be the
sole responsibility of the state. EPA’s
proposed action intrudes on the primary
responsibility of the state and local
governments to implement the Clean
Air Act (MSCC).
Response: The commenters’
characterization of EPA’s role regarding
SIPs is not accurate. We lack authority
to question a state’s choices of
emissions limitations if they are part of
a plan that satisfies the standards of the
Clean Air Act. Train v. Natural
Resources Defense Council, 95 S.Ct.
1470, 1481–1482 (1975). In our 2002
and 2003 actions, we found that
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Montana’s SO2 SIP for Billings/Laurel
did not fully satisfy CAA requirements.
See 67 FR 22168, May 2, 2002 and 68
FR 27908, May 22, 2003. Thus, pursuant
to section 110(c) of the CAA, 42 U.S.C.
7410(c), we are required to promulgate
a FIP. In doing so, we stand in the state’s
shoes and have authority to determine
emissions limitations and other
measures for specific sources to fill gaps
in the SIP. Central Arizona Water
Conservation District v. EPA, 990 F.2d
1531, 1541 (9th Cir. 1993); South
Terminal Corp. v. EPA, 504 F.2d 646,
668 (1st Cir. 1974) (citing previous
version of CAA section 110(c)).
We note that we have not reopened
our SIP actions as part of this action.
Thus, to the extent the commenters are
expressing their disagreement with
EPA’s actions on the SIP, their
comments are not relevant to this
action, and EPA is not re-considering
them here.
(b) Comment (WETA): Since the State
of Montana has already taken
appropriate actions to reduce sulfur
dioxide emissions, EPA does not have
the authority under the CAA to adopt
the proposed FIP.
Response: See response to comment
II.B.1.(a), above. The adequacy of the
State of Montana’s actions has already
been considered by EPA in other
rulemaking actions that addressed the
State’s SIP submission. Those actions
are not the subject of EPA’s present
rulemaking, which promulgates the
necessary measures to remedy the
deficiencies EPA identified in its prior
SIP reviews.
(c) Comment (MSCC): States have
primacy, and because EPA did not
choose to exercise its rights in the
comprehensive and competent state
decision process, EPA may not default
and then act.
Response: Under section 110(c) of the
Act, EPA is not required to participate
in a state’s administrative process before
promulgating a FIP.
(d) Comment (MSCC, MDEQ,
ExxonMobil): EPA has no authority to
question the wisdom of a state’s choices
of emission limitations if they are part
of a plan that satisfies the standards of
§ 110(a)(2) of the Act. As long as the
ultimate effect of a state’s choice of
emission limitations is compliance with
the NAAQS, the state is at liberty to
adopt whatever mix of emission
limitations it deems best suited to its
particular situation. There is no
evidence provided by EPA that Montana
reached its material conclusions or
choices in the SIP unreasonably.
Additionally, EPA has not shown that
additional controls beyond the SIP
measures adopted by Montana are
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necessary to meet or assure SO2 NAAQS
compliance.
Response: See our responses to
comments II.A.1.(a) and II.B.1.(a), above.
Much of this comment pertains to our
actions on Montana’s SIP. We are not
revisiting or reopening comment on
those actions here. Our basis for finding
that the SIP was not adequate to ensure
attainment and meet other CAA
requirements is described in our actions
on the SIP. Once we disapprove part or
all of a required SIP, section 110(c) of
the Act requires that we issue a FIP. Our
obligation in this action is to correct the
SIP deficiencies we previously
identified. Thus, the findings that
triggered our responsibility to
promulgate a FIP were established in
the prior rulemaking actions reviewing
Montana’s SIP. EPA is not required to
repeat those findings in the FIP
rulemaking itself.
(e) Comment (ExxonMobil): EPA
cannot propose a FIP to replace a SIP,
unless the SIP is substantially
inadequate to ensure compliance with
the CAA.
Response: The commenter misstates
the standard for promulgation of a FIP.
Section 110(c) of the CAA is
straightforward—a FIP is required if (1)
EPA finds that a state has failed to make
a required submission; (2) EPA finds
that a plan submission does not satisfy
the completeness criteria established
under section 110(k)(1)(A) of the CAA;
or (3) EPA disapproves a SIP in whole
or in part. EPA partially disapproved
the Billings/Laurel SO2 SIP; thus, a FIP
is required. Contrary to the commenter’s
assertion, the obligation to promulgate a
FIP is not contingent on an EPA finding
of substantial inadequacy. As explained
above, the findings triggering our
responsibility to promulgate a FIP were
made in the prior actions reviewing
Montana’s SIP.
(f) Comment (MSCC): The commenter
claims EPA’s action violates the Tenth
Amendment to the Constitution. The
commenter also claims EPA’s FIP is
dictating the required controls in
contravention of the holdings in
Commonwealth of Virginia v. EPA, 108
F.3d 1397 (D.C. Cir. 1997) and
Bethlehem Steel v. Gorsuch, 742 F.2d
1028 (7th Cir. 1984).
Response: Our FIP compels no action
on the part of the State and is not
`
coercive vis-a-vis the State. Our FIP
contains requirements applicable to four
private companies. The Tenth
Amendment is not implicated. Nor do
our actions contravene Commonwealth
of Virginia or Bethlehem Steel. The
former case held that EPA cannot, in a
SIP Call, dictate that a state adopt a
particular control measure to
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demonstrate attainment of the NAAQS.
EPA had issued a SIP Call finding that
the SIPs of 12 states were inadequate to
meet the ozone NAAQS and in its SIP
Call rule, specified that the states
needed to submit SIPs that included the
California Low Emission Vehicle
Program. In this matter, we are
promulgating a FIP, not issuing a SIP
Call. We are not directing any action by
the State. Thus, the Commonwealth of
Virginia case is not relevant to our FIP.
Bethlehem Steel is also not relevant to
our FIP action. In that case, the 7th
Circuit held that it was improper for
EPA to partially approve an Indiana SIP
revision so as to render it more stringent
than the State intended. We are
promulgating a FIP in this action, not
acting on a SIP; thus, Bethlehem Steel
does not apply. As we note elsewhere,
once we disapprove a SIP, we are
required to promulgate a FIP, and in
promulgating the FIP, we stand in the
state’s shoes. See section 110(c) of the
CAA, 42 U.S.C. 7410(c); Central Arizona
Water Conservation District v. EPA, 990
F.2d 1531, 1541 (9th Cir. 1993).
(g) Comment (MSCC): The commenter
argues that the cases EPA cited in the
preamble to the proposed Billings/
Laurel FIP, regarding its FIP authority,
do not speak to the central question—
‘‘When and on what authority may the
EPA undertake the draconian act of
displacing a state’s implementation
plan?’’ The commenter argues that the
question is particularly sensitive in this
case because the State and the sources
spent years negotiating the SIP.
Response: As noted in response to
comment II.B.1.(e), the CAA requires
that we promulgate a FIP whenever we
disapprove a SIP, in whole or in part.
While we are sensitive to the fact that
the State and sources spent years
negotiating the SIP, that does not change
our obligation under the CAA.
2. No Adequate Basis for FIP
(a) Comment (MSCC, ExxonMobil):
Because EPA must find substantive
noncompliance with some provision of
the Clean Air Act, specifically, failure to
attain NAAQS, and because that finding
of substantial inadequacy must be
clearly stated, the present FIP decision
must fall. It is inadequate on both
counts. EPA has not provided any
evidence that the State plan is not
working.
Response: See our response to
comment II.B.1.(e), above. The evidence
supporting EPA’s determinations
regarding the adequacy of Montana’s
SIP is contained in the record for those
rulemaking actions, and need not be
repeated here. EPA’s disapproval of the
SIP triggered the obligation for a FIP. No
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separate showing that the State plan is
not working or does not meet CAA
requirements is needed as part of this
action. Commenters’ comments
regarding EPA’s SIP actions are not
relevant for this rulemaking.
(b) Comment (ExxonMobil): Even
when the EPA has statutory authority
for a particular rule, its technical
decisions about the level of pollutant
reduction needed to comply with the
CAA and the control strategies
necessary to meet the level of pollutant
reduction must be rational. Courts
‘‘confronted with important and
seemingly plausible objections going to
the heart of a key technical
determination * * * ’’ will not presume
that EPA would never behave
irrationally. South Terminal
Corporation v. Environmental
Protection Agency, 504 F.2d 646, 665
(1st Cir. 1974). In South Terminal
Corporation, various interested parties
challenged EPA’s FIP on technical
grounds. Id. at 662–66. The court held
that EPA failed to adequately support its
decision to promulgate the rules
contained in the FIP and remanded the
case to EPA to develop the record. Id.
at 666. The court questioned EPA’s
position in light of contradictory
modeling and data, concluding that ‘‘it
is not clear whether or not the ambient
air at Logan meets, or will without
controls by mid-1975 will meet, the
national primary standard.’’ Id. 664.
Similarly, in the present FIP proposal,
EPA has neither determined appropriate
current modeling nor used currently
available information.
Response: The standards for judicial
review of this rulemaking action are
contained in section 307(d)(9) of the
CAA, 42 U.S.C. 7607(d)(9). We believe
the emission limitations and other
requirements in this FIP are reasonable
and that the situation in the cited case
is not analogous.3 The commenter has
not identified any modeling that
contradicts our attainment
demonstration, which forms the basis
for the FIP’s emission limitations; nor
has the commenter shown that a
different model would result in
substantially different emission
limitations. Our responses pertaining to
model selection and input data are
contained in section II.E., below.
Further, we note that it does not appear
3 In South Terminal Corporation, EPA had
determined emissions reductions needed to achieve
the ozone and carbon dioxide NAAQS based on
monitored values that the Court found highly
questionable (petitioners claimed the ozone monitor
was defective). South Terminal Corporation, 504
F.2d 646, 662 (1974). The commenter seems to
suggest that the Court rejected EPA’s modeling
approach, but in fact, the Court was satisfied with
the rollback modeling that EPA used. Id.
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21423
the commenter is suggesting that the
entire SIP should be re-done based on
more current modeling and more up-todate information. On the contrary, the
commenter seems satisfied with the
EPA-approved emission limitations in
the SIP,4 which were based on the very
modeling that the commenter now
claims is unreliable.
(c) Comment (ExxonMobil): Citing
Hall v. United States Environmental
Protection Agency, 273 F.3d 1146, 1159
(9th Cir. 2001), the commenter states
that in acting on a SIP, the test EPA
applies is to ‘‘measure the existing level
of pollution, compare it with the
national standards, and determine the
effect on this comparison of specified
emission modifications.’’ The
commenter argues that in the FIP
proposal, EPA did not correctly identify
the existing level of pollution and
ignored the substantial evidence of
permanently reduced SO2 emissions
and levels in the Billings/Laurel area.
The commenter also argues that EPA’s
authority is limited by its mandate
under the CAA to ensure attainment and
maintenance of the NAAQS as well as
the CAA’s other general requirements.
Response: See responses to comments
II.A.1.(a), II.A.2(b), and II.E.1.(e) and (g).
Also, the Hall case involved a challenge
to EPA’s approval of a SIP revision for
Clark County, Nevada, and EPA’s
interpretation of section 110(l) of the
CAA, which provides that EPA may not
approve a SIP revision if it would
interfere with attainment or other
applicable requirements of the CAA.
EPA asserted that its approval of the
Clark County SIP revision was
consistent with section 110(l) because
the revision did not relax the existing
SIP. The Court disagreed, holding that
110(l) requires more—a determination
that the specific revision, when
considered in the context of the SIP
elements already in place, can meet the
Act’s attainment requirements. Hall at
1152, 1159. It was in these
circumstances that the Court expected
EPA to determine the extent of pollution
reductions required and evaluate
whether the reductions resulting from
the revision would be sufficient to attain
the NAAQS.
In its reference to Hall, the commenter
appears to be conflating two disparate
concepts. The Hall Court was
addressing EPA’s action on a SIP
revision and indicating that EPA was
not adequately evaluating whether Clark
County’s rule change would interfere
4 Among other things, the commenter asserts that
the state SIP requirements are adequate to protect
the NAAQS. See reference document YYYY, page
27.
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jlentini on PROD1PC65 with RULES2
with attainment and other CAA
requirements. The Court was not
establishing a standard for a FIP or
indicating that EPA was requiring more
than necessary for the area, which
seems to be what the commenter is
suggesting in the case of the Billings/
Laurel FIP. As we explain in greater
depth elsewhere in this notice, we are
not starting from scratch with our FIP.
Instead, we are working within the
framework of the existing Billings/
Laurel SIP to fill the gaps resulting from
our partial and limited disapproval of
discrete SIP elements. In this unique
circumstance, where only discrete
elements of the SIP were deficient, the
CAA does not require us to reevaluate
or replace the entire SIP or the basic
modeling approach upon which it was
based. Nothing in the CAA requires EPA
to reject an entire SIP when only certain
elements within it are not approvable,
and doing so, where that is not
necessary to address a discrete
deficiency, would be inconsistent with
the basic scheme of cooperative
federalism embodied in the CAA.
Nor are we required as part of this FIP
to revisit our SIP Call or the bases for
our SIP disapproval. Our task is to fix
the portions of the SIP that were
deficient. It is reasonable to continue to
treat as valid the factors we found
adequate to support the portions of the
SIP we approved, and augment and/or
replace those factors that we found
inadequate. In fact, based on the holding
in Train v. NRDC, 421 U.S. 57 (1975),
recited by this commenter and others, it
would be inappropriate for EPA to now
reject or replace the portions of the SIP
that we approved as meeting the CAA’s
requirements, because to do so would be
to intrude on the State’s authority under
the CAA to establish the mix of controls
for the area.5 The State, of course,
remains free to submit a SIP revision
that reflects a different mix of controls
across all the sources. This would be the
mechanism, for example, whereby the
5 To the extent the commenter is arguing that we
may do no more in this FIP than appears minimally
necessary to attain the NAAQS, we reject that
notion as well. See, e.g., Central Arizona Water
Conservation District v. EPA, 990 F.2d 1531, 1541
(9th Cir. 1993) (EPA ‘‘stands in the shoes of the
defaulting State, and all of the rights and duties that
would otherwise fall to the State accrue instead to
EPA.’’) Under the CAA, states are not restricted to
barely meeting the NAAQS. In fact, the opposite is
true—states may exceed minimum requirements.
See CAA section 116, 42 U.S.C. 7416. In any event,
our modeled attainment demonstration resulted in
projected values just at the 24-hour SO2 NAAQS
(365 µg/m3) and just below the 3-hour SO2 NAAQS
(1291.5 µg/m3). However, we think we had
discretion to adopt limits (to replace those we
disapproved) consistent with modeled ambient
concentrations further below the NAAQS, if we had
felt a larger margin of safety was justified to ensure
attainment and maintenance.
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State could adopt SIP limits that
correlate to refinery consent decree
limits.6 If the State were to submit such
a revision, we would evaluate the
revision according to the Act, our
regulations, and the relevant cases.
(d) Comment (ExxonMobil): EPA’s
proposal imposes costly technology
requirements not rationally designed to
achieving their stated objectives. While
EPA has authority to impose an
emission limitation, the emission
limitation must be necessary to attain
NAAQS. City of Santa Rosa v. EPA, 534
F.2d 150, 155 (9th Cir. 1976), vacated on
other grounds, 429 U.S. 990 (1976). The
EPA derived its authority in City of
Santa Rosa from its statutory mandate
to ensure compliance with NAAQS and
the fact that no alternative to its
proposal was adequate to ensure
compliance with NAAQS. It is clear that
Montana’s existing SIP, supplemented
as it is by further state and federally
enforceable consent decrees are a more
than adequate alternative.
Response: The cited case actually
stands for the proposition that EPA’s
authority to adopt measures to meet the
NAAQS is expansive. EPA adopted a
FIP provision that would have required
a substantial reduction (up to 100%) in
the supply of gasoline to major
metropolitan areas in California,
including Los Angeles. Even the EPA
acknowledged that the rule would cause
severe social and economic disruption,
and the EPA Administrator at the time
publicly advocated amendments to the
CAA to provide relief from EPA’s own
FIP rule. Nonetheless, the Court held
that economic and social disruption are
not cognizable if (1) a measure is
necessary to attain the NAAQS; (2) there
is no statutory limitation on EPA’s
authority to adopt the measure; and (3)
there are no equally effective, less
burdensome alternatives. City of Santa
Rosa at 151–154.
The measures EPA is promulgating in
this FIP are in no way comparable to the
reduction in gasoline supply at issue in
the City of Santa Rosa case. Our FIP is
narrowly tailored to fill the gaps in the
Billings/Laurel SIP. Section 110(c)
requires us to promulgate the FIP. There
is no statutory limitation on our
authority to adopt the measures we are
adopting. On the contrary, section
110(a)(2)(A) of the Act requires
enforceable emission limitations as
necessary or appropriate to meet the
applicable requirements of the Act,
6 As we allude to in sections II.A.2.(b), II.D.4., and
II.E.1.(e), the consent decree limits would need to
be translated into limits that support an attainment
demonstration for the SO2 NAAQS. In sections
II.A.2.(b) and II.D.4., we identify some of our
concerns with the consent decree limits.
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which include attainment and
maintenance of the SO2 NAAQS. Using
ISC, the same model the State used to
set the commenter’s emission limits in
the SIP, we have determined emission
levels consistent with attainment and
established corresponding emission
limits on the flares, MSCC’s main stack,
and other emission units, whose
emission limits we disapproved in our
SIP action. While the authority to
require monitoring, recordkeeping, and
reporting requirements can be inferred
from CAA sections 110(a)(2)(A) and (C),
section 110(a)(2)(F) of the Act
specifically indicates that the EPA
Administrator may prescribe the
installation, maintenance, and
replacement of monitoring equipment
by stationary sources, as well as
reporting requirements. Our
requirement for the refineries and MSCC
to install monitoring equipment to
measure flare gas flow and
concentrations is consistent with this
authority and is rationally related to the
goals of the FIP, i.e., to ensure
attainment and maintenance of the SO2
NAAQS. We do not believe estimating
flare emissions or emissions from other
units is a sufficient substitute for realtime monitoring for purposes of this
FIP; estimation is not an equally
effective technique.
The commenter argues that the
existing SIP and the State and federally
enforceable consent decrees are a more
than adequate alternative to our FIP
requirements. This comment ignores the
fact that we disapproved portions of the
SIP as not meeting the CAA’s
requirements. Elsewhere we explain
that the consent decree provisions are
not sufficient to meet the CAA’s
requirements under section 110 related
to attainment and maintenance of the
NAAQS. See, e.g., sections II.A.2.(b),
II.D.4., and II.E.1.(e).
(e) Comment (MSCC): EPA’s failure to
issue the FIP within the CAA’s two-year
deadline is important in this case. As a
result of EPA’s delay, EPA should have
to consider the cleanup of emissions
that has occurred and significant
changes in modeling technology.
Response: We regret that it has taken
this long to issue the FIP. We disagree
that missing the two-year deadline
obviates our duty or the need for the
FIP. The State has not submitted a SIP
revision correcting the portions of the
SIP that we disapproved, despite the
passage of time. Regarding the argument
that we should have considered the
reduction in emissions since we
disapproved the SIP, see our responses
to comments in section II.A. In section
II.E, we respond to comments arguing
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that we should have used newer
modeling technology.
C. Flare Monitoring
1. Flare Flow Monitoring
(a) Comment (MSCC): The core
flowmeter technology application for
flare systems seems to be an established
technology, with thousands of
installations completed around the
world on other types of gas and liquid
streams. However, none was identified
that is following the precise
specifications of the FIP proposal.
Installation and operation of a flow
meter in flare gas service at MSCC are
probably achievable today, but not at
the flow range below 1 fps, and not with
conventional QA/QC procedures. Flow
monitors have a difficult time
measuring or reliably detecting low flow
velocities (under approximately 1.0 fps)
without false positives or false
negatives. EPA should revise the
proposed rule that currently indicates:
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‘‘[t]he minimum detectable velocity of the
flow monitoring device(s) shall be 0.1 feet
per second (fps). The flow monitoring
device(s) shall continuously measure the
range of flow rates corresponding to
velocities from 0.5 to 275 fps and have a
manufacturer’s specified accuracy of ±5%
over the range of 1 to 275 fps.
The revised rule should read ‘‘[t]he
minimum resolution of the flow monitoring
device(s) shall be 0.1 feet per second (fps)
when measuring flow rates above 1.0 fps. The
device(s) shall continuously measure the
range of flow rates corresponding to
velocities from 1.0 to 275 fps and have a
manufacturer’s specified accuracy of ±5%
over the range of that range.’’
The rule should also clarify if
‘‘accuracy’’ is intended to be 5% of the
full-scale range of the instrument (13.7
fps is 5% of 275 fps), or if this is
intended to be 5% of the measured flow,
which would be 0.05 fps at a flow of 1
fps, and would clearly be nonachievable with a resolution of 0.1 fps.
Response: EPA proposed the
volumetric flow monitoring
specifications based on what we saw
was achievable in vendor literature (see
reference documents NN and OO) and
what was being required by regulation
in the Bay Area Air Quality
Management District (BAAQMD) (see
reference document LL) and South
Coast Air Quality Management District
(SCAQMD) (see reference document
CCC).
The commenter asserts that
installation and operation of a flow
meter at the flow range below 1 fps are
not achievable. However, various
sources indicate that ultrasonic flow
meters can measure in the range of 0.1
to 1 fps. For example, in ‘‘Flare Gas
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Ultrasonic Flow Meter,’’ J.W. Smalling,
L.D. Brawsell, L.C. Lynnwoth and D.
Russel Wallace, Proceedings ThirtyNinth Annual Symposium on
Instrumentation for the Process
Industries, 1984, the authors reported
‘‘initially, a modest objective was
established to develop an ultrasonic
flow switch capable of detecting leaks in
flare lines corresponding to flow
velocity on the orders of 0.3 ms/ (1 ft/
s). As testing continued, however, it
became apparent that the equipment
could measure flows below 0.03 m/s
(0.1ft/s) and up to at least 6 m/s (20
ft/s) in flare stacks * * *’’ (see reference
document KKKKK). See also reference
document OO, ‘‘the DigitalFlowGF868
meter achieves rangeability of 2750 to 1.
It measures velocities from 0.1 to 275
ft/s (0.03 to 85 m/s) in both directions,
in steady or rapidly changing flow, in
pipes from 3 in. to 120 in. (76 mm to
3 m) in diameter.’’
Additionally, the BAAQMD (see
reference document LL) and SCAQMD
(see reference document CCC) require
flow meters on flares. BAAQMD
requires that the minimum detectable
velocity shall be 0.1 fps and the
SCAQMD requires monitors with a
velocity range of 0.1 to 250 fps. Based
on conversations with the BAAQMD, it
appears that the refineries in the Bay
Area have installed flow meters meeting
the requirements of the rule (see
reference document OOOOO).
Based on the above, we conclude that
flow meters are available that can
measure in the velocity range below 1.0
fps, and other regulatory authorities are
requiring such flow meters with
success.
The commenter also claims that
installation and operation of a flow
meter are probably not achievable with
conventional QA/QC procedures. The
QA/QC procedures are discussed below
in response to comment II.C.1.(d).
The commenter argues that flow
monitors have a difficult time
measuring or reliably detecting low flow
velocities (under approximately 1.0 fps)
without false positives or false
negatives. As indicated in the response
to comment II.C.1.(b) below, there are
approaches available for improving
measurement accuracy in the 0.1 to 1.0
fps range. In addition, as the response
to comment II.C.1.(b) indicates, in the
final FIP we are specifying a separate
accuracy range for the velocity range of
0.1 to 1 fps. Finally, we describe how
we are addressing the false positive and
false negative flows in response to
comment II.C.1.(c).
The commenter asked that the rule
clarify if ‘‘accuracy’’ of the instrument is
intended to be 5% of the full-scale range
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of the instrument or 5% of the measured
flow. In the rule, we have clarified that
‘‘accuracy’’ of the instrument is the
accuracy of the measured flow and not
the ‘‘full-scale range’’ of the instrument.
The commenter also suggests some
changes to the rule. Apart from adding
a separate accuracy range for the
velocity range of 0.1 to 1 fps and
clarifying that accuracy is based on the
measured flow, we are not making any
additional changes to this aspect of the
rule. We explain our reasoning in the
response to this comment II.C.1.(a) and
in the responses to comments II.C.1.(b)–
(d), below.
(b) Comment (ExxonMobil, WSPA):
Manufacturers of flow monitoring
instrumentation publish impressive
performance specifications regarding
velocity measurement range and
accuracy, but often manufacturers’
claims are not actually achieved in
practice over the long term. To achieve
a high level of measurement
performance in the field requires
adequate lengths of straight flare header
pipe upstream and downstream of the
monitor, the absence of flow
disturbances, etc. Where these criteria
cannot be met, the advertised or
predicted performance of the flow
monitoring system may not be fully
realized in practice. MSCC claimed that
significant piping modifications and
possible flare relocation would be
required to provide such runs at
accessible locations. CHS Inc. asserted
that it is likely that the CHS refinery
flare header will not have adequate
distances of undisturbed piping for
ideal installation. In this case, either
major, costly piping modification will
be required or the accuracy criteria will
not be achievable.
Response: The commenters are correct
that piping modifications may be
appropriate to optimize the
measurements. Each flare system will
have unique flow measurement location
issues and will have to be addressed on
a case-by-case basis. Sources may need
to work with the flow monitor
manufacturer and flow testers to assure
that the monitors meet the FIP’s
specifications for accuracy and
representativeness and manufacturer’s
requirements for assuring ongoing
equipment performance.
In addition to making piping
modifications (e.g. flow straighteners),
other approaches are available to
improve the measurement accuracy in
the 0.1 to 1.0 fps range. Among the
approaches are the use of additional
monitoring paths, monitoring paths of
longer length, and unconventional
monitor configurations and path
locations. Another approach involves
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the use of Computer Fluid Dynamics
(CFD) for the existing piping. CFD
analysis has been used to provide
correction factors for a series of
velocities across the range of flow
velocities. For example, these factors
have been used to correct flow
measurement data for disturbances
caused by upstream pipe irregularities.
These approaches are discussed in ‘‘A
Total Approach to Flare Gas Flow
Measurement for Environmental
Compliance,’’ Gordon Mackie, Jed
Matson and Mike Scelzo, Institute of
Measurement and Control—
Environmental Conference 2006. (See
reference document LLLLL.) (See also
Note to Billings/Laurel SO2 FIP File
regarding conversations with GE
Sensing (reference document
MMMMM)).
Finally, to address concerns regarding
the measurement accuracy in the 0.1 to
1.0 fps range, we are revising the rule to
indicate that the flow monitor must
have a manufacturer’s specified
accuracy of ± 20% over the range 0.1 to
1 fps. Based on conversations with a
vendor, we believe this is achievable.
The vendor indicated that they have
provided methodologies for sources to
meet the SCAQMD rule, which also
requires 20% accuracy in the 0.1 to 1.0
fps range. Methodologies include a
second interrogation path or
straightening of pipe. (See reference
document MMMMM.)
(c) Comment (ExxonMobil, WSPA,
NPRA, MSCC): Consistently achieving
low flow detection limits can be very
difficult. Spurious signal, resulting in
‘‘eddy’’ currents and back-and-forth
flows in the flare header, can easily
limit the detection and accuracy of low
flow readings. Furthermore, sometimes
a flow monitor will show an indication
of flow even though water seals ahead
of the flare stack remain intact (i.e.,
there is not flow to the flares). Other
regulations in other jurisdictions allow
the sources other means to positively
determine when the flare is not
operating (e.g., flare on/off monitoring
device, pressure of water seal).
ExxonMobil recommends that similar
language be considered by the
stakeholder process for inclusion in the
EPA’s proposed FIP, and thereby
remove the uncertainty of low flow
reading. MSCC claimed that the EPA
proposed FIP language should be
revised to allow flare operations to be
monitored by other means, and to
disregard low flow readings when the
flare is not operating to eliminate falsely
reported SO2 emissions, when in fact
there are none.
Response: We agree that it is
appropriate to include in the regulation
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the ability to use other secondary means
to determine whether flow is reaching
the flare when the flow monitor
indicates low flow. If the secondary
device indicates that no flow is going to
the flare, yet the continuous flow
monitor is indicating flow, the
presumption will be that no flow is
going to the flare. We have revised the
final rule to allow the use of flare water
seal monitoring devices to determine
whether there is flow going to the flare,
in addition to the continuous flow
monitoring device. See response to
comment II.F.1.(a) regarding the
comment seeking a stakeholder process.
(d) Comment (ExxonMobil, WSPA): A
limitation of flare gas monitoring
systems is the inability to provide for an
independent ‘‘in situ’’ verification of
accuracy. For example, there is no
practical way to vary the flare gas flow
that the monitor sees, and no practical
way to utilize a reference method.
Consequently, the calibration of a
monitor is performed electronically, and
the demonstration of accuracy is based
on that calibration method. MSCC
asserted that the proposed FIP does not
provide adequate guidance to allow
development of an acceptable QA/QC
system for routine calibration or daily
checks of the system. Without clear
guidance, it is not possible to specify a
system for a systems integrator (DAS/
reporting) or an end-user to design or
build a system to accomplish these
checks.
Response: Since refinery flares
contain highly variable flows and highly
combustible material, in situ
verification of flow measurement
accuracy is difficult. For that reason, the
performance specifications in the FIP
rely in large part on procedures
developed by the ultrasonic flow
monitor manufacturers 7 for
commissioning monitors to assure the
monitors will meet performance
specifications on an ongoing basis.
Manufacturers have established
procedures for conducting annual or
more frequent verifications of the
performance of installed flow monitors
as well as for the initial installation and
performance verification (see reference
document NNNNN). Based on
manufacturer established procedures
(Id.), we expect that the annual
verification procedures will address
elements such as:
1. Verification of the Flowmeter with
Reference Transducers—the purpose is to
evaluate all flowmeter subsystems with
factory-certified ultrasonic transducers;
7 Ultrasonic flow monitors will most likely be the
monitors installed to meet the FIP’s flow
monitoring performance specifications.
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2. Mechanical Inspection of Flowmeter
Transducers—the purpose is to visually
verify the integrity of the flare gas flowmeter
transducers and to clean any accumulated
debris from the transducer faces;
3. Zero Flow Verification—the purpose is
to evaluate the operation of the transducer
pair in the flare gas process (the integrity of
the original process transducers is tested in
a controlled environment);
4. Input/Output Verification—the purpose
is to verify the calibration of the analog I/O
of the flare gas flowmeter;
5. Electronic Flow Simulation—the
purpose is to demonstrate the operation of
the flare gas flowmeter over the full
measurement range of the instrument; and
6. Flowmeter System Reinstallation and
Test—the purpose is to verify that all
mechanical systems were properly aligned.
It should also be noted that since
ultrasonic flow monitors do not contain
any moving parts, their performance is
not expected to deteriorate over time.
One ultrasonic flow monitoring vendor
provided information on the reliability
and availability of the transducers
(sensors in the flare that transmit and
receive the ultrasound) they have
installed. The information indicates that
the 3,998 transducers installed between
first quarter 2005 and first quarter 2007
had a reliability percentage of 94.32%
and an availability percentage of
99.96%. (See reference documents
MMMMM and XXXXXX.) (See also
reference document LLLLL, ‘‘A Total
Approach to Flare Gas Flow
Measurement for Environmental
Compliance,’’ Gordon Mackie, Jed
Matson and Mike Scelzo, GE Sensing,
Institute of Measurement and Control,
Environmental Conference 2006, and
reference document NNNNN, April 5,
2007, email from Jed Matson, GE
Sensing, to Laurie Ostrand, EPA,
containing flare gas flow meter
procedures.
(e) Comment (COPC): ConocoPhillips
asserts it would need to replace a GE
Panametrics flare flow monitor that is
well-suited to the variable flow
conditions it experiences, but does not
conform precisely to the proposed
specifications. It is difficult to quantify
what additional benefit this change
would provide although the cost is
significant and quantifiable. The benefit
evaluation is further clouded because of
the relatively recent installation of the
Flare Gas Recovery Unit (FGRU). There
is no flow to measure in the flare header
when the FGRU is operating. The FGRU
operates on a full-time basis, with the
exception of nominal periods of
malfunction or maintenance.
Response: As indicated above, each
source will have unique issues that will
have to be addressed on a case-by-case
basis.
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We understand that ConocoPhillips
has a FGRU and ExxonMobil will be
installing one. We do not agree that a
source with a FGRU should be
exempted from monitoring flow to the
flare. We still believe it is reasonable to
include this requirement to gain an
accurate picture of occasions when flow
is going to the flare. We note that other
areas that have required refinery flare
monitoring (SCAQMD and the
BAAQMD) have not eliminated the flare
monitoring requirements at sources with
FGRUs. (See Note to Billings/Laurel SO2
FIP File regarding conversations with
BAAQMD, reference document
OOOOO.) However, as indicated below,
we are providing sources other means to
determine total sulfur concentrations in
the gas stream to the flare.
Additionally, we note that the
ConocoPhillips refinery in Rodeo,
California has installed flare flow meters
and that the refinery also has a flare gas
recovery system. The ConocoPhillips
San Francisco Refinery’s July 2007 Flare
Minimization Plan (FMP), pages 3–7,
indicates that flow meters have been
installed on the Main and MP30 flares
per the BAAQMD Regulation 12–11–
501. EPA’s Billings/Laurel FIP contains
flare flow monitoring specifications very
similar to the specifications in
BAAQMD Regulation 12–11–501. The
July 2007 FMP indicates ‘‘The
installation of the flow meters provides
for enhanced recognition of flaring
events. The flow meters help reduce
flaring by providing an accurate means
to measure and provide indication as to
when flaring is occurring. The flow
meters are especially useful for small
flaring events which may not be
detectable from visual flare stack
monitoring only. The meters help to
track and record all instances of flaring
as well as giving Unit Operators
immediate indication that flaring is
occurring so that they can take action to
reduce flaring.’’ (See reference
document PPPPP.)
(f) Comment (MSCC): The proposed
40 CFR 52.1392(h)(2)(iii) appears to be
in error. The rule indicates that ‘‘The
flare gas stream volumetric flow rate
shall be measured on an actual wet basis
in SCFH.’’ Actual wet basis would be
abbreviated as ACFH. SCFH means
standard cubic feet per hour, meaning
that the data has been corrected to
standard temperature and pressure. The
SCFH could be replaced with ACFH.
Alternately, the term ‘‘actual’’ could be
removed from the section, leaving ‘‘wet
basis in SCFH.’’ SCFH (corrected for
temperature and pressure) can also be
used to compute a mass emission rate of
sulfur dioxide, provided that any
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concentration measurements of sulfur
are also made on a ‘‘wet’’ basis.
Response: The commenter is correct.
We are revising the regulatory text to
read: ‘‘The flare gas stream volumetric
flow rate shall be measured on an actual
wet basis, converted to Standard
Conditions, and reported in SCFH.’’
(g) Comment (several commenters):
Several commenters express a general
concern that the technology will not be
able to meet the performance
specifications.
Response: See responses to comments
II.C.1.(a)–(c), above.
(h) Comment (YVAS): YVAS concurs
with the proposed volumetric flow
monitoring requirements.
Response: We acknowledge receipt of
the supportive comment.
2. Flare Total Sulfur Analyzers
(a) Comment (ExxonMobil, WSPA,
COPC): SCAQMD staff was not able to
identify a single commercial sulfur
analyzer in service on a refinery flare
system. It is unreasonable for EPA to
conclude that sulfur analyzer
technology is either ‘‘available’’ or
‘‘reliable.’’ MSCC was not able to
identify any installations where flare gas
monitoring was, in fact, covering a range
from 0–100% sulfur.
Response: EPA has identified two
sources where analyzers are on lines
leading to the refinery flare.
Specifically, the Tesoro refinery in the
Bay Area, California, has two Thermo
Electron Tracker XP continuous H2S
analyzers. The Tesoro analyzers are dual
range instruments, 0–1% and 0–5% (see
reference document OOOOO).
Additionally, the Shell refinery in Puget
Sound, Washington, uses an analyzer
that thermally oxidizes total sulfur to
SO2 and then measures the SO2. The
analyzer can measure up to 40,000 ppm
of SO2 (see reference document
QQQQQ). Finally, as indicated in the
response to comment II.C.2.(b) below,
the SCAQMD recently reported on a
pilot project study, testing a total sulfur
analyzer at the BP Carson facility in
southern California, and indicated that
the ‘‘preliminary results have
demonstrated the feasibility of
measuring total sulfur emissions from
vent gases directed to flares.’’
The proposed FIP did not specifically
require that an analyzer be capable of
measuring in the range from 1–100%
sulfur, although the preamble implied
and the record reported conversations
with vendors indicating that analyzers
could measure in the range from 1–
100% sulfur. We are clarifying the final
FIP to indicate that the total sulfur
analyzers should measure in the range
of concentrations that are normally
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21427
present in the gas stream to the flare. In
cases when the total sulfur analyzer is
not working or where the concentration
of the total sulfur exceeds the range of
the monitor, methods established in the
flare monitoring plan required by the
FIP shall be used to determine total
sulfur concentrations, which shall then
be used to calculate SO2 emissions. In
quarterly reports, sources shall indicate
when these other methods are used.
(b) Comment (ExxonMobil, WSPA):
SCAQMD Rule 1118 had an important
provision requiring an analyzer pilot
project, and one Los Angeles area
refiner is currently engaged with a
sulfur analyzer demonstration project. It
is conceivable that the pilot project
could result in the conclusion that the
analyzer being evaluated could not
provide sufficient accuracy, that the
system was not maintainable, or that
there were other problems.
Response: On June 1, 2007, the
SCAQMD presented to its Governing
Board an ‘‘Implementation Status
Report for 2006 for Rule 1118—Control
of Emissions from Refinery Flares.’’
Agenda No. 27 discusses the total sulfur
(TS) analyzer pilot project at the BP
refinery in Carson and indicates:
The TS pilot project is in the final step
prior to certification of the analyzer.
Although several adjustments and redesign of
sampling equipment were required; [sic]
preliminary results have demonstrated the
feasibility of measuring total sulfur emissions
from vent gases directed to flares. Based on
these results, two refineries have already
placed purchase orders for their TS
analyzers.
In the May 15, 2007, ‘‘Implementation
Status Report for 2006 for Rule 1118—
Control of Emissions From Refinery
Flares,’’ attached to Agenda No. 27, the
SCAQMD concludes:
Although they are behind schedule to
comply with the July 1, 2007 monitoring
requirements, the pilot projects are moving
ahead convincingly towards completion by
the end of 2007. As the rule is forcing new
technologies for flare emission reporting,
analyzer vendors have responded to the
challenge and several options are now
available, such as calorimeters, gas
chromatographs, mass spectrometers and
Pulsed UV Fluorescence analyzers, for
continuously measuring HHV [higher heating
value] and TS. Therefore, staff expects full
implementation of the continuous
monitoring provisions of the rule once the
pilot projects are complete. Since the
refineries could not meet the monitoring
requirements by July 1, 2007, the refineries
petitioned and were granted variances in late
April 2007 by the AQMD Hearing Board to
install and operate their flare monitoring
systems over the next two years.
See reference document RRRRR.
Based on the above information, the
total sulfur pilot project did not
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conclude that the analyzer being
evaluated could not provide sufficient
accuracy, that the system was not
maintainable, or that there were other
insurmountable problems.
(c) Comment (ExxonMobil): EPA and
industry need more time to review the
SCAQMD pilot project test results and
conclusions as they become available
over the next few months and to
determine if the technology that was
tested is technically viable and whether
or not a more cost effective alternative
technology may be available. MSCC
recommends that the implementation of
total sulfur monitoring on the flares be
delayed at least until the full results
from the long-term program in
California are available, and the
capability of the market to supply and
support such systems in severe weather
locations such as Montana is
demonstrated. At that point EPA should
revise and then issue the final rule, after
full stakeholder involvement in the
process and full consideration of
realistically available options.
Response: See responses to comments
II.C.2.(a) and (b), above. Also, as noted
in response to comment II.C.3.(a),
below, EPA is revising the proposed FIP
to allow other methods to determine
total sulfur concentration in the gas
stream to the flare. See response to
comment II.F.1.(a) regarding the request
for a stakeholder process.
(d) Comment (ExxonMobil):
Recognizing that these total sulfur
analyzer systems do not, by themselves,
provide any air quality benefit, and
considering that there are alternatives to
continuous analyzers (e.g., individual
grab samples, etc.), ExxonMobil submits
that the proposed requirement to install
continuous analyzers requires further
evaluation in the stakeholder process.
Response: As discussed under
response to comment II.C.1.(a), below,
our final FIP allows other methods to
determine total sulfur concentration in
the gas stream going to the flare,
including grab or integrated sampling
methods. This should address the
commenter’s concerns. However, we
note that whether or not total sulfur
analyzer systems provide any air quality
benefit by themselves is immaterial; the
FIP establishes emission limits to assure
that the SO2 NAAQS are attained and
maintained and it is essential that the
FIP include reliable mechanisms to
determine compliance with the limits.
See, e.g., CAA section 110(a)(2)(F), 42
U.S.C. 7410(a)(2)(F). Finally, as we
noted in our May 14, 2007, proposal to
revise subpart J of the new source
performance standards (NSPS), and to
adopt new subpart Ja, the requirement
to monitor flare emissions in the
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SCAQMD in fact resulted in reduced
flaring (72 FR 27178, at 27195) (see
reference document SSSSS).
(e) Comment (ExxonMobil, WSPA):
Cost of installing total sulfur analyzers
should be further evaluated given that
the analyzers themselves do not provide
an air quality benefit. Costs of total
sulfur analyzer pilot project in the
South Coast area expected to be in the
range of 3 to 5 million dollars.
Response: See response to comment
II.C.2.(d), above. Additionally, the cost
of the South Coast pilot project was
higher than expected because it was a
pilot study and because some
difficulties were encountered during the
study. (See also note to Billings/Laurel
SO2 FIP File regarding conversations
with SCAQMD, reference document
TTTTT.)
Also, in its ‘‘Implementation Status
Report for 2006 for Rule 1118—Control
of Emissions From Refinery Flares,’’
May 15, 2007, the SCAQMD reported
that refineries involved in the pilot
projects reported that monitoring costs
were estimated to be about 2 to 4.7
million dollars per flare. After looking at
the breakdown of the costs, SCAQMD
staff concluded that the total sulfur and
higher heating value analyzer costs were
comparable to staff’s original estimates.
However, the costs to design and build
the monitoring system were
significantly different. Research and
development (R&D), engineering, labor/
oversight, piping/electrical, analyzer
shelters, and contingencies stated by the
refineries represented approximately 75
to 85 percent of the flare monitoring
system cost. (See reference document
RRRRR.)
SCAQMD also indicated that in a
related development, ExxonMobil
informed staff in January 2007 that
ExxonMobil was taking a different
approach and was going to use a
different technology, namely, gas
chromatography (GC) for both the TS
and the HHV analyzer; the estimated
cost given to SCAQMD staff was 1 to 2
million dollars. ExxonMobil advised
SCAQMD staff that similar instruments
had been used at ExxonMobil’s flares in
Baytown, TX, and Chalmette, LA, for
monitoring H2S and the BTU content of
vent gases for compliance with EPA and
Texas Commission on Environmental
Quality (TCEQ) regulations. (Id.)
(f) Comment (CHS Inc.): Analysis of
total sulfur in a flare system is
challenging because of the wide range of
sulfur concentrations possible as well as
the number of individual sulfur
compounds potentially present. It is the
understanding of CHS that there is not
one commercial total sulfur analyzer in
service on a refinery flare.
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Response: See response to comment
II.C.2.(a), above.
(g) Comment (MSCC): Since H2S is
believed to be the principal
(overwhelming) sulfur component of
candidate flares, further consideration is
warranted as to whether the ‘‘total’’
sulfur component is the appropriate
methodology, given the clear lack of
existing equipment for the full potential
range of concentrations of flare gases,
and the complexity involved in
continuously converting a variable
mixture into a single component such as
SO2 or H2S. EPA should evaluate
whether there is a real, necessary, and
significant need to require total sulfur
analysis instead of allowing a somewhat
simpler H2S analysis of flare gases.
Response: The commenter has not
provided any technical analyses
supporting the notion that H2S is the
overwhelming component of the total
sulfur in the gas stream to its flares or
other flares in the area. EPA reported in
the May 14, 2007, proposed new source
performance standards (NSPS) for
Subpart Ja (72 FR 27178, at 27194) (see
reference document SSSSS) that ‘‘based
on available data, we understand that a
significant portion of the sulfur in fuel
gas from coking units is in the form of
methyl mercaptan and other reduced
sulfur compounds. These compounds
will also be converted to SO2 in the fuel
gas combustion unit, which means the
SO2 emissions will be higher than the
amount predicted when H2S is the only
sulfur-containing compound in the fuel
gas.’’ See also the response to comment
II.C.2.(a), above. Therefore, in the FIP
we are still requiring that the gas stream
to the flare be analyzed for total sulfur.
(h) Comment (ConocoPhillips, MSCC):
In a typical CEMS installation, the
analyzers are subjected to frequent
testing with gases intended to represent
a ‘‘zero’’ condition and a ‘‘span’’
condition which is specified as a
significant percent of full scale of the
analyzer. ‘‘Total Sulfur’’ analyzers,
operating over a wide range of
concentrations, present some special
concerns for span gases. If the proposed
FIP requires high concentration
analyzers, it also needs to incorporate
protocols to establish calibration
standards for these analyzers.
ConocoPhillips indicates that flare gas
sulfur concentrations can be highly
variable, which makes the comparison
required by the Relative Accuracy Test
Audit (RATA) difficult. The sulfur
analyzer captures samples in a series of
periodic discrete ‘‘grab’’ samples, to be
averaged over the period of total sample
time. Comparison sample techniques
vary, but in general involve getting a
continuous sample over a period of
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time, with the concentration averaged
over that time period. Depending on the
variability of the concentration over this
time period, the average of the discrete
‘‘grab’’ samples has the potential to be
different than the average of the
continuous RATA sample. When the
concentrations are numerically low, this
difference is compounded and skews
the accuracy calculations. This poses a
significant risk of failing the RATA
specifications, thereby voiding the
monitor data and imposing a
compliance issue (even if the difference
is a few parts per million).
ConocoPhillips believes that this
requirement is not technically valid for
the operations for which it is being
proposed.
Response: As indicated in response to
II.C.2.(b), above, the BP Pilot Project is
nearing completion and expected to be
a success. Also, see note to Billings/
Laurel SO2 FIP File regarding
conversations with SCAQMD (reference
document TTTTT). With respect to the
calibration of the analyzer, SCAQMD
indicated that there are several issues
that need to be addressed. Specifically,
one needs to assure that (1) the correct
calibration gas is in the bottle, (2) the
sample lines do not absorb or desorb
sulfur, (3) the probe is positioned
appropriately, and (4) all flow testing or
other sample collection is correlated
temporally with the analyzer
measurements to ensure representative
comparisons.
(i) Comment (ExxonMobil): EPA
recognized the impracticality of
concentration monitoring for flares
during the recent Consent Decree
negotiations. CEMS were deemed
unnecessary and impractical for flares,
unless the flare was in continuous use.
Response: The basis for the FIP is
different than the consent decrees. The
FIP assures attainment of the SO2
NAAQS, a health-based standard, and
the consent decrees assure that the new
source performance standards (NSPS),
technology-based standards, are met.
Because of these differences, we believe
it is appropriate to take a different
approach.
We disagree with the commenter’s
statement that ‘‘EPA recognized the
impracticality of concentration
monitoring for flares during the recent
Consent Decree negotiations. CEMS
were deemed unnecessary and
impractical for flares.’’ The CDs
required that compliance with 40 CFR
60.104(a) be determined by several
options, one of which was to install and
operate a CEMS per 40 CFR supbart J
(e.g. see paragraph 77 of CHS Inc.’s CD,
reference document JJJJJ):
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77. All continuous or intermittent,
routinely-generated refinery fuel gas streams
that are routed to the flare header at Cenex
shall be equipped with a CEMS as required
by 40 CFR § 60.105(a)(4) or with a parametric
monitoring system approved by EPA as an
alternative monitoring plan (‘‘AMP’’) under
40 CFR § 60.13(i), at the combined juncture
prior to the flare. Cenex shall comply with
the reporting requirements of 40 CFR Part 60,
Subpart J, for the Refinery Flare.
We also note that the proposed NSPS
Subpart Ja includes a total sulfur
standard and CEMS requirements for
fuel gas combustion devices, which are
defined to include flares. (See 72 FR
27178 (May 14, 2007), reference
document SSSSS.)
(j) Comment (MSCC): MSCC is aware
that it may be possible to use gas
chromatography systems to attempt to
meet the proposed FIP requirements.
Due to time constraints, they were not
able to investigate this subject
thoroughly.
Response: As indicated in response to
II.C.2.(e), ExxonMobil reported to the
SCAQMD that it is using gas
chromatography for its total sulfur and
higher heating value analyzers.
ExxonMobil has advised SCAQMD staff
that similar instruments have been used
on its flares in Baytown, TX, and
Chalmette, LA, for monitoring H2S and
the BTU content of vent gases for
compliance with EPA and Texas
Commission on Environmental Quality
(TCEQ) regulations. (See reference
document RRRRR.) Also, see note to
Billings/Laurel SO2 FIP File regarding
conversations with SCAQMD (reference
document TTTTT).
(k) Comment (several commenters): A
general concern is expressed that the
technology is not there to meet
performance specifications.
Response: See responses to above
comments II.C.2.(a) and (b).
(l) Comment (YVAS): YVAS concurs
that total sulphur concentrations and
not just H2S be monitored.
Response: We acknowledge receipt of
the comment and the support for our
proposal.
3. Miscellaneous Flare Monitoring
Concerns
(a) Comment (COPC, CHS Inc.,
MSCC): The proposed FIP should allow
for Alternative Monitoring Plans (AMPs)
to determine compliance.
ConocoPhillips argued that AMPs are
technically sound data gathering plans
that are developed based on site-specific
factors. These AMPs allow a facility to
comply based on equivalent but
customized criteria. CHS Inc. claimed
that uncertainty of the monitoring
capabilities and the quality assurance/
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quality control requirements makes it
reasonable for EPA to allow for AMPs
similar to other EPA regulations. MSCC
indicated that it calculates and reports
the amount of SO2 emitted during each
flaring event based on the recent
content, and estimated flow gas(es)
flared, based on reasonable technical
judgment and indirect metering
calculations. MSCC asserted that EPA
has failed to show any significant errors
or omissions with these methods.
Response: EPA is revising the
proposed FIP to allow other methods to
determine total sulfur concentration in
the gas stream going to the flare. The
other methods allow sources to use grab
or integrated sampling, followed by
sample analysis, to determine total
sulfur concentration of the gas stream
going to the flare. These grab and
integrated sampling methods are
currently allowed in the BAAQMD rule
(see reference document LL), and
similar methods have been allowed by
the SCAQMD. Two of the refinery
companies (ConocoPhillips and
ExxonMobil) in the Billings area also
have refineries in the Bay Area and/or
the South Coast Area and should be
familiar with these manual methods.
Specifically, we are revising the rule
to indicate that the total sulfur
concentration of the gas stream going to
the flare can be determined by: (1) A
total sulfur concentration monitoring
system as we proposed on July 12, 2006,
and including the changes we have
identified here; or (2) grab sampling or
integrated sampling.
If a source chooses to use the grab or
integrated sampling methods, the
requirement to obtain a grab or
integrated sample will be triggered if the
velocity of the gas stream to the flare in
any consecutive 15-minute period
continuously exceeds 0.5 feet per
second (fps) and shall continue until the
flow rate of the gas stream to the flare
in any consecutive 15-minute period is
continuously 0.5 fps or less.
Additionally, the rule indicates that a
grab or integrated sample will not be
required if any water seal monitoring
device indicates that flow is not going
to the flare. See discussion in response
to comment II.C.1.(c). Under these
conditions, if the water seal monitoring
device indicates that there is no flow
going to the flare, yet the continuous
flow monitor indicates flow, the
presumption will be that no flow is
going to the flare.
For grab sampling, a sample shall be
collected within 15 minutes after the
triggering conditions occur (see above),
and the sampling frequency, thereafter,
shall be one sample every 3 hours. For
integrated sampling, a sample shall be
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collected within 15 minutes after the
triggering conditions occur (see above),
and the sampling frequency, thereafter,
shall consist of a minimum of 1 aliquot
for each 15-minute period until the
sample container is full, or until the end
of a 3-hour period is reached, whichever
comes sooner. Within 30 minutes
thereafter, a new sample container shall
be placed in service. For grab and
integrated sampling, sampling shall
continue until sampling is no longer
required (see above).
Samples obtained by either grab or
integrated sampling shall be analyzed
for total sulfur concentration using
ASTM Method D4468–85 (Reapproved
2000) ‘‘Standard Test Method for Total
Sulfur in Gaseous Fuels by
Hydrogenolysis and Rateometric
Colorimetry’’ (see reference document
MMMMMM); ASTM Method D5504–01
(Reapproved 2006) ‘‘Standard Test
Method for Determination of Sulfur
Compounds in Natural Gas and Gaseous
Fuels by Gas Chromatography and
Chemiluminescence’’ (reference
document NNNNNN); or 40 CFR part
60, Appendix A–5, Method 15A
‘‘Determination of Total Reduced Sulfur
Emissions From the Sulfur Recovery
Plants in Petroleum Refineries.’’ Total
sulfur concentration shall be reported as
H2S or SO2 in ppm. Proper QA/QC
procedures shall be used to assure that
the samples are obtained and analyzed
appropriately.
We chose the trigger level for two
reasons. First, the rule indicates that the
minimum detectable velocity of the flow
monitoring device(s) shall be 0.1 fps and
the flow monitoring devices shall
continuously measure the range of flows
corresponding to 0.5 to 275 fps. Since
0.5 fps is the minimum flow measure
required, it is a reasonable trigger level
to ensure protectiveness. Second, flow
monitoring software averages all the
readings in a 15-minute timeframe and
records/reports the average flow. Using
the minimum recorded/reported
timeframe is reasonable to ensure
protectiveness.
With respect to using estimations,
technical judgment, and indirect
metering to calculate emissions from the
flare, because this FIP is designed to
protect the NAAQS, we are choosing to
require real-time direct monitoring
methods to determine emissions. We do
not believe estimations, technical
judgments, and indirect metering are
adequate substitutes for real-time
monitoring for purposes of the FIP.
(b) Comment (ExxonMobil, WSPA,
COPC, CHS Inc., MSCC): The proposed
requirement for a facility to install,
commission, and calibrate flow
monitoring systems and continuous
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18:55 Apr 18, 2008
Jkt 214001
sulfur analyzer systems within 180 days
after receiving EPA approval of a
monitoring plan is a requirement that
would simply be impossible to meet.
Response: Based on the comments
received, we have revised the FIP to
allow 365 days, rather than 180 days,
after EPA approval of the flare
monitoring plan to install continuous
flow monitors and to begin determining
total sulfur concentrations on the gas
stream to the flare. Based on
conversations with an ultrasonic flow
monitor manufacturer, BAAQMD, and
SCAQMD (see reference documents
MMMMM, OOOOO, and TTTTT,
respectively), we believe this additional
time is reasonable to install continuous
flow monitors and total sulfur analyzers
or to initiate grab or integrated
sampling.
(c) Comment (MSCC, ExxonMobil):
The FIP implies that pilot and purge gas
must be monitored. Pilot and purge gas
lines are separate from the main header
vent gas lines. Monitoring these other
relatively small gas flows to the flare is
a waste of effort and resources. The pilot
gas is usually a small natural gas stream
of low flow and essentially zero sulfur
content. The small purge gas line
usually is natural gas, refinery fuel gas,
or inert gas such as carbon dioxide or
nitrogen, or mixtures of such gases with
air or steam. In either case, the flow is
not high and usually ExxonMobil does
not expect high sulfur content. These
two stream types (pilot gas, purge gas)
cannot physically be mixed with the
main vent gas stream for measurement
of flow and sulfur content by one set of
monitors, without defeating their
essential purposes of safety. Given the
nature of the pilot gas and purge gas
streams, it is not reasonable to require
flow and sulfur monitors which meet
the proposed FIP specs on these
streams. Regulations from other areas
allow the flow and sulfur content of
pilot and purge gas to be estimated/
monitored by other devices or sampling
means. It is recommended that the
proposed FIP language be re-written to
clearly exempt pilot gases and purge
line gases from the proposed FIP
monitoring requirements. Neither can
reasonably be considered as a
significant source of sulfur dioxide.
ExxonMobil asserted that EPA’s
proposed FIP requirement for the
Billings/Laurel area is neither
reasonable nor legally supportable.
Response: In conversations with the
SCAQMD, we learned that in some
instances they had seen copious
emissions due to flare pilot and purge
gas (see reference document TTTTT).
SCAQMD indicated, as do the
commenters above, that in some cases
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refinery fuel gas is used as a purge gas.
Refinery fuel gas can have high sulfur
content. Because of the potential for SO2
emissions from the burning of pilot and
purge gas, we believe it is necessary to
account for these emissions and include
them when determining the total
emissions from the flare.
We agree that the proposed FIP
implied that the pilot and purge gas
should be monitored by the analyzers
on the flare line used to measure flow
and concentration of the gas stream to
the flare. We are revising the FIP to
require flow and H2S concentration
monitoring of the pilot and purge gas as
one possible method to determine sulfur
dioxide emissions from the burning of
such gas in the flare. However, the FIP
allows sources to forego monitoring if
certain requirements are met. First, if
facilities certify that only natural gas or
an inert gas is used for the pilot and/or
purge gas, then the gas does not need to
be monitored. Second, if facilities can
measure other parameters so that
volumetric flows, expressed in SCFH, of
pilot and purge gas can be calculated
(based on the design and the
parameters), then the flows do not need
to be monitored. Third, if the H2S
concentration of the pilot or purge gas
can be determined through other
methods, then the H2S concentration
does not need to be monitored. Once
flow and H2S concentration of the pilot
and purge gas are determined, sources
must then calculate the SO2 emissions
from the pilot and purge gas. The
calculated SO2 emissions will then be
added to the other SO2 emissions from
the flare to determine compliance with
the flare SO2 emission limits. Also, we
are revising the reporting requirements
to require sources to: (1) Certify in the
quarterly reports if pilot or purge gas is
not monitored because only natural gas
or an inert gas is used as the pilot and/
or purge gas; or (2) report flow and H2S
concentration of the pilot and/or purge
gas and the resultant SO2 emissions.
(d) Comment (MSCC): Flow and
concentration monitoring would be
costly and there is no justification for
such costs and complexity given that
the area is in attainment for the NAAQS.
Response: See response to comments
II.C.2.(d) and II.C.3.(c), above.
(e) Comment (YVAS): YVAS concurs
that each source submit for EPA review
a quality assurance and quality control
plan for each of the continuous
monitors.
Response: We acknowledge receipt of
the comment and the support for our
proposal.
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D. Flare Limits
1. Concerns With Flare Emission Limit
(a) Comment (CHS Inc, MSCC): The
proposed flaring limit of 150 lbs SO2/3
hour period was used in the model to
represent routine flaring and
background SO2 concentrations. This
threshold was never intended to and did
not account for malfunctions, startups,
or shutdowns.
Response: The FIP fills the gap for the
provisions of the SIP that were
disapproved. In its attainment
demonstration modeling, the State
modeled emissions from flares at 150
lbs of SO2/3-hour period, yet the SIP did
not contain corresponding emission
limits for the flares. This was the basis
for our disapproval of part of the SIP.
We believe we have appropriately
addressed malfunction, startup, and
shutdown in this final rule. See section
II.D.3., below.
Certain assumptions were made in the
State’s attainment demonstration for the
Billings/Laurel SO2 SIP. Included in the
assumptions was that flares had routine
emissions of 150 lbs of SO2/3-hour
period. To assure attainment and
maintenance of the NAAQS, the SIP or
a FIP must contain enforceable emission
limits on the flares. This is fully
explained in our proposed action on the
Billings/Laurel SO2 SIP (64 FR 40791,
40801, July 28, 1999) and in the
response to comments contained in our
final action on the Billings/Laurel SO2
SIP (67 FR 22168, 22179, May 2, 2002).
The State of Montana has flare
provisions that apply to CHS Inc.,
ConocoPhillips, ExxonMobil, and
MSCC. See CHS Inc.’s, ConocoPhillips’,
ExxonMobil’s, and MSCC’s exhibit A–1,
adopted by the Montana Board of
Environmental Review on June 12, 1998
(reference documents QQQQQQ,
PPPPPP, UUUUU, and OOOOOO).
Exhibit A–1 contains additional State
requirements that were not submitted
for inclusion in the SO2 SIP. Among
these is an emission limit on flares of
150 lbs of SO2/3-hour period, the value
the State relied on to model attainment.
These flare provisions do not and would
not satisfy the SIP/FIP requirements of
the CAA for two reasons. First, they
were never submitted to EPA to be
included as part of the SIP. Second, the
flare provisions contain automatic
exemptions for malfunction, startup,
and shutdown. This is inconsistent with
EPA’s longstanding interpretation of the
CAA, which is that, since SIPs must
provide for attainment and maintenance
of the NAAQS and the achievement of
the PSD increments, all periods of
excess emission must be considered
violations. Accordingly, any provision
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that allows for an automatic exemption
for excess emission is prohibited.8
(b) Comment (NEDA/CAP, MSCC,
ExxonMobil): The capriciousness of
EPA’s proposed FIP provision affecting
flaring is that EPA recognizes in the
proposed notice that sources likely will
be unable to comply with the
continuous flaring emission limitations.
Yet the proposed FIP would allow
citizens to bring actions for violations of
unattainable limits when EPA or the
State likely would choose to exercise its
prosecutorial discretion. Such a
regulatory ‘‘Catch-22’’ is both
unreasonable and unlawful.
Response: We respectfully disagree
with the commenter. First, in our
proposal we did not say that sources
will be unable to comply with the
continuous flaring emission limitations.
We note that, after receiving the
refineries’ estimates of routine flare
emissions, the State established as a
State-only limit the same numerical
flare limit we are adopting, and the
refineries and MSCC agreed to the
stipulations containing those limits. See
67 FR 22180, col. 2, May 2, 2002, and
reference documents UUUUU,
OOOOOO, PPPPPP, QQQQQQ, and
SSSSSS. Also, at the time of our SIP
action, Conoco indicated to us that
routine emissions from its flare were
expected to be less than 150 lbs SO2/3hour period. See 67 FR 22180, col. 2,
May 2, 2002, and reference document
RRRRRR. Based on this information, we
have concluded that the refineries and
MSCC will be able to comply with the
150 lbs SO2/3-hour flare limit under
normal operating conditions.
We did say in our proposal that we
recognize flares are sometimes used as
emergency devices and that it may be
difficult to comply with the flare limits
during malfunctions. See 71 FR 39264,
col. 1, July 12, 2006. However, contrary
to the commenters’ assertions, our
decision to require an emission limit
that may be difficult to meet under
certain conditions is not capricious,
unreasonable, or unlawful.
There is often a conflict, which is not
limited to refinery flare emissions,
between a source’s ability to control
emissions during certain operating
conditions and the CAA’s requirement
to attain and protect the NAAQS. Our
fundamental responsibility under the
CAA with respect to SIPs/FIPs,
however, is to ensure the NAAQS are
attained and other CAA requirements
are met. See CAA sections 110(a) and
8 See reference document RRR, September 20,
1999, memorandum entitled ‘‘State Implementation
Plans: Policy Regarding Excess Emissions During
Malfunctions, Startup, and Shutdown.’’
PO 00000
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21431
(l), 42 U.S.C. 7410(a) and (l); reference
document RRR, September 20, 1999,
memorandum titled ‘‘State
Implementation Plans: Policy Regarding
Excess Emissions During Malfunctions,
Startup, and Shutdown,’’ from Steven
A. Herman and Robert Perciasepe, to
Regional Administrators (hereafter
‘‘1999 excess emissions
memorandum’’); City of Santa Rosa v.
EPA, 534 F.2d 150, 155 (9th Cir. 1976),
vacated on other grounds, 429 U.S. 990
(1976). Thus, we have long held that
outright or ‘‘automatic’’ exemptions
from emission limits needed to
demonstrate attainment of the NAAQS
are not appropriate, something we
indicated in our proposed FIP. See our
1999 excess emissions memorandum,
reference document RRR, and our
proposed FIP, 71 FR 39264, col. 1, July
12, 2006. Our interpretation on this
issue has been upheld by the U.S. Court
of Appeals for the 6th Circuit: in a 2000
decision, the Court rejected a challenge
to EPA’s disapproval of a Michigan SIP
revision that provided an automatic
exemption from SIP limits during
malfunction, startup, and shutdown
periods. Michigan Department of
Environmental Quality v. EPA, 230 F.3d
181 (6th Cir. 2000).
As we explained as long ago as 1977,
the appropriate approach in SIPs/FIPs is
to require continuous compliance in
order to create an incentive for sources
to properly operate and maintain their
facilities and to improve their operation
and maintenance practices over time.
See, e.g., 42 FR 21472, April 27, 1977
(reference document VVVVV), and 42
FR 58171, November 8, 1977 (reference
document WWWWW). We explained
that an automatic exemption would
encourage the source to claim after
every period of excess emissions that
the exemption applied, and that instead
the proper means to provide relief to
sources was through the exercise of
enforcement discretion in appropriate
circumstances. Id.
Later, in 1999, we indicated that
states could include in their SIPs, as an
alternative to the enforcement discretion
approach, narrowly tailored affirmative
defense provisions to address source
difficulties meeting emission limits
during malfunction, startup, and
shutdown periods. See reference
document RRR, our 1999 excess
emissions memorandum. In this 1999
memorandum we reiterated our longheld view that, ‘‘because excess
emissions might aggravate air quality so
as to prevent attainment or interfere
with maintenance of the ambient air
quality standards, EPA views all excess
emissions as violations of applicable
emission limitation[s].’’ We also
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repeated our recognition that some
malfunctions may be unavoidable.
Thus, while flares may have unique
characteristics, the underlying conflict
between the ability to comply and need
to meet the NAAQS is the same. We do
not believe the nature of the emission
point should dictate a different
approach to protection of the NAAQS.
Whether considering stack emissions at
a power plant or other source, or flare
emissions at a refinery, the SIP/FIP
should be structured to provide the
source with the incentive to properly
design, operate, and maintain its
facility. An outright exemption from the
emission limits would not do this.
To provide relief to the sources for
truly unavoidable violations, while still
maintaining appropriate incentives for
compliance, we are providing an
affirmative defense to penalties for
violations of flare limits during
malfunctions, startups, and shutdowns.
The elements of the defense, which a
source would have to prove in court or
before an administrative judge, are
enumerated in our final rule and are
consistent with the elements described
in our 1999 excess emissions
memorandum. The gist of these
elements is that a source must take all
possible steps to prevent exceedances of
the limits and to minimize the amount,
duration, and impact of those
exceedances. These same or similar
criteria have been adopted by other
regulatory agencies, including the State
of Colorado and Maricopa County,
Arizona, in excess emissions rules. See,
e.g., Colorado Air Quality Control
Commission Common Provisions
Regulation, 5 CCR 1001–2, Sections II.E.
and J. (reference document TTTTTT);
Maricopa County Air Pollution Control
Rules, Rule 140, ‘‘Excess Emissions’’,
Section 400 (reference document
ZZZZZ).
Finally, we reject commenters’
assertion that citizens will necessarily
pursue enforcement where the State and
EPA do not, but in any event, this
possibility is inherent in the structure of
the CAA; Congress provided citizens
with the ability to enforce SIPs and
FIPs. This inherent structure is not a
reason for us in this rulemaking action
to change our longstanding
interpretations regarding the proper
treatment of excess emissions.
(c) Comment (NEDA/CAP): Industry
contends that it is virtually impossible
to meet the proposed limits during
flaring, since flares themselves are not
process units when they are treating
excess gases during malfunction events.
EPA has presented no information in
this notice or elsewhere to the contrary.
On this basis alone, if the mass emission
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limits for flares are not made less
stringent, the FIP must recognize in its
final action that flares must be available
for use during malfunctions and
emergencies to protect the safety of
employees and the public, as well as
equipment integrity, regardless of the
mass emission rate of the time.
Response: The FIP is not intended to
jeopardize the safety of refineries, their
workers, or neighbors. Our SIP policy 9
has long recognized that imposing
penalties for violations of emission
limitations for sudden and unavoidable
malfunctions caused by circumstances
entirely beyond the control of the owner
or operator may not be appropriate.
States, EPA, and citizens have the
ability to exercise enforcement
discretion to refrain from taking
enforcement action in these
circumstances. In addition, EPA has
revised the FIP to provide sources with
the ability to assert an affirmative
defense to penalties for violations of
flare limits during malfunction, startup,
and shutdown. However, while we
recognize some violations may be
unavoidable, we also believe that
sources have a responsibility to do their
best to achieve continuous compliance
and to minimize the number, duration,
and severity of malfunctions and other
events leading to excess emissions.
(d) Comment (MSCC): Various
jurisdictions have attempted to address
flare emissions. There is no uniform
federal requirement or regulation
requiring such limits or monitoring,
particularly for short term limits, or for
malfunction, startup, and shutdown
controls. It is difficult to understand any
reason that the Montana SIP for
Billings/Laurel is ‘‘substantially
inadequate’’ regarding flaring or for
proposing restrictions going far beyond
those in effect in any jurisdiction or
federal rule.
Response: Regardless of what other
areas are doing with respect to flare
emissions, we must fulfill our
responsibility to fill the gaps of the
provisions of the SIP that we
disapproved. Each area must be
addressed on a case-by-case basis. The
response to comment II.D.1.(a) and our
notice of proposed rulemaking express
why we believe the FIP should contain
emission limits for flares in the Billings/
Laurel area. Regarding the comment
about substantial inadequacy, please see
our response to comment II.B.2.(a),
above.
9 See reference document RRR, September 20,
1999, memorandum entitled ‘‘State Implementation
Plans: Policy Regarding Excess Emissions During
Malfunctions, Startup, and Shutdown.’’
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(e) Comment (MSCC): There is no
reasonable basis to believe that flaring,
as practiced in this air-shed, prevents
attainment and maintenance of NAAQS,
or that it is inadequately regulated, or
that it has an impact on health, welfare,
or commerce among states, as years of
experience confirm. The State of
Montana flare provisions are adequate.
No federal action is needed.
Response: This comment goes to the
validity of our SIP action and is not
relevant here. See our response to
comment II.B.2.(a), above.
(f) Comment (MDEQ): Imposing a
mass-based emission limit (and the
necessary and ancillary requirements for
measuring flows and concentration) on
a flare increases the regulatory workload
while providing a marginal benefit.
Currently, Montana’s Malfunction rule
(ARM 17.8.110) provides Montana with
enforcement discretion during
malfunction events.
Response: We note that the State has
mass-based emission limits on the flares
in the Billings/Laurel SO2 area. See CHS
Inc.’s, ConocoPhillips’, ExxonMobil’s,
and MSCC’s exhibit A–1, adopted by the
Montana Board of Environmental
Review on June 12, 1998 (reference
documents QQQQQQ, PPPPPP,
UUUUU, and OOOOOO). Exhibit A–1
contains State requirements that were
not submitted for inclusion in the SO2
SIP. The provisions of exhibit A–1 also
appear in the sources’ Title V permits
and are labeled as State-only provisions.
See, for example, ConocoPhillips’ Title
V permit (see reference document
XXXXX).
The exhibit A–1 requirements
indicate that the facilities shall not
allow SO2 emissions from any flare,
unless the emissions are a minor flaring
event (defined as less than or equal to
150 pounds per 3-hour period), or the
result of start-up, shutdown, or a
malfunction. Exhibit A–1 does not
indicate how compliance with the
emission limit is determined and only
requires reporting of flare emissions that
are not minor flaring events.
Presumably, the additional workload
provided by the FIP, that the State is
referring to, is in evaluating the
continuous analyzers and receiving
quarterly reports. We believe the
additional workload is warranted and
necessary to determine compliance with
the flare emission limits and assure that
the SO2 NAAQS will be attained and
maintained. See, e.g., CAA sections
110(a)(2)(A), (C), and (F), 42 U.S.C.
7410(a)(2)(A), (C), and (F).
We do not understand the intent of
the comment that indicates MDEQ has
enforcement discretion under its
malfunction rule in ARM 17.8.110
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(reference document YYYYY). Before
MDEQ could decide whether or not to
pursue an enforcement action for
violations of the State-only flare limit,
MDEQ would need to evaluate
information submitted by sources.
Additionally, we note that in response
to our proposed action on the Billings/
Laurel SIP, the State said the following:
‘‘The State agrees with EPA that the SIP
is incomplete without enforceable
emission limitations applicable to flares,
and that such limitations should
correspond to the emission rates used in
the attainment demonstrations.
However, after significant effort to
address the issue, the State was unable
to find a workable solution that would
meet EPA’s concerns.’’ See document
#IV.A–23, comment #3, from docket
#R8–99–01; 67 FR 22183, col. 1, May 2,
2002; and reference document ZZZZZZ.
(g) Comment (YVAS): YVAS concurs
with EPA’s further assumption (page
39264), that ‘‘the 3-hour SO2 NAAQS
would be attained’’ if ‘‘the limit for the
main flares was established at 500
pounds of SO2 per calendar day.’’ Since
there is apparently precedent (as noted
on page 39263 FR) ‘‘contained in
settlements between the United States
and CHS Inc, ConocoPhillips and
ExxonMobil,’’ YVAS further agrees to
and accepts EPA’s reasoning that ‘‘the
500 pound value for this FIP (should) be
imposed as an enforceable limit and not
just a trigger point for further analysis’’
as a starting point. However, the ‘‘500
lbs per day limit,’’ if extended for any
length of time, is not acceptable. Based
on acquired information, YVAS does
not think this limit would be punitive,
nor would it be impossible for industry
sources to attain. It is accepted that zero
emissions may not be possible or
attainable, but any lower emissions rate
would be a public benefit. And,
although a compliance drop could
create greater industry noncompliance
and require more enforcement action,
YVAS does not believe the more
stringent standards would create more
noncompliance problems for the
sources.
Response: We have decided to retain
the proposed limit of 150 lbs of SO2/3hour period. A more stringent limit than
either proposed is unnecessary to
ensure attainment of the NAAQS. Thus,
we believe it is reasonable not to impose
a more stringent limit as the commenter
suggests.
(h) Comment (Citizen): The proposed
rule should not be adopted unless
recognized medical opinion concerning
the cumulative health risks of the
release of 500 lbs per day of sulphur
dioxide into the area’s airshed is
analyzed. Specifically, what
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justification criteria are being used to
establish the 500 lb. minimum per day
base in the Proposed Rule. And, as
noted on page 39264 of the Federal
Register dated July 12 announcing the
FIP, EPA says ‘‘if we adopted the 500
pound value in this FIP, we would
impose it as an enforceable emission
limit.’’ If there are still questions
concerning the 500 lb per day emission
limit, why is it being proposed? Is there
a lower and perhaps ‘‘better’’ emission
limit per day that should be considered?
Response: The current SO2 NAAQS
were set to protect public health and
welfare after consideration of various
scientific data. It is not our role here to
re-evaluate the NAAQS, but to ensure
they are met. Through modeling we
determined that both limits would
protect the SO2 NAAQS. While a lower
limit might be attractive, we are setting
the limits at 150 lbs of SO2/3-hour
period, a level sufficient to meet the SO2
NAAQS; we think this is reasonable.
See response to comment II.A.2.(b). See
also our response to comments
pertaining to SO2 NAAQS and SO2
Health Effects (II.F.9. and 10.,
respectively) below.
(i) Comment (MDEQ): MDEQ believes
that hard cap emission limits on flares
are good but believes that the flare
emission limits will be more accepted if
malfunction, startup, and shutdown
exemptions are introduced.
Response: We acknowledge MDEQ’s
support for hard cap emission limits on
flares. Regarding exemptions for
malfunction, startup, and shutdown, see
our responses to comments II.D.1.(b)
and (c), above.
As indicated above, to address
industry concerns regarding
malfunctions, startup, and shutdown,
we are revising the FIP to provide
sources the ability to assert an
affirmative defense to penalties for
violations of flare limits during
malfunction, startup, and shutdown.
2. Safety Device
(a) Comment (CHS Inc., WETA, MPA,
NPRA): From a safety standpoint, there
are concerns with flare limits applying
at all times, including malfunction,
startup, and shutdown. Flares are
primarily safety devices, designed as a
means to ensure the safety of employees
and the community and to maintain the
integrity of refinery equipment during
situations that are not representative of
normal operations. It will be precedent
setting if the EPA views these infrequent
events as enforcement situations. It
would, in essence, require facilities to
choose between maintaining a safe,
controlled refinery and violating the
FIP.
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Response: See responses to comments
II.D.1.(b) and (c), above. As we indicate
in our response to comment II.D.1.(c),
the FIP is not intended to jeopardize the
safety of refineries, their workers, or the
community. However, we believe it
would be inconsistent with CAA
sections 110(a) and (l) to provide an
outright exemption from the flare limits
during malfunction, startup, and
shutdown periods. Instead, to provide
some measure of relief to the sources,
we have included an affirmative defense
to penalties in our final FIP rule. If a
source takes steps consistent with the
elements of the affirmative defense,
excess flaring emissions during
malfunction, startup, and shutdown
periods would not be penalized. We
have considered several additional
factors: First, historically, the sources
have used the flares as part of their
routine operations, i.e., in nonemergency conditions. See September
28, 1995, letter from Bob Raisch to
Douglas Skie (reference document
SSSSSS); 67 FR 22180, col. 2, May 2,
2002. Also, in its comments on the FIP
(reference document QQQQ), CHS Inc.
indicated that the 150 lbs/3-hour value
was used in the original model to
represent routine flaring and
background SO2 concentrations. MSCC
indicated in its comments on the FIP
(reference document WWWW) that
flares can be used for handling streams
other than those arising from
malfunction, startup, and shutdown.
Second, flaring events have not
necessarily been as infrequent as the
commenter implies. From the first
quarter of 2005 through the second
quarter of 2007, source reports indicate
that MSCC and the 3 refineries
experienced over 150 flaring events
with SO2 emissions greater than 150
pounds over 3 hours. See reference
document HHHHHH. Third, the
emissions during these events can be
very high—the State estimated that
emissions during malfunctions could be
as high as 6,000 pounds/3-hour period,
and the sources’ own reports for first
quarter 2005 through second quarter
2007 reflect emissions as high as 12,400
pounds over a 2-hour period. See
reference documents SSSSSS and
HHHHHH. The maximum value
reported for a flaring event during the
period was 40,800 pounds of SO2 over
an unknown duration, and there were
numerous events in the thousands of
pounds. See reference document
HHHHHH. Fourth, we want to ensure
that the owners/operators design,
operate, and maintain their facilities to
minimize flare emissions by minimizing
the conditions that lead to malfunctions,
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startups, and shutdowns. In the FIP
context, the appropriate way to do this
is by establishing a flare emission limit
that is not subject to outright
exemptions. Fifth, the State and EPA
have already viewed these events as
enforcement situations in the context of
the refinery initiative and, through the
consent decrees, have created the
expectation that the refineries will
minimize flare emissions. We explain in
this preamble why the conditions of the
consent decrees, while beneficial, are
not sufficient for purposes of the FIP.
See, e.g., responses to comments
II.A.2.(b), II.D.4., and II.E.1.(e). We also
note that MSCC is not subject to a
consent decree. Finally, the air does not
care whether emissions come out of a
flare that is used as a safety device at a
refinery or a stack at a power plant or
other facility.10 In both cases, the
emissions of SO2 impact air quality, and
EPA’s charge is to address those impacts
so as to protect the NAAQS.
(b) Comment (WSPA, MSCC,
ExxonMobil): EPA proposes that flare
limits apply at all times without
exception. It would be virtually
impossible to comply with SOx mass
emission limits at all times and for all
malfunctions for the simple reason that
the primary function of a refinery flare
is to serve as a safety device. Flares
must be available for use during
malfunctions and emergencies to protect
equipment and the safety of employees
and the public.
Response: See responses to comments
II.D.1.(b) and (c), and II.D.2.(a), above.
(c) Comment (NPRA): The U.S.
Chemical Safety Board (CSB) urges the
installation of flares. The CSB sites
flares as a ‘‘safer alternative’’ when
compared to other techniques. Clearly
the CSB recommendation is at odds
with Agency’s proposal.
Response: See responses to comments
II.D.1.(b) and (c), and II.D.2.(a), above.
Also, we do not believe our action is at
odds with the CSB’s recommendations.
In this action, we are not opining on the
use of flares versus other techniques.
We are not telling the refineries or
MSCC to stop using their flares.
However, flares are an emission point at
the refineries and MSCC, they have been
the source of routine emissions
10 In theory, a smokestack could also be
characterized as a safety device; among other
things, a stack is used to prevent harmful ground
level concentrations of pollutants. In addition, gases
are sometimes bypassed around control devices
directly to the stack to avoid damage to control
devices and/or other dangerous conditions. In the
SIP/FIP context, we do not believe it is appropriate
to automatically exempt these stack emissions, even
though the stack may serve a safety purpose. See
our 1999 excess emissions memorandum, reference
document RRR.
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18:55 Apr 18, 2008
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historically, and they can be the source
of very large quantities of emissions in
a short period of time. We believe it is
necessary and appropriate to impose
limits on the flare emissions to fill one
of the gaps in the SIP, to support our
attainment demonstration, and to create
appropriate incentives for the sources in
the design, operation, and maintenance
of their facilities.
3. Malfunction, Startup, and Shutdown
(a) Comment (WSPA, MSCC,
ExxonMobil): In working with the South
Coast Air Quality Management District,
they were careful not to compromise
safety by restricting, either explicitly or
implicitly, the use of flares during
emergencies through the imposition of
mass emission limits or otherwise.
Response: See responses to comments
II.D.1.(b) and (c), and II.D.2.(a), above.
Our FIP does not require or direct the
sources to not use their flares during
emergencies. Unlike the South Coast or
Bay Area,11 however, we are required to
promulgate a FIP that demonstrates
attainment of the SO2 NAAQS.
Consequently, it is necessary and
appropriate that we impose emission
limits on the flares that are consistent
with our modeled attainment
demonstration. To address industry
concerns, we are providing an
affirmative defense to penalties for
excess flare emissions during
malfunction, startup, and shutdown
periods.
We note that SCAQMD’s rule 1118(d)
imposes annual SO2 performance targets
for flare emissions (caps on the amount
of SO2 emitted from flares in one year).
The performance targets are based on
the crude processing capacity and
become more stringent over time.
Malfunction, startup, and shutdown
emissions count towards the annual
performance targets unless they meet
certain narrowly defined exemptions in
rule 1118(k). Sources that exceed their
annual performance targets must submit
a flare minimization plan and are
subject to mitigation fees of up to four
million dollars a year (see reference
document CCC).
(b) Comment (WSPA, MSCC,
ExxonMobil): It is essential for EPA to
recognize the true nature of
malfunctions at refineries, and the fact
that there is no practical way to regulate
11 The Bay Area prohibits all refinery flaring
unless the flaring is consistent with a flare
minimization plan or is caused by an emergency.
See BAAQMD rule 12–12–301 (reference document
AAAAAAA). The South Coast rule requires
minimization of flaring and prohibits combustion of
vent gas in the flare except during emergencies,
shutdowns, startups, turnarounds or essential
operational needs. See SCAQMD rule 1118(c)(4)
(reference document CCC).
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the release of vent gases during
malfunctions, or, to treat the emergency
vent gases to remove sulfur compounds
prior to combustion in the flare.
Response: See responses to comments
II.D.1.(b) and (c), II.D.2.(a), and
II.D.3.(a), above. Also, we understand
that while a malfunction is underway, it
may be impossible to treat the gases
prior to combustion in the flare.
However, we do not agree that all
malfunctions are categorically
unavoidable. We are concerned with the
causes leading to the malfunctions and
the steps taken after the malfunction
begins to mitigate its effects. We are
promulgating an affirmative defense
provision along with the flare emission
limits that should ensure sources take
all steps within their control to avoid
malfunctions and minimize their
impacts on air quality once they occur.
We believe this is reasonable and
appropriate to ensure protection of the
NAAQS.
(c) Comment (WETA): Pursuing the
adoption of this FIP could potentially
result in the setting of an inconsistent
national policy for malfunction, startup,
and shutdown.
Response: We do not agree with the
comment. The FIP would not be setting
inconsistent national policy for
malfunction, startup, and shutdown
occurrences. To the contrary, we are
following our national policy with
respect to malfunctions, startup, and
shutdown as expressed in the 1999
excess emissions memorandum (see
reference document RRR).
(d) Comment (MSCC): MSCC believes
that the approach taken by the State of
Montana in providing for minimization
of flaring, above a reasonably
determined de minimis threshold, and
clear exceptions for malfunctions,
startup, shutdowns and other
operational needs is the sound
approach, to address the reality that
there are, and will be situations such as
malfunctions, startups, and shutdowns
and emergencies that are beyond the
reasonable control of a source, in the
operation of flares.
Response: We recognize there may be
violations of flare emission limits
during malfunctions, startups,
shutdowns, and emergencies that are
beyond the control of a source;
accordingly, we are providing sources
with the ability to assert an affirmative
defense to penalties for violations of
flare limits that occur during
malfunction, startup, and shutdown
periods. We believe this is a reasonable
approach, consistent with our views
that automatic exemptions are not
appropriate for emission limits relied on
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to demonstrate attainment of the
NAAQS.
(e) Comment (COPC): The rule as
written will ultimately put
ConocoPhillips in the position of having
to choose between compliance with an
environmental regulation and
maintaining safe operating conditions.
This is an untenable position which can
be avoided by acknowledging in rule
language that flare SO2 emissions can
occur during periods of malfunction,
startup, and shutdown, provided that
accepted management systems are
followed.
Response: See responses to comments
II.D.1.(b) and (c), and II.D.2.(a), above.
We believe the provision of the
affirmative defense to penalties for
excess emissions during malfunction,
startup, and shutdown periods
appropriately and reasonably addresses
the commenter’s concerns.
(f) Comment (COPC): A FIP program
that adopts the same evaluation
procedures for malfunctions, startups,
and shutdowns for flares is preferred to
a fiction that a facility can maintain a
flare emission limit in all malfunction,
startup, or shutdown events regardless
of size or magnitude.
Response: See response to comments
II.D.3.(a), (b), (c), (d), and (e), above.
(g) Comment (YVAS): Specific to
flaring emergencies by the sources, any
added controls on flaring to protect the
public (from SO2 exceedences) is
essential and is common sense.
Response: We acknowledge the
comment and support for our proposal.
4. Subject to NSPS
Comment (CHS Inc.) It should be
noted that the CHS refinery flare is
subject to NSPS Subpart J as a result of
the consent decree. This limits the H2S
content of the routine refinery fuel gas
streams routed to the flare and requires
monitoring to demonstrate compliance
with the limit.
Response: As indicated by the
commenter, the consent decree limits
the H2S content of the routine refinery
fuel gas streams routed to the flare.
However, there are several reasons why
the H2S ppm limit alone is not sufficient
to support the FIP’s attainment
demonstration.
First, flow information is needed to
translate H2S ppm values into pounds of
SO2 for a given period of time. Flow
rates to the flares can vary widely.
Without knowing potential worst-case
flows to the flare, we cannot determine
whether the consent decree H2S ppm
limit would assure compliance with the
FIP 150 pounds of SO2/3-hour limit at
the 3 refineries. Therefore, we cannot
conclude that the consent decree H2S
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limit, even absent the additional
concerns we discuss below, would
assure attainment of the SO2 NAAQS.
Second, during certain situations, as
indicated in 40 CFR 60.8(c) and
60.104(a)(1), the H2S limit does not
apply. Specifically, the consent decree
indicates that the CHS Inc. refinery flare
is an affected facility under 40 CFR part
60, subparts A and J for fuel gas
combustion devices and that fuel gases
combusted in the refinery flare shall
comply with the emission limit of 40
CFR 60.104(a)(1). However, 40 CFR
60.104(a)(1) exempts process upset
gases and certain types of fuel gas from
the emission limit. Additionally, the
provisions in 40 CFR 60.8(c) indicate
that emissions in excess of the level of
the applicable emission limit during
periods of malfunction, startup, and
shutdown shall not be considered a
violation of the applicable emission
limit unless otherwise specified in the
applicable standard. Emission limits for
demonstrating attainment and
maintenance of the NAAQS must apply
at all times. (See responses to comments
II.D.1.(b) and II.D.2.(a), above, and
reference document RRR.)
Third, the alternative monitoring plan
(AMP), that was approved pursuant to
the consent decree and NSPS
requirements (see reference document
LLLLLL) for the refinery flare fuel gas
combustion device, primarily relies on
quarterly measurement of the H2S
content of some of the refinery fuel gas
streams that go to the flare using stain
tubes; more frequent measurement may
be required for a limited time depending
on the concentration measured.
Although this may be acceptable under
the terms of the consent decree and the
NSPS, we believe more frequent testing
is necessary for determining compliance
with an emission limit set to assure
attainment and maintenance of the
NAAQS.
5. Affirmative Defense/1999 Excess
Emissions Memorandum
(a) Comment (WSPA): The availability
of an affirmative defense is desirable.
Even though EPA may allow for the
assertion of affirmative defenses, the
affirmative defense would only be
allowed for the mitigation of penalties.
This is an unreasonable position in
which to place refiners subject to the
proposed requirements.
Response: We are providing an
affirmative defense to penalties in the
final rule, but not to injunctive relief.
This is consistent with the Clean Air
Act interpretations expressed in our
1999 excess emissions memorandum.
See reference document RRR. We
believe it is reasonable to retain the
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authority to seek injunctive relief for all
exceedances of emission limits so that
we remain able to protect the NAAQS,
regardless of source ‘‘culpability’’ for
any specific exceedance.
We note that in our proposed FIP
preamble, we invited comment
regarding whether it would be
appropriate to extend an affirmative
defense to the FIP sources for
exceedances of their flare limits during
malfunctions, startup, and shutdown.
See 71 FR 39264, July 12, 2006. There
we said the following:
‘‘We do interpret the CAA to allow owners
and operators of sources to assert an
affirmative defense to penalties in
appropriate circumstances, but normally we
would not view such an affirmative defense
as appropriate in areas where a single source
or small group of sources has the potential
to cause an exceedance of the NAAQS. See
1999 policy statement. We solicit comment
on whether it would be appropriate to
include in our final FIP the ability to assert
an affirmative defense to penalties only (not
injunctive relief) for violations of the flare
limits.’’
We have decided to provide an
affirmative defense for violations of the
flare limits during malfunction, startup,
and shutdown. We believe this
represents a deviation from our 1999
excess emissions memorandum because
in the Billings/Laurel area, one or more
of the FIP sources may have the
potential to cause an exceedance of the
SO2 NAAQS. In the unique
circumstances of this FIP, with the rule
language we are adopting, we believe a
deviation from the 1999 excess
emissions memorandum is warranted.
For example, we have included rule
language that indicates the affirmative
defense is not available if, during the
period of the excess emissions, there
was an exceedance of the SO2 NAAQS
that could be attributed to the emitting
source. At least one other EPA Region
has approved an affirmative defense
provision with this language. See
Maricopa County Rule 140 (reference
document ZZZZZ), which Region 9
approved on August 27, 2002 (67 FR
54957) (reference document AAAAAA).
Although not identical to the 1999
excess emissions memorandum, this
rule language should provide a
significant incentive to the facilities to
take steps to avoid and reduce flaring
whenever possible.
Also, based on our experience since
the 1999 excess emissions
memorandum was issued, we believe
that the elements of the affirmative
defense delineated in the 1999 excess
emissions memorandum, which
elements we have adopted in this FIP,
provide a very significant incentive for
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facilities to do all they can to comply
with their emission limits. It is not clear
that the incentive is significantly
different than would be present under a
traditional enforcement discretion
approach, particularly when sources
assume that enforcement action will
rarely be taken for infrequent or small
violations. Finally, we have considered
industry comments regarding safety
concerns, and while we do not agree
that emissions from flares should be
treated entirely differently from
emissions from stacks and other points,
we think our resolution of this issue
appropriately and reasonably addresses
industry concerns.
(b) Comment (WETA): Any flare
emission limitations should include, at
the least, an allowance for an affirmative
defense for malfunction, startup, and
shutdown circumstances.
Response: See response to comment
II.D.5.(a), above.
(c) Comment (NEDA/CAP): EPA
should adopt a broad affirmative
defense for penalties and injunctive
relief for malfunctions as part of the
mass emission limit for flares. MPA
indicated that the FIP should not be
adopted in the proposed form because
the failure to include an affirmative
defense for flaring resulting from
malfunctions poses a significant safety
risk to employees and the public with
no corresponding benefit.
Response: See response to comment
II.D.5.(a), above.
(d) Comment (NEDA/CAP): NEDA/
CAP is concerned about the potential for
EPA’s establishment of any precedent
with regard to limiting the availability
of affirmative malfunction defenses in
nonattainment areas generally. NEDA/
CAP is also concerned with the
application of the 1999 Malfunction
Policy in the Billings/Laurel proposed
FIP because the Policy has never been
subject to notice and comment
rulemaking, but the application of the
policy results in clear legal
consequences for regulated entities in
contravention of Appalachian Power v.
EPA, 208 F.3d 1015 (D.C. Cir. 2000).
Response: See response to comment
II.D.5.(a), above. Also, we respectfully
disagree with the commenter that we are
contravening the Appalachian Power
case holding. In our proposal, we
proposed that the flare limits would
apply at all times but took comment on
the application of an affirmative defense
to penalties for those limits. In this final
rulemaking, we have decided to provide
the affirmative defense to penalties. The
commenter had a full opportunity to
comment on our proposal, which
included a discussion of our
interpretations of the CAA with respect
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to the treatment of excess emissions
during malfunction, startup, and
shutdown. See 71 FR 39264, col. 1, July
12, 2006. We have considered the
commenter’s comments along with all
other comments.
(e) Comment (NEDA/CAP): NEDA/
CAP is also concerned that EPA has
made no demonstration that ‘‘a single
source or small group of sources has the
potential to cause an exceedence of the
NAAQS,’’ or that the NAAQS in this air
basin is in fact, any more vulnerable to
a NAAQS exceedence from these
sources than any other nonattainment
areas is from a small group of sources.
If finalized, the failure to provide an
affirmative defense for malfunctions
would be entirely arbitrary and
unreasonable. Moreover, as a national
precedent with severe legal
consequences for sources in other
nonattainment areas, adoption of this
proposed FIP provision would be highly
vulnerable to legal challenge for failure
to meet the Clean Air Act’s notice and
comment procedures under a federal
court’s recent decision in
Environmental Integrity Project v. EPA,
425 F.3d 992 (D.C. Cir. 2005).
Response: In our final action, we are
providing an affirmative defense to
penalties for the flare limits. We
disagree with the commenter’s assertion
regarding notice and comment
procedures; we believe we have met all
applicable requirements and provided
fair notice regarding our intentions in
our notice of proposed rulemaking. We
proposed that the flare limits would
apply at all times and also invited
comment on whether it would be
appropriate to extend an affirmative
defense for the flare limits to the four
sources subject to the FIP. Our final
action is a logical outgrowth of our
proposal; we have decided to provide an
affirmative defense to penalties for
violations of the flare limits during
malfunction, startup, and shutdown.
While our action on this FIP may have
some impact on other SIPs and FIPs
based on the logic we have applied, our
rule is only directly applicable to the
four sources subject to the FIP. It is
possible EPA may reach a different
decision in future rulemaking.
(f) Comment (API, COPC, MSCC,
ExxonMobil): While EPA’s 1999
Malfunction policy does state EPA’s
position that affirmative defenses are
not appropriate ‘‘where a single source
or small group of sources has the
potential to cause an exceedence of the
NAAQS,’’ API and others are unaware
of any instance where EPA has utilized
this exception from its general policy
allowing for the assertion of affirmative
defenses during malfunctions. In this
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case, EPA has made no demonstration to
justify an exception to the general
allowance for affirmative defenses for
malfunction events. Consequently, API
urges EPA to allow the assertion of
affirmative defenses in the final FIP.
Additionally, ConocoPhillips indicated
that because of the harsh consequences,
EPA should only apply this exception to
its policy where it is clearly
demonstrated that there is very real,
extended potential for a single or small
group of sources to cause an exceedence
of the NAAQS. This is not present in
this case. In fact, actual monitoring has
shown that even during malfunction,
ambient NAAQS violations do not
occur. ConocoPhillips urges EPA to
allow the assertion of affirmative
defenses for both penalties and
injunctive relief in the final FIP.
Response: See our prior responses to
comments II.D.5.(a), (d), and (e). Also,
we note that on two occasions, one in
1985 and one in 1995, flaring resulting
from malfunctions at ConocoPhillips
caused ambient exceedances of the SO2
NAAQS (see reference documents
DDDDDDD and EEEEEEE).
(g) Comment (NEDA/CAP, MSCC):
The proposed FIP appears to
misinterpret the 1999 Malfunction
Policy. The July 12 preamble for
adoption of the FIP appears to suggest
that prosecutorial discretion would
never be allowed in a nonattainment
area where the agency decides that ‘‘one
or a group of sources are directly
implicated in nonattainment of a
NAAQS.’’ In fact, the 1999 Policy
recommends that such situations have
to be addressed in the underlying
standards themselves through narrowlytailored SIP revisions. Moreover, in no
event does the 1999 Malfunction Policy
ever prohibit the use of prosecutorial
discretion.
Response: Enforcement discretion or
prosecutorial discretion is always
available. The question in this case was
whether it was appropriate to codify an
affirmative defense, which we have
done in our final rule. We have not
misinterpreted our 1999 policy.
(h) Comment (NEDA/CAP, API):
There is no rational basis in the
proposed FIP or the 1999 Malfunction
Policy to limit the affirmative defense to
penalties. NEDA/CAP asserts that such
a limitation is not reasonable since the
malfunction condition during which the
exceedence of the applicable limitation
occurs would be unavoidable.
Response: We respectfully disagree.
There could be instances in which
malfunctions are unavoidable based on
current plant layout and operating
parameters but in which some form of
corrective action would still be
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appropriate. We cannot predict the
exact nature of those circumstances, but
protection of the NAAQS and public
health is not an intermittent obligation;
we are required to assure attainment
and maintenance of the NAAQS at all
times, not just when sources are in
normal operation mode or when
attainment is convenient. See, e.g., City
of Santa Rosa v. EPA, 534 F.2d 150 (9th
Cir. 1976), vacated and remanded on
other grounds sub nom. Pacific Legal
Foundation v. EPA, 429 U.S. 990 (1976)
(‘‘ ‘Neither EPA nor this court has any
right to decide that it is better to
maintain pollutants at a level hazardous
to health than to require the degree of
public sacrifice needed to reduce them
to tolerable limits’ ’’, citing South
Terminal Corp. v. EPA, 504 F.2d 646, at
656 (1st Cir. 1974); South Terminal
Corp. v. EPA, 504 F.2d 646, 675 (1st Cir.
1974) (‘‘[I]t seems plain that Congress
intended the Administrator to enforce
compliance with air quality standards
even if the costs were great.’’) Preserving
injunctive remedies ensures that we
remain able to protect air quality
standards and PSD increments in
accordance with our fundamental
responsibilities under the CAA. See
CAA sections 110(a) and (l), 42 U.S.C.
7410(a) and (l). See, also, the discussion
of this issue in our 1999 excess
emissions memorandum, reference
document RRR.
(i) Comment (MSCC, ExxonMobil): An
exception and affirmative defense
should be available under the FIP that
is at least consistent with the consent
decrees executed by EPA and the State
of Montana with most of the affected
sources.
Response: As we have noted
previously, the consent decrees and the
FIP serve different purposes. We have
adopted an affirmative defense
provision that is consistent with the
protection of the NAAQS.
(j) Comment (Citizen): On page 39264
is the statement ‘‘We are proposing that
the flare limits will apply at all times
without exception.’’ Laudable as that
seems, EPA then subsequently states,
‘‘We solicit comment on whether it
would be appropriate to include in our
final FIP the ability to assert an
affirmative defense to penalties only
(not injunctive relief) for violations of
flare limits.’’ If the former statement is
accepted, what are the penalties for
exceeding flare limits and how will they
be imposed and will the public be
advised which refinery exceeds a flare
limit and how often could that happen
to the detriment of air quality in this
area?
Response: In this final rulemaking
action, we have promulgated an
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affirmative defense to penalties for
exceedances of the flare limits during
malfunction, startup, and shutdown.
Under this approach all excess
emissions are considered violations.
However, if we or anyone else brings an
enforcement action, the facility may
then assert the defense to penalties. To
establish the defense, the facility must
demonstrate to the judge that it took
appropriate steps to avoid the excess
emissions and met other requirements,
the details of which are contained in our
final rule. If the facility cannot establish
the defense, it may be subject to CAA
penalties up to $32,500 per day. We do
not typically advise the public when a
limit is exceeded or which facility has
exceeded a limit, although we often
alert the public through the press when
we bring an enforcement action. Under
the FIP, the subject sources must submit
reports to EPA identifying their
emissions. Those reports are available to
the public through the Freedom of
Information Act (FOIA). The
establishment of flare requirements
should help reduce flaring incidents.
6. Installation of Additional SO2
Reduction Equipment
Comment (ExxonMobil): EPA’s
proposed FIP does not allow for time for
the design and installation of facilities
necessary to comply with the proposed
flare emissions limitations. The
facilities required for compliance with
the proposed FIP go above and beyond
what was built for the SIP or what will
be built for the Consent Decree. For
EPA’s proposed FIP, the required
controls have not yet been identified.
Response: It is not clear what facilities
the commenter is envisioning. Without
greater detail, it is difficult to respond
to the comment. However, the FIP
imposes no specific requirement for the
sources to install control equipment to
limit flare emissions, and the limit we
are imposing is the same one the State
imposed on the sources, and which
continues to be included in their
permits. Our expectation is that sources
will take all steps within their control
to avoid flaring events and minimize
their impacts on air quality if they do
occur.
To the extent that the commenter is
referring to the time needed to design
and install flare monitoring systems
required by the FIP, we have extended
the deadline for installation from 180
days to 365 days after EPA approval of
the flare monitoring plan.
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E. Concerns With Dispersion Modeling
1. Policy Issues
(a) Comment (MSCC, ExxonMobil):
Out-of-Date and Invalid Model Choice.
(i) The proposed FIP uses the same
model as that used in the SIP. EPA’s
models have changed since the time the
SIP was developed. It is inappropriate to
propose and justify more restrictive
requirements on sources without
considering more current modeling
techniques and requirements. The older
model may be more appropriate to
confirm an existing situation or permit
minor changes. However, the FIP goes
beyond minor changes.
Response: The commenter is correct
that a newer model is now available. For
new SIPs, we would require states to
use EPA’s most recent model. However,
this is a unique situation. The State
developed the Billings/Laurel SO2 SIP
using the ISC model, which was current
at that time, and we approved various
source-specific emission limits in the
SIP based on the State’s modeling effort.
The purpose of this FIP is to fill gaps in
the approved SIP. We are not intending
or required to re-do the entire SIP. See,
e.g., section 302(y) of the CAA, 42
U.S.C. 7602(y) (‘‘Federal
implementation plan’’ means a plan (or
portion thereof) promulgated by the
Administrator to fill all or a portion of
a gap or otherwise correct all or a
portion of an inadequacy in a State
implementation plan * * *’’); McCarthy
v. Thomas, 27 F.3d 1363, 1365 (9th Cir.
1994) (A FIP is ‘‘a set of enforceable
federal regulations that stand in the
place of deficient portions of a SIP.’’)
Accordingly, we think it is reasonable to
rely on the same model the State used
to develop the SIP. That way, all
emission limits in the SIP and FIP will
have been established on the same basis.
We note that MDEQ tested the
performance of the ISC model when the
Billings/Laurel SO2 SIP was being
developed, and the results showed that
the model performance exceeded the
performance criteria for models of this
type. The FIP modeling represents a
minor change to MDEQ’s basic
approach. The sources in the SIP
modeling are characterized in the
modeling inputs as 25 point and volume
sources and, except for minor
corrections provided by the sources, the
major FIP-related change in modeling
involves only one source: The MSCC
100-meter stack. We had to change the
inputs for MSCC’s 100-meter stack
because the State gave too much stack
height credit to MSCC’s stack in the SIP
modeling, and we, consequently,
disapproved MSCC’s SIP emission
limits and the SIP attainment
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demonstration. Otherwise, the FIP
modeling uses meteorology data,
receptors, and stack parameters for
sources other than MSCC that are nearly
identical to those used in the SIP
modeling.
We also note that ISC remained an
accepted EPA model at the time we
proposed our FIP, and it is reasonable
to finalize the FIP based on the same
model. Switching models after our
proposal would have required us to repropose the FIP and would have
delayed the FIP further.
(ii) A newer model, ‘‘AERMOD,’’ has
been adopted as the EPA regulatory
default model. It is clear that AERMOD
is now preferred for regulatory use over
the model used in the SIP development.
Consideration needs to be afforded to
models available today, and particularly
to the model reasonably believed to give
the most accurate results. The
stakeholder process should be used to
determine which dispersion model
should be used for the FIP
(ExxonMobil).
Response: See our response to
comment II.E.1.(a)(i), above. We also
note that AERMOD has more complex
software than ISC and, as a result, it
would be extremely difficult to perform
the 1320 model simulations necessary to
establish emission limitations that
would address buoyancy flux variations
that were included in the State’s SIP. A
stakeholder process is not required by
the CAA and would merely serve to
delay issuance of the FIP.
(b) Comment (MSCC): Out-of-Date
Model Input. Any dispersion modeling
used for the proposed FIP must include
improved techniques regarding building
downwash. A new method for
calculating the downwash effects
buildings have on predicted ambient
concentrations has been developed. The
new technique is known as ‘‘Plume Rise
Model Enhancement’’ (PRIME)
algorithm. This technique is now
commonly in practice in both ISC–
PRIME and AERMOD. EPA’s FIP
modeling does not use this technique.
Response: The PRIME downwash
technique was never formally adopted
by EPA for use in ISC. In order for states
to employ this technique, EPA regional
offices needed to authorize its use on a
case-by-case basis until ISC was
replaced as the reference model on
December 9, 2006. The plume rise
technique used in ISC was the
recommended approach at the time the
State developed the SIP, and the
technique served the modeling
community well for many years.
(c) Comment (MSCC, ExxonMobil):
Modeling Violates EPA’s Own
Requirements. The modeling used for
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the proposed FIP does not meet EPA’s
own guidelines and requirements
because of the model used, lack of
current building profile, and numerous
other problems found elsewhere.
Response: See our response to
comment II.E.1.(a)(i), above. The
modeling approach was extensively
discussed with regulatory agencies and
the public when the SIP was developed,
and the ISC-based modeling approach
met the requirements of EPA’s
Guideline on Air Quality Models.
(d) Comment (MSCC): Modeling File
Naming Convention. EPA’s modeling
files and Technical Support Document,
both contained in the docket, do not
provide a reference to the naming
conventions used in the modeling effort.
While it is possible to dissect some of
the naming conventions, it was not
possible to discern each and every file
and its purpose. Therefore, the
reviewers are not certain that all the
modeling attempts, purposes and
nuances have been accounted for in the
analysis. The commenter recommends a
more complete description of the
naming convention and the purpose
behind each modeling effort needs to be
explained.
Response: At the recommendation of
industry, MDEQ allowed the use of
buoyancy flux in establishing emission
limits, which made the modeling far
more complex. As a result, many more
modeling files are included than is
typically the case in SIP modeling
applications. To improve
documentation, some extraneous
modeling files have been removed and
a text file added to explain naming
conventions. The naming convention
used for the Billings/Laurel SO2 FIP
modeling files is typical of that used by
the modeling community. To a modeler,
the naming convention helps define the
purpose behind the modeling effort. On
July 13, 2007, the revised modeling files
were indexed in the electronic docket
contained on https://
www.regulations.gov, and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF.
(e) Comment (MSCC, ExxonMobil):
Out-of-date and Invalid Emissions
Rates. Federally enforceable emission
rates from refinery consent decrees have
not been included in the FIP modeling.
EPA has used 10-year-old emission
inventory data that compromise the
accuracy of the results. Reductions that
have occurred in the past ten years have
been ignored. The settlement documents
related to the 1998 SIP contain
requirements that substantially change
the SO2 emission limits, and, therefore,
the results of any modeling
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demonstration (ExxonMobil). Without
including these existing emission
reductions from the SIP and near term
future reductions from consent decrees,
EPA’s proposed FIP ignores state and
federally enforceable SO2 emission
reductions already in place.
Response: See our responses to
comments II.A.2.(b), II.B.2.(d) and II.D.4.
The FIP modeling accounts for the
limits that we approved in the Billings/
Laurel SO2 SIP and those we are
promulgating in the FIP. We cannot
include State requirements that were
not submitted with the SIP.
Additionally, the ExxonMobil consent
decree limits have not been translated
into short term emission limits by
MDEQ and made a part of the SIP. Short
term emission limits are required to
ensure compliance with the 3-hour and
24-hour average SO2 NAAQS. Also, the
consent decrees do not address all of the
stacks/sources involved in the SIP/FIP.
(f) Comment (MSCC): MSCC has
concerns with using the SIP modeling.
The predecessor model routines had
been discredited (‘‘invalidated’’) in this
valley following a study done years
earlier by the State. The model, even in
the 1990’s, did not represent state of the
art in modeling science and was
admittedly prone to serious overpredictions, particularly in so-called
intermediate and complex terrain.
Response: As noted above, the
modeling was EPA’s preferred model at
the time of the SIP, has been validated
for use in the Billings/Laurel area, and
has been used extensively throughout
the United States in setting emission
limits for nearly two decades. The
model has not been ‘‘invalidated’’ for
use in the Billings/Laurel area. See also
our discussion of related issues in our
May 2, 2002, final action on the
Billings/Laurel SO2 SIP, 67 FR 22168,
22183.
(g) Comment (ExxonMobil): Only the
current actually existing emission
sources with proper geographical
coordinates should be used as inputs to
the dispersion model.
Response: We do not understand what
the commenter is referring to when they
indicate ‘‘only the current actually
existing emission sources * * * should
be used as inputs to the dispersion
model.’’ With respect to geographical
coordinates used in the modeling, they
were provided by the sources in
response to EPA’s CAA Section 114
information request. The incorrect
source coordinate for MSCC in the
modeling files has been corrected.12 On
12 In reference document WW, Technical Support
Document, Dispersion Modeling to Support Sulfur
Dioxide (SO2) Emission Limits in Federal
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July 13, 2007, the revised modeling files
were indexed in the electronic docket
contained on https://
www.regulations.gov and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF. To the
extent the commenter is asserting that
actual emission rates should be used as
inputs to the dispersion model, we
respectfully disagree. As described more
fully in our response to comment
II.E.1.(e), above, potential emissions
rather than actual emissions are used in
SO2 attainment demonstrations, per
longstanding EPA policy and 40 CFR
part 51, Appendix W requirements.
Accordingly, in our attainment
demonstration, we modeled the
emission limits we approved in the SIP
and any new emission limits we are
promulgating in the FIP. Thus, with the
exception of certain units at MSCC, we
modeled the same emission rates that
the State used in its SIP modeling.
(h) Comment (ExxonMobil): Only the
verified actual stack heights should be
used as inputs to the dispersion model.
Response: Stack height regulations
determine the stack height values that
are used as inputs to dispersion models
in SIP attainment demonstrations. In
some cases this value may not be the
same as the actual stack height. See 40
CFR 51.118. For example, under our
stack height regulations, 65 meters is the
appropriate stack height value for
MSCC’s SRU stack, even though the
stack is 100 meters tall. We believe we
have used the correct stack height
values in all cases, and the commenter
did not indicate that any specific stack
Implementation Plan (FIP) for Billings/Laurel,
Montana, June 2006, we indicated that one
suggested change that was not incorporated into the
EPA FIP modeling involved the coordinate system
used in the model to identify source location.
MDEQ developed the original source locations
based on the UTM NAD27 (North America Datum
of 1927) coordinate system, and EPA has retained
that coordinate system in our modeling. It appeared
that several of the suggested changes to source
locations were based on NAD83 values. The newer
coordinate system can affect source locations by up
to 200 meters. In dispersion modeling on the scale
of the current modeling domain, consistency
between the source and receptor locations is the
most important consideration. For this reason,
suggested changes that appeared to be based on the
NAD83 were not included in the modeling.
However, changes that address local inconsistencies
in measured distances between fixed stacks (such
as at MSCC) on a specific property were
incorporated in EPA’s modeling using UTM
NAD27. Sensitivity testing of the model showed
that even the NAD27/NAD83 differences did not
significantly affect total predicted concentrations;
the principal effect was, in some instances, to shift
the location of the maximum impact to a different
receptor. An electronic record (compact disk) of
EPA’s sensitivity testing of the model is contained
in the docket. See reference document EEE in
Docket Number EPA–R08–OAR–2006–0098.
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height value we used in our modeling
was incorrect.
(i) Comment (ExxonMobil): The
meteorological data to be used as input
to the dispersion model should reflect
the most representative information.
The meteorological set to be used
should be chosen based on availability
and based on those monitored
parameters that are best able to take full
advantage of the latest dispersion
modeling techniques.
Response: EPA believes that the
meteorological data from the Billings
airport that was used in the SIP/FIP
modeling is representative of conditions
within the modeling domain. The
Billings airport is located in an open
area with good exposure to prevailing
wind flow and has a long period of
record. Five years of historical weather
data (1984, 1986, 1987, 1988, and 1989)
were used in the modeling to ensure
that the full range of possible
meteorological conditions were
evaluated in the modeling. To our
knowledge the Billings airport data have
the longest period of record of any site
in the Billings area. When the State
developed the SIP modeling approach
that EPA has now used for the FIP, the
State tested ISC model performance
using the Billings airport data. That
evaluation showed acceptable model
performance.
(j) Comment (ExxonMobil): EPA
should be modeling emission rates to
levels that predict values slightly less
than the NAAQS. This modeling
concept is referred to as ‘‘pushing the
model to failure.’’ This approach is
designed to determine the maximum
emission limits allowed by regulation
under acceptable modeling protocol. By
proposing mass emission limits on
flares of 150 pounds of SO2 per 3-hour
period or 500 pounds of SO2 per
calendar day, EPA has chosen to use,
without further consideration, mass
emission limits that do not ‘‘push the
model to failure’’ but instead arbitrarily
limit the sources to mass emission
limits that go far beyond protecting the
NAAQS.
Response: Emission inputs to the
model were established using criteria
contained in 40 CFR part 51, Appendix
W, Section 8. The emission limits set by
the modeling analysis are based on
emission rates that would just meet the
NAAQS. They are not based on
‘‘arbitrary limits’’ that go ‘‘far beyond
protecting the NAAQS’’. For example,
with the limits we are establishing and
the SIP limits we approved, our
modeling resulted in a high value of 354
µg/m3 which would exactly meet the 24hour SO2 NAAQS of 365 µg/m3 when
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background concentrations of 11 µg/m3
are considered.
(k) Comment (MDEQ): Montana
continues to affirm the use of the ICS3
model.
Response: We acknowledge receipt of
the comment and the support for the
model used.
(l) Comment (ExxonMobil): EPA has
not used current accurate process and
meteorological inputs in its modeling.
This is contrary to EPA’s assurance in
its May 2002 final rule that: ‘‘Any future
modeling in the Billings/Laurel area
should incorporate all corrections. The
SIP limitations are based on the best
information available at the time the
attainment demonstration was modeled,
and the same will be true for any FIP
limitations that are developed.’’ 67 FR
22189. Also, in its May 2002 final rule,
EPA stated that: ‘‘We agree that future
modeling should include all corrected
data.’’ 67 FR 22189. However, EPA has
ignored critical factual data for purposes
of developing the proposed FIP.
Response: The commenter ignores the
context and meaning of EPA’s
statements in its 2002 SIP action. The
cited quotes were part of our response
to specific comments from one source
that there were errors in the State
modeling numbers used for that source’s
stack parameters. The comment was:
‘‘CEMS data now indicate an error in
the assumed buoyancy flux for MSCC’s
main stack; the current modeling
protocol contains an assumption which
significantly underestimates the average
rise in emissions. Any revised modeling
should correct this assumption.’’ 67 FR
22189. We were merely agreeing that
future modeling should include
corrected stack parameters based on
CEMS measurements: ‘‘CEMS
measurements of flow and temperature
data provide the best estimates of stack
parameters, and values based on CEMS
data should be used in any future SIP
modeling for Billings provided the
CEMS data are accurate.’’ Id. We were
not indicating we would use a new
model, different meteorological data, or
consider entirely new structures. In fact,
on the same page of our 2002 notice, we
said the following:
‘‘In addition, dispersion models and data
bases are continually being improved. The
task of demonstrating attainment could never
be completed if we or the State were
compelled to update the analysis with each
new refinement. For the FIP, we intend to
continue to use ISC2 as the applicable model
to fill in the gaps in the State’s attainment
demonstration created by our disapproval of
the emission limitations for MSCC’s 100meter stack. Some source parameters have
been corrected since the 1994 modeling
analysis (see Response V.D.4.(d), above), but
we intend to use the same meteorological
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data and modeling protocols the State used,
so that the results will be comparable.’’
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For a more complete discussion of our
basis for selecting the model and data
inputs we have used, please refer to the
other responses to comments in this
section II.E, our proposed FIP, and our
TSD for the proposed FIP.
2. Technical Issues
(a) Comment (MSCC, ExxonMobil):
Incorrect Source Location. The location
of the small boiler stacks at MSCC that
are modeled as a volume source is
incorrect. The error occurs by the nature
in which the X and Y coordinates are
entered into the SRI file. The entry is off
by one column.
Response: This has been corrected.
On July 13, 2007, the revised modeling
files were indexed in the electronic
docket contained on https://
www.regulations.gov and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF.
(b) Comment (MSCC): Incorrect
Emission Rate. Table 2 of EPA’s
Dispersion Modeling Technical Support
Document shows the modeling value of
136.21 g/sec for MSCC’s SRU-100-meter
stack. An emission rate of 150.0 g/sec
was modeled in the majority of the EPA
modeling. If the proposed emission
limit of 3003.1 lb/3-hours (126.13 g/sec)
is correct, then the number that should
appear in both the table and the input
files is 126.13 (g/sec) to be consistent
with the emission limit.
Response: In the State’s original SIP
modeling submittal there were 1,320
modeling scenarios with various
buoyancy flux combinations that were
tested, and it was determined that only
a few of these resulted in concentrations
that threatened the NAAQS. EPA
conducted screening to eliminate the
need for refined modeling of those
scenarios where the NAAQS were not
threatened. The 150 g/sec emission rate
was used provisionally to determine
which modeling scenarios would result
in the maximum ground level
concentrations, and was not used to set
MSCC’s proposed emission limit. Once
the appropriate modeling scenarios
were determined by EPA, only those
scenarios were used to conduct the
refined modeling to establish an
emission limit of 126.13 g/sec. The
commenter is correct that there is a
discrepancy between Table 2 in EPA’s
Dispersion Modeling Technical Support
Document (reference document WW)
and the modeling input files. The input
files for the limited modeling scenarios
reflected the correct value, 126.13 g/sec.
Table 2 of the TSD contains the wrong
value.
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(c) Comment (MSCC, ExxonMobil):
Missing Modeling Files. Three source
input files (SRI files) were not included
in Reference Document EEE, the basis
for the modeling conclusion and the
proposed emission limit for MSCC’s 100
meter stack. It appears that these files
were actually used in model runs.
Response: We have added the
referenced modeling files. On July 13,
2007, the revised modeling files were
indexed in the electronic docket
contained on https://
www.regulations.gov and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF.
(d) Comment (MSCC, ExxonMobil):
Hanging Modeling Files. A source input
file (ref_5t.sri) is included in Reference
Document EEE. However, this input file
does not appear to be used in any input
(RUN) and output files (OPF) files. It is
not possible to comment effectively on
the adequacy of the model without
knowing the file’s purpose.
Response: This was a test file
inadvertently included in the electronic
record. It has now been deleted. On July
13, 2007, the revised modeling files
were indexed in the electronic docket
contained on https://
www.regulations.gov and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF.
(e) Comment (MSCC, ExxonMobil):
Outdated Building Profile Data. The
dispersion modeling runs do not
contain up-to-date information
regarding building profile data. EPA’s
use of 10-year old historical data is not
logical considering the agency requested
and received certain building data in its
December 2003 request.
Response: Building profile data were
current at the time the MDEQ prepared
the SIP. EPA is not updating the inputs
to reflect recent changes in building
dimensions or changes in dispersion
models. We are simply correcting
deficiencies in the MDEQ’s SIP
modeling. If we were to follow the
commenters’ suggestion, we would have
to revisit the entire SIP, including SIP
limits we approved. The CAA does not
require us to re-open the entire SIP. See
response to comment II.E.1.(a), above.
(f) Comment (MSCC): Variable ‘‘HB’’
and ‘‘PW’’ Not Used. In order to execute
the FIP model, EPA requested source
specific information including the
modeling terms HB and PW. These
values may be input into the IGM
model, however, this information is
superseded by direction-specific
building parameters by the model while
executing in all cases (stacks) of interest.
In other words, the data that was coded
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by EPA in the model runs were ignored
by IGM (in favor of other information)
and therefore of no value. Instead,
specific building data (discussed above)
should have been entered into the
program. There is at least one
substantial building, the YELP coke
barn, that should have been included in
the 2006 model runs.
Response: See responses to comments
II.E.1.(a) and II.E.2.(e), above. As noted
above, to the extent possible, EPA is
using the model inputs and model
settings selected by the State at the time
of SIP preparation and used in the IGM
code. The model input selections reflect
modeling practice and conditions at the
time of the SIP. The coke barn did not
exist at the time the SIP was prepared.
HB and PW values reflect the
dimensions of the facilities that had
large structures nearby and that MDEQ
included for downwash processing in
their SIP modeling. While the
commenter is correct that, in the IGM
model, these values were superseded by
other data, obtaining these values was
useful to us as a screening tool, and
inputting these values into the model
did not affect the validity of the results.
(g) Comment (MSCC, ExxonMobil):
Compliance Analysis Not Valid. The FIP
proposal notes that there is a ‘‘trigger
point’’ of 500 lb/calendar day in various
‘‘settlements’’ between EPA and
refineries. The proposal goes on to
assert that a modeling analysis was
conducted assuming the flares emitted
SO2 at a rate of 500 lb/3-hours and that
the model demonstrated compliance to
this alternative. A review of the
modeling files, however, indicates that
the ‘‘controlling’’ model run that
defined MSCC’s emission limit for the
100-meter stack (modeled at 65 meters)
did not include this 500 lb/3-hour flare
emission rate option.
Response: We solicited comment on
whether we should limit the flares to
500 lbs of SO2 per calendar day. We
have not adopted that option. But, for
purposes of the attainment
demonstration, we modeled the 500 lbs
as if it were emitted over a 3-hour
period rather than a calendar day. We
wanted to assure that if all the calendarday allowed emissions were emitted in
a 3-hour period, the 3-hour NAAQS
would still be protected. Those
modeling files are contained in the
docket.
However, the controlling model run
that defined MSCC’s emission limit for
the SRU 100-meter stack was for the 24hour NAAQS. There was no need to
model the 500 lbs of SO2/calendar day
to show compliance with the 24-hour
NAAQS since we had already modeled
the flares at 1200 lbs of SO2/calendar
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day. Since attainment of the 24-hour
NAAQS was shown at 1200 lbs of SO2/
calendar day, the area would still show
attainment at 500 lbs of SO2/calendar
day.
F. Miscellaneous Comments
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1. Stakeholder Process
(a) Comment (CHS Inc.): If EPA
intends to regulate malfunctions,
startups, and shutdowns, a stakeholder’s
process should be used to accurately
develop a reasonable flare limit.
Response: EPA announced its
proposed FIP in the Federal Register on
July 12, 2006, invited public comment,
and identified the time and place for a
public hearing. A public hearing was
held in Billings, Montana, on August 10,
2006. Only one person from industry
spoke at the hearing. Prior to the hearing
and at the hearing itself, no one
mentioned the concept of a stakeholder
process. In addition, we provided nearly
four months for the affected facilities
and other members of the public to
submit written comments and
suggestions regarding our proposed FIP,
including a substantial extension to our
original 60-day comment period in an
attempt to reasonably accommodate
State and industry requests. We have
made a number of changes in response
to comments received. If the affected
facilities had other ideas about how we
could better structure the FIP, they had
ample opportunity to express those
concepts.
We have complied with the
requirements of the CAA as set forth in
section 307(d) regarding public
participation for the FIP. We are not
required to hold a stakeholder process.
Issues regarding malfunctions, startups,
and shutdowns are addressed above.
(b) Comment (CHS Inc., ExxonMobil,
MPA): It would be in the best interest of
all involved that a stakeholder process
be used to determine what, if any,
enhancements to the Montana SIP are
appropriate.
Response: See response to comment
II.F.1.(a), above.
(c) Comment (WETA, COPC): If the
EPA feels strongly that consideration
should be given to different controls for
SO2, then a stakeholder process should
be utilized to consider issues and
relevant information in deciding if a
further SIP or FIP is necessary.
Response: See response to comment
II.F.1.(a), above.
(d) Comment (MSCC, ExxonMobil):
EPA has developed the proposed FIP in
a vacuum as to the affected parties. It is
inappropriate for EPA to not consult the
affected facilities in any meaningful
way. The process used by Montana in
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developing the SIP should be used in
the FIP. A stakeholder process will
allow all parties an opportunity to
ensure that the best available
information is considered in
formulating any proposed requirements.
Response: See response to comment
II.F.1.(a), above.
2. Ripple Effect
(a) Comment (WETA): The commenter
is concerned not only with the impact
of the FIP on the refineries in the area
but the potential ripple effect on the
businesses, workers, and other
consumers who daily use and depend
on the variety of products produced by
the petroleum refineries in the Billings/
Laurel area.
Response: We acknowledge the
commenter’s concerns. We recognize
that our FIP will result in costs to MSCC
and the refineries, which they may or
may not pass on to consumers. We have
tried to be sensitive to the costs MSCC
and the refineries may incur to meet the
FIP’s requirements, which potentially
would affect the costs of products to
consumers. For example, where we
determined less costly methods to
monitor SO2 concentrations could
achieve similar results, we are allowing
these other methods to be used.
However, our ultimate charge under the
CAA is to protect the SO2 NAAQS,
recognizing that cost impacts to sources
and consumers may occur. See, e.g., City
of Santa Rosa v. EPA, 534 F.2d 150 (9th
Cir.1976), vacated and remanded on
other grounds sub nom. Pacific Legal
Foundation v. EPA, 429 U.S. 990 (1976).
(b) Comment (citizen): The
commenter is a dryland farmer and uses
an ammonium sulfate (thiasol) fertilizer,
which is a by-product of the refinery
process. He says he is doing as much as
he can to be environmentally
conscientious and not introduce metals
into the soils found in other fertilizers.
This requires him to use the thiasol that
is refinery-produced. He requests that
EPA not exacerbate a bad situation for
agriculture, which increases costs to a
major industry which is marginal in
profitability and major in importance to
the State of Montana.
Response: See response to comment
II.F.2.(a), above.
3. Extend Comment Period
Comment (COPC, ExxonMobil, MSCC,
WETA, YCC): Commenters asked for
additional time to comment on the
proposed FIP, until at least December
11, 2006.
Response: The public comment
period on the FIP proposal ran from July
12, 2006, through November 3, 2006—
almost four months. Additionally, a
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21441
public hearing was held in Billings,
Montana, on August 10, 2006. EPA
believes it provided sufficient time and
opportunity for all commenters to
provide comments on the proposed FIP.
4. EPA’s Strategic Plan
Comment (COPC): The proposed FIP,
which contains inflexible flare emission
limits and strictly-specified monitor
installations requirements, is
inconsistent with EPA’s Strategic Plan,
which commits EPA to ‘‘finding
innovative solutions and collaborating
with others.’’
Response: We acknowledge the
commenter’s concerns. However, we are
charged with meeting the CAA’s
requirement to assure that the SO2
NAAQS are met and maintained.
Accordingly, the FIP adopts flare
emission limits and compliance
determining methods.
It should be noted that the discussion
on Innovation and Collaboration in the
‘‘2006–2011 EPA Strategic Plan,
Charting Our Course,’’ September 2006
(reference document BBBBBB), pertains
to complex environmental challenges
where broad-based problems cannot be
solved with conventional regulatory
controls. We do not think this is
relevant here. We are merely
establishing limits on flares and
methods to determine compliance with
those limits.
5. FIP Provisions in Title V Permits
Comment (MDEQ): Montana
acknowledges that the FIP provisions, if
promulgated, will be incorporated in
Title V permits. However, Montana
expects EPA will take the lead on
implementing and enforcing the FIP
provisions.
Response: EPA intends to assume
primary responsibility to implement
and enforce the FIP. However, the FIP
requirements will be ‘‘applicable
requirements’’ under Title V, which,
therefore, must be included in Title V
permits for the affected sources and be
enforceable by the State.
6. Length of Time it Took EPA To
Propose FIP
Comment (YVAS): Since the 1990
Clean Air Act requires NAAQS for SO2
to protect public health, YVAS deplores
this ‘‘inadequacy [sic] and ‘‘nonattainment’’ and deplores further that
the EPA did not adequately and in
timely fashion, take necessary steps to
enforce the CAA’s provisions to protect
the air quality in the Billings/Laurel
area in a reasonably suitable time period
regardless of any mitigating
circumstances. A specific justification
explaining this lapse in EPA’s
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responsibilities for not acting in the
public interest is essential to the
residents of the Billings/Laurel area
given that at the time, the Billings/
Laurel Sulphur Dioxide Area was
subject to excessive amounts—estimated
to be over 35,000 tons (1993)—of SO2
atmospheric pollution.
Response: We believe EPA’s SIP Call
and subsequent State and EPA actions
to address the SIP Call have helped
reduce SO2 emissions in the Billings/
Laurel area. There is no question that
this process has taken longer than it
should have.
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7. EPA Enforcement
Comment (YVAS): YVAS insists that
the EPA consistently monitor industry
emissions in order that industry sources
continue to comply with the SIP and/or
the ‘‘more stringent requirements under
other provisions of the CAA’’ or ‘‘SIPapproved permit programs.’’
Response: EPA intends to take the
lead in enforcing the emission limits
and monitoring requirements contained
in the FIP. Congress intended that states
have primary responsibility for
implementing and enforcing their SIPs.
Additionally, states may take the lead in
implementing and enforcing other CAA
programs (e.g., News Source
Performance Standards (NSPS),
Maximum Achievable Control
Technology (MACT) standards, Title V
permitting), either through EPA
delegation or program approvals. In the
latter cases, we have an oversight role
and may take enforcement action under
section 113 of the CAA for violations of
a SIP or other CAA requirements when
a state does not take action or when its
action is considered ineffective.
EPA Region 8 communicates regularly
with the MDEQ regarding sources. We
have regular meetings with MDEQ
regarding sources that are violating
emission limit requirements and discuss
the MDEQ’s proposed or ongoing
actions to address these violations. We
intend to continue to carry out our
oversight responsibility for the SIP and
other CAA requirements for the
Billings/Laurel sources. If we determine
that the MDEQ is not taking appropriate
action for violations of the SIP, or other
CAA requirements, we will take
appropriate action.
8. Further Emission Reductions
Comment (YVAS): Although the
industry is attaining lower yearly
decreases of SO2 since 1994, with
presumably a better and ‘‘healthier’’ air
quality in the area thereby, the
assumption logically follows that
industry should be required to comply
with further reduced SO2 release levels.
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Nowhere in this FIP is there an attempt
to address the issue of a further
reduction in the total emissions of the
industrial sources in the Billings/Laurel
area. Accordingly, YVAS believes that
all anti-lower SO2 emission arguments
are irrelevant against the demand for
protecting public health standards and
additional reduction of SO2 emissions is
mandatory under the CAA. Failing to
address a further SO2 emissions
reduction should be considered another
serious breach of your responsibility to
the Billings/Laurel public. Why did EPA
not include a discussion towards
reducing the total SO2 emissions in the
Billings/Laurel Sulphur Dioxide area in
this FIP and since EPA did not include
that discussion here, does EPA plan to
do that and if so, when?
Response: The 1970 CAA established
the air quality management process as a
basic philosophy for air pollution
control in this country. Under this
system, we establish air quality goals
(NAAQS) for criteria pollutants. States
develop control programs (termed SIPs)
to attain and maintain these NAAQS.
Our fundamental obligation in the SIP/
FIP context is to ensure that the NAAQS
are met, not reduce emissions to zero.
Thus a reduction of SO2 emissions is
mandatory only to the extent needed to
attain the NAAQS. However, under
section 116 of the CAA, states may
adopt and enforce any air pollutant
standard, limitation, or control
requirement so long as it is no less
stringent than that required by the CAA.
Put another way, states can require that
the air be cleaner than the NAAQS. Our
goal in the FIP is to ensure attainment
of the SO2 NAAQS.
9. SO2 NAAQS
(a) Comment (YVAS): Nowhere in this
FIP is any reference made to what clean
air standards should be under the CAA
or NAAQS. Commenters should have
been informed as to those standards in
this FIP in order to fairly judge as
acceptable or non-acceptable the release
standards proposed for the sources in
this FIP. How can the public adequately
comment on clean air issues when those
standards are unknown to the public?
Further, referring the general public to
sources where those standards would be
found is a disservice to the public since
many of those sources of such
information may be unattainable or
unavailable.
Response: The July 12, 2006,
proposed FIP did identify the 24-hour
and 3-hour SO2 NAAQS under the
modeling discussion (71 FR 39259,
starting at 71 FR 39270, col. 1). The SO2
NAAQS were previously established
(see discussion below), and EPA was
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not seeking comment on any changes to
the NAAQS in this FIP action.
Two sections of the CAA govern the
establishment and revision of NAAQS.
Section 108 (42 U.S.C. 7408) directs the
Administrator to identify pollutants
which ‘‘may reasonably be anticipated
to endanger public health or welfare’’
and to issue air quality criteria for them.
These air quality criteria are to ‘‘reflect
the latest scientific knowledge useful in
indicating the kind and extent of all
identifiable effects on public health or
welfare which may be expected from the
presence of [a] pollutant in the ambient
air.’’
Section 109 (42 U.S.C. 7409) directs
the Administrator to propose and
promulgate ‘‘primary’’ and ‘‘secondary’’
NAAQS for pollutants identified under
section 108. Section 109(b)(1) defines a
primary standard as one ‘‘the attainment
and maintenance of which, in the
judgement of the Administrator, based
on the criteria and allowing an adequate
margin of safety, [is] requisite to protect
the public health.’’ A secondary
standard, as defined in section
109(b)(2), must ‘‘specify a level of air
quality the attainment and maintenance
of which, in the judgement of the
Administrator, based on [the] criteria, is
requisite to protect the public welfare
from any known or anticipated adverse
effects associated with the presence of
[the] pollutant in the ambient air.’’
Welfare effects are defined in section
302(h), 42 U.S.C. 7602(h), to include
‘‘effects on soils, water, crops,
vegetation, manmade materials,
animals, wildlife, weather, visibility and
climate, damage to and deterioration of
property, and hazards to transportation,
as well as effects on economic values
and on personal comfort and wellbeing.’’
On April 30, 1971 (reference
document CCCCCC), the Environmental
Protection Agency (EPA) promulgated
primary and secondary NAAQS for
sulfur oxides (SOx) (measured as SO2)
(then codified as 40 CFR 410.4 and
410.5). The primary standards were set
at 365 micrograms per cubic meter (µg/
m3) (0.14 parts per million (ppm)),
averaged over a 24-hour period and not
to be exceeded more than once per year,
and 80 µg/m3 (0.03 ppm) annual
arithmetic mean. The secondary
standard was set at 1,300 µg/m3 (0.5
ppm) averaged over a period of 3 hours
and not to be exceeded more than once
per year. In accordance with sections
108 and 109 of the CAA, in the 1990’s,
EPA reviewed and revised the health
and welfare criteria upon which these
primary and secondary SO2 standards
were based. On April 21, 1993 (58 FR
21351) (reference document DDDDDD),
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EPA announced its final decision under
section 109(d)(1) of the CAA that the
revisions of the secondary SO2 NAAQS
were not appropriate at that time. On
May 22, 1996 (61 FR 25566) (reference
document EEEEEE), EPA announced its
final decision under section 109(d)(1) of
the CAA that the revision of the primary
SO2 NAAQS was not appropriate at that
time. EPA is currently reviewing the
primary and secondary standards again
to determine whether they should be
revised.
The Code of Federal Regulations
(CFR) is available at most public
libraries and on the internet at: https://
ecfr.gpoaccess.gov/. Likewise, the CAA
is also available at most public libraries
and on the internet at EPA’s Web site:
https://www.epa.gov/air/caa/.
(b) Comment (citizen): The rejection
of Montana’s Plan to control air quality
in the Billings/Laurel air shed 4 years
previously has left a serious gap in the
air quality in this air shed.
Response: We acknowledge this
comment. See response to comment
II.F.6., above.
10. SO2 Health Effects
(a) Comment (Citizen): The air is so
bad near the commenter’s house that
she needs to close the windows. She has
headaches and burning eyes and
sinuses. How safe is it for the families?
Commenter is concerned that air
emissions affect landscape and river
areas. Commenter would like EPA to
assure that refineries do not off-gas
unmeasureable blasts of pollution as she
has seen them do over her water,
county, and home.
Response: We acknowledge this
comment. The FIP, along with other
requirements contained in the SIP, will
provide an enforceable mechanism to
assure that the SO2 NAAQS in the
future will be protected in the Billings/
Laurel area. Since EPA initially
requested the State to revise the
Billings/Laurel SO2 SIP, actual SO2
emissions from companies have been
cut by more than half and there have
been measured improvements in air
quality. The SIP and FIP contain an
enforceable control strategy to help
ensure that the SO2 NAAQS are attained
and maintained.
(b) Comment (Citizen): Since national
air quality standards are more stringent
than Montana requires, serious health
risks to area residents is probable and
cannot be ignored.
Response: See response to comment
II.F.10.(a), above. Note that the State’s
ambient standards, in some cases, are
more stringent than the national
standards. Subchapter 2 of the
Administrative Rules of Montana (ARM)
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contains the Montana ambient air
quality standards (MAAQS). The
MAAQS are not contained in the
federally-approved SIP; the CAA does
not require that the standards be in the
federally-approved SIP. The SO2
MAAQS are contained in ARM 17.8.210
(see reference document FFFFFF) and
are as follows: (1)(a) Hourly average—
0.50 ppm, not to be exceeded more than
18 times in any 12 consecutive months;
(1)(b) 24-hour average—0.10 ppm, not to
be exceeded more than once per year;
and (1)(c) annual average—0.02 ppm,
not to be exceeded. The 24-hour and
annual SO2 MAAQS are more stringent
than EPA’s 24-hour and annual SO2
NAAQS. The State has a 1-hour average
SO2 MAAQS and EPA has a 3-hour
average SO2 NAAQS. The State does not
require that plans be developed to
assure attainment and maintenance of
the MAAQS, whereas, EPA does require
plans to assure that the NAAQS are
attained and maintained.
(c) Comment (Citizen): Commenter
works the evening shift near the
industrial sector and the refineries and
the coke plant. He notices that at night
the air becomes more sour. Depending
upon which way the wind is blowing or
whatever is occurring in the area, it will
burn his eyes and nose. It will start to
burn his lungs and inflame his chest
and it will make it harder for him to
breathe. The air is like a smoke-filled
barroom. He used to live in this area as
well. Commenter feels it degrades the
quality of his life. He’s standing up for
his lungs.
Response: See response to comment
II.F.10.(a)., above.
11. Public Process
(a) Comment (Citizen): Since there has
been no public disclosure of the EPA’s
plans for complying with the standards
(considered as minimal by local public
health advocates) as set forth in the
National standards (which also have not
been provided publicity to create public
awareness of those standards), the EPA
should not proceed with any rule
making unless the public receives an
opportunity to comment.
Response: EPA announced its
proposed FIP in the Federal Register on
July 12, 2006. In the July 12, 2006
Federal Register notice, EPA provided
for the opportunity of a public hearing.
A public hearing was held in Billings,
Montana on August 10, 2006. At the
hearing, EPA discussed its proposed
FIP. Additionally, EPA’s proposed
notice indicated that detailed
information regarding the proposed FIP
was available on the Internet. We have
complied with the requirements of
section 307(d) of the CAA regarding
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21443
public disclosure and the administrative
requirements for proposing the FIP. We
are announcing this final FIP in the
Federal Register as well. A discussion
of the SO2 NAAQS is provided above.
(b) Comment (Citizen): Plans for
controlling emissions ‘‘at the source’’
must be provided by the EPA at any
public meeting announced by the EPA
and those plans should be announced
publicly in advance of the meeting in
order for the public to understand what
the effects and results of such plans will
be on the air shed quality of the
Billings/Laurel metropolitan area.
Response: See response to comment
II.F.11.(a), above.
12. Stack Height
(a) Comment (Citizen): Included in
EPA’s emission control plans must be a
stringent requirement that none of the
three area refineries or the Montana
Sulphur and Chemical company may
construct any emissions stack or flaring
system of 100 meters or higher.
Information concerning the probable
effects, distance, wind patterns, content
etc. of the dispersal plumes of stacks of
this height should be provided to the
public at any hearing in order that
public comment on this crucial aspect
of the emission control plan may be
properly analyzed. Under no
circumstances should the 100-meter
height be considered as a minimum
permissible height by the EPA or by the
companies involved for any stack or
flaring system.
Response: EPA does not restrict the
physical height of a smoke stack. See 40
CFR 51.118(a). However, we do restrict
the credit a company receives for its
stack height in the modeling used to
determine whether a SIP will meet
national standards for specific air
pollutants. Id. The stack height credit is
based on the greater of the following: (1)
A height of 65 meters, (2) a height based
on a formula that considers the
surrounding buildings, or (3) a height
based on technical modeling studies
which show a certain height is
necessary to avoid high levels of
pollutants in the nearby area. See 40
CFR 51.100(ii).
EPA has rules that apply to tall stacks;
otherwise, companies could avoid
installing needed pollution control
equipment. Industry could simply build
higher stacks and emit into the air
additional pollutant levels that would
not violate local air quality standards,
but could eventually affect the air
quality of communities farther
downwind. This is because the higher
the stack height, the greater the
dispersion of pollutants and the less
likely they will reach the ground in the
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vicinity of the stack. EPA does allow
increases to stack height credits when
the stacks meet the conditions noted
above.
EPA disapproved part of the Billings/
Laurel SO2 SIP because MSCC’s stack
height credit did not meet the
conditions noted above. EPA believes
that the appropriate stack height credit
for the MSCC SRU 100-meter stack is 65
meters. The 65-meter stack height credit
was used in the modeling for the FIP.
We did not identify any other concerns
with the stack height credit used for
other sources in the SIP.
(b) Comment (Citizen): Studies,
including wind roses of the dispersal
pattern of all stacks of 65 meters and
higher should be provided to the public
at a hearing of the final FIP, in order that
the public comment on this crucial
aspect of the emission control plan may
be properly analyzed.
Response: The CAA directs EPA to
take public comment on proposed FIPs,
not final FIPs. See CAA section 307(d).
EPA’s modeling studies for the
proposed FIP were contained in the
docket for the proposed FIP and
available for review during the comment
period on the proposed FIP.
Additionally, on July 13, 2007, the
revised modeling files were indexed in
the electronic docket contained on
https://www.regulations.gov and a
compact disk containing the modeling
files was placed in the docket for this
action. See reference document FFFFF.
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13. General Support
(a) Comment (Citizen): The
commenter wants to lend support to
what EPA is trying to do here and the
proposals that EPA is making, and he
thinks it is very much on target and for
his benefit, and he would hope the
industries who are being regulated in
this sense will find a way to make it
worth their while to do it also.
Response: We acknowledge receipt of
the comment and the support for our
proposal.
(b) Comment (Citizen): Commenter
encourages EPA to carry on the work we
have been doing, to encourage
movement in the positive direction of
reducing emissions.
Response: We acknowledge receipt of
the comment and the support for our
proposal.
(c) Comment (Citizen): Commenter
appreciates the changes that EPA is
making and thinks the people in
Billings deserve them. Commenter feels
the industries need to step up to the
plate and be responsible for their
emissions.
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Response: We acknowledge receipt of
the comment and the support for our
proposal.
14. SIP Escape Clause
Comment (MSCC): The SIP contains
an important ‘‘escape clause’’ by which
there was a general agreement that if the
State provided more favorable treatment
to one facility, the same accommodation
would be offered to the other facilities.
The present proposed FIP which
proposes to reduce MSCC’s stack height
credit and drastically reduce MSCC’s
emission limits will violate that clause.
This unwarranted intrusion into a
carefully-bargained agreement among
multiple parties, violates both the letter
and the spirit of the CAA.
Response: We are not bound by the
escape clause that the State approved; in
fact, we disapproved this aspect of the
SIP. See 67 FR 22168, May 2, 2002.
Instead, we are obligated to correct the
portions of the SIP we disapproved. We
disapproved MSCC’s main stack
emission limits because they were based
on inappropriate stack height credit.
The FIP establishes new limits for
MSCC’s main stack that are consistent
with our modeled attainment
demonstration, based on a Good
Engineering Practice (GEP) stack height
credit of 65 meters. While it is not clear
to us how this violates the Stateapproved escape clause, setting
emission limits for MSCC’s main stack
consistent with our stack height
regulations and necessary to
demonstrate attainment of the NAAQS
does not violate the CAA. On the
contrary, setting such limits is required
by the CAA, regardless of the Stateapproved escape clause.
G. MSCC Specific Issues
1. Variable Emission Limit
(a) Comment (MSCC): EPA offers
surprisingly little discussion as to why
a variable limit was not proposed for
Montana Sulphur. EPA’s reasoning
seems to ignore that MSCC has been
operating under a variable emissions
limit that has been modeled, monitored,
and enforced for close to a decade.
Response: EPA’s reasoning for not
offering a variable limit is discussed in
the July 12, 2006, proposal notice (see
71 FR 39259, starting at 39268, col. 2)
and reference document WW
‘‘Technical Support Document’’
contained in EPA Docket No. EPA–R08–
OAR–2006–0098. Additionally, to our
knowledge, the SIP limits for two
sources in Billings (ExxonMobil and
Montana Power) are the only instances
in the United States where variable
emission limits based on buoyancy flux
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have been adopted, approved, and
implemented. The thousands of other
emission limitations nationwide are
based on a single fixed buoyancy flux
value similar to what we proposed for
MSCC.
(b) Comment (MSCC): Complicated to
Model. (i) MSCC agrees that it is more
complicated to model a variable
emission rate than a fixed emission rate.
That alone is not sufficient reason to
deny MSCC the variable emission rate.
Also, much has changed since the
original modeling effort. Computer
speed, memory, data handling, and
storage are all improved.
Response: Modeling was one of the
reasons we offered for not providing a
variable emission limit; however, it was
not the only reason. Although computer
speed, data handling, and storage are
improved since the MDEQ developed
the Billings/Laurel SO2 SIP, there would
still be a considerable effort on EPA’s
part to model a variable emission limit
for the SRU 100-meter stack. Therefore,
we used EPA’s historical practice of
selecting mean values of historical data.
Individual stationary sources in SIP
attainment demonstrations are typically
modeled assuming a single
representative value for the model input
parameters that affect plume rise. Model
input parameters that affect plume rise
include stack gas temperature and
volume flow, or buoyancy flux. If
emissions are held constant, ground
level concentrations would tend to
decrease during periods with higher
plume rise associated with elevated
stack gas temperature and increased
stack flow velocities. Conversely,
ground level concentrations would tend
to increase during periods with reduced
stack gas temperatures and stack flow
velocities. The State opted to set
emission limitations based on variable
buoyancy flux values for three of the
sources. MDEQ identified a total of 11
buoyancy flux modeling scenarios for
MSCC, 12 for ExxonMobil, and 10 for
the Corette Power Plant. Modeling all
possible combinations of scenarios
required the State to model a total of
1,320 combinations for each year of
meteorological data processed. EPA
used a fixed buoyancy flux value for
modeling MSCC and that reduced the
number of potential modeling scenarios
to 120. EPA reviewed the modeling
results in the State’s attainment
modeling to identify which scenarios (of
the 120 possible scenarios) would
produce the highest concentrations.
Based on this selection process, EPA
modeled approximately 50 scenarios in
the FIP modeling, and we believe that
these scenarios represent the limiting
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(i.e. maximum predicted concentration)
case.
(ii) It is completely arbitrary to create,
model, approve, monitor, and enforce
variable limits at other Billings facilities
but to deny the same courtesy for MSCC
claiming that it is, in this case alone, too
complicated a modeling effort.
Response: Again, modeling was not
the sole reason for not providing a
variable emission limit for MSCC’s SRU
100-meter stack. Although EPA
approved the variable emission limits at
other Billings facilities, we did so with
reservations. (See our July 28, 1999,
proposed rulemaking action on the
Billings/Laurel SO2 SIP, 64 FR 40791,
starting at 40794, col. 3, and our May 2,
2002, final rulemaking action, 67 FR
22168, starting at 22206, col. 2, for a full
discussion of our concerns with the
variable emission limit concept.) Since
EPA is taking the lead in establishing
emission limits for MSCC’s SRU 100meter stack and will take the lead in
enforcing the FIP, EPA has chosen not
to model and provide a variable
emission limit. We believe our exercise
of discretion so as to simplify FIP
development and enforcement is
reasonable, particularly where the data
indicate MSCC will be able to comply
with a fixed emission limit without
additional controls and where fixed
limits are the norm in SIPs throughout
the country.
(c) Comment (MSCC): Complicated to
Monitor. Buoyancy flux has been
measured and reported to DEQ for a
period of about eight years, with very
high reliability. It is simply illogical to
argue or imply that monitoring
buoyancy flux is a task not worthy or
too complicated in nature. One cannot
deny the historical evidence that it has
been measured successfully for many
years and that it does not require any
monitor instrumentation not already
required to measure sulfur dioxide.
Response: See response to comment
II.G.1.(b)(ii), above.
(d) Comment (MSCC): Complicated to
Enforce. EPA’s reason for not proposing
a variable limit for MSCC due to
enforcement is puzzling. If EPA
approved variable emission limits for
other sources, even though the same
enforcement concern exists, it should
also be approved for MSCC.
Response: The State developed the
original SIP that allows variable
emissions for several sources. The State
takes the lead in enforcing the SIP, and
EPA takes an oversight role. EPA
approved portions of the SIP, including
variable emission limits at two sources,
and we did so with reservations. Since
we would be taking the lead in
enforcing the FIP, we have chosen not
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to place an increased burden on
ourselves to enforce a variable limit. See
also the response to comment II.G.1.(e),
below.
(e) Comment (MSCC): Variable Limit
is Better Science. Though it involves
incremental initial work, from a
modeling perspective, the use of
variable limits is better science. It
replaces a false assumption in modeling
(constant, average stack conditions
under all operating scenarios) with
factual information so that plume
height, which is variable, can be more
accurately represented. Plume height,
just like mass emissions, is normally
variable and is critical to calculation of
downwind concentrations.
Response: In addition to looking at air
quality impacts of the FIP, we also need
to assure that the FIP is enforceable.
Although we may agree with the
commenter that the variable emission
limitation will result in fewer emissions
when the buoyancy of the plume is
lower, it will also result in higher
emissions when the buoyancy of the
plume is higher. Additionally, a variable
emission limit is more difficult to
enforce. Granted the same instruments
would be used to determine compliance
whether the emission limit is fixed or
variable. However, in addition to
confirming that the source is in
compliance with a variable emission
limit, agencies will also need to confirm
that the variable emission limitation
was determined correctly. Therefore, we
believe that variable emission limits
increase the workload and add a layer
of complexity that is not found with
fixed emission limitations. Because of
this enforcement complexity, we do not
agree with the commenter that variable
emission limitations are a superior
approach to setting emission
limitations.
(f) Comment (MSCC): Fixed Limit
Compliance. Although MSCC has been
able to meet the proposed FIP limit for
several years, it must be noted that
MSCC has not always been able to
operate within such limits, and that
MSCC was not operating its sulfur plant
at maximum capacity during the time
periods cited by EPA. The primary
reason MSCC can operate under EPA’s
proposed limit arises from MSCC’s
voluntary installation of SuperClaus TM.
The SuperClaus unit must be shut down
periodically for repair. MSCC needs the
variable limit to be in compliance when
SuperClaus unit is shut down. MSCC
should not be punished for its good
behavior by requiring control
technology and lower emissions than is
necessary to maintain NAAQS.
Response: EPA’s proposed FIP limit
for MSCC’s SRU 100-meter stack was
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determined through modeling as the
limit needed to assure attainment of the
SO2 NAAQS. Since the NAAQS are
health-based standards, as a general
matter, SIPs/FIPs must assure
attainment of the NAAQS on a
continuous basis.
We note that apparently MSCC was
able to conduct maintenance on the
SuperClaus unit in 2003, 2004, and
2005 without exceeding the proposed 3hour and 24-hour FIP SRU 100-meter
limits. MSCC may be able to perform its
maintenance on the SuperClaus unit
when other process equipment at
ExxonMobil is down for maintenance.
Additionally, we understand that MSCC
intends to install a second SuperClaus
unit to provide redundancy to the
existing SuperClaus equipment.
Installation is expected to begin in the
fourth quarter 2007, at the earliest
(reference documents GGGGGG and
BBBBBBB). Concerns about additional
emissions during maintenance should
be eliminated with the addition of a
second SuperClaus unit.
2. 100-Meter Stack Height Credit and
Emission Limit
(a) Comment: MSCC submitted
summary comments regarding its
position concerning good engineering
practice stack height credit for the 100meter SRU stack. MSCC noted that these
comments had generally been submitted
previously to both EPA and Montana.
MSCC claimed that it has not received
the proper stack height credit for the
100-meter SRU stack in the proposed
FIP.
Response: EPA disapproved the
State’s determination of stack height
credit for MSCC’s 100-meter SRU stack
on May 2, 2002 (67 FR 22168). In the
May 2, 2002, notice, starting on page
22209, we responded to all the stack
height comments MSCC previously
submitted. We hereby incorporate by
reference our responses from that
notice. We indicated in the May 2, 2002,
notice that ‘‘[w]e considered the
comments received and still believe we
should finalize our proposed
disapproval of the MSCC’s stack height
credit and SRU 100-meter stack
emission limitations. None of the
adverse comments has convinced us
that our interpretation of the CAA and
our regulations is unreasonable or that
we should change our proposed course
of action.’’ See our May 2002 final
action (67 FR 22168). EPA has
determined that the GEP stack height
credit for the 100-meter SRU stack is 65
meters and has used that height in
establishing the 100-meter SRU stack
emission limit. Our stack height
regulations, codified at 40 CFR 51.100
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and 51.118, provide that the degree of
emission limitation required for
pollutant control under an applicable
SIP shall not be affected by stack height
in excess of GEP stack height. The
central component of the regulations
consists of definitions of the term ‘‘good
engineering practice stack height.’’ GEP
stack height is the greater of (1) 65
meters (known as ‘‘de minimis’’ stack
height), (2) the height calculated using
a formula specified by regulations
(‘‘formula height’’), or (3) the height
demonstrated using fluid modeling or a
field study (‘‘non-formula height’’ or
‘‘above-formula height’’). See 40 CFR
51.100(ii)(1)–(3). Prior to our SIP action,
the State calculated the formula height
for the SRU 100-meter stack to be 47.8
meters (see reference documents
VVVVVV and WWWWWW). Per our
regulations, since this is lower than 65
meters, GEP stack height is 65 meters.
We have not received any new
information to indicate formula height
should be higher than 47.8 meters, nor
have we received a valid demonstration
for above-formula stack height credit.
See our proposed and final actions on
the Billings/Laurel SO2 SIP, 64 FR
40791 (July 28, 1999) and 67 FR 22168
(May 2, 2002), respectively. In light of
our prior decision on the fluid modeling
in the SIP action, and in the absence of
a new, valid, GEP stack height
demonstration, it would be
inappropriate in this FIP for us to use
a stack height value for MSCC that is
inconsistent with our prior action.
(b) Comment (YVAS): YVAS believes
the annual emission limit of 9,088,000
lbs of sulphur is too excessive because
YVAS believes this ‘‘proposed’’
emission to be a major contribution to
the total emissions of sulphur dioxide in
the Billings/Laurel area and is,
therefore, not acceptable. In addition,
EPA states that: ‘‘We (EPA) are
proposing fixed emission limits rather
than variable emission limits on MSCC’s
SRU 100 meter stack because they are
less complicated to model monitor and
enforce.’’ This proposal is inadequate
and does not address the continuing
high total SO2 emission limits you
intend permitting MSCC to continue to
release.
Response: Stack emission limits are
set to assure that the SO2 NAAQS are
met. As seen in the SIP and FIP, there
are 3-hour, 24-hour, and annual SO2
emission limits on most stacks. These
emission limits assure that the 3-hour,
24-hour, and annual SO2 NAAQS are
attained and maintained. As indicated
in the response to comment II.F.8.,
above, we cannot require states to adopt
provisions that go beyond attaining and
maintaining the NAAQS. The annual
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emission limit we proposed for the SRU
100-meter stack, and that we are now
promulgating in the FIP, assures that the
annual SO2 NAAQS will be attained and
maintained. Additionally, the 3-hour
and 24-hour SO2 NAAQS are more
controlling than the annual SO2
NAAQS. This means that more stringent
emission limits must be placed on
stacks to assure that the 3-hour and 24hour SO2 NAAQS are attained and
maintained than would be required to
assure that the annual SO2 NAAQS are
met.
(c) Comment (Citizen): Commenter
appreciates the logic of not allowing
increases in stack height credit.
Response: We acknowledge the
support for our proposal. Also, please
see our response to comment II.G.2.(a),
above.
3. 30-Meter Stack and Auxiliary Vent
Stack
(a) Comment (MSCC): Emissions
monitoring for 30-meter Stack and
Auxiliary Vent Stacks. EPA has
proposed unnecessarily complex,
redundant, and unneeded monitoring
and reporting requirements for both the
30-meter stack and the auxiliary vent
stacks. The emissions from these units
have minimal impact on model results.
These predicted concentrations are less
than 1% of the NAAQS. The emission
limit applicable is miniscule in
comparison with other uncertainties in
the implementation plan. Emissions
from these units, although authorized,
are infrequent. Venting to the boiler
stack is generally associated with events
such as maintenance. For operational
reliability and flexibility, MSCC needs
to be able to vent these boilers locally.
Monitoring these units is an expense
and requirement that serves no real or
useful purpose. Essentially the same
information is already gathered under
the State plan.
Response: As we indicated in our July
12, 2006, proposed FIP (71 FR 39259,
39268), it is necessary for EPA to require
methods to assure that the emission
limits for the 30-meter stack and
auxiliary vent stacks are met. However,
since MSCC has already established a
method to monitor these emissions
using length-of-stain detector tubes (e.g.,
¨
Drager Tubes),13 and since length-ofstain detector tubes are widely-used and
reliable, we have revised the FIP to
make its requirements similar to those
MSCC must already meet under the
State’s operating permit. Specifically,
13 See MSCC’s ‘‘Hydrogen Sulfide Fuel Gas
Monitoring Plan,’’ dated September 2000, that
fulfilled requirements of Montana Air Quality
Operating Permit 2611–00, Appendix H. (See
reference document IIIIII.)
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we have revised the method by which
MSCC shall determine the H2S content
of the fuel burned. Our final FIP
indicates that on a once-per-3-hour
period frequency until no heater or
boiler is exhausting to the 30-meter
stack or an auxiliary vent stack, MSCC
shall determine the H2S content of the
fuel burned using length-of-stain
detector tubes with the appropriate
sample tube range pursuant to ASTM
Method D4810–06, ‘‘Standard Test
Method for Hydrogen Sulfide in Natural
Gas Using Length-of-Stain Detector
Tubes’’ (see reference document
UUUUUU). The final FIP indicates that
if the results exceed the tube’s range,
another tube of a higher range must be
used until results are in the tube’s range.
(b) Comment (MSCC): Emission
Limit—100 ppm H2S—A Redundant
Limit. Having both a 12 lb/3-hour limit
and 100 ppm H2S limit creates doublejeopardy. Both limits are for solely and
exactly the same thing. If a particular 3hour period were to indicate 120 ppm,
it would be in violation of both limits.
This could (and is very likely to) occur
even if the units were not, in fact,
operating anywhere near an actual
emission rate of 12 lbs/3-hours. This
result is overkill and is not appropriate
or necessary for protection of the
NAAQS.
Response: In our FIP proposal, we
were attempting to simplify the method
to determine compliance with the mass
emission limits. The assumption in the
proposal was that if the H2S
concentration was below 100 ppm H2S,
then the source would be in compliance
with the mass emission limits. We were
not trying to create ‘‘double jeopardy’’
for MSCC. It appears that the
commenter believes the 100 ppm H2S
limit is too restrictive because the
source could be in compliance with the
mass emission limit but out of
compliance with the ppm limit.
In our final FIP we are keeping the
simplified method to determine
compliance with the mass emission
limits. We believe determining direct
compliance with the mass emission
limits would either require additional
monitoring equipment or methods and/
or would be unreliable due to potential
variation in boiler use and venting
practices. However, to address the
commenter’s concern, we are increasing
the H2S concentration limit to 160 ppm
per 3-hour period. We are adding a
calendar day H2S concentration limit of
100 ppm.
We selected the 160 ppm H2S per 3hour period limit for the following
reasons. First, as explained in greater
detail below, this value will protect the
3-hour SO2 NAAQS. Second, 160 ppm
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of H2S per 3-hour period is the current
NSPS limit for fuel gas combustion
devices. EPA reported the following in
its May 14, 2007, proposal to revise
subpart J of the new source performance
standards (NSPS), and to adopt new
subpart Ja:
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after consideration of current operating
practices, we concluded that amine
scrubbing units are still the predominant
technology for reduction of H2S in fuel gas
(and SO2 emissions from subsequent fuel gas
combustion). Considering the variability of
the fuel gas streams from various refinery
processing units, 160 ppmv also is still a
realistic short term H2S concentration limit.
However, one California Air Quality
Management District rule sets a 40 ppmv H2S
limit in fuel gas (averaged over 4 hours), and
several refiners have reported that the typical
fuel gas H2S concentrations (after scrubbing)
are in the same range.
(See 72 FR 27178, 27193.) Third, the
State’s SIP indicates that MSCC shall
burn only low sulfur fuel gas or natural
gas in any unit being exhausted through
the 30-meter stack (see MSCC’s exhibit
A, reference document II). Low sulfur
fuel gas is not defined in exhibit A.
However, an MDEQ staff member
indicated that the term ‘‘low sulfur fuel
gas’’ in the SIP would be gas with an
H2S concentration much lower than the
NSPS subpart J limit of 160 ppm (see
reference document GGGGGG). This
suggests that MSCC should already be
achieving a daily limit of 100 ppm.
To test the use of a 160 ppm limit, we
remodeled the area assuming the
emissions were 1.01 g/s from the 30meter stack and auxiliary vent stacks.
We derived the higher emission value
from the same assumptions and
calculations expressed in our proposal,
except we assumed a maximum H2S
concentration of 160 ppm (see 71 FR
39259, 39268, July 12, 2006). At the
higher three hour emissions, the area
would still show attainment of the 3hour SO2 NAAQS. However, the area
would not show attainment of the 24hour SO2 NAAQS if all 3-hour periods
in a calendar day were at the 160 ppm
level. Therefore, we are revising the FIP
to indicate that the H2S concentration in
the fuel burned in the heaters and
boilers, while any of the heaters and
boilers are exhausting to the SRU 30meter stack or auxiliary vents stacks,
shall not exceed 160 ppm per 3-hour
period and 100 ppm per calendar day.
The mass emission limits remain the
same as proposed. The revised modeling
files are indexed in the electronic
docket contained on https://
www.regulations.gov, and a compact
disk containing the modeling files has
been placed in the docket for this
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action. See reference document
KKKKKK.
(c) Comment (MSCC): Emission
Limit—100 ppm H2S—Overly Stringent.
The 100 ppm H2S limit, which is a
surrogate for the pound/hour SO2 limit,
is far too restrictive. EPA developed the
100 ppm H2S limit based on conditions
that have a miniscule probability of
occurring. It has the effect of
introducing a new, strict ‘‘performance
standard’’ into the mix of limits, where
such standard is not applicable.
Response: See response to II.G.3.(b),
above. Also, in order to protect the
NAAQS, it is reasonable to consider
potential worst-case conditions in
setting emission limits and compliance
determining methods.
(d) Comment (MSCC): Monitoring
Requirements. The requirement to
monitor the auxiliary vent stacks has
already been addressed through the
State plan; there is no inadequacy or
other basis to FIP this. The current
system already periodically measures
the H2S content in the fuel gas header
for gas that is not natural gas, using a
simple portable detector (non¨
electronic) such as a Drager tube or GasTec tube. The frequency of testing
necessity was determined through the
State’s plan and the frequency of such
testing steps up in response to high
measurements until the measurements
have returned to low levels. The present
plan also reasonably estimates the
volume of gas used in each boiler to
permit calculation of the SO2 emitted by
each auxiliary vent when in use, and
logs the venting location, as the State
plan provides.
Response: In large part, this comment
appears to pertain to our disapproval of
the relevant portion of the SIP. We note
that we have not reopened our SIP
action as part of this action and are not
considering comments on that action
here. To the extent the comment is
relevant to our FIP action, see response
to comment II.G.3.(b), above. As we
explain there, the FIP retains the
requirement that MSCC measure the
H2S content of the fuel burned but
increases the 3-hour concentration limit
to 160 ppm. The FIP also allows MSCC
to use length-of-stain detector tubes in
lieu of portable analyzers. However,
based on comments received, we are not
convinced that MSCC’s current methods
for determining direct compliance with
the mass emission limits are sufficiently
reliable or accurate for purposes of the
FIP due to potential variation in boiler
use and venting practices and lack of
equipment to directly measure relevant
parameters at or emissions from each
boiler. We believe additional monitoring
equipment would need to be installed,
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or additional monitoring would need to
be performed, at greater expense to
MSCC, to achieve adequate methods to
determine direct compliance with the
mass emission limits. The concentration
limits we are imposing are reasonable,
can be monitored at reasonable cost, and
will ensure protection of the NAAQS.
(e) Comment (MSCC): Monitoring
Cost. EPA proposes imposing significant
overly burdensome on-going costs to
track a minuscule amount of potential
or actual SO2 emissions.
Response: As we indicate in response
to comment II.G.3.(a), we have revised
the FIP to allow MSCC to use the same
devices to determine H2S concentrations
in the gas going to the 30-meter stack
and auxiliary vent stacks as MSCC is
using to meet State requirements
(length-of-stain detector tubes). While
the frequency of monitoring may be
somewhat different than the frequency
under the State’s permit, the final FIP
should not result in any substantial
additional monitoring costs for the 30meter stack and the auxiliary vent
stacks, particularly since MSCC
indicates emissions from these stacks
are infrequent.
H. ConocoPhillips Specific Issues
SRU/ATS Stack and Jupiter Flare
Comment (COPC): ConocoPhillips
urges EPA to delete the proposed
prohibition of simultaneous emissions
from the SRU/ATS stack and the Jupiter
flare even if the combined SO2
emissions are less than 25 lb/hr. This
merely imposes a compliance risk and
produces no environmental benefit.
Logic does not dictate that because both
sources were modeled as one point, that
combined, simultaneous emissions from
both are prohibited. Quite the contrary,
having modeled both sources as one
point supports and endorses the option
of both sources being able to emit a
combined total of the amount of SO2
which was modeled.
Response: EPA agrees that it is not
necessary to prohibit simultaneous
emissions from both emission points.
Attainment of the SO2 NAAQS would
be assured so long as the combined
emissions from both emission points do
not exceed 75.0 pounds per 3-hour
period. Since both emission points have
methods for determining emissions,
compliance with the emission limit
would be assured. We are revising the
regulatory text to eliminate the
restriction on simultaneous emissions
and any corresponding language.
Additionally, in the final regulatory text
we are clarifying the reporting
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and MDEQ and notify EPA and MDEQ
of RATAs.
I. ExxonMobil Specific Issues
jlentini on PROD1PC65 with RULES2
requirements to correspond to this
change.
2. Tutwiler Analysis
Comment (ExxonMobil): The
proposed FIP would require that
ExxonMobil measure the H2S
concentration of the fuel gas once every
three hours using the Tutwiler method
contained in 40 CFR 60.648 any time
the refinery fuel gas H2S CEMS
measures a concentration of greater than
1200 ppmv. The proposed once per 3hour Tutwiler analysis is less protective
than the existing requirement identified
in the alternative monitoring plan
(AMP) submitted to DEQ. The AMP
requires measurement of the fuel gas
¨
H2S concentration with Drager tubes on
an hourly basis anytime the fuel gas H2S
CEMS data are expected to be
unavailable for any reason for more than
one 3-hour block.
Response: In our proposed FIP, EPA
proposed a method for determining H2S
concentrations when the range of the
H2S CEMS is exceeded. ExxonMobil
commented that they currently use
another method for determining H2S
concentrations when the H2S CEMS is
not available. This other method has
been identified in an AMP submitted to
DEQ (reference document JJJJJJ). Since
ExxonMobil already has procedures
established for determining H2S
concentrations when the H2S CEMS is
¨
not available, namely, the use of Drager
Tubes, a type of length-of-stain detector
tube, and since length-of-stain detector
tubes are widely-used and reliable, EPA
is revising its FIP to incorporate the
other method identified by ExxonMobil.
Specifically, we are revising the FIP to
indicate that when the H2S
concentration in the refinery fuel gas
exceeds 1200 ppmv as measured by the
H2S CEMS, ExxonMobil shall measure
the H2S concentration on an hourly
basis using length-of-stain detector
tubes pursuant to ASTM Method
D4810–06, ‘‘Standard Test Method for
Hydrogen Sulfide in Natural Gas Using
Length-of-Stain Detector Tubes.’’ The
length-of-stain detector tubes shall have
the appropriate sample tube range. If the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range. The
hourly length-of-stain detector tubes
data will then be used to calculate SO2
emissions from refinery fuel gas
combustion and to determine
compliance with the emission limits in
40 CFR 52.1392(f)(3)(i).
1. Coker CO Boiler
Comment (ExxonMobil): The
proposed FIP would require that the
Coker CO Boiler stack CEMS operate at
all times. This is unnecessary because
the Coker Process gas is exhausted
through the nearby Yellowstone Energy
Limited Partnership Co-Generation
facility. During those hours, Coker CO
Boiler stack SO2 emissions are
monitored by the existing fuel gas CEM
for fuel gas combustion devices. The
existing SO2 SIP requires that a SO2
CEMS be operated on the Coker CO
Boiler stack during those few hours that
the Coker Process Gas is exhausted
through the Coker CO Boiler and stack.
Given that a CEMS is already required
for this source, nothing is served by
requiring ExxonMobil to report the
emissions and compliance assurance
data for this source to both EPA and
MDEQ. Nothing is served by requiring
ExxonMobil to notify both EPA and
MDEQ of required Relative Accuracy
Test Audits (RATA).
Response: It was not EPA’s intent to
require that the Coker CO Boiler stack
CEMS be operated at all times. Our
intent was to clarify that the Coker CO
Boiler CEMS already installed, in
conjunction with the appropriate
equations, must be used to determine
compliance with the emission limits
established in section 3(B)(1) of
ExxonMobil’s 2000 exhibit.
We are clarifying the FIP to indicate
that the Coker CO Boiler CEMS only
needs to be operating when
ExxonMobil’s Coker unit is operating
and Coker unit flue gases are exhausted
through the Coker CO Boiler stack. We
are also clarifying that whenever
ExxonMobil’s Coker unit is operating
and Coker unit flue gases are exhausted
through the Coker CO Boiler stack, the
CEMS shall immediately be operational.
Also, with respect to the SO2 CEMS, we
indicate that ExxonMobil shall perform
a Cylinder Gas Audit (CGA) or Relative
Accuracy Audit (RAA), which meets the
requirements of 40 CFR part 60,
Appendix F, within 8 hours of when the
Coker unit flue gases begin exhausting
through the Coker CO Boiler stack.
Finally, for both the SO2 and flow
CEMS, we indicate that ExxonMobil
shall perform an annual RATA, on the
CEMS.
Because we will have primary
responsibility to enforce the FIP, we
have retained the requirements that
ExxonMobil submit emissions and
compliance assurance data to both EPA
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3. ExxonMobil Emissions
Comment (YVAS): The question must
be asked that since ExxonMobil’s
emissions are appreciably higher than
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its two closest competitors, that a
significant lowering in total SO2
emissions in the Yellowstone Valley
could be attained if ExxonMobil would
be required to use that equipment under
either Federal EPA standards or under
the State of Montana emissions
requirements as well. That there is no
requirement to insist that ExxonMobil
use equipment/refining processes that
would lower its future SO2 emissions is
a deplorable lack of public concern to
YVAS’ best interests and should be
publicly examined by the EPA.
Response: EPA acknowledges this
comment. See response to comment
II.F.8., above.
J. CHS Inc. Specific Issues
Particulate Issues
Comment (YVAS): YVAS is
concerned that the Coker production
unit at CHS Inc. will not have to provide
a containment system shielding the
nearby area from the effects of
particulate pollution. This is a
deplorable lack of proper protection of
the public and, although addressing this
particular issue was apparently not
important to this FIP, since it was
completely omitted from this FIP, either
through oversight or deliberate
omission, YVAS seeks a ruling from the
EPA that could require CHS, Inc. to
address this issue and provide relief to
the public from this oversight.
Response: EPA acknowledges the
comment. However, the FIP addresses
only the provisions of the SO2 SIP that
we disapproved. Under CAA section
110(c), EPA’s authority is to remedy the
deficiencies we identified in the SO2
SIP.
III. Summary of the Final Rules and
Changes From the July 12, 2006,
Proposal
The following summarizes the final
FIP and the major changes from our July
12, 2006, FIP proposal. Generally, the
reasons for the changes made in the
final FIP appear in section II, above,
‘‘Issues Raised by Commenters and
EPA’s Response.’’ In some cases, the
reasons appear below. We also describe
some minor changes to the FIP in this
section.
A. Flare Requirements Applicable to All
Sources
Since the State’s attainment
demonstration assumed that the main
flares at each source were limited to 150
pounds of SO2 per 3-hour period, and
that the Jupiter Sulfur SRU flare would
share an emission limit of 75 pounds of
SO2 per 3-hour period with the Jupiter
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Sulfur SRU/ATS 14 stack, we proposed
flare emission limits that reflected the
State’s assumption that emissions from
these points would not exceed these
levels. While we proposed that 150
pounds of SO2 per 3-hour period be the
limit for the main flares, we also
solicited input on whether we should
instead limit the main flares to 500
pounds of SO2 per calendar day. The
final FIP requires that the main flares at
each source be limited to 150 pounds of
SO2 per 3-hour period and that the
Jupiter Sulfur flare share an emission
limit of 75 pounds of SO2 per 3-hour
period with the Jupiter Sulfur SRU/ATS
stack.
We also proposed that the flare limits
would apply at all times without
exception. We also solicited comment
on whether it would be appropriate to
include in our final FIP the ability to
assert an affirmative defense to penalties
only (not injunctive relief) for violations
of the flare limits. Under the final FIP,
flare limits apply at all times. However,
we have changed the proposed rule to
provide the ability for sources to assert
an affirmative defense to penalties only
(not injunctive relief) for violations of
the flare limits. The affirmative defense
provision includes notification
requirements that are distinct from the
FIP’s quarterly reporting requirements.
We proposed that compliance with
the flare emission limits would be
determined by continuous measurement
of the total sulfur concentration and
volumetric flow rate of the gas stream to
the flare(s), followed by calculation,
using appropriate equations, of SO2
emitted per 3-hour period.
We proposed that sources install,
calibrate, maintain, and operate a
continuous flow monitoring system
capable of measuring the total
volumetric flow of the gas stream
combusted in a flare in accordance with
the specifications described below. We
indicated that the flow monitoring
system could require one or more flow
monitoring devices or flow
measurements at one or more header
locations if one monitor could not
measure all of the volumetric flow to a
flare.
We proposed the following
volumetric flow monitoring
specifications:
(1) The minimum detectible velocity
of the flow monitoring device(s) would
be 0.1 feet per second (fps);
(2) The device(s) would continuously
measure the range of flow rates
corresponding to velocities from 0.5 to
275 fps and have a manufacturer’s
14 ATS
stands for Ammonium Thiosulfate.
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18:55 Apr 18, 2008
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specified accuracy of ± 5% over the
range of 1 to 275 fps;
(3) For correcting flow rate to
standard conditions (defined as 68°F
and 760 millimeters of mercury
(mmHg)), temperature and pressure
would be monitored continuously;
(4) The temperature and pressure
would be monitored in the same
location as the flow monitoring
device(s) and be calibrated to meet
accuracy specifications as follows:
Temperature would be calibrated
annually to within ± 2.0% at absolute
temperature and the pressure monitor
would be calibrated annually to within
± 5.0 mmHg;
(5) Flow monitoring device(s) would
be calibrated prior to installation to
demonstrate accuracy to within 5.0% at
flow rates equivalent to 30%, 60%, and
90% of monitor full scale; and
(6) After installation, the flow
monitoring devices would be calibrated
annually according to manufacturer’s
specifications.
The final FIP flow monitoring
provisions are the same as proposed
except that we are revising the following
provisions:
(1) With respect to the accuracy of the
flow monitor, the final FIP indicates
that the device(s) shall continuously
measure the range of flow rates
corresponding to velocities from 0.5 to
275 fps and have a manufacturer’s
specified accuracy of ± 5% of the
measured flow over the range of 1 to 275
fps and ± 20% of the measured flow
over the range of 0.1 to 1.0 fps.
(2) With respect to measurement of
volumetric flow rate, the final FIP
indicates that volumetric flow rate shall
be measured on an actual wet basis and
converted to standard conditions, and
reported in SCFH.
(3) With respect to temperature and
pressure monitors, the final FIP
indicates that temperature and pressure
monitors should be calibrated prior to
installation according to manufacturer’s
specifications. We inadvertently omitted
this requirement in our proposal.
We proposed that in cases where the
flow to the flare exceeds the range of the
monitor, other methods could be used to
determine the volumetric flow rate. In
the final FIP, we have clarified this
provision to read that in cases when the
volumetric flow monitor is not working
or where the flow exceeds the range of
the monitor, methods established in the
flare monitoring plan required by the
FIP shall be used to determine the
volumetric flow rate to the flare, which
shall then be used to calculate SO2
emissions. Additionally, we have
revised the quarterly reporting
requirements to be consistent with these
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21449
changes. The final FIP now indicates
that in quarterly reports, sources shall
indicate the date and time when a
monitor is not working or the range is
exceeded, and the other methods used
to determine flare emissions. We have
made these revisions to the final FIP so
that these provisions are consistent with
what we require in the flare monitoring
plan.
The final FIP also adds the ability for
sources to use means other than the
flow monitor to determine that the flare
is not operating when the flow monitor
registers low flow. Specifically, the final
FIP allows sources to use devices that
monitor the integrity of the flare water
seal. If these devices indicate that no
flow is going to the flare, yet the flow
monitor indicates there is flow, the
presumption will be that no flow is
going to the flare. We have also revised
the flare monitoring plan and reporting
requirements to recognize the use of,
and require reporting on, these other
flare flow devices.
We proposed that sources install,
calibrate, maintain, and operate an online analyzer system capable of
continuously determining the total
sulfur concentration of the gas stream
sent to a flare. We proposed that the
continuous monitoring occur at a
location or locations that are
representative of the gas combusted in
the flare and be capable of measuring
the expected range of total sulfur in the
gas stream to the flare. We proposed that
the total sulfur analyzer be installed,
certified (on a concentration basis), and
operated in accordance with 40 CFR
part 60, Appendix B, Performance
Specification 5, and be subject to and
meet the quality assurance and quality
control requirements (on a
concentration basis) of 40 CFR part 60,
Appendix F. Additionally, we proposed
that sources notify EPA in writing of
each Relative Accuracy Test Audit
(RATA) a minimum of 25 working days
prior to the actual testing. In the final
FIP, we are retaining the above
provisions, but are allowing the use of
other methods to determine total sulfur
concentration. See discussion below.
The final FIP also clarifies that the total
sulfur concentration monitor should
measure in the range of concentrations
that are normally present in the gas
stream to the flare.
In the final FIP, we are adding
provisions that indicate that, in cases
when the total sulfur analyzer is not
working or where the concentration of
the total sulfur exceeds the range of the
monitor, methods established in the
flare monitoring plan required by the
FIP shall be used to determine the total
sulfur concentrations, which shall than
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be used to calculate SO2 emissions.
Additionally, the final FIP indicates that
in quarterly reports, sources shall
indicate the date and time when a
monitor is not working, or the range is
exceeded, and the other methods used
to determine flare emissions. We have
made this addition to the FIP so that
these provisions are consistent with
what we require in the flare monitoring
plan.
In lieu of continuous total sulfur
concentration analyzers, the final FIP
allows sources to determine the total
sulfur concentration through grab or
integrated sampling. If a source chooses
to use one of these methods, the final
FIP provides a trigger by which sources
must begin the sampling and indicates
the analytical methods to be used to
determine the total sulfur concentration
in the sample. The final FIP also
provides that in cases where a grab or
integrated sample is not obtained or
analyzed, methods established in the
flare monitoring plan required by the
FIP shall be used to determine total
sulfur concentrations, which will then
be used to calculate SO2 emissions. The
flare monitoring plan and reporting
requirements have also been revised to
recognize the potential use of grab or
integrated sampling.
We proposed that within 180 days
after receiving EPA approval of the flare
monitoring plan, sources install and
calibrate, and thereafter calibrate,
maintain, and operate continuous flow
monitors and total sulfur concentration
analyzers. The final FIP has been
revised to allow sources 365 days after
receiving EPA approval of the flare
monitoring plan to install and calibrate,
and thereafter calibrate, maintain, and
operate the continuous volumetric flow
monitors and to start determining total
sulfur concentrations of the gas stream
by either continuous total sulfur
concentration analyzers or grab or
integrated sampling monitoring.
We proposed that each facility submit
a flare monitoring plan including,
among other things, information
regarding pilot and purge gas at each
flare and how the concentration and
volumetric flow monitors would
analyze the pilot and purge gases. The
final FIP indicates that if the facility
certifies that only natural gas or an inert
gas is used as pilot and/or purge gas,
monitoring the stream(s) consisting of
only natural gas or inert gas is not
required. However, if natural gas or
inert gas is not used for pilot and/or
purge gas, then the source must measure
the flow and H2S concentration of the
gas streams that do not consist of only
natural gas or inert gas or use other
methods approved by EPA in the flare
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Jkt 214001
installing a chain and lock on the valve
that supplies sour water stripper
overheads from the ‘‘old’’ SWS to the
main crude heater to insure that the
valve could not be opened. The
proposed FIP also required CHS Inc. to
maintain the chain and lock in place,
keep the valve closed at all times, and
log and report any noncompliance with
this provision. The final FIP is the same
as proposed.
monitoring plan to estimate flow and
H2S concentration. Pilot and purge gas
SO2 emissions will then be calculated
and added to the other SO2 emissions
from the flare to determine compliance
with the SO2 flare emission limits. We
have revised the reporting requirements
accordingly to require sources to either:
(1) Certify in the quarterly reports if
pilot and/or purge gas is not monitored
because only natural gas or inert gas is
used as the pilot and/or purge gas; or (2)
report flow, H2S concentration of, and
SO2 emissions from, the pilot and/or
purge gas.
We also added provisions that
indicate that in cases when any pilot or
purge gas flow monitor or H2S analyzer
is not working, or where the flow or
concentration of the H2S exceeds the
range of the monitor or analyzer,
methods established in the flare
monitoring plan required by the FIP
shall be used to determine the pilot and
purge gas flow and/or H2S
concentrations, which shall then be
used to calculate SO2 emissions. The
FIP indicates that in quarterly reports,
sources shall indicate the date and time
when a monitor or analyzer is not
working, or the range is exceeded, and
the other methods used to determine
flare emissions.
The flare monitoring plan
requirements have been revised to be
consistent with the pilot and purge gas
provisions described above.
We have added definitions of Aliquot,
Integrated sampling, Pilot gas, and
Purge gas to clarify the FIP’s flare
monitoring requirements. Finally, we
proposed quarterly reporting
requirements similar to the reporting
requirements contained in the Billings/
Laurel SO2 SIP and those contained in
40 CFR 60.7(c). We added to the
reporting requirements as necessary to
address the changes to other
requirements.
Flare Requirements
We proposed that ConocoPhillips’s
main flare be limited to 150 pounds of
SO2 per 3-hour period and that
compliance with the limit be
determined as discussed above. We also
proposed that at any one time,
ConocoPhillips could only use either
the north or south main flare. The final
FIP is the same as proposed except for
the flare monitoring changes applicable
to all sources mentioned above.
We proposed an emission limit of 75
pounds of SO2 per 3-hour period for the
Jupiter Sulfur SRU flare and SRU/ATS
stack and that emissions could only be
vented from the SRU flare when
emissions were not being vented from
the SRU/ATS stack. We proposed that
compliance with the SRU flare emission
limit, when Jupiter Sulfur vented
emissions to the SRU flare rather than
the SRU/ATS stack, be determined by
measuring the total sulfur concentration
and volumetric flow rate of the gas
stream to the flare.15 Our final FIP is the
same as proposed except that we have
removed the restriction that emissions
could only be vented from the SRU flare
when emissions were not being vented
from the SRU/ATS stack. Our final FIP
indicates that compliance with the
combined emission limit be determined
by summing the emissions from the
Jupiter Sulfur SRU flare and SRU/ATS
stack.
B. CHS Inc.
D. ExxonMobil
1. Flare Requirements
1. Flare Requirements
We proposed that ExxonMobil’s
primary process and turnaround flares
be limited to 150 pounds of SO2 per 3hour period and that compliance with
the limit be determined as discussed
above. Our proposal indicated that we
understood that the turnaround flare is
only used about 30–40 days every 5 to
6 years and is not normally operating.
Therefore, we proposed to establish one
combined emission limit for the primary
process and turnaround flares. Our
We proposed that CHS Inc.’s flare be
limited to 150 pounds of SO2 per 3-hour
period and that compliance with the
limit be determined as discussed above.
The final FIP is the same as proposed
except for the flare monitoring changes
applicable to all sources mentioned
above.
2. Combustion Sources Emission Limits
We proposed a prohibition in the FIP
on the burning of SWS overheads in the
main crude heater. We proposed that
compliance with the prohibition to not
burn SWS overheads in the main crude
heater be determined by CHS Inc.
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C. ConocoPhillips
15 Note that the SRU/ATS stack has an SO CEMS
2
and flow monitor to determine compliance when
emissions are vented through that stack.
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assumption was that the flow and
concentration monitoring devices
installed to measure the gas stream to
the primary process flare would also be
able to measure the gas stream to the
turnaround flare. However, we
indicated that if that was not the case,
ExxonMobil could propose another
method to determine emissions from the
turnaround flare. The final FIP is the
same as proposed except for the flare
monitoring changes applicable to all
sources mentioned above.
jlentini on PROD1PC65 with RULES2
2. Compliance Monitoring of Refinery
Fuel Gas Combustion Emission Limits
We proposed a method for measuring
the H2S concentrations in the refinery
fuel gas when the H2S concentrations in
the refinery fuel gas exceed the range of
the H2S CEMS. The method we
proposed is identical to the method
included in CHS Inc.’s 1998 exhibit.16
Specifically, we proposed that within
four hours of the initial determination
that the H2S concentrations in the
refinery fuel gas stream exceed the
upper range of the H2S CEMS,
ExxonMobil would have to initiate
sampling of the refinery fuel gas stream
at the fuel header on a once-per-3-hourperiod frequency using the Tutwiler
method in 40 CFR 60.648. The Tutwiler
method determines the H2S
concentration in the refinery fuel gas.
We also proposed that the Tutwilerderived H2S refinery fuel gas
concentration be used in calculations to
determine the hourly, 3-hour, and 24hour SO2 emission rates, in pounds,
from refinery fuel gas combustion.
These emission rates would then be
used to determine compliance with the
refinery fuel gas combustion emission
limits in ExxonMobil’s 1998 and 2000
exhibits when the H2S concentrations in
the refinery fuel gas stream exceeded
the upper range of the H2S CEMS.17
In our final FIP we have revised the
method by which ExxonMobil shall
obtain the H2S concentration of the
refinery fuel gas when the H2S
concentrations in the refinery fuel gas
exceed the range of the H2S CEMS.
Specifically, our final FIP indicates that
within four hours after the H2S CEMS
measures an H2S concentration in the
fuel gas stream greater than 1200 ppmv,
ExxonMobil shall initiate sampling of
the fuel gas stream at the fuel header on
a once-per-hour-period frequency using
length-of-stain detector tubes with the
16 See section 6(B)(3) of CHS Inc.’s 1998 exhibit.
(See reference document DD for a copy of the
exhibit.)
17 See sections 3(A)(1) and 3(B)(2) of
ExxonMobil’s 1998 and 2000 exhibits. (See
reference documents GG and HH for copies of the
exhibits.)
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18:55 Apr 18, 2008
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appropriate sample tube range. If the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range.
ExxonMobil shall continue to use the
length-of-stain detector tube method at
this frequency until the H2S CEMS
measures an H2S concentration in the
fuel gas stream equal to or less than
1200 ppmv continuously over a 3-hour
period. We also revised the equation
used to calculate the SO2 emissions
because of the change in the H2S
analysis method.
We proposed reporting requirements
similar to the requirements adopted by
the State for CHS Inc. and those
contained in 40 CFR 60.7(c). We added
a provision that requires ExxonMobil to
report information for periods when the
range of the refinery fuel gas CEMS is
exceeded.
3. Compliance Monitoring of Coker CO
Boiler Emission Limits
We proposed that existing SO2 and
flow CEMS, in conjunction with the
appropriate calculations mentioned
below, be used to determine compliance
with the emission limits established in
section 3(B)(1) of ExxonMobil’s 2000
exhibit. Specifically, we proposed that
at all times ExxonMobil operate and
maintain CEMS to measure SO2
concentrations from the Coker CO Boiler
stack and a continuous stack flow rate
monitor to measure stack gas flow rates
from the Coker CO Boiler stack. We
proposed that the SO2 and flow rate
CEMS meet the CEM Performance
Specifications contained in sections
6(C) and (D), respectively, of
ExxonMobil’s 1998 exhibit, except that
ExxonMobil would have to notify EPA
in writing of each annual RATA a
minimum of 25 working days prior to
actual testing.
Our final FIP is the same as proposed
except that we have deleted the
requirement that the flow and SO2
CEMS be operated at all times and
added the requirement that whenever
ExxonMobil’s Coker unit is operating
and Coker unit flue gases are exhausted
through the Coker CO Boiler stack, the
flow and SO2 CEMS shall be
immediately operational. We have also
clarified that ExxonMobil shall meet the
specifications contained in section 6(C)
of ExxonMobil’s 1998 exhibit, except
that ExxonMobil shall perform a
Cylinder Gas Audit (CGA) or Relative
Accuracy Audit (RAA) which meets the
requirements of 40 CFR part 60,
Appendix F, within eight hours of when
the Coker unit flue gases begin
exhausting through the Coker CO Boiler
stack and that ExxonMobil shall
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21451
perform an annual RATA on the flow
and SO2 CEMS.
We proposed that compliance with
ExxonMobil’s Coker CO Boiler emission
limits 18 be determined using the data
from the CEMS mentioned above and in
accordance with the appropriate
calculations described in ExxonMobil’s
1998 exhibit.19 We also proposed
reporting requirements similar to the
requirements adopted in the Billings/
Laurel SO2 SIP and those contained in
40 CFR 60.7(c). Our final FIP is the same
as proposed, except as noted above.
E. Montana Sulphur & Chemical
Company (MSCC)
1. Flare Requirements
We proposed that MSCC’s 80-foot
west flare, 125-foot east flare, and 100meter flare be limited to 150 pounds of
SO2 per 3-hour period combined total
and that compliance with the limit be
determined as discussed above. Our
final FIP is the same as proposed except
for the flare monitoring changes
applicable to all sources mentioned
above.
2. SRU 100-Meter Stack
We proposed the following emission
limits for the SRU 100-meter stack:
Emissions of SO2 not to exceed (a)
3,003.1 pounds per 3-hour period, (b)
24,025.0 pounds per calendar day, and
(c) 9,088,000.0 pounds per calendar
year. Our final FIP is the same as
proposed except that the 3-hour and
calendar day emission limits have been
slightly reduced due to minor
corrections in the modeling. The final
FIP emission limits for the SRU 100meter stack are as follows: Emissions of
SO2 shall not exceed (a) 2981.7 pounds
per 3-hour period, (b) 23,853.6 pounds
per calendar day, and (c) 9,088,000.0
pounds per calendar year
We proposed that compliance with
the above emission limits be determined
according to the methods established in
MSCC’s 1998 exhibit. Finally, we
proposed quarterly reporting
requirements similar to the reporting
requirements contained in the Billings/
Laurel SO2 SIP and those contained in
40 CFR 60.7(c). Our final FIP is the same
as proposed, except as noted above.
3. SRU 30-Meter Stack
We proposed the following mass
emission limits for the 30-meter stack:
Emissions of SO2 not to exceed: (a) 12.0
pounds per 3-hour period, (b) 96.0
18 See section 3(B)(1) of ExxonMobil’s 2000. (See
reference document HH for a copy of the exhibit.)
19 See sections 2(A)(1), (8), (11)(a), and (16) of
ExxonMobil’s 1998 exhibit. (See reference
document GG for a copy of the exhibit.)
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pounds per calendar day, and (c) 35,040
pounds per calendar year. The mass
emission limits remain the same as
proposed.
We proposed that H2S concentrations
in the fuel burned in the boilers and
heaters, while any boiler or heater was
exhausting through the SRU 30-meter
stack, be limited to 100 ppm of H2S or
less, averaged over a 3-hour period.
While we proposed the foregoing
approach for determining compliance
with the SRU 30-meter stack emission
limits, we also solicited input on
whether we should promulgate a
different compliance determining
method.
In our final FIP, we are keeping the
simplified method to determine
compliance with mass emission limits.
However, we are increasing the H2S
concentration limit to 160 ppm/3-hour
period and adding a calendar day H2S
concentration limit of 100 ppm.
We proposed that the H2S
concentration in the fuel be measured
using a portable H2S monitor. In our
final FIP, we have revised the method
by which MSCC shall determine the H2S
content of the fuel burned. Specifically,
our final FIP indicates that MSCC shall
determine the H2S content of the fuel
burned using length-of-stain detector
tubes with the appropriate sample tube
range. The final FIP indicates that if the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range.
Finally, we proposed quarterly
reporting requirements. The quarterly
reporting requirements are similar to the
reporting requirements contained in the
Billings/Laurel SO2 SIP and those
contained in 40 CFR 60.7(c). Our final
FIP is the same as proposed, except as
needed to address the changes noted
above.
jlentini on PROD1PC65 with RULES2
4. Combined SO2 Emission Limit From
the Auxiliary Vent Stacks
We proposed the following mass
emission limits for the auxiliary vent
stacks: emissions of SO2 not to exceed:
(a) 12.0 pounds per 3-hour period, (b)
96.0 pounds per calendar day, and (c)
35,040 pounds per calendar year. The
mass emission limits remain the same as
proposed. In our proposal, we indicated
that the issues associated with
monitoring compliance with these
limits were essentially the same as those
associated with monitoring compliance
with the SRU 30-meter stack emission
limits. Thus, we proposed the same
approach for monitoring compliance
with these emission limits as we
describe in section III.E.3, above.
Similarly, we solicited input on whether
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we should promulgate a different
compliance determining method.
In our final FIP, we are keeping the
simplified method to determine
compliance with mass emission limits.
However, we are increasing the H2S
concentration limit to 160 ppm/3-hour
period and adding a calendar day H2S
concentration limit of 100 ppm.
We proposed that the H2S
concentration in the fuel be measured
using a portable H2S monitor. In our
final FIP we have revised the method by
which MSCC shall determine the H2S
content of the fuel burned. Specifically,
our final FIP indicates that MSCC shall
determine the H2S content of the fuel
burned using length-of-stain detector
tubes with the appropriate sample tube
range. The final FIP indicates that if the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range.
Finally, we proposed quarterly
reporting requirements similar to
reporting requirements contained in the
Billings/Laurel SO2 SIP and those
contained in 40 CFR 60.7(c). Our final
FIP is the same as proposed, except as
noted above.
F. Modeling To Support Emission Limits
Our proposal discussed the modeling
conducted to support the emission
limits proposed for MSCC’s SRU 100meter stack. EPA received comments
regarding our modeling files that
identified the need for minor technical
corrections to those files. In response to
several of these comments, EPA has
revised its modeling files, as necessary,
to omit extraneous information, add
information that was inadvertently
omitted, make minor corrections, or
otherwise clarify the files. EPA does not
consider any of the revisions to be
significant. The only change with any
substantive impact—the correction to
the coordinates for MSCC described
below—results in a very slight decrease
in our proposed emission limit for
MSCC’s 100-meter stack from 126.13 g/
second to125.23 g/second, less than a 1
percent change. The specific changes
EPA has made are as follows:
(1) A commenter recommended that
the modeling files contain a more
complete description of the naming
convention and purpose behind each
modeling effort.
EPA changes: To improve
documentation, some extraneous
modeling files have been removed and
a text file added to explain the naming
conventions. The naming conventions,
typically used by modelers, help define
the purpose behind each modeling
effort.
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(2) One commenter indicated that
only proper geographical coordinates
should be used as inputs to the
dispersion modeling. Commenters
indicated that the location of the small
boiler stacks at MSCC that were
modeled as volume sources was
incorrect.
EPA changes: We have corrected the
incorrect source coordinate for MSCC’s
boiler stacks in the modeling files.
(3) One commenter indicated that
three source input files were not
included in reference document EEE.
EPA change: We have added the three
source input files to the compact disk
containing the modeling files.
(4) One commenter indicated that a
source input file (ref-5t.sri) was
included in reference document EEE but
did not appear to be used in any input
and output files.
EPA change: This was a test file that
we inadvertently included and have
now deleted.
On July 13, 2007, the revised
modeling files were indexed in the
electronic docket contained on https://
www.regulations.gov and a compact
disk containing the modeling files was
placed in the docket for this action. See
reference document FFFFF.
Also, as noted above, with respect to
the 30-meter stack and auxiliary vent
stacks, we are keeping the simplified
method to determine compliance with
the mass emission limits. However, we
are increasing the H2S concentration
limit to 160 ppm/3-hour period and
adding a calendar day H2S
concentration limit of 100 ppm. The
mass emission limits remain the same as
proposed.
We remodeled the area assuming the
emissions were 1.01 g/s from the 30meter stack and auxiliary vent stacks.
We derived the higher emission value
from the same assumptions and
calculations expressed in our proposal,
except we assumed a maximum H2S
concentration of 160 ppm (see 71 FR
39259, 39268, July 12, 2006). At the
higher 3-hour emissions, the area would
still show attainment of the 3-hour SO2
NAAQS. However, the area would not
show attainment of the 24-hour SO2
NAAQS if all 8 3-hour periods in a
calendar day were at the 160 ppm level.
Therefore, we are revising the FIP to
indicate that the H2S concentration in
the fuel burned in the heaters and
boilers, while any of the heaters and
boilers are exhausting to the SRU 30meter stack or auxiliary vents stacks,
shall not exceed 160 ppm per 3-hour
period and 100 ppm per calendar day.
The revised modeling files are indexed
in the electronic docket contained on
https://www.regulations.gov, and a
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compact disk containing the modeling
files was placed in the docket for this
action. See reference document
KKKKKK.
IV. Statutory and Executive Order
Reviews
A. Executive Order 12866, Regulatory
Planning and Review
Under Executive Order 12866, 58 FR
51735 (October 4, 1993), all ‘‘regulatory
actions’’ that are ‘‘significant’’ are
subject to Office of Management and
Budget (OMB) review and the
requirements of the Executive Order. A
‘‘regulatory action’’ is defined as ‘‘any
substantive action by an agency
(normally published in the Federal
Register) that promulgates or is
expected to result in the promulgation
of a final rule or regulation, including
* * * notices of proposed rulemaking.’’
A ‘‘regulation or rule’’ is defined as ‘‘an
agency statement of general
applicability and future effect, * * * ’’
The FIP is not subject to OMB review
under E.O. 12866 because it applies to
only four specifically named facilities,
with requirements unique to each
facility, and is, therefore, not a rule of
general applicability. Thus, it is not a
‘‘regulatory action’’ under E.O. 12866
and was not submitted to OMB for
review.
jlentini on PROD1PC65 with RULES2
B. Paperwork Reduction Act
This action does not impose an
information collection burden under the
provisions of the Paperwork Reduction
Act, 44 U.S.C. 3501 et seq. Burden is
defined at 5 CFR 1320.3(b). Under the
Paperwork Reduction Act, 44 U.S.C.
3501 et seq., OMB must approve all
‘‘collections of information’’ by EPA.
The Act defines ‘‘collection of
information’’ as a requirement for
‘‘answers to * * * identical reporting or
recordkeeping requirements imposed on
ten or more persons * * * ’’ 4 U.S.C.
3502(3)(A). Because the FIP only applies
to four companies, the Paperwork
Reduction Act does not apply.
C. Regulatory Flexibility Act
Under the Regulatory Flexibility Act
(RFA), 5 U.S.C. section 601 et seq., EPA
generally must prepare a regulatory
flexibility analysis of any rule subject to
notice and comment rulemaking
requirements unless EPA certifies that
the rule will not have a significant
economic impact on a substantial
number of small entities. Small entities
include small businesses, small not-forprofit enterprises, and small
governmental jurisdictions. 5 U.S.C.
603, 604, and 605(b).
This FIP will not have a significant
economic impact on a substantial
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number of small entities because this
FIP applies to only four sources (CHS
Inc., ConocoPhillips, ExxonMobil and
MSCC) in the Billings/Laurel, Montana
area. Therefore, I certify that this action
will not have a significant economic
impact on a substantial number of small
entities.
D. Unfunded Mandates Reform Act
Title II of the Unfunded Mandates
Reform Act of 1995, Public Law 04 4,
establishes requirements for Federal
agencies to assess the effects of their
regulatory actions on State, local, and
tribal governments and the private
sector. Under section 202 of UMRA,
EPA generally must prepare a written
statement, including a cost benefit
analysis, for proposed rules and for final
rules with ‘‘Federal mandates’’ that may
result in the expenditure by State, local,
and tribal governments, in the aggregate,
or by the private sector, of $100 million
or more in any one year. Before
promulgating an EPA rule for which a
written statement is needed, section 205
of the UMRA generally requires EPA to
identify and consider a reasonable
number of regulatory alternatives and
adopt the least costly, most cost
effective, or least burdensome
alternative that achieves the objectives
of the rule. The provisions of section
205 do not apply when they are
inconsistent with applicable law.
Moreover, section 205 allows EPA to
adopt an alternative other than the least
costly, most cost-effective or least
burdensome alternative if the
Administrator publishes with the final
rule an explanation why that alternative
was not adopted. Before EPA establishes
any regulatory requirements that might
significantly or uniquely affect small
governments, including tribal
governments, it must have developed
under section 203 of UMRA a small
government agency plan. The plan must
provide for notifying potentially
affected small governments, enabling
officials of affected small governments
to have meaningful and timely input in
the development of EPA regulatory
proposals with significant Federal
intergovernmental mandates, and
informing, educating, and advising
small governments on compliance with
the regulatory requirements.
EPA has determined that this rule
does not contain a Federal mandate that
may result in the expenditure of $100
million for State, local and tribal
governments, in the aggregate, or the
private sector in any one year. The FIP
does not impose any enforceable duties
on state, local, or tribal governments.
Although the FIP would impose
enforceable duties on entities in the
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21453
private sector, the costs are expected to
be less than $100 million in any one
year. Thus, today’s rule is not subject to
the requirements of 202 and 205 of the
UMRA.
EPA has determined that this rule
contains no regulatory requirements that
might significantly or uniquely affect
small governments, because it imposes
no requirements on small governments.
Nor will the rule impact small
governments in any significant or
unique way. Thus, today’s rule is not
subject to the requirements of section
203 of the UMRA.
E. Executive Order 13132, Federalism
Executive Order, 13132, entitled
‘‘Federalism’’ (64 FR 43255, August 10,
1999), requires EPA to develop an
accountable process to ensure
‘‘meaningful and timely input by State
and local officials in the development of
regulatory policies that have federalism
implications.’’ ‘‘Policies that have
federalism implications’’ include
regulations that have ‘‘substantial direct
effects on the States, on the relationship
between the national government and
the States, or on the distribution of
power and responsibilities among the
various levels of government.’’
The final rule does not have
federalism implications. It will not have
substantial direct effects on the States,
on the relationship between the national
government and the States, or on the
distribution of power and
responsibilities among the various
levels of government, as specified in
Executive Order 13132. This rule
establishes standards appropriate for
four companies in the Billings/Laurel,
Montana area, and, thus, does not
directly affect any State or local
government. It does not alter the
relationship or the distribution of power
and responsibilities established by the
Clean Air Act. Thus, Executive Order
13132 does not apply to this rule.
F. Executive Order 13175, Coordination
With Indian Tribal Governments
Executive Order 13175, entitled
‘‘Consultation and Coordination with
Indian Tribal Governments’’ (65 FR
67249, November 9, 2000), requires EPA
to develop an accountable process to
ensure ‘‘meaningful and timely input by
tribal officials in the development of
regulatory policies that have tribal
implications.’’ This final rule does not
have tribal implications, as specified in
Executive Order 13175. It will not have
substantial, direct effects on tribal
governments, on the relationship
between the Federal government and
Indian tribes, or on the distribution of
power and responsibilities between the
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Federal government and Indian tribes as
specified in Executive Order 13175.
This Action does not involve or impose
any requirements that affect Indian
Tribes. Thus, Executive Order 13175
does not apply to this rule.
G. Executive Order 13045, Protection of
Children From Environmental Health
Risks and Safety Risks
Executive Order 13045: ‘‘Protection of
Children from Environmental Health
Risks and Safety Risks’’ (62 FR 19885,
April 23, 1997), applies to any rule that:
(1) Is determined to be ‘‘economically
significant’’ as defined under Executive
Order 12866, and (2) concerns an
environmental health or safety risk that
EPA has reason to believe may have a
disproportionate effect on children. If
the regulatory action meets both criteria,
the Agency must evaluate the
environmental health or safety effects of
the planned rule on children, and
explain why the planned regulation is
preferable to other potentially effective
and reasonably feasible alternatives
considered by the Agency.
This FIP is not subject to the
Executive Order because it is not
economically significant as defined in
Executive Order 12866. Further, EPA
interprets Executive Order 13045 as
applying only to those regulatory
actions that are based on health or safety
risks, such that the analysis required
under section 5–501 of the Order has
the potential to influence the regulation.
This FIP is not subject to Executive
Order 13045 because it implements a
previously promulgated health and
safety-based Federal standard.
jlentini on PROD1PC65 with RULES2
H. Executive Order 13211, Actions That
Significantly Affect Energy Supply,
Distribution, or Use
This rule is not subject to Executive
Order 13211, ‘‘Actions Concerning
Regulations That Significantly Affect
Energy Supply, Distribution, or Use’’ (66
FR 28355, May 22, 2001) because it is
not a significant regulatory action under
Executive Order 12866.
I. National Technology Transfer and
Advancement Act
As noted in the proposed rule,
Section 12(d) of the National
Technology Transfer and Advancement
Act (NTTAA) of 1995, Public Law No.
104–113 (15 U.S.C. 272 note), directs
EPA to use voluntary consensus
standards in its regulatory activities
unless to do so would be inconsistent
with applicable law or otherwise
impractical. Voluntary consensus
standards (VCS) are technical standards
(e.g., materials specifications, test
methods, sampling procedures, business
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practices) that are developed or adopted
by voluntary consensus standards
bodies. The NTTAA directs EPA to
provide Congress, through OMB,
explanations when the Agency decides
not to use available and applicable
voluntary standards.
This rulemaking involves technical
standards. We have identified three VCS
that can be used in lieu of EPA methods.
The American Society for Testing and
Materials (ASTM) Methods D4468–85
(Reapproved 2000) and D5504–01
(Reapproved 2006) are acceptable
methods for determining total sulfur
concentrations in the gas streams going
to facility flares in lieu of using a
continuous total sulfur analyzer in
accordance with 40 CFR part 60,
Appendix B, Performance Specification
5. ASTM Method D4810–06 is an
acceptable method for determining the
hydrogen sulfide concentration in
ExxonMobil’s refinery fuel gas in lieu of
using the Tutwiler method described in
40 CFR 60.648. We are incorporating
these methods by reference in 40 CFR
52.1392(j).
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order (EO) 12898 (59 FR
7629 (Feb. 16, 1994)) establishes federal
executive policy on environmental
justice. Its main provision directs
federal agencies, to the greatest extent
practicable and permitted by law, to
make environmental justice part of their
mission by identifying and addressing,
as appropriate, disproportionately high
and adverse human health or
environmental effects of their programs,
policies, and activities on minority
populations and low-income
populations in the United States.
EPA has determined that this final
rule will not have disproportionately
high and adverse human health or
environmental effects on minority or
low-income populations because it
increases the level of environmental
protection for all affected populations
without having any disproportionately
high and adverse human health or
environmental effects on any
population, including any minority or
low-income population. This final rule
establishes emission limits and
compliance determining methods at
four sources in the Billings/Laurel,
Montana area to assure that the SO2
NAAQS are met.
K. Congressional Review Act
The Congressional Review Act, 5
U.S.C. section 801 et seq., as added by
the Small Business Regulatory
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Enforcement Fairness Act of 1996,
generally provides that before a rule
may take effect, the agency
promulgating the rule must submit a
rule report, which includes a copy of
the rule, to each House of the Congress
and to the Comptroller General of the
United States. Section 804 exempts from
section 801 the following types of rules:
(1) Rules of particular applicability; (2)
rules relating to agency management or
personnel; and (3) rules of agency
organization, procedure, or practice that
do not substantially affect the rights or
obligations of non-agency parties. 5
U.S.C. 804(3). EPA is not required to
submit a rule report regarding today’s
action under section 801 because this is
a rule of particular applicability; it only
applies to four specifically named
sources, with requirements unique to
each facility.
L. Petitions for Judicial Review
Under section 307(b)(1) of the Clean
Air Act, petitions for judicial review of
this action must be filed in the United
States Court of Appeals for the
appropriate circuit by June 20, 2008.
Filing a petition for reconsideration by
the Administrator of this final rule does
not affect the finality of this rule for the
purposes of judicial review nor does it
extend the time within which a petition
for judicial review may be filed, and
shall not postpone the effectiveness of
such rule or action. This action may not
be challenged later in proceedings to
enforce its requirements. (See CAA
section 307(b)(2).)
List of Subjects in 40 CFR Part 52
Environmental protection, Air
pollution control, Incorporation by
reference, Intergovernmental relations,
Reporting and recordkeeping
requirements, Sulfur oxides.
Dated: March 28, 2008.
Stephen L. Johnson,
Administrator.
For reasons stated in the preamble, 40
CFR part 52 is amended as follows:
I
PART 52—[AMENDED]
1. The authority citation for part 52
continues to read as follows:
I
Authority: 42 U.S.C. 7401 et seq.
Subpart BB—Montana
2. Subpart BB is amended by adding
§ 52.1392 to read as follows:
I
§ 52.1392 Federal Implementation Plan for
the Billings/Laurel Area.
(a) Applicability. This section applies
to the owner(s) or operator(s), including
any new owner(s) or operator(s) in the
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event of a change in ownership or
operation, of the following facilities in
the Billings/Laurel, Montana area: CHS
Inc. Petroleum Refinery, Laurel
Refinery, 803 Highway 212 South,
Laurel, MT; ConocoPhillips Petroleum
Refinery, Billings Refinery, 401 South
23rd St., Billings, MT; ExxonMobil
Petroleum Refinery, 700 Exxon Road,
Billings, MT; and Montana Sulphur &
Chemical Company, 627 Exxon Road,
Billings, MT.
(b) Scope. The facilities listed in
paragraph (a) of this section are also
subject to the Billings/Laurel SO2 SIP, as
approved at 40 CFR 52.1370(c)(46) and
(52). In cases where the provisions of
this FIP address emissions activities
differently or establish a different
requirement than the provisions of the
approved SIP, the provisions of this FIP
take precedence.
(c) Definitions. For the purpose of this
section, we are defining certain words
or initials as described in this
paragraph. Terms not defined below
that are defined in the Clean Air Act or
regulations implementing the Clean Air
Act, shall have the meaning set forth in
the Clean Air Act or such regulations.
(1) Aliquot means a fractional part of
a sample that is an exact divisor of the
whole sample.
(2) Annual Emissions means the
amount of SO2 emitted in a calendar
year, expressed in pounds per year
rounded to the nearest pound, where:
Annual emissions = S Daily emissions
within the calendar year.
(3) Calendar Day means a 24-hour
period starting at 12 midnight and
ending at 12 midnight, 24 hours later.
(4) Clock Hour means a twenty-fourth
(1⁄24) of a calendar day; specifically any
of the standard 60-minute periods in a
day that are identified and separated on
a clock by the whole numbers one (1)
through 12.
(5) Continuous Emission Monitoring
System or CEMS means all continuous
concentration and volumetric flow rate
monitors, associated data acquisition
equipment, and all other equipment
necessary to meet the requirements of
this section for continuous monitoring.
(6) Daily Emissions means the amount
of SO2 emitted in a calendar day,
expressed in pounds per day rounded to
the nearest tenth (1⁄10) of a pound,
where:
Daily emissions = S 3-hour emissions
within a calendar day.
(7) EPA means the United States
Environmental Protection Agency.
(8) Exhibit means for a given facility
named in paragraph (a) of this section,
exhibit A to the stipulation of the
Montana Department of Environmental
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Quality and that facility, adopted by the
Montana Board of Environmental
Review on either June 12, 1998, or
March 17, 2000.
(9) 1998 Exhibit means for a given
facility named in paragraph (a) of this
section, the exhibit adopted by the
Montana Board of Environmental
Review on June 12, 1998.
(10) 2000 Exhibit means for a given
facility named in paragraph (a) of this
section, the exhibit adopted by the
Montana Board of Environmental
Review on March 17, 2000.
(11) Flare means a combustion device
that uses an open flame to burn
combustible gases with combustion air
provided by uncontrolled ambient air
around the flame. This term includes
both ground and elevated flares.
(12) The initials Hg mean mercury.
(13) Hourly means or refers to each
clock hour in a calendar day.
(14) Hourly Average means an
arithmetic average of all valid and
complete 15-minute data blocks in a
clock hour. Four (4) valid and complete
15-minute data blocks are required to
determine an hourly average for each
CEMS per clock hour.
Exclusive of the above definition, an
hourly CEMS average may be
determined with two (2) valid and
complete 15-minute data blocks, for two
(2) of the 24 hours in any calendar day.
A complete 15-minute data block for
each CEMS shall have a minimum of
one (1) data point value; however, each
CEMS shall be operated such that all
valid data points acquired in any 15minute block shall be used to determine
the 15-minute block’s reported
concentration and flow rate.
(15) Hourly Emissions means the
pounds per clock hour of SO2 emissions
from a source (including, but not
limited to, a flare, stack, fuel oil system,
sour water system, or fuel gas system)
determined using hourly averages and
rounded to the nearest tenth (1⁄10) of a
pound.
(16) The initials H2S mean hydrogen
sulfide.
(17) Integrated sampling means an
automated method of obtaining a
sample from the gas stream to the flare
that produces a composite sample of
individual aliquots taken over time.
(18) The initials MBER mean the
Montana Board of Environmental
Review.
(19) The initials MDEQ mean the
Montana Department of Environmental
Quality.
(20) The initials mm mean
millimeters.
(21) The initials MSCC mean the
Montana Sulphur & Chemical Company.
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(22) Pilot gas means the gas used to
maintain the presence of a flame for
ignition of gases routed to a flare.
(23) Purge gas means a continuous gas
stream introduced into a flare header,
flare stack, and/or flare tip for the
purpose of maintaining a positive flow
that prevents the formation of an
explosive mixture due to ambient air
ingress.
(24) The initials ppm mean parts per
million.
(25) The initials SCFH mean standard
cubic feet per hour.
(26) The initials SCFM mean standard
cubic feet per minute.
(27) Standard Conditions means (a) 20
°C (293.2 °K, 527.7 °R, or 68.0 °F) and
one (1) atmosphere pressure (29.92
inches Hg or 760 mm Hg) for stack and
flare gas emission calculations, and (b)
15.6 °C (288.7 °K, 520.0 °R, or 60.3 °F)
and one (1) atmosphere pressure (29.92
inches Hg or 760 mm Hg) for refinery
fuel gas emission calculations.
(28) The initials SO2 mean sulfur
dioxide.
(29) The initials SWS mean sour water
stripper.
(30) The term 3-hour emissions means
the amount of SO2 emitted in each of
the eight (8) non-overlapping 3-hour
periods in a calendar day, expressed in
pounds and rounded to the nearest
tenth (1⁄10) of a pound, where:
3 hour emissions = Σ Hourly emissions
within the 3-hour period.
(31) The term 3-hour period means
any of the eight (8) non-overlapping 3hour periods in a calendar day:
Midnight to 3 a.m., 3 a.m. to 6 a.m., 6
a.m. to 9 a.m., 9 a.m. to noon, noon to
3 p.m., 3 p.m. to 6 p.m., 6 p.m. to 9
p.m., 9 p.m. to midnight.
(32) Turnaround means a planned
activity involving shutdown and startup
of one or several process units for the
purpose of performing periodic
maintenance, repair, replacement of
equipment, or installation of new
equipment.
(33) Valid means data that are
obtained from a monitor or meter
serving as a component of a CEMS
which meets the applicable
specifications, operating requirements,
and quality assurance and control
requirements of section 6 of
ConocoPhillips’, CHS Inc.’s,
ExxonMobil’s, and MSCC’s 1998
exhibits, respectively, and this section.
(d) CHS Inc. emission limits and
compliance determining methods.
(1) Introduction. The provisions for
CHS Inc. cover the following units:
(i) The flare.
(ii) Combustion sources, which
consist of those sources identified in the
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combustion sources emission limit in
section 3(A)(1)(d) of CHS Inc.’s 1998
exhibit.
(2) Flare requirements.
(i) Emission limit. The total emissions
of SO2 from the flare shall not exceed
150.0 pounds per 3-hour period.
(ii) Compliance determining method.
Compliance with the emission limit in
paragraph (d)(2)(i) of this section shall
be determined in accordance with
paragraph (h) of this section.
(3) Combustion sources.
(i) Restrictions. Sour water stripper
overheads (ammonia (NH3) and H2S
gases removed from the sour water in
the sour water stripper) shall not be
burned in the main crude heater. At all
times, CHS Inc. shall keep a chain and
lock on the valve that supplies sour
water stripper overheads from the old
sour water stripper to the main crude
heater and shall keep such valve closed.
(ii) Compliance determining method.
CHS Inc. shall log and report any
noncompliance with the requirements
of paragraph (d)(3)(i) of this section.
(4) Data reporting requirements.
(i) CHS Inc. shall submit quarterly
reports beginning with the first calendar
quarter following May 21, 2008. The
quarterly reports shall be submitted
within 30 days of the end of each
calendar quarter. The quarterly reports
shall be submitted to EPA at the
following address: Air Program Contact,
EPA Montana Operations Office,
Federal Building, 10 West 15th Street,
Suite 3200, Helena, MT 59626.
The quarterly report shall be certified
for accuracy in writing by a responsible
CHS Inc. official. The quarterly report
shall consist of both a comprehensive
electronic-magnetic report and a written
hard copy data summary report.
(ii) The electronic report shall be on
magnetic or optical media, and such
submittal shall follow the reporting
format of electronic data being
submitted to the MDEQ. EPA may
modify the reporting format delineated
in this section, and, thereafter, CHS Inc.
shall follow the revised format. In
addition to submitting the electronic
quarterly reports to EPA, CHS Inc. shall
also record, organize, and archive for at
least five (5) years the same data, and
upon request by EPA, CHS Inc. shall
provide EPA with any data archived in
accordance with this provision. The
electronic report shall contain the
following:
(A) Hourly average total sulfur
concentrations as H2S or SO2 in ppm in
the gas stream to the flare;
(B) Hourly average H2S concentrations
of the flare pilot and purge gases in
ppm;
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(C) Hourly average volumetric flow
rates in SCFH of the gas stream to the
flare;
(D) Hourly average volumetric flow
rates in SCFH of the flare pilot and
purge gases;
(E) Hourly average temperature (in °F)
and pressure (in mm or inches of Hg) of
the gas stream to the flare;
(F) Hourly emissions from the flare in
pounds per clock hour; and
(G) Daily calibration data for all flare,
pilot gas, and purge gas CEMS.
(iii) The quarterly written report shall
contain the following information:
(A) The 3-hour emissions in pounds
per 3-hour period from each flare;
(B) Periods in which only natural gas
or an inert gas was used as flare pilot
gas or purge gas or both;
(C) The results of all quarterly
Cylinder Gas Audits (CGA), Relative
Accuracy Audits (RAA), and annual
Relative Accuracy Test Audits (RATA)
for all total sulfur analyzer(s) and H2S
analyzer(s), and the results of all annual
calibrations and verifications for the
volumetric flow, temperature, and
pressure monitors;
(D) For all periods of flare volumetric
flow rate monitoring system or total
sulfur analyzer system downtime, flare
pilot gas or purge gas volumetric flow or
H2S analyzer system downtime, or
failure to obtain or analyze a grab or
integrated sample, the written report
shall identify:
(1) Dates and times of downtime or
failure;
(2) Reasons for downtime or failure;
(3) Corrective actions taken to
mitigate downtime or failure; and
(4) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(E) For all periods that the range of
the flare or any pilot or purge gas
volumetric flow rate monitor(s), any
flare total sulfur analyzer(s), or any pilot
or purge gas H2S analyzer(s) is
exceeded, the written report shall
identify:
(1) Date and time when the range of
the volumetric flow monitor(s), total
sulfur analyzer(s), or H2S analyzer(s)
was exceeded; and
(2) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(F) For all periods that the flare
volumetric flow monitor or monitors are
recording flow, yet any Flare Water Seal
Monitoring Device indicates there is no
flow, the written report shall identify:
(1) Date, time, and duration when the
flare volumetric flow monitor(s)
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recorded flow, yet any Flare Water Seal
Monitoring Device indicated there was
no flow;
(G) For each 3-hour period in which
the flare emission limit is exceeded, the
written report shall identify:
(1) The date, start time, and end time
of the excess emissions;
(2) Total hours of operation with
excess emissions, the hourly emissions,
and the 3-hour emissions;
(3) All information regarding reasons
for operating with excess emissions; and
(4) Corrective actions taken to
mitigate excess emissions;
(H) The date and time of any
noncompliance with the requirements
of paragraph (d)(3)(i) of this section; and
(I) When no excess emissions have
occurred or the continuous monitoring
system(s) or manual system(s) have not
been inoperative, repaired, or adjusted,
such information shall be stated in the
report.
(e) ConocoPhillips emission limits
and compliance determining methods.
(1) Introduction. The provisions for
ConocoPhillips cover the following
units:
(i) The main flare, which consists of
two flares—the north flare and the south
flare—that are operated on alternating
schedules. These flares are referred to
herein as the north main flare and south
main flare, or generically as the main
flare.
(ii) The Jupiter Sulfur SRU flare,
which is the flare at Jupiter Sulfur,
ConocoPhillips’ sulfur recovery unit.
(2) Flare requirements.
(i) Emission limits.
(A) Combined emissions of SO2 from
the main flare (which can be emitted
from either the north or south main
flare, but not both at the same time)
shall not exceed 150.0 pounds per 3hour period.
(B) Emissions of SO2 from the Jupiter
Sulfur SRU flare and the Jupiter Sulfur
SRU/ATS stack (also referred to as the
Jupiter Sulfur SRU stack) shall not
exceed 75.0 pounds per 3-hour period,
600.0 pounds per calendar day, and
219,000 pounds per calendar year.
(ii) Compliance determining method.
(A) Compliance with the emission
limit in paragraph (e)(2)(i)(A) of this
section shall be determined in
accordance with paragraph (h) of this
section. In the event that a single
monitoring location cannot be used for
both the north and south main flare,
ConocoPhillips shall monitor the flow
and measure the total sulfur
concentration at more than one location
in order to determine compliance with
the main flare emission limit.
ConocoPhillips shall log and report any
instances when emissions are vented
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from the north main flare and south
main flare simultaneously.
(B) Compliance with the emission
limits and requirements in paragraph
(e)(2)(i)(B) of this section shall be
determined by summing the emissions
from the Jupiter Sulfur SRU flare and
SRU/ATS stack. Emissions from the
Jupiter Sulfur SRU flare shall be
determined in accordance with
paragraph (h) of this section and the
emissions from the Jupiter Sulfur SRU/
ATS stack shall be determined pursuant
to ConocoPhillips’ 1998 exhibit (see
section 4(A) of the exhibit).
(3) Data reporting requirements.
(i) ConocoPhillips shall submit
quarterly reports on a calendar year
basis, beginning with the first calendar
quarter following May 21, 2008. The
quarterly reports shall be submitted
within 30 days of the end of each
calendar quarter. The quarterly reports
shall be submitted to EPA at the
following address: Air Program Contact,
EPA Montana Operations Office,
Federal Building, 10 West 15th Street,
Suite 3200, Helena, MT 59626.
The quarterly report shall be certified
for accuracy in writing by a responsible
ConocoPhillips official. The quarterly
report shall consist of both a
comprehensive electronic-magnetic
report and a written hard copy data
summary report.
(ii) The electronic report shall be on
magnetic or optical media, and such
submittal shall follow the reporting
format of electronic data being
submitted to the MDEQ. EPA may
modify the reporting format delineated
in this section, and, thereafter,
ConocoPhillips shall follow the revised
format. In addition to submitting the
electronic quarterly reports to EPA,
ConocoPhillips shall also record,
organize, and archive for at least five (5)
years the same data, and upon request
by EPA, ConocoPhillips shall provide
EPA with any data archived in
accordance with this provision. The
electronic report shall contain the
following:
(A) Hourly average total sulfur
concentrations as H2S or SO2 in ppm in
the gas stream to the ConocoPhillips
main flare and Jupiter Sulfur SRU flare;
(B) Hourly average H2S concentrations
of the ConocoPhillips main flare and
Jupiter Sulfur SRU flare pilot and purge
gases in ppm;
(C) Hourly average volumetric flow
rates in SCFH of the gas streams to the
ConocoPhillips main flare and Jupiter
Sulfur SRU flare;
(D) Hourly average volumetric flow
rates in SCFH of the ConocoPhillips
main flare and Jupiter Sulfur SRU flare
pilot and purge gases;
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(E) Hourly average temperature (in °F)
and pressure (in mm or inches of Hg) of
the gas streams to the ConocoPhillips
main flare and Jupiter Sulfur SRU flare;
(F) Hourly emissions in pounds per
clock hour from the ConocoPhillips
main flare and Jupiter Sulfur SRU flare;
and
(G) Daily calibration data for all flare,
pilot gas, and purge gas CEMS.
(iii) The quarterly written report shall
contain the following information:
(A) The 3-hour emissions in pounds
per 3-hour period from the
ConocoPhillips main flare and the sum
of the combined 3-hour emissions from
the Jupiter Sulfur SRU/ATS stack and
Jupiter Sulfur SRU flare in pounds per
3-hour period;
(B) Periods in which only natural gas
or an inert gas was used as flare pilot
gas or purge gas or both;
(C) The results of all quarterly
Cylinder Gas Audits (CGA), Relative
Accuracy Audits (RAA), and annual
Relative Accuracy Test Audits (RATA)
for all total sulfur analyzer(s) and H2S
analyzer(s), and the results of all annual
calibrations and verifications for the
volumetric flow, temperature, and
pressure monitors;
(D) For all periods of flare volumetric
flow rate monitoring system or total
sulfur analyzer system downtime, flare
pilot gas or purge gas volumetric flow or
H2S analyzer system downtime, or
failure to obtain or analyze a grab or
integrated sample, the written report
shall identify:
(1) Dates and times of downtime or
failure;
(2) Reasons for downtime or failure;
(3) Corrective actions taken to
mitigate downtime or failure; and
(4) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(E) For all periods that the range of
the flare or any pilot or purge gas
volumetric flow rate monitor(s), any
flare total sulfur analyzer(s), or any pilot
or purge gas H2S analyzer(s) is
exceeded, the written report shall
identify:
(1) Date and time when the range of
the volumetric flow monitor(s), total
sulfur analyzer(s), or H2S analyzer(s)
was exceeded, and
(2) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(F) For all periods that the flare
volumetric flow monitor or monitors are
recording flow, yet any Flare Water Seal
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21457
Monitoring Device indicates there is no
flow, the written report shall identify:
(1) Date, time, and duration when the
flare volumetric flow monitor(s)
recorded flow, yet any Flare Water Seal
Monitoring Device indicated there was
no flow;
(G) Identification of dates, times, and
duration of any instances when
emissions were vented from the north
and south main flares simultaneously;
(H) For each 3-hour period in which
a flare emission limit is exceeded, the
written report shall identify:
(1) The date, start time, and end time
of the excess emissions;
(2) Total hours of operation with
excess emissions, the hourly emissions,
and the 3-hour emissions;
(3) All information regarding reasons
for operating with excess emissions; and
(4) Corrective actions taken to
mitigate excess emissions; and
(I) When no excess emissions have
occurred or the continuous monitoring
system(s) or manual system(s) have not
been inoperative, repaired, or adjusted,
such information shall be stated in the
report.
(f) ExxonMobil emission limits and
compliance determining methods.
(1) Introduction. The provisions for
ExxonMobil cover the following units:
(i) The Primary process flare and the
Turnaround flare. The Primary process
flare is the flare normally used by
ExxonMobil. The Turnaround flare is
the flare ExxonMobil uses for about 30
to 40 days every 5 to 6 years when the
facility’s major SO2 source, the fluid
catalytic cracking unit, is not normally
operating.
(ii) The following refinery fuel gas
combustion units: The FCC CO Boiler,
F–2 crude/vacuum heater, F–3 unit, F–
3X unit, F–5 unit, F–700 unit, F–201
unit, F–202 unit, F–402 unit, F–551
unit, F–651 unit, standby boiler house
(B–8 boiler), and Coker CO Boiler (only
when the Yellowstone Energy Limited
Partnership (YELP) facility is receiving
ExxonMobil Coker unit flue gas or
whenever the ExxonMobil Coker is not
operating).
(iii) Coker CO Boiler stack.
(2) Flare requirements.
(i) Emission limit. The total combined
emissions of SO2 from the Primary
process and Turnaround refinery flares
shall not exceed 150.0 pounds per 3hour period.
(ii) Compliance determining method.
Compliance with the emission limit in
paragraph (f)(2)(i) of this section shall be
determined in accordance with
paragraph (h) of this section. If
volumetric flow monitoring device(s)
installed and concentration monitoring
methods used to measure the gas stream
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to the Primary Process flare cannot
measure the gas stream to the
Turnaround flare, ExxonMobil may
apply to EPA for alternative measures to
determine the volumetric flow rate and
total sulfur concentration of the gas
stream to the Turnaround flare. Before
EPA will approve such alternative
measures, ExxonMobil must agree that
the Turnaround flare will be used only
during refinery turnarounds of limited
duration and frequency—no more than
60 days once every five (5) years—
which restriction shall be considered an
enforceable part of this FIP. Such
alternative measures may consist of
reliable flow estimation parameters to
estimate volumetric flow rate and
manual sampling of the gas stream to
the flare to determine total sulfur
concentrations, or such other measures
that EPA finds will provide accurate
estimations of SO2 emissions from the
Turnaround flare.
(3) Refinery fuel gas combustion
requirements.
(i) Emission limits. The applicable
emission limits are contained in section
3(A)(1) of ExxonMobil’s 2000 exhibit
and section 3(B)(2) of ExxonMobil’s
1998 exhibit.
(ii) Compliance determining method.
For the limits referenced in paragraph
(f)(3)(i) of this section, the compliance
determining methods specified in
section 4(B) of ExxonMobil’s 1998
exhibit shall be followed except when
the H2S concentration in the refinery
fuel gas stream exceeds 1200 ppmv as
measured by the H2S CEMS required by
section 6(B)(3) of ExxonMobil’s 1998
exhibit (the H2S CEMS.) When such
value is exceeded, the following
compliance monitoring method shall be
employed:
(A) ExxonMobil shall measure the
H2S concentration in the refinery fuel
gas according to the procedures in
paragraph (f)(3)(ii)(B) of this section and
calculate the emissions according to the
equations in paragraph (f)(3)(ii)(C) of
this section.
(B) Within four (4) hours after the H2S
CEMS measures an H2S concentration in
the refinery fuel gas stream greater than
1200 ppmv, ExxonMobil shall initiate
sampling of the refinery fuel gas stream
at the fuel header on a once-per-hour
frequency using length-of-stain detector
tubes pursuant to ASTM Method
D4810–06, ‘‘Standard Test Method for
Hydrogen Sulfide in Natural Gas Using
Length-of-Stain Detector Tubes’’
(incorporated by reference, see
paragraph (j) of this section) with the
appropriate sample tube range. If the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range.
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ExxonMobil shall continue to use the
length-of-stain detector tube method at
this frequency until the H2S CEMS
measures an H2S concentration in the
refinery fuel gas stream equal to or less
than 1200 ppmv continuously over a 3hour period.
(C) When the length-of-stain detector
tube method is required, SO2 emissions
from refinery fuel gas combustion shall
be calculated as follows: the Hourly
emissions shall be calculated using
equation 1, 3-hour emissions shall be
calculated using equation 2, and the
Daily emissions shall be calculated
using equation 3.
Equation 1: EH = K * CH * QH
Where:
EH = Refinery fuel gas combustion hourly
emissions in pounds per hour, rounded
to the nearest tenth of a pound;
K= 1.688 × 10-7 in (pounds/standard cubic
feet (SCF))/parts per million (ppm);
CH = Hourly refinery fuel gas H2S
concentration in ppm determined by the
length-of-stain detector tube method as
required by paragraph (f)(3)(ii)(B) of this
section; and
QH = actual fuel gas firing rate in standard
cubic feet per hour (SCFH), as measured
by the monitor required by section
6(B)(8) of ExxonMobil’s 1998 exhibit.
Equation 2: (Refinery fuel gas
combustion 3-hour emissions) = Σ
(Hourly emissions within the 3hour period as determined by
equation 1).
Equation 3: (Refinery fuel gas
combustion daily emissions) = Σ (3hour emissions within the day as
determined by equation 2).
(4) Coker CO Boiler stack
requirements.
(i) Emission limits. When
ExxonMobil’s Coker unit is operating
and Coker unit flue gases are burned in
the Coker CO Boiler, the applicable
emission limits are contained in section
3(B)(1) of ExxonMobil’s 2000 exhibit.
(ii) Compliance determining method.
(A) Compliance with the emission
limits referenced in paragraph (f)(4)(i) of
this section shall be determined by
measuring the SO2 concentration and
flow rate in the Coker CO Boiler stack
according to the procedures in
paragraphs (f)(4)(ii)(B) and (C) of this
section and calculating emissions
according to the equations in paragraph
(f)(4)(ii)(D) of this section.
(B) Beginning on May 21, 2008,
ExxonMobil shall operate and maintain
a CEMS to measure sulfur dioxide
concentrations in the Coker CO Boiler
stack. Whenever ExxonMobil’s Coker
unit is operating and Coker unit flue
gases are exhausted through the Coker
CO Boiler stack, the CEMS shall be
operational and shall achieve a temporal
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sampling resolution of at least one (1)
concentration measurement per minute,
meet the requirements expressed in the
definition of ‘‘hourly average’’ in
paragraph (c)(14) of this section, and
meet the CEMS Performance
Specifications contained in section 6(C)
of ExxonMobil’s 1998 exhibit, except
that ExxonMobil shall perform a
Cylinder Gas Audit (CGA) or Relative
Accuracy Audit (RAA) which meets the
requirements of 40 CFR part 60,
Appendix F, within eight (8) hours of
when the Coker unit flue gases begin
exhausting through the Coker CO Boiler
stack. ExxonMobil shall perform an
annual Relative Accuracy Test Audit
(RATA) on the CEMS and notify EPA in
writing of each annual RATA a
minimum of 25 working days prior to
actual testing.
(C) Beginning on May 21, 2008,
ExxonMobil shall operate and maintain
a continuous stack flow rate monitor to
measure the stack gas flow rates in the
Coker CO Boiler stack. Whenever
ExxonMobil’s Coker unit is operating
and Coker unit flue gases are exhausted
through the Coker CO Boiler stack, this
CEMS shall be operational and shall
achieve a temporal sampling resolution
of at least one (1) flow rate measurement
per minute, meet the requirements
expressed in the definition of ‘‘hourly
average’’ in paragraph (c)(14) of this
section, and meet the Stack Gas Flow
Rate Monitor Performance
Specifications of section 6(D) of
ExxonMobil’s 1998 exhibit, except that
ExxonMobil shall perform an annual
Relative Accuracy Test Audit (RATA)
on the CEMS and notify EPA in writing
of each annual RATA a minimum of 25
working days prior to actual testing.
(D) SO2 emissions from the Coker CO
Boiler stack shall be determined in
accordance with the equations in
sections 2(A)(1), (8), (11)(a), and (16) of
ExxonMobil’s 1998 exhibit.
(5) Data reporting requirements.
(i) ExxonMobil shall submit quarterly
reports beginning with the first calendar
quarter following May 21, 2008. The
quarterly reports shall be submitted
within 30 days of the end of each
calendar quarter. The quarterly reports
shall be submitted to EPA at the
following address: Air Program Contact,
EPA Montana Operations Office,
Federal Building, 10 West 15th Street,
Suite 3200, Helena, MT 59626.
The quarterly report shall be certified
for accuracy in writing by a responsible
ExxonMobil official. The quarterly
report shall consist of both a
comprehensive electronic-magnetic
report and a written hard copy data
summary report.
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(ii) The electronic report shall be on
magnetic or optical media, and such
submittal shall follow the reporting
format of electronic data being
submitted to the MDEQ. EPA may
modify the reporting format delineated
in this section, and, thereafter,
ExxonMobil shall follow the revised
format. In addition to submitting the
electronic quarterly reports to EPA,
ExxonMobil shall also record, organize,
and archive for at least five (5) years the
same data, and upon request by EPA,
ExxonMobil shall provide EPA with any
data archived in accordance with this
provision. The electronic report shall
contain the following:
(A) Hourly average total sulfur
concentrations as H2S or SO2 in ppm in
the gas stream to the flare(s);
(B) Hourly average H2S concentrations
of the flare pilot and purge gases in
ppm;
(C) Hourly average SO2 concentrations
in ppm from the Coker CO Boiler stack;
(D) Hourly average volumetric flow
rates in SCFH of the flare pilot and
purge gases;
(E) Hourly average volumetric flow
rates in SCFH in the gas stream to the
flare(s) and in the Coker CO Boiler
stack;
(F) Hourly average H2S concentrations
in ppm from the refinery fuel gas
system;
(G) Hourly average refinery fuel gas
combustion units’ actual fuel firing rate
in SCFH;
(H) Hourly average temperature (in °F)
and pressure (in mm or inches of Hg) of
the gas stream to the flare(s);
(I) Hourly emissions in pounds per
clock hour from the flare(s), Coker CO
Boiler stack, and refinery fuel gas
combustion system; and
(J) Daily calibration data for the CEMS
described in paragraphs (f)(2)(ii),
(f)(3)(ii) and (f)(4)(ii) of this section.
(iii) The quarterly written report shall
contain the following information:
(A) The 3-hour emissions in pounds
per 3-hour period from the flare(s),
Coker CO Boiler stack, and refinery fuel
gas combustion system;
(B) Periods in which only natural gas
or an inert gas was used as flare pilot
gas or purge gas or both;
(C) Daily emissions in pounds per
calendar day from the Coker CO Boiler
stack and refinery fuel gas combustion
system;
(D) The results of all quarterly or
other Cylinder Gas Audits (CGA),
Relative Accuracy Audits (RAA), and
annual Relative Accuracy Test Audits
(RATA) for the CEMS described in
paragraphs (f)(2)(ii) (flare total sulfur
analyzer(s); pilot gas or purge gas H2S
analyzer(s)), (f)(3)(ii), and (f)(4)(ii) of
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this section, and the results of all annual
calibrations and verifications for the
volumetric flow, temperature, and
pressure monitors;
(E) For all periods of flare volumetric
flow rate monitoring system or total
sulfur analyzer system downtime, Coker
CO Boiler stack CEMS downtime,
refinery fuel gas combustion system
CEMS downtime, flare pilot gas or purge
gas volumetric flow or H2S analyzer
system downtime, or failure to obtain or
analyze a grab or integrated sample, the
written report shall identify:
(1) Dates and times of downtime or
failure;
(2) Reasons for downtime or failure;
(3) Corrective actions taken to
mitigate downtime or failure; and
(4) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(F) For all periods that the range of
the flare or any pilot or purge gas
volumetric flow rate monitor(s), any
flare total sulfur analyzer(s), or any pilot
or purge gas H2S analyzer(s) is
exceeded, the written report shall
identify:
(1) Date and time when the range of
the volumetric flow monitor(s), total
sulfur analyzer(s), or H2S analyzer(s)
was exceeded, and
(2) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(G) For all periods that the range of
the refinery fuel gas CEMS is exceeded,
the written report shall identify:
(1) Date, time, and duration when the
range of the refinery fuel gas CEMS was
exceeded;
(H) For all periods that the flare
volumetric flow monitor or monitors are
recording flow, yet any Flare Water Seal
Monitoring Device indicates there is no
flow, the written report shall identify:
(1) Date, time, and duration when the
flare volumetric flow monitor(s)
recorded flow, yet any Flare Water Seal
Monitoring Device indicated there was
no flow;
(I) For each 3-hour period and
calendar day in which the flare
emission limits, the Coker CO Boiler
stack emission limits, or the fuel gas
combustion system emission limits are
exceeded, the written report shall
identify:
(1) The date, start time, and end time
of the excess emissions;
(2) Total hours of operation with
excess emissions, the hourly emissions,
the 3-hour emissions, and the daily
emissions;
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(3) All information regarding reasons
for operating with excess emissions; and
(4) Corrective actions taken to
mitigate excess emissions; and
(J) When no excess emissions have
occurred or the continuous monitoring
system(s) or manual system(s) have not
been inoperative, repaired, or adjusted,
such information shall be stated in the
report.
(g) Montana Sulphur & Chemical
Company (MSCC) emission limits and
compliance determining methods.
(1) Introduction. The provisions for
MSCC cover the following units:
(i) The flares, which consist of the 80foot west flare, 125-foot east flare, and
100-meter flare.
(ii) The SRU 100-meter stack.
(iii) The auxiliary vent stacks and the
units that can exhaust through the
auxiliary vent stacks, which consist of
the Railroad Boiler, the H–1 Unit, the
H1–A unit, the H1–1 unit and the H1–
2 unit.
(iv) The SRU 30-meter stack and the
units that can exhaust through the SRU
30-meter stack. The units that can
exhaust through the SRU 30-meter stack
are identified in section 3(A)(2)(d) and
(e) of MSCC’s 1998 exhibit.
(2) Flare requirements.
(i) Emission limit. Total combined
emissions of SO2 from the 80-foot west
flare, 125-foot east flare, and 100-meter
flare shall not exceed 150.0 pounds per
3-hour period.
(ii) Compliance determining method.
Compliance with the emission limit in
paragraph (g)(2)(i) of this section shall
be determined in accordance with
paragraph (h) of this section. In the
event MSCC cannot monitor all three
flares from a single location, MSCC shall
establish multiple monitoring locations.
(3) SRU 100-meter stack
requirements.
(i) Emission limits. Emissions of SO2
from the SRU 100-meter stack shall not
exceed:
(A) 2,981.7 pounds per 3-hour period;
(B) 23,853.6 pounds per calendar day;
and
(C) 9,088,000 pounds per calendar
year.
(ii) Compliance determining method.
(A) Compliance with the emission
limits contained in paragraph (g)(3)(i) of
this section shall be determined by the
CEMS and emission testing methods
required by sections 6(B)(1) and (2) and
section 5, respectively, of MSCC’s 1998
exhibit.
(B) MSCC shall notify EPA in writing
of each annual source test a minimum
of 25 working days prior to actual
testing.
(C) The CEMS referenced in
paragraph (g)(3)(ii)(A) of this section
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shall achieve a temporal sampling
resolution of at least one (1)
concentration and flow rate
measurement per minute, meet the
requirements expressed in the definition
of ‘‘hourly average’’ in paragraph (c)(14)
of this section, and meet the ‘‘CEM
Performance Specifications’’ in sections
6(C) and (D) of MSCC’s 1998 exhibit,
except that MSCC shall also notify EPA
in writing of each annual Relative
Accuracy Test Audit at least 25 working
days prior to actual testing.
(4) Auxiliary vent stacks.
(i) Emission limits.
(A) Total combined emissions of SO2
from the auxiliary vent stacks shall not
exceed 12.0 pounds per 3-hour period;
(B) Total combined emissions of SO2
from the auxiliary vent stacks shall not
exceed 96.0 pounds per calendar day;
(C) Total combined emissions of SO2
from the auxiliary vent stacks shall not
exceed 35,040 pounds per calendar
year; and
(D) The H2S concentration in the fuel
burned in the Railroad Boiler, the H–1
Unit, the H1–A unit, the H1–1 unit, and
the H1–2 unit, while any of these units
is exhausting to the auxiliary vent
stacks, shall not exceed 160 ppm per 3hour period and 100 ppm per calendar
day.
(ii) Compliance determining method.
(A) Compliance with the emission
limits in paragraph (g)(4)(i) of this
section shall be determined by
measuring the H2S concentration of the
fuel burned in the Railroad Boiler, the
H–1 Unit, the H1–A unit, the H1–1 unit,
and the H1–2 unit (when fuel other than
natural gas is burned in one or more of
these units) according to the procedures
in paragraph (g)(4)(ii)(C) of this section.
(B) Beginning June 20, 2008, MSCC
shall maintain logs of:
(1) The dates and time periods that
emissions are exhausted through the
auxiliary vent stacks,
(2) The heaters and boilers that are
exhausting to the auxiliary vent stacks
during such time periods, and
(3) The type of fuel burned in the
heaters and boilers during such time
periods.
(C) Beginning June 20, 2008, MSCC
shall measure the H2S content of the
fuel burned when fuel other than
natural gas is burned in a heater or
boiler that is exhausting to an auxiliary
vent stack. MSCC shall begin measuring
the H2S content of the fuel at the fuel
header within one (1) hour from when
a heater or boiler begins exhausting to
an auxiliary vent stack and on a onceper-3-hour period frequency until no
heater or boiler is exhausting to an
auxiliary vent stack. To determine the
H2S content of the fuel burned, MSCC
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shall use length-of-stain detector tubes
pursuant to ASTM Method D4810–06,
‘‘Standard Test Method for Hydrogen
Sulfide in Natural Gas Using Length-ofStain Detector Tubes’’ (incorporated by
reference, see paragraph (j) of this
section) with the appropriate sample
tube range. If the results exceed the
tube’s range, another tube of a higher
range must be used until results are in
the tube’s range.
(5) SRU 30-meter stack.
(i) Emission limits.
(A) Emissions of SO2 from the SRU
30-meter stack shall not exceed 12.0
pounds per 3-hour period;
(B) Emissions of SO2 from the SRU
30-meter stack shall not exceed 96.0
pounds per calendar day;
(C) Emissions of SO2 from the SRU
30-meter stack shall not exceed 35,040
pounds per calendar year; and
(D) The H2S concentration in the fuel
burned in the heaters and boilers
described in paragraph (g)(1)(iv) of this
section, while any of these units is
exhausting to the SRU 30-meter stack,
shall not exceed 160 ppm per 3-hour
period and 100 ppm per calendar day.
(ii) Compliance determining method.
(A) Compliance with the emission
limits in paragraph (g)(5)(i) of this
section shall be determined by
measuring the H2S concentration of the
fuel burned in the heaters and boilers
described in paragraph (g)(1)(iv) of this
section (when fuel other than natural
gas is burned in one or more of these
heaters or boilers) according to the
procedures in paragraph (g)(5)(ii)(C) of
this section.
(B) Beginning June 20, 2008, MSCC
shall maintain logs of:
(1) The dates and time periods that
emissions are exhausted through the
SRU 30-meter stack,
(2) The heaters and boilers that are
exhausting to the SRU 30-meter stack
during such time periods, and
(3) The type of fuel burned in the
heaters and boilers during such time
periods.
(C) Beginning June 20, 2008, MSCC
shall measure the H2S content of the
fuel burned when fuel other than
natural gas is burned in a heater or
boiler that is exhausting to the SRU 30meter stack. MSCC shall begin
measuring the H2S content of the fuel at
the fuel header within one (1) hour from
when any heater or boiler begins
exhausting to the SRU 30-meter stack
and on a once-per-3-hour period
frequency until no heater or boiler is
exhausting to the SRU 30-meter stack.
To determine the H2S content of the fuel
burned, MSCC shall use length-of-stain
detector tubes pursuant to ASTM
Method D4810–06, ‘‘Standard Test
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Method for Hydrogen Sulfide in Natural
Gas Using Length-of-Stain Detector
Tubes’’ (incorporated by reference, see
paragraph (j) of this section) with the
appropriate sample tube range. If the
results exceed the tube’s range, another
tube of a higher range must be used
until results are in the tube’s range.
(6) Data reporting requirements:
(i) MSCC shall submit quarterly
reports beginning with the first calendar
quarter following May 21, 2008. The
quarterly reports shall be submitted
within 30 days of the end of each
calendar quarter. The quarterly reports
shall be submitted to EPA at the
following address: Air Program Contact,
EPA Montana Operations Office,
Federal Building, 10 West 15th Street,
Suite 3200, Helena, MT 59626.
The quarterly report shall be certified
for accuracy in writing by a responsible
MSCC official. The quarterly report
shall consist of both a comprehensive
electronic-magnetic report and a written
hard copy data summary report.
(ii) The electronic report shall be on
magnetic or optical media, and such
submittal shall follow the reporting
format of electronic data being
submitted to the MDEQ. EPA may
modify the reporting format delineated
in this section, and, thereafter, MSCC
shall follow the revised format. In
addition to submitting the electronic
quarterly reports to EPA, MSCC shall
also record, organize, and archive for at
least five (5) years the same data, and
upon request by EPA, MSCC shall
provide EPA with any data archived in
accordance with this provision. The
electronic report shall contain the
following:
(A) Hourly average total sulfur
concentrations as H2S or SO2 in ppm, in
the gas stream to the flare(s);
(B) Hourly average H2S concentrations
of the flare pilot and purge gases in
ppm;
(C) Hourly average SO2 concentrations
in ppm from the SRU 100-meter stack;
(D) Hourly average volumetric flow
rates in SCFH in the gas stream to the
flare(s) and in the SRU 100-meter stack;
(E) Hourly average volumetric flow
rates in SCFH of the flare pilot and
purge gases;
(F) Hourly average temperature (in (F)
and pressure (in mm or inches of Hg) in
the gas stream to the flare(s);
(G) Hourly emissions in pounds per
clock hour from the flare(s) and SRU
100-meter stack;
(H) Daily calibration data for all flare
CEMS, all pilot gas and purge gas
CEMS, and the SRU 100-meter stack
CEMS;
(iii) The quarterly written report shall
contain the following information:
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(A) The 3-hour emissions in pounds
per 3-hour period from the flare(s) and
SRU 100-meter stack, and 3-hour H2S
concentrations in the fuel burned in the
heaters and boilers described in
paragraphs (g)(1)(iii) and (iv) of this
section while any of these units is
exhausting to the SRU 30-meter stack or
auxiliary vent stacks and burning fuel
other than natural gas;
(B) Periods in which only natural gas
or an inert gas was used as flare pilot
gas or purge gas or both;
(C) Daily emissions in pounds per
calendar day from the SRU 100-meter
stack;
(D) Annual emissions of SO2 in
pounds per calendar year from the SRU
100-meter stack;
(E) The results of all quarterly
Cylinder Gas Audits (CGA), Relative
Accuracy Audits (RAA) and annual
Relative Accuracy Test Audits (RATA)
for all total sulfur analyzer(s), all H2S
analyzer(s), and the SRU 100-meter
stack CEMS, and the results of all
annual calibrations and verifications for
the volumetric flow, temperature, and
pressure monitors;
(F) For all periods of flare volumetric
flow rate monitoring system or total
sulfur analyzer system downtime, SRU
100-meter CEMS downtime, flare pilot
gas or purge gas volumetric flow or H2S
analyzer system downtime, failure to
obtain or analyze a grab or integrated
sample, or failure to obtain an H2S
concentration sample as required by
paragraphs (g)(4)(ii)(C) and (g)(5)(ii)(C)
of this section, the written report shall
identify:
(1) Dates and times of downtime or
failure;
(2) Reasons for downtime or failure;
(3) Corrective actions taken to
mitigate downtime or failure; and
(4) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(G) For all periods that the range of
the flare or any pilot or purge gas
volumetric flow rate monitor(s), any
flare total sulfur analyzer(s), or any pilot
or purge gas H2S analyzer(s), is
exceeded, the written report shall
identify:
(1) Date and time when the range of
the volumetric flow monitor(s), total
sulfur analyzer(s), or H2S analyzer(s)
was exceeded; and
(2) The other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, used to determine flare
emissions;
(H) For all periods that the flare
volumetric flow monitor or monitors are
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recording flow, yet any Flare Water Seal
Monitoring Device indicates there is no
flow, the written report shall identify:
(1) Date, time, and duration when the
flare volumetric flow monitor(s)
recorded flow, yet any Flare Water Seal
Monitoring Device indicated there was
no flow;
(I) For each 3-hour period and
calendar day in which the flare
emission limit, the SRU 100-meter stack
emission limits, the SRU 30-meter stack
emission limits, or auxiliary vent stack
emission limits are exceeded, the
written report shall identify:
(1) The date, start time, and end time
of the excess emissions;
(2) Total hours of operation with
excess emissions, the hourly emissions,
the 3-hour emissions, and the daily
emissions;
(3) All information regarding reasons
for operating with excess emissions; and
(4) Corrective actions taken to
mitigate excess emissions;
(J) For instances in which emissions
are exhausted through the auxiliary vent
stacks or 30-meter stack, the quarterly
written report shall identify:
(1) The dates and time periods that
emissions were exhausted through the
auxiliary vent stacks or the 30-meter
stack;
(2) The heaters and boilers that were
exhausting to the auxiliary vent stacks
or 30-meter stack during such time
periods; and
(3) The type of fuel burned in the
heaters and boilers during such time
periods; and
(K) When no excess emissions have
occurred or the continuous monitoring
system(s) or manual system(s) have not
been inoperative, repaired, or adjusted,
such information shall be stated in the
report.
(h) Flare compliance determining
method.
(1) Compliance with the emission
limits in paragraphs (d)(2)(i), (e)(2)(i),
(f)(2)(i) and (g)(2)(i) of this section shall
be determined by measuring the total
sulfur concentration and volumetric
flow rate of the gas stream to the flare(s)
(corrected to one (1) atmosphere
pressure and 68° F) and using the
methods contained in the flare
monitoring plan required by paragraph
(h)(5) of this section. The volumetric
flow rate of the gas stream to the flare(s)
shall be determined in accordance with
the requirements in paragraph (h)(2) of
this section and the total sulfur
concentration of the gas stream to the
flare(s) shall be determined in
accordance with paragraph (h)(3) of this
section.
(2) Flare flow monitoring:
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(i) Within 365 days after receiving
EPA approval of the flare monitoring
plan required by paragraph (h)(5) of this
section, each facility named in
paragraph (a) of this section shall install
and calibrate, and, thereafter, calibrate,
maintain and operate, a continuous flow
monitoring system capable of measuring
the volumetric flow of the gas stream to
the flare(s) in accordance with the
specifications contained in paragraphs
(h)(2)(iii) through (vi) of this section.
The flow monitoring system shall
require more than one flow monitoring
device or flow measurements at more
than one location if one monitor cannot
measure the total volumetric flow to
each flare.
(ii) Volumetric flow monitors meeting
the proposed volumetric flow
monitoring specifications below should
be able to measure the majority of
volumetric flow in the gas streams to the
flare. However, in rare events (e.g.,
upset conditions) the flow to the flare
may exceed the range of the monitor. In
such cases, or when the volumetric flow
monitor or monitors are not working,
other methods approved by EPA in the
flare monitoring plan required by
paragraph (h)(5) of this section shall be
used to determine the volumetric flow
rate to the flare, which shall then be
used to calculate SO2 emissions. In
quarterly reports, sources shall indicate
when these other methods are used.
(iii) The flare gas stream volumetric
flow rate shall be measured on an actual
wet basis, converted to Standard
Conditions, and reported in SCFH. The
minimum detectable velocity of the flow
monitoring device(s) shall be 0.1 feet
per second (fps). The flow monitoring
device(s) shall continuously measure
the range of flow rates corresponding to
velocities from 0.5 to 275 fps and have
a manufacturer’s specified accuracy of
±5% of the measured flow over the
range of 1.0 to 275 fps and ±20% of the
measured flow over the range of 0.1 to
1.0 fps. The volumetric flow monitor(s)
shall feature automated daily
calibrations at low and high ranges. The
volumetric flow monitor(s) shall be
calibrated annually according to
manufacturer’s specifications.
(iv) For correcting flow rate to
standard conditions (defined as 68°F
and 760 mm, or 29.92 inches, of Hg),
temperature and pressure shall be
monitored continuously. Temperature
and pressure shall be monitored in the
same location as volumetric flow, and
the temperature and pressure monitors
shall be calibrated prior to installation
according to manufacturer’s
specifications and, thereafter, annually
to meet accuracy specifications as
follows: The temperature monitor shall
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be calibrated to within ± 2.0% at
absolute temperature and the pressure
monitor shall be calibrated to within ±
5.0 mmHg;
(v) The flow monitoring device(s)
shall be calibrated prior to installation
to demonstrate accuracy of the
measured flow to within 5.0% at flow
rates equivalent to 30%, 60%, and 90%
of monitor full scale.
(vi) Each volumetric flow device shall
achieve a temporal sampling resolution
of at least one (1) flow rate measurement
per minute, meet the requirements
expressed in the definition of ‘‘hourly
average’’ in paragraph (c)(14) of this
section, and be installed in a manner
and at a location that will allow for
accurate measurements of the total
volume of the gas stream going to each
flare. Each temperature and pressure
monitoring device shall achieve a
temporal sampling resolution of at least
one (1) measurement per minute, meet
the requirements expressed in the
definition of ‘‘hourly average’’ in
paragraph (c)(14) of this section, and be
installed in a manner that will allow for
accurate measurements.
(vii) In addition to the continuous
flow monitors, facilities may use flare
water seal monitoring devices to
determine whether there is flow going to
the flare. If used, owners or operators
shall install, calibrate, operate, and
maintain these devices according to
manufacturer’s specifications. The
devices shall include a continuous
monitoring system that:
(A) Monitors the status of the water
seal to indicate when flow is going to
the flare;
(B) Automatically records the time
and duration when flow is going to the
flare; and
(C) Verifies that the physical seal has
been restored after flow has been sent to
the flare.
If the water seal monitoring devices
indicate that there is no flow going to
the flare, yet the continuous flow
monitor is indicating flow, the
presumption will be that no flow is
going to the flare.
(viii) Each facility named in
paragraph (a) of this section, that does
not certify that only natural gas or an
inert gas is used for both the pilot gas
and purge gas, shall determine the
volumetric flow of each pilot gas and
purge gas stream for which natural gas
or inert gas is not used by one of the
following methods:
(A) Measure the volumetric flow of
the gas using continuous flow
monitoring devices on an actual wet
basis, converted to Standard Conditions,
and reported in SCFH. Each flow
monitoring device shall achieve a
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temporal sampling resolution of at least
one (1) flow rate measurement per
minute, meet the requirements
expressed in the definition of ‘‘hourly
average’’ in paragraph (c)(14) of this
section, and be installed in a manner
and at a location that will allow for
accurate measurements of the total
volume of the gas. Gas flow rate monitor
accuracy determinations shall be
required at least once every 48 months
or more frequently at routine refinery
turn-around. In cases when the flow
monitoring device or devices are not
working or the range of the monitoring
device(s) is exceeded, other methods
approved by EPA in the flare monitoring
plan required by paragraph (h)(5) of this
section shall be used to determine
volumetric flow of the gas which shall
then be used to calculate SO2 emissions.
In quarterly reports, sources shall
indicate when other methods are used;
or
(B) Use parameters and methods
approved by EPA in the flare monitoring
plan required by paragraph (h)(5) of this
section to calculate the volumetric flows
of the gas, in SCFH.
(3) Flare concentration monitoring:
(i) Within 365 days after receiving
EPA approval of the flare monitoring
plan required by paragraph (h)(5) of this
section, each facility named in
paragraph (a) of this section shall
determine the total sulfur concentration
of the gas stream to the flare(s) using
either continuous total sulfur analyzers
or grab or integrated sampling with lab
analysis, as described in the following
paragraphs:
(A) Continuous total sulfur
concentration monitoring. If a facility
chooses to use continuous total sulfur
concentration monitoring, the following
requirements apply:
(1 ) The facility shall install and
calibrate, and, thereafter, calibrate,
maintain and operate, a continuous total
sulfur concentration monitoring system
capable of measuring the total sulfur
concentration of the gas stream to each
flare. Continuous monitoring shall occur
at a location or locations that are
representative of the gas combusted in
the flare and be capable of measuring
the normally expected range of total
sulfur in the gas stream to the flare. The
concentration monitoring system shall
require more than one concentration
monitoring device or concentration
measurements at more than one location
if one monitor cannot measure the total
sulfur concentration to each flare. Total
sulfur concentration shall be reported as
H2S or SO2 in ppm. In cases when the
total sulfur analyzer or analyzers are not
working or the concentration of the total
sulfur exceeds the range of the
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analyzer(s), other methods, approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section, shall be used to determine total
sulfur concentrations, which shall then
be used to calculate SO2 emissions. In
quarterly reports, sources shall indicate
when these other methods are used.
(2 ) The total sulfur analyzer(s) shall
achieve a temporal sampling resolution
of at least one (1) concentration
measurement per 15 minutes, meet the
requirements expressed in the definition
of ‘‘hourly average’’ in paragraph (c)(14)
of this section, be installed, certified (on
a concentration basis), and operated in
accordance with 40 CFR part 60,
Appendix B, Performance Specification
5, and be subject to and meet the quality
assurance and quality control
requirements (on a concentration basis)
of 40 CFR part 60, Appendix F.
(3) Each affected facility named in
paragraph (a) of this section shall notify
the Air Program Contact at EPA’s
Montana Operations Office, Federal
Building, 10 West 15th Street, Suite
3200, Helena, MT 59626, in writing of
each Relative Accuracy Test Audit a
minimum of 25 working days prior to
the actual testing.
(B) Grab or integrated total sulfur
concentration monitoring: If a facility
chooses grab or integrated sampling
instead of continuous total sulfur
concentration monitoring, the facility
shall comply with the methods
specified in either paragraph
(h)(3)(i)(B)(1) (‘‘Grab Sampling’’) or
(h)(3)(B)(i)(B)(2 ) (‘‘Integrated
Sampling’’), and the requirements of
paragraphs (h)(3)(i)(B)(3) (‘‘Sample
Analysis’’), (h)(3)(i)(B)(4)
(‘‘Exemptions’’), and (h)(3)(i)(B)(5)
(‘‘Missing or Unanalyzed Sample’’) of
this section, as follows:
(1) Grab Sampling. Each facility that
chooses to use grab sampling shall meet
the following requirements: if the flow
rate of the gas stream to the flare in any
consecutive 15-minute period
continuously exceeds 0.5 feet per
second (fps) and the water seal
monitoring device, if any, indicates that
flow is going to the flare, a grab sample
shall be collected within 15 minutes.
The grab sample shall be collected at a
location that is representative of the gas
combusted in the flare. Thereafter, the
sampling frequency shall be one (1) grab
sample every three (3) hours, which
shall continue until the velocity of the
gas stream going to the flare in any
consecutive 15-minute period is
continuously 0.5 fps or less. Samples
shall be analyzed according to
paragraph (h)(3)(i)(B)(3) of this section.
The requirements of this paragraph
(h)(3)(i)(B)(1) shall apply to each flare at
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a facility for which the sampling
threshold is exceeded.
(2) Integrated Sampling. Each facility
that chooses to use integrated sampling
shall meet the following requirements: if
the flow rate of the gas stream to the
flare in any consecutive 15-minute
period continuously exceeds 0.5 feet per
second (fps) and the water seal
monitoring device, if any, indicates that
flow is going to the flare, a sample shall
be collected within 15 minutes. The
sample shall be collected at a location
that is representative of the gas
combusted in the flare. The sampling
frequency, thereafter, shall be a
minimum of one (1) aliquot for each 15minute period until the sample
container is full, or until the end of a 3hour period is reached, whichever
comes sooner. Within 30 minutes
thereafter, a new sample container shall
be placed in service, and sampling on
this frequency, and in this manner, shall
continue until the velocity of the gas
stream going to the flare in any
consecutive 15-minute period is
continuously 0.5 fps or less. Samples
shall be analyzed according to
paragraph (h)(3)(i)(B)(3) of this section.
The requirements of this paragraph
(h)(3)(i)(B)(2) shall apply to each flare at
a facility for which the sampling
threshold is exceeded.
(3) Samples shall be analyzed using
ASTM Method D4468–85 (Reapproved
2000) ‘‘Standard Test Method for Total
Sulfur in Gaseous Fuels by
Hydrogenolysis and Rateometric
Colorimetry,’’ (incorporated by
reference, see paragraph (j) of this
section) ASTM Method D5504–01
(Reapproved 2006) ‘‘Standard Test
Method for Determination of Sulfur
Compounds in Natural Gas and Gaseous
Fuels by Gas Chromatography and
Chemiluminescence,’’ (incorporated by
reference, see paragraph (j) of this
section) or 40 CFR part 60, Appendix
A–5, Method 15A ‘‘Determination of
Total Reduced Sulfur Emissions From
the Sulfur Recovery Plants in Petroleum
Refineries.’’ Total sulfur concentration
shall be reported as H2S or SO2 in ppm.
(4) Exemptions. For facilities using a
sampling method specified in either
paragraph (h)(3)(i)(B)(1) (‘‘Grab
Sampling’’) or (h)(3)(i)(B)(2) (‘‘Integrated
Sampling’’) of this section, obtaining a
sample is not required if flaring is a
result of a catastrophic or other unusual
event, including a major fire or an
explosion at the facility, such that
collecting a sample at the EPA-approved
location during the relevant period is
infeasible or constitutes a safety hazard,
provided that the owner or operator
shall collect a sample at an alternative
location if feasible, safe, and
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representative of the flaring event. The
owner or operator shall demonstrate to
EPA that it was infeasible or unsafe to
collect a sample or to collect a sample
at the sampling location approved by
EPA in the flare monitoring plan
required by paragraph (h)(5) of this
section. The owner or operator shall
also demonstrate to EPA that any
sample collected at an alternative
location is representative of the flaring
incident. If a facility experiences
ongoing difficulties collecting grab or
integrated samples in accordance with
its flare monitoring plan approved by
EPA pursuant to paragraph (h)(5) of this
section, EPA may require the facility to
revise its flare monitoring plan and use
continuous total sulfur concentration
monitoring as described in paragraph
(h)(3)(i)(A) of this section or other
reliable method to determine total sulfur
concentrations of the gas stream to the
flare.
(5) Missing or Unanalyzed Samples.
For facilities using a sampling method
specified in either paragraph
(h)(3)(i)(B)(1) (‘‘Grab Sampling’’) or
(h)(3)(i)(B)(2) (‘‘Integrated Sampling’’) of
this section, if a required sample is not
obtained or analyzed for any reason,
other methods approved by EPA in the
flare monitoring plan required by
paragraph (h)(5) of this section shall be
used to determine total sulfur
concentrations, which shall then be
used to calculate SO2 emissions. In
quarterly reports, sources shall indicate
when these other methods are used.
(6) Reporting. For facilities using a
sampling method specified in either
paragraph (h)(3)(i)(B)(1 ) (‘‘Grab
Sampling’’) or (h)(3)(i)(B)(2 )
(‘‘Integrated Sampling’’) of this section,
since normally only one (1) sample per
flare will be analyzed for a 3-hour
period, the total sulfur concentration of
a sample obtained during a given 3-hour
period shall be substituted for each hour
of such 3-hour period. If integrated
sampling for a flare produces more than
one (1) sample container during a 3hour period, and the gas in each
container is analyzed separately, the
concentrations for the containers shall
be averaged. For that flare, the resulting
average shall be substituted for each
hour of the 3-hour period during which
the sampling occurred. The substituted
hourly total sulfur concentrations
determined per this paragraph shall be
used to determine hourly emissions
from the flare.
(ii) Each facility named in paragraph
(a) of this section that does not certify
that only natural gas or an inert gas is
used for both the pilot gas and purge gas
shall determine the H2S concentration
of each pilot gas and purge gas stream
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21463
for which natural gas or inert gas is not
used by one of the following methods:
(A) Measure the H2S concentration of
the gas by continuous H2S analyzer. The
H2S concentration analyzer(s) shall
achieve a temporal sampling resolution
of at least one (1) concentration
measurement per three (3) minutes,
meet the requirements expressed in the
definition of ‘‘hourly average’’ in
paragraph (c)(14) of this section, be
installed, certified (on a concentration
basis), and operated in accordance with
40 CFR part 60, Appendix B,
Performance Specification 2, and be
subject to and meet the quality
assurance and quality control
requirements (on a concentration basis)
of 40 CFR part 60, Appendix F. In cases
where the H2S analyzer or analyzers are
not working or the H2S concentration
exceeds the range of the analyzer(s),
other methods approved by EPA in the
flare monitoring plan required by
paragraph (h)(5) of this section shall be
used to determine the H2S concentration
of the gas, which shall then be used to
calculate SO2 emissions. In quarterly
reports, sources shall indicate when
other methods are used; or
(B) Use methods approved by EPA as
part of the facility’s flare monitoring
plan required by paragraph (h)(5) of this
section to estimate the H2S
concentration of the gas.
(4) Calculation of SO2 emissions from
flares. Methods for calculating hourly
and 3-hour SO2 emissions from flares
shall be submitted to EPA as part of the
flare monitoring plan required by
paragraph (h)(5) of this section.
Following approval by EPA, such
methods shall be followed for
calculating hourly and 3-hour SO2
emissions from a facility’s flare(s).
(5) By October 20, 2008, each facility
named in paragraph (a) of this section
shall submit a flare monitoring plan.
Each flare monitoring plan shall
include, at a minimum, the following:
(i) A facility plot plan showing the
location of each flare in relation to the
general plant layout;
(ii) Drawing(s) with dimensions,
preferably to scale, and an as-built
process flow diagram of the flare(s)
identifying major components, such as
flare header, flare stack, flare tip(s) or
burner(s), purge gas system, pilot gas
system, water seal, knockout drum, and
molecular seal;
(iii) A representative flow diagram
showing the interconnections of the
flare system(s) with vapor recovery
system(s), process units, and other
equipment as applicable;
(iv) A complete description of the gas
flaring process for an integrated gas
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Federal Register / Vol. 73, No. 77 / Monday, April 21, 2008 / Rules and Regulations
flaring system that describes the method
of operation of the flares;
(v) A complete description of the
vapor recovery system(s) which have
interconnection to a flare, such as
compressor description(s); design
capacities of each compressor and the
vapor recovery system; and the method
currently used to determine and record
the amount of vapors recovered;
(vi) A complete description of the
proposed method to monitor, determine,
and record the total volume and total
sulfur concentration of gases combusted
in the flare, including drawing(s) with
dimensions, preferably to scale,
showing the following information for
the proposed flare gas stream
monitoring systems:
(A) The locations to be used for all
monitoring and sampling, including, but
not limited to: Flare flow monitors, total
sulfur analyzers, concentration
integrated sampling, concentration grab
sampling, water seal monitoring
devices, pilot and purge gas flow
monitors, and pilot and purge gas
concentration monitors;
(vii) A description of the method(s)
used to determine, and reasoning
behind, all monitoring and sampling
locations;
(viii) The following information
regarding pilot gas and purge gas for
each flare:
(A) Type(s) of gas used;
(B) A complete description of the
monitor(s) to be used, or the other
parameters that will be used and
monitored, to determine volumetric
flows of the pilot gas and purge gas
streams for which natural gas or inert
gas is not used; and
(C) A complete description of the
analyzer(s) to be used to determine, or
other methods that will be used to
estimate, the H2S concentrations in the
pilot gas and purge gas streams for
which natural gas or inert gas is not
used;
(ix) A detailed description of
manufacturer’s specifications,
including, but not limited to, make,
model, type, range, precision, accuracy,
calibration, maintenance, quality
assurance procedure, and any other
relevant specifications and information
referenced in paragraphs (h)(2) and (3)
of this section for all existing and
proposed flow monitoring devices and
total sulfur analyzers;
(x) The following information if grab
or integrated sampling is used:
(A) A complete description of
proposed analytical and sampling
methods if grab or integrated sampling
methods will be used for determining
the total sulfur concentration of the gas
stream going to the flare;
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18:55 Apr 18, 2008
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(B) A detailed description of
manufacturer’s specifications,
including, but not limited to, make,
model, type, maintenance, and quality
assurance procedures for the integrated
sampling device, if used; and
(C) A complete description of the
proposed method to alert personnel
designated to collect samples that the
trigger for collecting a sample has
occurred;
(xi) A complete description of the
methods to be used to estimate flare
emissions when any flare, pilot gas, or
purge gas volumetric flow monitoring
devices, total sulfur analyzers, or grab or
integrated sampling methods, or pilot
gas or purge gas H2S analyzers are not
working or available, or the operating
range of the monitors or analyzers is
exceeded;
(xii) A complete description of the
proposed data recording, collection, and
management system and any other
relevant specifications and information
referenced in paragraphs (h)(2) and (3)
of this section for each flare monitoring
system;
(xiii) The following information for
each flare using a water seal monitoring
device:
(A) A detailed description of
manufacturer’s specifications,
including, but not limited to, make,
model, type, maintenance, and quality
assurance procedures;
(B) A complete description of the
proposed methods to determine that the
water seal is no longer intact and flow
is going to the flare, and the data used
to establish, and reasoning behind, these
methods;
(xiv) A schedule for the installation
and operation of each flare monitoring
system consistent with the deadline in
paragraphs (h)(2) and (h)(3) of this
section; and
(xv) A complete description of the
methods to be used for calculating
hourly and 3-hour SO2 emissions from
flares.
(6) Thirty (30) days prior to installing
any continuous monitor or integrated
sampler pursuant to paragraphs (h)(2)
and (3) of this section, each facility
named in paragraph (a) of this section
shall submit for EPA review a quality
assurance/quality control (QA/QC) plan
for each monitor or sampler being
installed.
(i) Affirmative defense provisions for
exceedances of flare emission limits
during malfunctions, startups, and
shutdowns.
(1) In response to an action to enforce
the emission limits in paragraphs
(d)(2)(i), (e)(2)(i), (f)(2)(i), and (g)(2)(i) of
this section, owners and/or operators of
the facilities named in paragraph (a) of
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this section may assert an affirmative
defense to a claim for civil penalties for
exceedances of such limits during
periods of malfunction, startup, or
shutdown. To establish the affirmative
defense and to be relieved of a civil
penalty in any action to enforce such a
limit, the owner or operator of the
facility must meet the notification
requirements of paragraph (i)(2) of this
section in a timely manner and prove by
a preponderance of evidence that:
(i) For claims of malfunction:
(A) The excess emissions were caused
by a sudden, unavoidable breakdown of
equipment, or a sudden, unavoidable
failure of a process to operate in the
normal or usual manner, beyond the
control of the owner or operator;
(B) The excess emissions:
(1) Did not stem from any activity or
event that could have been foreseen and
avoided, or planned for; and
(2) Could not have been avoided by
better operation and maintenance
practices;
(C) Repairs were made as
expeditiously as possible when the
applicable emission limitations were
being exceeded. Off-shift and overtime
labor were used, to the extent
practicable;
(D) The amount and duration of the
excess emissions (including any bypass)
were minimized to the maximum extent
practicable during periods of such
emissions;
(ii) For claims of startup or shutdown:
(A) All or a portion of the facility was
in startup or shutdown mode, resulting
in the need to route gases to the flare;
(B) The periods of excess emissions
that occurred during startup and
shutdown were short and infrequent
and could not have been prevented
through careful planning and design or
better operation and maintenance
practices; and
(C) The frequency and duration of
operation in startup or shutdown mode
were minimized to the maximum extent
practicable;
(iii) For claims of malfunction,
startup, or shutdown:
(A) If the excess emissions resulted
from a bypass of control equipment or
a process, then the bypass was
unavoidable to prevent loss of life,
personal injury, or severe property
damage;
(B) All possible steps were taken to
minimize the impact of the excess
emissions on ambient air quality;
(C) All emissions monitoring systems
were kept in operation if at all possible;
(D) The owner or operator’s actions in
response to the excess emissions were
documented by properly signed,
contemporaneous operating logs;
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(E) The excess emissions were not
part of a recurring pattern indicative of
inadequate design, operation, or
maintenance;
(F) At all times, the facility was
operated in a manner consistent with
good practices for minimizing
emissions; and
(G) During the period of excess
emissions, there were no exceedances of
the SO2 NAAQS that could be attributed
to the emitting source.
(2) Notification. The owner or
operator of the facility experiencing an
exceedance of its flare emission limit(s)
during startup, shutdown, or
malfunction shall notify EPA verbally as
soon as possible, but no later than noon
of EPA’s next working day, and shall
submit written notification to EPA
within 30 days of the initial occurrence
of the exceedance. The written
notification shall explain whether and
how the elements set forth in paragraph
(i)(1) of this section were met, and
include all supporting documentation.
(3) Injunctive relief. The Affirmative
Defense Provisions contained in
paragraph (i)(1) of this section shall not
VerDate Aug<31>2005
18:55 Apr 18, 2008
Jkt 214001
be available to claims for injunctive
relief.
(j) Incorporation by reference. (1) The
materials listed in this paragraph are
incorporated by reference in the
corresponding paragraphs noted. These
incorporations by reference are
approved by the Director of the Federal
Register in accordance with 5 U.S.C.
552(a) and 1 CFR part 51. These
materials are incorporated as they exist
on the date of the approval, and notice
of any change in these materials will be
published in the Federal Register. The
materials are available for purchase at
the corresponding address noted below,
and all are available for inspection at
the National Archives and Records
Administration (NARA) and at the Air
Program, EPA, Region 8, 1595 Wynkoop
Street, Denver, CO. For information on
the availability of this material at
NARA, call 202–741–6030, or go to:
https://www.archives.gov/
federal_register/
code_of_federal_regulations/
ibr_locations.html.
(2) The following materials are
available for purchase from the
PO 00000
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21465
following address: American Society for
Testing and Materials (ASTM), 100 Barr
Harbor Drive, Post Office Box C700,
West Conshohocken, PA 19428–2959,
www.astm.org, or by calling (610) 832–
9585.
(i) ASTM Method D4468–85
(Reapproved 2000), Standard Test
Method for Total Sulfur in Gaseous
Fuels by Hydrogenolysis and
Rateometric Colorimetry, IBR approved
for paragraph (h)(3)(i)(B)(3) of this
section.
(ii) ASTM Method D4810–06,
Standard Test Method for Hydrogen
Sulfide in Natural Gas Using Length-ofStain Detector Tubes, IBR approved for
paragraphs (f)(3)(ii)(B), (g)(4)(ii)(C), and
(g)(5)(ii)(C) of this section.
(ii) ASTM Method D5504–01
(Reapproved 2006), Standard Test
Method for Determination of Sulfur
Compounds in Natural Gas and Gaseous
Fuels by Gas Chromatography IBR
approved for paragraph (h)(3)(i)(B)(3) of
this section.
[FR Doc. E8–7868 Filed 4–18–08; 8:45 am]
BILLING CODE 6560–50–P
E:\FR\FM\21APR2.SGM
21APR2
Agencies
[Federal Register Volume 73, Number 77 (Monday, April 21, 2008)]
[Rules and Regulations]
[Pages 21418-21465]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: E8-7868]
[[Page 21417]]
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Part II
Environmental Protection Agency
-----------------------------------------------------------------------
40 CFR Part 52
Federal Implementation Plan for the Billings/Laurel, Montana, Sulfur
Dioxide Area; Final Rule
Federal Register / Vol. 73, No. 77 / Monday, April 21, 2008 / Rules
and Regulations
[[Page 21418]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 52
[EPA-R08-OAR-2006-0098; FRL-8551-2]
RIN 2008-AA01
Federal Implementation Plan for the Billings/Laurel, MT, Sulfur
Dioxide Area
AGENCY: Environmental Protection Agency (EPA).
ACTION: Final rule.
-----------------------------------------------------------------------
SUMMARY: The Environmental Protection Agency (EPA) is promulgating a
Federal Implementation Plan (FIP) containing emission limits and
compliance determining methods for several sources located in Billings
and Laurel, Montana. EPA is promulgating a FIP because of our previous
partial and limited disapprovals of the Billings/Laurel Sulfur Dioxide
(SO2) State Implementation Plan (SIP). The intended effect of this
action is to assure attainment of the SO2 National Ambient Air Quality
Standards (NAAQS) in the Billings/Laurel, Montana area. EPA is taking
this action under sections 110, 301, and 307 of the Clean Air Act
(Act).
DATES: Effective Date: This final rule is effective May 21, 2008. The
incorporation by reference of certain publications listed in this
regulation is approved by the Director of the Federal Register as of
May 21, 2008.
ADDRESSES: EPA has established a docket for this action under Docket ID
No. EPA-R08-OAR-2006-0098. All documents in the docket are listed on
the https://www.regulations.gov Web site. Although listed in the index,
some information is not publicly available, e.g., Confidential Business
Information (CBI) or other information whose disclosure is restricted
by statute. Certain other material, such as copyrighted material, is
not placed on the Internet and will be publicly available only in hard
copy form. Publicly available docket materials are available either
electronically through https://www.regulations.gov or in hard copy at
the Air and Radiation Program, Environmental Protection Agency (EPA),
Region 8, 1595 Wynkoop Street, Denver, Colorado 80202-1129. EPA
requests that if at all possible, you contact the individual listed in
the FOR FURTHER INFORMATION CONTACT section to view the hard copy of
the docket. You may view the hard copy of the docket Monday through
Friday, 8 a.m. to 4 p.m., excluding Federal holidays.
FOR FURTHER INFORMATION CONTACT: Laurie Ostrand, Air and Radiation
Program, Environmental Protection Agency (EPA), Region 8, 1595 Wynkoop
Street, Denver, Colorado 80202-1129, (303) 312-6437,
ostrand.laurie@epa.gov.
SUPPLEMENTARY INFORMATION:
Table of Contents
Definitions
I. Background of the Final Rules
II. Issues Raised by Commenters and EPA's Response
A. FIP Not Necessary
B. EPA Exceeded Its Authority in Proposing a FIP
C. Flare Monitoring
D. Flare Limits
E. Concerns With Dispersion Modeling
F. Miscellaneous Comments
G. MSCC Specific Issues
H. ConocoPhillips Specific Issues
I. ExxonMobil Specific Issues
J. CHS Inc. Specific Issues
III. Summary of the Final Rules and Changes From the July 12, 2006,
Proposal
A. Flare Requirements Applicable to All Sources
B. CHS Inc.
C. ConocoPhillips
D. ExxonMobil
E. Montana Sulphur & Chemical Company (MSCC)
F. Modeling to Support Emission Limits
IV. Statutory and Executive Order Reviews
A. Executive Order 12866, Regulatory Planning Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132, Federalism
F. Executive Order 13175, Coordination With Indian Tribal
Governments
G. Executive Order 13045, Protection of Children From
Environmental Health Risks and Safety Risks
H. Executive Order 13211, Actions That Significantly Affect
Energy Supply, Distribution, or Use
I. National Technology Transfer and Advancement Act
J. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
K. Congressional Review Act
L. Petitions for Judicial Review
Definitions
For the purpose of this document, we are giving meaning to certain
words or initials as follows:
(i) The words or initials Act or CAA mean or refer to the Clean Air
Act, unless the context indicates otherwise.
(ii) The initials API mean or refer to the American Petroleum
Institute.
(iii) The initials BAAQMD mean or refer to the Bay Area Air Quality
Management District.
(iv) The initials CEMS mean or refer to continuous emission
monitoring system.
(v) The initials CO mean or refer to carbon monoxide.
(vi) The initials COPC mean or refer to ConocoPhillips.
(vii) The words EPA, we, us or our mean or refer to the United
States Environmental Protection Agency.
(viii) The initials FIP mean or refer to Federal Implementation
Plan.
(ix) The initials H2S mean or refer to hydrogen sulfide.
(x) The initials MBER mean or refer to the Montana Board of
Environmental Review.
(xi) The initials MDEQ mean or refer to the Montana Department of
Environmental Quality.
(xii) The initials MPA mean or refer to the Montana Petroleum
Association.
(xiii) The initials MSCC mean or refer to the Montana Sulphur &
Chemical Company.
(xiv) The initials NAAQS mean or refer to National Ambient Air
Quality Standards
(xv) The initials NEDA/CAP mean or refer to the National
Environmental Development Association's Clean Air Project.
(xvi) The initials NPRA mean or refer to the National Petrochemical
& Refiners Association.
(xvii) The initials SCAQMD mean or refer to the South Coast Air
Quality Management District.
(xviii) The initials SIP mean or refer to State Implementation
Plan.
(xix) The initials SO2 mean or refer to sulfur dioxide.
(xx) The words State or Montana mean the State of Montana, unless
the context indicates otherwise.
(xxi) The initials SRU mean or refer to sulfur recovery unit.
(xxii) The initials SWS mean or refer to sour water stripper.
(xxiii) The initials WETA mean or refer to the Western
Environmental Trade Association.
(xxiv) The initials WSPA mean or refer to the Western States
Petroleum Association.
(xxv) The initials YCC mean or refer to the Yellowstone County
Commissioners.
(xxvi) The initials YVAS mean or refer to the Yellowstone Valley
Audubon Society.
I. Background of the Final Rules
The Clean Air Act (Act) requires EPA to establish national ambient
air quality standards (NAAQS) that protect public health and welfare.
NAAQS have been established for SO2 as follows: 0.030 parts
per million (ppm) annual standard, not to be exceeded in a calendar
year; 0.14 ppm 24-hour standard, not to be exceeded more than once per
calendar year; and 0.5 ppm 3-hour standard, not to be exceeded more
[[Page 21419]]
than once per calendar year. See 40 CFR 50.4 and 50.5. The Act also
requires states to prepare and gain EPA approval of a plan, termed a
State Implementation Plan (SIP), to assure that the NAAQS are attained
and maintained.
Dispersion modeling completed in 1991 and 1993 for the Billings/
Laurel area of Montana predicted that the SO2 NAAQS were not
being attained. As a result, in March 1993 EPA (pursuant to sections
110(a)(2)(H) and 110(k)(5) of the Act, 42 U.S.C. 7410(a)(2)(H) and
7410(k)(5)) requested the State of Montana to revise its previously
approved SO2 SIP for the Billings/Laurel area. See 58 FR
41450, August 4, 1993. In response, the State submitted revisions to
the SO2 SIP on September 6, 1995, August 27, 1996, April 2,
1997, July 29, 1998, and May 4, 2000.
On May 2, 2002 (67 FR 22168) and May 22, 2003 (68 FR 27908), we
partially approved, partially disapproved, limitedly approved, and
limitedly disapproved the Billings/Laurel SO2 SIP. In those
actions we disapproved the following:
The attainment demonstration due to issues with various
emission limits, inappropriate stack height credit, and lack of
emission limits on flares.
The emission limits for Montana Sulphur & Chemical
Company's (MSCC's) sulfur recovery unit (SRU) 100-meter stack and the
stack height credit on which those limits were based.
The emission limits for MSCC's auxiliary vent stacks due
to lack of an adequate limit on fuel burned in the associated heaters
and boilers and lack of a reliable compliance determining method.
The emission limits for MSCC's 30-meter stack due to lack
of an adequate limit on fuel burned in the associated heaters and
boilers, and lack of a reliable compliance determining method.
Provisions that allowed sour water stripper overheads to
be burned in the flares at CHS Inc. and ExxonMobil.
ExxonMobil's refinery fuel gas combustion device emission
limits and associated compliance determining methods.
ExxonMobil's Coker CO Boiler stack emission limits and
associated compliance determining methods.
CHS Inc.'s combustion source emission limits and certain
associated compliance determining methods.
On June 10, 2002, MSCC petitioned the United States Court of
Appeals for the Ninth Circuit for review of EPA's May 2, 2002, final
SIP action. Subsequently, MSCC and EPA agreed to a stay of the
litigation pending EPA's final action on this FIP. The case is
captioned Montana Sulphur & Chemical Company v. United States
Environmental Protection Agency, No. 02-71657. No petitions for
judicial review were filed regarding EPA's May 22, 2003, SIP action.
On July 12, 2006 (71 FR 39259), EPA proposed Federal Implementation
Plan (FIP) provisions for the Billings/Laurel, Montana area because of
our disapproval of portions of Montana's Billings/Laurel SO2
SIP. In our proposal, we indicated that our FIP would not replace the
SIP entirely, but instead would only replace elements of, or fill gaps
in, the SIP.
In promulgating today's rules, EPA is fulfilling its mandatory duty
under section 110(c) of the Act. Under section 110(c), whenever we
disapprove a SIP, in whole or in part, we are required to promulgate a
FIP. Specifically, section 110(c) provides:
``(1) The Administrator shall promulgate a Federal
implementation plan at any time within 2 years after the
Administrator--
(A) Finds that a State has failed to make a required submission
or finds that the plan or plan revision submitted by the State does
not satisfy the minimum criteria established under [section
110(k)(1)(A)],\1\ or
---------------------------------------------------------------------------
\1\ Section 110(k)(1) requires the Administrator to promulgate
minimum criteria that any plan submission must meet before EPA is
required to act on the submission. These completeness criteria are
set forth at 40 CFR 51, Appendix V.
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(B) Disapproves a State implementation plan submission in whole
or in part, unless the State corrects the deficiency, and the
Administrator approves the plan or plan revision, before the
Administrator promulgates such Federal implementation plan.''
Thus, because we disapproved portions of the Billings/Laurel
SO2 SIP, and the attainment demonstration, we are required
to promulgate a FIP.
Section 302(y) defines the term ``Federal implementation plan'' in
pertinent part, as:
``[A] plan (or portion thereof) promulgated by the Administrator
to fill all or a portion of a gap or otherwise correct all or a
portion of an inadequacy in a State implementation plan, and which
includes enforceable emission limitations or other control measures,
means or techniques (including economic incentives, such as
marketable permits or auctions or emissions allowances) * * *.''
More simply, a FIP is ``a set of enforceable federal regulations
that stand in the place of deficient portions of a SIP.'' McCarthy v.
Thomas, 27 F.3d 1363, 1365 (9th Cir. 1994). As the Court of Appeals for
the D.C. Circuit noted in a 1995 case, FIPs are powerful tools to
remedy deficient state action:
The FIP provides an additional incentive for state compliance
because it rescinds state authority to make the many sensitive
technical and political choices that a pollution control regime
demands. The FIP provision also ensures that progress toward NAAQS
attainment will proceed notwithstanding inadequate action at the
state level.
Natural Resources Defense Council, Inc. v. Browner, 57 F.3d 1122,
1124 (D.C. Cir. 1995).
When EPA promulgates a FIP, courts have not required EPA to
demonstrate explicit authority for specific measures: ``We are inclined
to construe Congress' broad grant of power to the EPA as including all
enforcement devices reasonably necessary to the achievement and
maintenance of the goals established by the legislation.'' South
Terminal Corp. v. EPA, 504 F.2d 646, 669 (1st Cir. 1974). As the Ninth
Circuit stated in a case involving a FIP with far-reaching consequences
in Los Angeles: ``The authority to regulate pollution carries with it
the power to do so in a manner reasonably calculated to reach that
end.'' City of Santa Rosa v. EPA, 534 F.2d 150, 155 (9th Cir. 1976),
vacated and remanded on other grounds sub nom. Pacific Legal Foundation
v. EPA, 429 U.S. 990 (1976).
In addition to giving EPA remedial authority, section 110(c)
enables EPA to assume the powers that the state would have to protect
air quality, when the state fails to adequately discharge its planning
responsibility. As the Ninth Circuit held, when EPA acts to fill in the
gaps in an inadequate state plan under section 110(c), EPA `` `stands
in the shoes of the defaulting State, and all of the rights and duties
that would otherwise fall to the State accrue instead to EPA.' ''
Central Arizona Water Conservation District v. EPA, 990 F.2d 1531, 1541
(9th Cir. 1993). As the First Circuit held in an early case:
``[T]he Administrator must promulgate promptly regulations
setting forth `an implementation plan for a State' should the state
itself fail to propose a satisfactory one * * * The statutory scheme
would be unworkable were it read as giving to EPA, when promulgating
an implementation plan for a state, less than those necessary
measures allowed by Congress to a state to accomplish federal clean
air goals. We do not adopt any such crippling interpretation.''
South Terminal Corp. v. EPA, supra, at 668 (citing previous version
of section 110(c)).
The Billings/Laurel SO2 FIP establishes emission limits
and compliance determining methods for four sources located in
Billings/Laurel, Montana, to replace/fill gaps in portions of the SIP
we disapproved, and to
[[Page 21420]]
support our attainment demonstration. Three of the sources are
petroleum refineries: CHS Inc., ConocoPhillips (including the Jupiter
Sulfur facility), and ExxonMobil. The fourth source is Montana Sulphur
& Chemical Company, which provides sulfur recovery for the ExxonMobil
refinery.
The following is a summary of the major components of our FIP rule:
(1) The FIP establishes flare emission limits at all four sources
(150 lbs SO2/3-hour period at all but the Jupiter Sulfur
flare, 75 lbs SO2/3-hour period shared limit for the Jupiter
Sulfur flare and the Jupiter Sulfur SRU/ATS stack) and monitoring
methods to determine compliance with those limits. The FIP includes an
affirmative defense to penalties for violations of the flare limits
that occur during malfunction, startup, and shutdown periods. To
determine flare emissions, the FIP requires concentration monitoring
(which can consist of continuous monitoring, grab sampling, or
integrated sampling) and continuous flow monitoring.
(2) The FIP prohibits the burning of sour water stripper overheads
in CHS Inc.'s main crude heater and requires CHS Inc. to keep the valve
between the old sour water stripper and the main crude heater closed,
chained, and locked.
(3) The FIP provides that emission limits for identified ExxonMobil
refinery fuel gas combustion units are contained in the SIP, and
establishes compliance determining methods for instances in which the
H2S concentration in the refinery fuel gas stream exceeds
1200 ppmv. These methods involve the use of length-of-stain detector
tubes on a once-per-hour frequency.
(4) The FIP provides that emission limits for ExxonMobil's Coker CO
Boiler stack, when ExxonMobil's Coker unit is operating and Coker unit
flue gases are burned in the Coker CO Boiler, are contained in the SIP.
The FIP establishes compliance determining methods for these emission
limits that require measurement of the SO2 concentration and
flow rate in the Coker CO Boiler stack using CEMS.
(5) The FIP establishes emission limits on MSCC's SRU 100-meter
stack, based on good engineering practice (GEP) stack height credit of
65 meters, with compliance with these limits to be determined using
methods already approved in the SIP. The FIP does not provide variable
emission limits for this stack.
(6) The FIP establishes emission limits and compliance determining
methods for MSCC's auxiliary vent stacks and SRU 30-meter stack. In
addition to mass limits, the FIP establishes concentration limits on
fuel burned in the units that vent to the auxiliary vent stacks and SRU
30-meter stack. These concentration limits are 160 ppm H2S
per 3-hour period and 100 ppm H2S per calendar day. When
trigger events specified in the rule occur, MSCC must measure the
H2S concentration in the fuel using length-of-stain detector
tubes on a once-per-3-hour period.
(7) The FIP establishes various recordkeeping and reporting
requirements.
It is important to note that, in cases where the provisions of the
FIP address emissions activities differently or establish different
requirements than provisions of the SIP, the provisions of the FIP take
precedence. We also caution that if any of the four sources are subject
to requirements under other provisions of the Act (e.g., section 111 or
112, part C of title I, or SIP-approved permit programs under part A of
title I), our promulgation of the FIP does not excuse any of the
sources from meeting such requirements. Finally, our promulgation of
the FIP does not imply any sort of applicability determination under
other provisions of the Act (e.g., section 111 or 112, part C of title
I, or SIP-approved permit programs under part A of title I).
II. Issues Raised by Commenters and EPA's Response
A. FIP Not Necessary
1. Ambient Data and Historical Modeling Show Attainment
(a) Comment (CHS Inc., COPC, ExxonMobil, NPRA, MPA, MDEQ, MSCC,
WETA): The FIP is not necessary for attainment of the NAAQS because
ambient data show that the Billings/Laurel area has been for many years
and continues to be in attainment with both the Federal and State
SO2 ambient air quality standards for all averaging periods.
Response: EPA does not agree that a FIP is not necessary because
ambient data show attainment of the SO2 NAAQS. Ambient
monitoring is limited in time and in space. Ambient monitoring can
measure pollutant concentrations only as they occur; it cannot predict
future concentrations when emission levels and meteorological
conditions may differ from present conditions.
EPA has long held that ambient monitoring data alone generally are
not adequate for SO2 attainment demonstrations.
Additionally, a small number of ambient SO2 monitors usually
are not representative of the air quality for an area. (See reference
document GGGGG, April 21, 1983, memorandum from Sheldon Meyers,
Director, Office of Air Quality Planning and Standards (OAQPS), to
Regional Air and Waste Division Directors, titled ``Section 107
Designation Policy Summary,'' and reference document HHHHH, September
4, 1992, memorandum from John Calcagni, Director, Air Quality
Management Division, OAQPS, to Regional Air Division Directors, titled
``Procedures for Processing Requests to Redesignate Areas to
Attainment.'')
Typically, modeling estimates of maximum ambient concentrations are
based on a fairly infrequent combination of meteorological and source
operating conditions. To capture such results on an ambient monitor
would normally require a prohibitively large and expensive network.
Therefore, dispersion modeling is generally necessary to
comprehensively evaluate sources' impacts and to determine the areas of
expected high concentrations. (Id.) Air quality modeling results would
be especially important if sources were not emitting at their maximum
level during the monitoring period or if the monitoring period did not
coincide with potentially worst-case meteorological conditions.
Further, ambient monitoring data are not adequate if sources are using
stacks with actual heights greater than good engineering practice stack
height (which indeed is the case with MSCC and ConocoPhillips) or other
dispersion techniques for which SIP/FIP modeling credit is not allowed.
(See also our discussion of related issues in our final action on the
Billings/Laurel SO2 SIP (67 FR 22168, 22185-22187, May 2,
2002.))
Ambient monitoring data and air quality modeling data for a
particular area can sometimes appear to conflict. This is primarily due
to the fact that modeling results may predict maximum SO2
concentration at receptors where no monitors are located.
Moreover, our SIP Call for the Billings/Laurel area was based on
modeled violations of the SO2 NAAQS, not monitored
violations. (See reference documents Y and Z.) We took final action on
the SIP Call in our May 2, 2002, action on the Billings/Laurel SIP (67
FR 22168, 22173), and we are not revisiting it in this FIP action. It
would be inconsistent and inappropriate to now rely solely on
monitoring to determine necessary measures and demonstrate attainment.
It is especially important to recognize that, as a result of our
partial and limited disapproval of the Billings/
[[Page 21421]]
Laurel SO2 SIP, we are legally obligated to promulgate a FIP
for the area. See section 110(c)(1) of the CAA, 42 U.S.C. 7410(c)(1).
However, the SIP deficiencies that triggered our partial and limited
disapproval were varied and were not necessarily associated with
problems that could be measured at an ambient monitor. For example, one
basis for disapproval of the SIP was the State's use of improper (too
tall) stack height credit for MSCC in modeling attainment of the NAAQS.
In the real world, emissions at the actual (100 meter) height of the
stack create less impact on monitored ambient concentrations in the
Billings/Laurel area than if the emissions were emitted from a lower
stack. Nonetheless, we had to partially disapprove the SIP due to the
State's inappropriate grant of stack height credit, and section 110(c)
of the CAA requires that we correct the deficiency. Since the State did
not model attainment at the proper stack height credit for MSCC's
stack, it was necessary that we do so and set emission limits for the
stack consistent with our attainment demonstration. We believe MSCC has
consistently been meeting the emission limits we are adopting, so there
may be no reduction in actual emissions from the stack, but that does
not mean the CAA allows us to forego this aspect of the FIP.
Likewise, CAA sections 110(a)(2)(A) and (C) require that SIP
control measures be enforceable. We disapproved several source
monitoring methods because they were not adequate to determine
compliance under all operating conditions. It may be impossible to
measure the impact these SIP deficiencies may have on ambient
SO2 concentrations in the area, but the CAA still requires
that we correct the deficiencies. Regarding the emission limits and
compliance determining methods for the flares, the State-only flare
limits, which the State relied on to demonstrate attainment, may have
positively impacted flare emissions in the past few years. However, the
State did not include the State-only flare limits or adequate
compliance determining methods in the SIP. Thus, the SIP remains
deficient. We now have the responsibility to ensure that emission
limits relied on to demonstrate attainment are included in the SIP and
are practically enforceable, consistent with the requirements of
section 110 of the Act.
(b) Comment (MSCC, MDEQ): The State's SIP modeling, along with
appropriate emission limits, show attainment of the NAAQS.
Response: EPA addressed this issue in its actions on Montana's SIP
submissions. As explained in those actions, EPA does not agree that the
State's SIP modeling, along with appropriate emission limits, show
attainment of the NAAQS. EPA's formal determinations regarding the
attainment demonstration and emission limits were made in final actions
on May 2, 2002 (67 FR 22168) and May 22, 2003 (68 FR 27908). The FIP
fills the gaps for the provisions we disapproved.
We note that we have not reopened our SIP actions as part of this
action. Thus, to the extent the commenters are expressing their
disagreement with EPA's actions on the SIP, their comments are not
relevant to this action, and EPA is not re-considering them here.
(c) Comment (ExxonMobil): EPA's proposed FIP ignores the
substantial improvement in air quality in the Billings/Laurel area and
instead predicts exceedances of NAAQS based upon modeling performed as
long as 15 years ago. EPA's FIP proposal must be further examined in
light of subsequent developments, including correct modeling and
consideration of currently available information indicating compliance.
Response: See response to comment II.A.1.(a), above, regarding
ambient data and response to comments in section II.E., below,
regarding modeling.
2. Existing Controls Sufficient
(a) Comment (MDEQ, MSCC, COPC, ExxonMobil, MPA, NPRA, WETA): The
FIP offers questionable improvements because the existing control plan
provisions submitted by the state are adequate and contain sufficient
SO2 emission controls and strategies and provide for the
implementation, maintenance, and enforcement of the SO2
NAAQS.
Response: EPA addressed the adequacy of Montana's SIP submissions
in its final actions on the SIP. As explained in those actions, EPA
does not agree that the State's SIP control plan provisions are
adequate and contain sufficient SO2 emission controls to
show attainment of the NAAQS. EPA's formal determinations regarding the
attainment demonstration and emission control plan were made in final
actions on May 2, 2002 (67 FR 22168) and May 22, 2003 (68 FR 27908). In
our May 2002 and May 2003 actions we disapproved various control plan
provisions. The FIP fills the gaps for the provisions we disapproved.
The FIP offers necessary improvements to the SIP by imposing new
emission limits and reliable compliance determining methods to ensure
attainment of the SO2 NAAQS.
We note that we have not reopened our SIP actions as part of this
action. Thus, to the extent the commenters are expressing their
disagreement with EPA's actions on the SIP, their comments are not
relevant to this action, and EPA is not re-considering them here.
(b) Comment (CHS Inc., WETA, COPC, MDEQ, ExxonMobil, NPRA): In
addition to the SIP, SO2 emissions in the Billings/Laurel
area have decreased as a result of Consent Decrees and Montana Air
Quality Permit changes. These limits are all federally enforceable
because there are Title V operating permit conditions (CHS Inc.). EPA
did not consider these emission reductions in making its determination
that the FIP was necessary. The FIP proposal does not otherwise
acknowledge the practical effects of the recent consent decrees between
the primary refinery parties subject to regulation as well as other
permitting actions that have occurred over the past eight years (MSCC,
COPC).
Response: EPA did not consider the emission reductions that
resulted, or will result, from the consent decrees and/or State permit
revisions to determine that the FIP was necessary or include the
emission reductions in our modeling for several reasons.
First, the FIP is required because we disapproved the SIP, and the
State has not made revisions to the SIP to address the SIP's flaws. As
noted in other responses, because we disapproved the SIP, we have a
legal obligation to promulgate a FIP. See CAA section 110(c), 42 U.S.C.
7410(c).
Second, even though permits and consent decrees are federally
enforceable, some permits can be revised without EPA approval and
consent decrees have a limited lifespan.\2\ To protect the integrity of
the attainment demonstration, and our statutory role in assessing SIP/
FIP adequacy, we believe that stationary source emission limits
necessary to demonstrate attainment must be included in the FIP (or
approved SIP). See, e.g., CAA sections 110(a)(2)(A), 110(i), 110(k)(3)-
(6), and 110(l), 42 U.S.C. 7410(a)(2)(A), (i), (k)(3)-(6), and (l).
This ensures that changes to those limits will only be made with EPA's
approval as a SIP or FIP revision,
[[Page 21422]]
following notice and comment rulemaking.
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\2\ The State can revise construction permits without EPA
approval, and, while EPA has authority to object to Title V permits,
that authority is only available to ensure that underlying
applicable requirements are included in the Title V permits. Thus,
if those underlying requirements change, EPA may have no recourse at
the Title V stage.
---------------------------------------------------------------------------
Third, the consent decrees and permitting actions, for some
emission points, do not contain SO2 emission limits that are
consistent with the averaging times of the SO2 NAAQS,
specifically, the 3-hour and calendar day averaging periods. For
example, the SIP establishes 3-hour, calendar day, and calendar year
emission limits for CHS Inc.'s FCC regenerator/CO boiler stack. The
January 17, 2007, final State construction permit (reference document
IIIII) and the consent decree (reference document JJJJJ) indicate that
the FCC regenerator stack SO2 emissions shall not exceed 50
ppm by volume (corrected to 0% O2) for a 7-day rolling
average [or a fresh feed of 0.3 percent by weight] and 25 ppm by volume
(corrected to 0% O2) for a 365-day rolling average. None of
the commenters has suggested these limits be converted to FIP mass
limits that would apply over a 3-hour averaging period, and the State
has not submitted a SIP revision with such limits.
It should be noted that EPA did solicit comment on whether we
should limit the main flares to 500 pounds of SO2 per
calendar day. This value is consistent with the trigger point for
certain analyses contained in settlements (i.e., consent decrees)
between the United States and CHS Inc., ConocoPhillips, and ExxonMobil.
We received limited comments on this proposal and have decided to keep
the limit at 150 pounds of SO2 per 3-hour period to maintain
consistency with the State's State-only limit.
B. EPA Exceeded Its Authority in Proposing a FIP
1. State's Responsibility
(a) Comment (WETA, MPA, ExxonMobil): EPA's role is limited to
determining whether or not a SIP is attaining and maintaining the
NAAQS. Selecting the source mix and various control measures to achieve
these ends has been determined by courts to be the sole responsibility
of the state. EPA's proposed action intrudes on the primary
responsibility of the state and local governments to implement the
Clean Air Act (MSCC).
Response: The commenters' characterization of EPA's role regarding
SIPs is not accurate. We lack authority to question a state's choices
of emissions limitations if they are part of a plan that satisfies the
standards of the Clean Air Act. Train v. Natural Resources Defense
Council, 95 S.Ct. 1470, 1481-1482 (1975). In our 2002 and 2003 actions,
we found that Montana's SO2 SIP for Billings/Laurel did not
fully satisfy CAA requirements. See 67 FR 22168, May 2, 2002 and 68 FR
27908, May 22, 2003. Thus, pursuant to section 110(c) of the CAA, 42
U.S.C. 7410(c), we are required to promulgate a FIP. In doing so, we
stand in the state's shoes and have authority to determine emissions
limitations and other measures for specific sources to fill gaps in the
SIP. Central Arizona Water Conservation District v. EPA, 990 F.2d 1531,
1541 (9th Cir. 1993); South Terminal Corp. v. EPA, 504 F.2d 646, 668
(1st Cir. 1974) (citing previous version of CAA section 110(c)).
We note that we have not reopened our SIP actions as part of this
action. Thus, to the extent the commenters are expressing their
disagreement with EPA's actions on the SIP, their comments are not
relevant to this action, and EPA is not re-considering them here.
(b) Comment (WETA): Since the State of Montana has already taken
appropriate actions to reduce sulfur dioxide emissions, EPA does not
have the authority under the CAA to adopt the proposed FIP.
Response: See response to comment II.B.1.(a), above. The adequacy
of the State of Montana's actions has already been considered by EPA in
other rulemaking actions that addressed the State's SIP submission.
Those actions are not the subject of EPA's present rulemaking, which
promulgates the necessary measures to remedy the deficiencies EPA
identified in its prior SIP reviews.
(c) Comment (MSCC): States have primacy, and because EPA did not
choose to exercise its rights in the comprehensive and competent state
decision process, EPA may not default and then act.
Response: Under section 110(c) of the Act, EPA is not required to
participate in a state's administrative process before promulgating a
FIP.
(d) Comment (MSCC, MDEQ, ExxonMobil): EPA has no authority to
question the wisdom of a state's choices of emission limitations if
they are part of a plan that satisfies the standards of Sec. 110(a)(2)
of the Act. As long as the ultimate effect of a state's choice of
emission limitations is compliance with the NAAQS, the state is at
liberty to adopt whatever mix of emission limitations it deems best
suited to its particular situation. There is no evidence provided by
EPA that Montana reached its material conclusions or choices in the SIP
unreasonably. Additionally, EPA has not shown that additional controls
beyond the SIP measures adopted by Montana are necessary to meet or
assure SO2 NAAQS compliance.
Response: See our responses to comments II.A.1.(a) and II.B.1.(a),
above. Much of this comment pertains to our actions on Montana's SIP.
We are not revisiting or reopening comment on those actions here. Our
basis for finding that the SIP was not adequate to ensure attainment
and meet other CAA requirements is described in our actions on the SIP.
Once we disapprove part or all of a required SIP, section 110(c) of the
Act requires that we issue a FIP. Our obligation in this action is to
correct the SIP deficiencies we previously identified. Thus, the
findings that triggered our responsibility to promulgate a FIP were
established in the prior rulemaking actions reviewing Montana's SIP.
EPA is not required to repeat those findings in the FIP rulemaking
itself.
(e) Comment (ExxonMobil): EPA cannot propose a FIP to replace a
SIP, unless the SIP is substantially inadequate to ensure compliance
with the CAA.
Response: The commenter misstates the standard for promulgation of
a FIP. Section 110(c) of the CAA is straightforward--a FIP is required
if (1) EPA finds that a state has failed to make a required submission;
(2) EPA finds that a plan submission does not satisfy the completeness
criteria established under section 110(k)(1)(A) of the CAA; or (3) EPA
disapproves a SIP in whole or in part. EPA partially disapproved the
Billings/Laurel SO2 SIP; thus, a FIP is required. Contrary
to the commenter's assertion, the obligation to promulgate a FIP is not
contingent on an EPA finding of substantial inadequacy. As explained
above, the findings triggering our responsibility to promulgate a FIP
were made in the prior actions reviewing Montana's SIP.
(f) Comment (MSCC): The commenter claims EPA's action violates the
Tenth Amendment to the Constitution. The commenter also claims EPA's
FIP is dictating the required controls in contravention of the holdings
in Commonwealth of Virginia v. EPA, 108 F.3d 1397 (D.C. Cir. 1997) and
Bethlehem Steel v. Gorsuch, 742 F.2d 1028 (7th Cir. 1984).
Response: Our FIP compels no action on the part of the State and is
not coercive vis-[agrave]-vis the State. Our FIP contains requirements
applicable to four private companies. The Tenth Amendment is not
implicated. Nor do our actions contravene Commonwealth of Virginia or
Bethlehem Steel. The former case held that EPA cannot, in a SIP Call,
dictate that a state adopt a particular control measure to
[[Page 21423]]
demonstrate attainment of the NAAQS. EPA had issued a SIP Call finding
that the SIPs of 12 states were inadequate to meet the ozone NAAQS and
in its SIP Call rule, specified that the states needed to submit SIPs
that included the California Low Emission Vehicle Program. In this
matter, we are promulgating a FIP, not issuing a SIP Call. We are not
directing any action by the State. Thus, the Commonwealth of Virginia
case is not relevant to our FIP. Bethlehem Steel is also not relevant
to our FIP action. In that case, the 7th Circuit held that it was
improper for EPA to partially approve an Indiana SIP revision so as to
render it more stringent than the State intended. We are promulgating a
FIP in this action, not acting on a SIP; thus, Bethlehem Steel does not
apply. As we note elsewhere, once we disapprove a SIP, we are required
to promulgate a FIP, and in promulgating the FIP, we stand in the
state's shoes. See section 110(c) of the CAA, 42 U.S.C. 7410(c);
Central Arizona Water Conservation District v. EPA, 990 F.2d 1531, 1541
(9th Cir. 1993).
(g) Comment (MSCC): The commenter argues that the cases EPA cited
in the preamble to the proposed Billings/Laurel FIP, regarding its FIP
authority, do not speak to the central question--``When and on what
authority may the EPA undertake the draconian act of displacing a
state's implementation plan?'' The commenter argues that the question
is particularly sensitive in this case because the State and the
sources spent years negotiating the SIP.
Response: As noted in response to comment II.B.1.(e), the CAA
requires that we promulgate a FIP whenever we disapprove a SIP, in
whole or in part. While we are sensitive to the fact that the State and
sources spent years negotiating the SIP, that does not change our
obligation under the CAA.
2. No Adequate Basis for FIP
(a) Comment (MSCC, ExxonMobil): Because EPA must find substantive
noncompliance with some provision of the Clean Air Act, specifically,
failure to attain NAAQS, and because that finding of substantial
inadequacy must be clearly stated, the present FIP decision must fall.
It is inadequate on both counts. EPA has not provided any evidence that
the State plan is not working.
Response: See our response to comment II.B.1.(e), above. The
evidence supporting EPA's determinations regarding the adequacy of
Montana's SIP is contained in the record for those rulemaking actions,
and need not be repeated here. EPA's disapproval of the SIP triggered
the obligation for a FIP. No separate showing that the State plan is
not working or does not meet CAA requirements is needed as part of this
action. Commenters' comments regarding EPA's SIP actions are not
relevant for this rulemaking.
(b) Comment (ExxonMobil): Even when the EPA has statutory authority
for a particular rule, its technical decisions about the level of
pollutant reduction needed to comply with the CAA and the control
strategies necessary to meet the level of pollutant reduction must be
rational. Courts ``confronted with important and seemingly plausible
objections going to the heart of a key technical determination * * * ''
will not presume that EPA would never behave irrationally. South
Terminal Corporation v. Environmental Protection Agency, 504 F.2d 646,
665 (1st Cir. 1974). In South Terminal Corporation, various interested
parties challenged EPA's FIP on technical grounds. Id. at 662-66. The
court held that EPA failed to adequately support its decision to
promulgate the rules contained in the FIP and remanded the case to EPA
to develop the record. Id. at 666. The court questioned EPA's position
in light of contradictory modeling and data, concluding that ``it is
not clear whether or not the ambient air at Logan meets, or will
without controls by mid-1975 will meet, the national primary
standard.'' Id. 664. Similarly, in the present FIP proposal, EPA has
neither determined appropriate current modeling nor used currently
available information.
Response: The standards for judicial review of this rulemaking
action are contained in section 307(d)(9) of the CAA, 42 U.S.C.
7607(d)(9). We believe the emission limitations and other requirements
in this FIP are reasonable and that the situation in the cited case is
not analogous.\3\ The commenter has not identified any modeling that
contradicts our attainment demonstration, which forms the basis for the
FIP's emission limitations; nor has the commenter shown that a
different model would result in substantially different emission
limitations. Our responses pertaining to model selection and input data
are contained in section II.E., below. Further, we note that it does
not appear the commenter is suggesting that the entire SIP should be
re-done based on more current modeling and more up-to-date information.
On the contrary, the commenter seems satisfied with the EPA-approved
emission limitations in the SIP,\4\ which were based on the very
modeling that the commenter now claims is unreliable.
---------------------------------------------------------------------------
\3\ In South Terminal Corporation, EPA had determined emissions
reductions needed to achieve the ozone and carbon dioxide NAAQS
based on monitored values that the Court found highly questionable
(petitioners claimed the ozone monitor was defective). South
Terminal Corporation, 504 F.2d 646, 662 (1974). The commenter seems
to suggest that the Court rejected EPA's modeling approach, but in
fact, the Court was satisfied with the rollback modeling that EPA
used. Id.
\4\ Among other things, the commenter asserts that the state SIP
requirements are adequate to protect the NAAQS. See reference
document YYYY, page 27.
---------------------------------------------------------------------------
(c) Comment (ExxonMobil): Citing Hall v. United States
Environmental Protection Agency, 273 F.3d 1146, 1159 (9th Cir. 2001),
the commenter states that in acting on a SIP, the test EPA applies is
to ``measure the existing level of pollution, compare it with the
national standards, and determine the effect on this comparison of
specified emission modifications.'' The commenter argues that in the
FIP proposal, EPA did not correctly identify the existing level of
pollution and ignored the substantial evidence of permanently reduced
SO2 emissions and levels in the Billings/Laurel area. The
commenter also argues that EPA's authority is limited by its mandate
under the CAA to ensure attainment and maintenance of the NAAQS as well
as the CAA's other general requirements.
Response: See responses to comments II.A.1.(a), II.A.2(b), and
II.E.1.(e) and (g). Also, the Hall case involved a challenge to EPA's
approval of a SIP revision for Clark County, Nevada, and EPA's
interpretation of section 110(l) of the CAA, which provides that EPA
may not approve a SIP revision if it would interfere with attainment or
other applicable requirements of the CAA. EPA asserted that its
approval of the Clark County SIP revision was consistent with section
110(l) because the revision did not relax the existing SIP. The Court
disagreed, holding that 110(l) requires more--a determination that the
specific revision, when considered in the context of the SIP elements
already in place, can meet the Act's attainment requirements. Hall at
1152, 1159. It was in these circumstances that the Court expected EPA
to determine the extent of pollution reductions required and evaluate
whether the reductions resulting from the revision would be sufficient
to attain the NAAQS.
In its reference to Hall, the commenter appears to be conflating
two disparate concepts. The Hall Court was addressing EPA's action on a
SIP revision and indicating that EPA was not adequately evaluating
whether Clark County's rule change would interfere
[[Page 21424]]
with attainment and other CAA requirements. The Court was not
establishing a standard for a FIP or indicating that EPA was requiring
more than necessary for the area, which seems to be what the commenter
is suggesting in the case of the Billings/Laurel FIP. As we explain in
greater depth elsewhere in this notice, we are not starting from
scratch with our FIP. Instead, we are working within the framework of
the existing Billings/Laurel SIP to fill the gaps resulting from our
partial and limited disapproval of discrete SIP elements. In this
unique circumstance, where only discrete elements of the SIP were
deficient, the CAA does not require us to reevaluate or replace the
entire SIP or the basic modeling approach upon which it was based.
Nothing in the CAA requires EPA to reject an entire SIP when only
certain elements within it are not approvable, and doing so, where that
is not necessary to address a discrete deficiency, would be
inconsistent with the basic scheme of cooperative federalism embodied
in the CAA.
Nor are we required as part of this FIP to revisit our SIP Call or
the bases for our SIP disapproval. Our task is to fix the portions of
the SIP that were deficient. It is reasonable to continue to treat as
valid the factors we found adequate to support the portions of the SIP
we approved, and augment and/or replace those factors that we found
inadequate. In fact, based on the holding in Train v. NRDC, 421 U.S. 57
(1975), recited by this commenter and others, it would be inappropriate
for EPA to now reject or replace the portions of the SIP that we
approved as meeting the CAA's requirements, because to do so would be
to intrude on the State's authority under the CAA to establish the mix
of controls for the area.\5\ The State, of course, remains free to
submit a SIP revision that reflects a different mix of controls across
all the sources. This would be the mechanism, for example, whereby the
State could adopt SIP limits that correlate to refinery consent decree
limits.\6\ If the State were to submit such a revision, we would
evaluate the revision according to the Act, our regulations, and the
relevant cases.
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\5\ To the extent the commenter is arguing that we may do no
more in this FIP than appears minimally necessary to attain the
NAAQS, we reject that notion as well. See, e.g., Central Arizona
Water Conservation District v. EPA, 990 F.2d 1531, 1541 (9th Cir.
1993) (EPA ``stands in the shoes of the defaulting State, and all of
the rights and duties that would otherwise fall to the State accrue
instead to EPA.'') Under the CAA, states are not restricted to
barely meeting the NAAQS. In fact, the opposite is true--states may
exceed minimum requirements. See CAA section 116, 42 U.S.C. 7416. In
any event, our modeled attainment demonstration resulted in
projected values just at the 24-hour SO2 NAAQS (365
[mu]g/m\3\) and just below the 3-hour SO2 NAAQS (1291.5
[mu]g/m\3\). However, we think we had discretion to adopt limits (to
replace those we disapproved) consistent with modeled ambient
concentrations further below the NAAQS, if we had felt a larger
margin of safety was justified to ensure attainment and maintenance.
\6\ As we allude to in sections II.A.2.(b), II.D.4., and
II.E.1.(e), the consent decree limits would need to be translated
into limits that support an attainment demonstration for the
SO2 NAAQS. In sections II.A.2.(b) and II.D.4., we
identify some of our concerns with the consent decree limits.
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(d) Comment (ExxonMobil): EPA's proposal imposes costly technology
requirements not rationally designed to achieving their stated
objectives. While EPA has authority to impose an emission limitation,
the emission limitation must be necessary to attain NAAQS. City of
Santa Rosa v. EPA, 534 F.2d 150, 155 (9th Cir. 1976), vacated on other
grounds, 429 U.S. 990 (1976). The EPA derived its authority in City of
Santa Rosa from its statutory mandate to ensure compliance with NAAQS
and the fact that no alternative to its proposal was adequate to ensure
compliance with NAAQS. It is clear that Montana's existing SIP,
supplemented as it is by further state and federally enforceable
consent decrees are a more than adequate alternative.
Response: The cited case actually stands for the proposition that
EPA's authority to adopt measures to meet the NAAQS is expansive. EPA
adopted a FIP provision that would have required a substantial
reduction (up to 100%) in the supply of gasoline to major metropolitan
areas in California, including Los Angeles. Even the EPA acknowledged
that the rule would cause severe social and economic disruption, and
the EPA Administrator at the time publicly advocated amendments to the
CAA to provide relief from EPA's own FIP rule. Nonetheless, the Court
held that economic and social disruption are not cognizable if (1) a
measure is necessary to attain the NAAQS; (2) there is no statutory
limitation on EPA's authority to adopt the measure; and (3) there are
no equally effective, less burdensome alternatives. City of Santa Rosa
at 151-154.
The measures EPA is promulgating in this FIP are in no way
comparable to the reduction in gasoline supply at issue in the City of
Santa Rosa case. Our FIP is narrowly tailored to fill the gaps in the
Billings/Laurel SIP. Section 110(c) requires us to promulgate the FIP.
There is no statutory limitation on our authority to adopt the measures
we are adopting. On the contrary, section 110(a)(2)(A) of the Act
requires enforceable emission limitations as necessary or appropriate
to meet the applicable requirements of the Act, which include
attainment and maintenance of the SO2 NAAQS. Using ISC, the
same model the State used to set the commenter's emission limits in the
SIP, we have determined emission levels consistent with attainment and
established corresponding emission limits on the flares, MSCC's main
stack, and other emission units, whose emission limits we disapproved
in our SIP action. While the authority to require monitoring,
recordkeeping, and reporting requirements can be inferred from CAA
sections 110(a)(2)(A) and (C), section 110(a)(2)(F) of the Act
specifically indicates that the EPA Administrator may prescribe the
installation, maintenance, and replacement of monitoring equipment by
stationary sources, as well as reporting requirements. Our requirement
for the refineries and MSCC to install monitoring equipment to measure
flare gas flow and concentrations is consistent with this authority and
is rationally related to the goals of the FIP, i.e., to ensure
attainment and maintenance of the SO2 NAAQS. We do not
believe estimating flare emissions or emissions from other units is a
sufficient substitute for real-time monitoring for purposes of this
FIP; estimation is not an equally effective technique.
The commenter argues that the existing SIP and the State and
federally enforceable consent decrees are a more than adequate
alternative to our FIP requirements. This comment ignores the fact that
we disapproved portions of the SIP as not meeting the CAA's
requirements. Elsewhere we explain that the consent decree provisions
are not sufficient to meet the CAA's requirements under section 110
related to attainment and maintenance of the NAAQS. See, e.g., sections
II.A.2.(b), II.D.4., and II.E.1.(e).
(e) Comment (MSCC): EPA's failure to issue the FIP within the CAA's
two-year deadline is important in this case. As a result of EPA's
delay, EPA should have to consider the cleanup of emissions that has
occurred and significant changes in modeling technology.
Response: We regret that it has taken this long to issue the FIP.
We disagree that missing the two-year deadline obviates our duty or the
need for the FIP. The State has not submitted a SIP revision correcting
the portions of the SIP that we disapproved, despite the passage of
time. Regarding the argument that we should have considered the
reduction in emissions since we disapproved the SIP, see our responses
to comments in section II.A. In section II.E, we respond to comments
arguing
[[Page 21425]]
that we should have used newer modeling technology.
C. Flare Monitoring
1. Flare Flow Monitoring
(a) Comment (MSCC): The core flowmeter technology application for
flare systems seems to be an established technology, with thousands of
installations completed around the world on other types of gas and
liquid streams. However, none was identified that is following the
precise specifications of the FIP proposal. Installation and operation
of a flow meter in flare gas service at MSCC are probably achievable
today, but not at the flow range below 1 fps, and not with conventional
QA/QC procedures. Flow monitors have a difficult time measuring or
reliably detecting low flow velocities (under approximately 1.0 fps)
without false positives or false negatives. EPA should revise the
proposed rule that currently indicates:
``[t]he minimum detectable velocity of the flow monitoring device(s)
shall be 0.1 feet per second (fps). The flow monitoring device(s)
shall continuously measure the range of flow rates corresponding to
velocities from 0.5 to 275 fps and have a manufacturer's specified
accuracy of 5% over the range of 1 to 275 fps.
The revised rule should read ``[t]he minimum resolution of the
flow monitoring device(s) shall be 0.1 feet per second (fps) when
measuring flow rates above 1.0 fps. The device(s) shall continuously
measure the range of flow rates corresponding to velocities from 1.0
to 275 fps and have a manufacturer's specified accuracy of 5% over the range of that range.''
The rule should also clarify if ``accuracy'' is intended to be 5%
of the full-scale range of the instrument (13.7 fps is 5% of 275 fps),
or if this is intended to be 5% of the measured flow, which would be
0.05 fps at a flow of 1 fps, and would clearly be non-achievable with a
resolution of 0.1 fps.
Response: EPA proposed the volumetric flow monitoring
specifications based on what we saw was achievable in vendor literature
(see reference documents NN and OO) and what was being required by
regulation in the Bay Area Air Quality Management District (BAAQMD)
(see reference document LL) and South Coast Air Quality Management
District (SCAQMD) (see reference document CCC).
The commenter asserts that installation and operation of a flow
meter at the flow range below 1 fps are not achievable. However,
various sources indicate that ultrasonic flow meters can measure in the
range of 0.1 to 1 fps. For example, in ``Flare Gas Ultrasonic Flow
Meter,'' J.W. Smalling, L.D. Brawsell, L.C. Lynnwoth and D. Russel
Wallace, Proceedings Thirty-Ninth Annual Symposium on Instrumentation
for the Process Industries, 1984, the authors reported ``initially, a
modest objective was established to develop an ultrasonic flow switch
capable of detecting leaks in flare lines corresponding to flow
velocity on the orders of 0.3 ms/ (1 ft/s). As testing continued,
however, it became apparent that the equipment could measure flows
below 0.03 m/s (0.1ft/s) and up to at least 6 m/s (20 ft/s) in flare
stacks * * *'' (see reference document KKKKK). See also reference
document OO, ``the DigitalFlowGF868 meter achieves rangeability of 2750
to 1. It measures velocities from 0.1 to 275 ft/s (0.03 to 85 m/s) in
both directions, in steady or rapidly changing flow, in pipes from 3
in. to 120 in. (76 mm to 3 m) in diameter.''
Additionally, the BAAQMD (see reference document LL) and SCAQMD
(see reference document CCC) require flow meters on flares. BAAQMD
requires that the minimum detectable velocity shall be 0.1 fps and the
SCAQMD requires monitors with a velocity range of 0.1 to 250 fps. Based
on conversations with the BAAQMD, it appears that the refineries in the
Bay Area have installed flow meters meeting the requirements of the
rule (see reference document OOOOO).
Based on the above, we conclude that flow meters are available that
can measure in the velocity range below 1.0 fps, and other regulatory
authorities are requiring such flow meters with success.
The commenter also claims that installation and operation of a flow
meter are probably not achievable with conventional QA/QC procedures.
The QA/QC procedures are discussed below in response to comment
II.C.1.(d).
The commenter argues that flow monitors have a difficult time
measuring or reliably detecting low flow velocities (under
approximately 1.0 fps) without false positives or false negatives. As
indicated in the response to comment II.C.1.(b) below, there are
approaches available for improving measurement accuracy in the 0.1 to
1.0 fps range. In addition, as the response to comment II.C.1.(b)
indicates, in the final FIP we are specifying a separate accuracy range
for the velocity range of 0.1 to 1 fps. Finally, we describe how we are
addressing the false positive and false negative flows in response to
comment II.C.1.(c).
The commenter asked that the rule clarify if ``accuracy'' of the
instrument is intended to be 5% of the full-scale range of the
instrument or 5% of the measured flow. In the rule, we have clarified
that ``accuracy'' of the instrument is the accuracy of the measured
flow and not the ``full-scale range'' of the instrument.
The commenter also suggests some changes to the rule. Apart from
adding a separate accuracy range for the velocity range of 0.1 to 1 fps
and clarifying that accuracy is based on the measured flow, we are not
making any additional changes to this aspect of the rule. We explain
our reasoning in the response to this comment II.C.1.(a) and in the
responses to comments II.C.1.(b)-(d), below.
(b) Comment (ExxonMobil, WSPA): Manufacturers of flow monitoring
instrumentation publish impressive performance specifications regarding
velocity measurement range and accuracy, but often manufacturers'
claims are not actually achieved in practice over the long term. To
achieve a high level of measurement performance in the field requires
adequate lengths of straight flare header pipe upstream and downstream
of the monitor, the absence of flow disturbances, etc. Where these
criteria cannot be met, the advertised or predicted performance of the
flow monitoring system may not be fully realized in practice. MSCC
claimed that significant piping modifications and possible flare
relocation would be required to provide such runs at accessible
locations. CHS Inc. asserted that it is likely that the CHS refinery
flare header will not have adequate distances of undisturbed piping for
ideal installation. In this case, either major, costly piping
modification will be required or the accuracy criteria will not be
achievable.
Response: The commenters are correct that piping modifications may
be appropriate to optimize the measurements. Each flare system will
have unique flow measurement location issues and will have to be
addressed on a case-by-case basis. Sources may need to work with the
flow monitor manufacturer and flow testers to assure that the monitors
meet the FIP's specifications for accuracy and representativeness and
manufacturer's requirements for assuring ongoing equipment performance.
In addition to making piping modifications (e.g. flow
straighteners), other approaches are available to improve the
measurement accuracy in the 0.1 to 1.0 fps range. Among the approaches
are the use of additional monitoring paths, monitoring paths of longer
length, and unconventional monitor configurations and path locations.
Another approach involves
[[Page 21426]]
the use of Computer Fluid Dynamics (CFD) for the existing piping. CFD
analysis has been used to provide correction factors for a series of
velocities across the range of flow velocities. For example, these
factors have been used to correct flow measurement data for
disturbances caused by upstream pipe irregularities. These approaches
are discussed in ``A Total Approach to Flare Gas Flow Measurement for
Environmental Compliance,'' Gordon Mackie, Jed Matson and Mike Scelzo,
Institute of Measurement and Control--Environmental Conference 2006.
(See reference document LLLLL.) (See also Note to Billings/Laurel
SO2 FIP File regarding conversations with GE Sensing
(reference document MMMMM)).
Finally, to address concerns regarding the measurement accuracy in
the 0.1 to 1.0 fps range, we are revising the rule to indicate that the
flow monitor must have a manufacturer's specified accuracy of 20% over the range 0.1 to 1 fps. Based on conversations with a
vendor, we believe this is achievable. The vendor indicated that they
have provided methodologies for sources to meet the SCAQMD rule, which
also requires 20% accuracy in the 0.1 to 1.0 fps range. Methodologies
include a second interrogation path or straightening of pipe. (See
reference document MMMMM.)
(c) Comment (ExxonMobil, WSPA, NPRA, MSCC): Consistently achieving
low flow detection limits can be very difficult. Spurious signal,
resulting in ``eddy'' currents and back-and-forth flows in the flare
header, can easily limit the detection and accuracy of low flow
readings. Furthermore, sometimes a flow monitor will show an indication
of flow even though water seals ahead of the flare stack remain intact
(i.e., there is not flow to the flares). Other regulations in other
jurisdictions allow the sources other means to positively determine
when the flare is not operating (e.g., flare on/off monitoring device,
pressure of water seal). ExxonMobil recommends that similar language be
considered by the stakeholder process for inclusion in the EPA's
proposed FIP, and thereby remove the uncertainty of low flow reading.
MSCC claimed that the EPA proposed FIP language should be revised to
allow flare operations to be monitored by other means, and to disregard
low flow readings when the flare is not operating to eliminate falsely
reported SO2 emissions, when in fact there are none.
Response: We agree that it is appropriate to include in the
regulation the ability to use other secondary means to determine
whether flow is reaching the flare when the flow monitor indicates low
flow. If the secondary device indicates that no flow is going to the
flare, yet the continuous flow monitor is indicating flow, the
presumption will be that no flow is going to the flare. We have revised
the final rule to allow the use of flare water seal monitoring devices
to determine whether there is flow going to the flare, in addition to
the continuous flow monitoring device. See response to comment
II.F.1.(a) regarding the comment seeking a s