Oil and Natural Gas Sector: New Source Performance Standards and National Emission Standards for Hazardous Air Pollutants Reviews, 52738-52843 [2011-19899]
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
40 CFR Parts 60 and 63
[EPA–HQ–OAR–2010–0505; FRL–9448–6]
RIN 2060–AP76
Oil and Natural Gas Sector: New
Source Performance Standards and
National Emission Standards for
Hazardous Air Pollutants Reviews
Environmental Protection
Agency (EPA).
ACTION: Proposed rule.
AGENCY:
This action announces how
the EPA proposes to address the reviews
of the new source performance
standards for volatile organic compound
and sulfur dioxide emissions from
natural gas processing plants. We are
proposing to add to the source category
list any oil and gas operation not
covered by the current listing. This
action also includes proposed
amendments to the existing new source
performance standards for volatile
organic compounds from natural gas
processing plants and proposed
standards for operations that are not
covered by the existing new source
performance standards. In addition, this
action proposes how the EPA will
address the residual risk and technology
review conducted for the oil and natural
gas production and natural gas
transmission and storage national
emission standards for hazardous air
pollutants. This action further proposes
standards for emission sources within
these two source categories that are not
currently addressed, as well as
amendments to improve aspects of these
national emission standards for
hazardous air pollutants related to
applicability and implementation.
Finally, this action addresses provisions
in these new source performance
standards and national emission
standards for hazardous air pollutants
related to emissions during periods of
startup, shutdown and malfunction.
DATES: Comments must be received on
or before October 24, 2011.
Public Hearing. Three public hearings
will be held to provide the public an
opportunity to provide comments on
this proposed rulemaking. One will be
held in the Dallas, Texas area, one in
Pittsburgh, Pennsylvania, and one in
Denver, Colorado, on dates to be
announced in a separate document.
Each hearing will convene at 10 a.m.
local time. For additional information
on the public hearings and requesting to
speak, see the SUPPLEMENTARY
INFORMATION section of this preamble.
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SUMMARY:
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Submit your comments,
identified by Docket ID Number EPA–
HQ–OAR–2010–0505, by one of the
following methods:
• Federal eRulemaking Portal: https://
www.regulations.gov: Follow the
instructions for submitting comments.
• Agency Web site: https://
www.epa.gov/oar/docket.html. Follow
the instructions for submitting
comments on the Air and Radiation
Docket Web site.
• E-mail: a-and-r-docket@epa.gov.
Include Docket ID Number EPA–HQ–
OAR–2010–0505 in the subject line of
the message.
• Facsimile: (202) 566–9744.
• Mail: Attention Docket ID Number
EPA–HQ–OAR–2010–0505, 1200
Pennsylvania Ave., NW., Washington,
DC 20460. Please include a total of two
copies. In addition, please mail a copy
of your comments on the information
collection provisions to the Office of
Information and Regulatory Affairs,
Office of Management and Budget
(OMB), Attn: Desk Officer for the EPA,
725 17th Street, NW., Washington, DC
20503.
• Hand Delivery: United States
Environmental Protection Agency, EPA
West (Air Docket), Room 3334, 1301
Constitution Ave., NW., Washington,
DC 20004, Attention Docket ID Number
EPA–HQ–OAR–2010–0505. Such
deliveries are only accepted during the
Docket’s normal hours of operation, and
special arrangements should be made
for deliveries of boxed information.
Instructions: Direct your comments to
Docket ID Number EPA–HQ–OAR–
2010–0505. The EPA’s policy is that all
comments received will be included in
the public docket without change and
may be made available online at https://
www.regulations.gov, including any
personal information provided, unless
the comment includes information
claimed to be confidential business
information (CBI) or other information
whose disclosure is restricted by statute.
Do not submit information that you
consider to be CBI or otherwise
protected through https://
www.regulations.gov or e-mail. The
https://www.regulations.gov Web site is
an ‘‘anonymous access’’ system, which
means the EPA will not know your
identity or contact information unless
you provide it in the body of your
comment. If you send an e-mail
comment directly to the EPA without
going through https://
www.regulations.gov, your e-mail
address will be automatically captured
and included as part of the comment
that is placed in the public docket and
made available on the Internet. If you
submit an electronic comment, the EPA
ADDRESSES:
ENVIRONMENTAL PROTECTION
AGENCY
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recommends that you include your
name and other contact information in
the body of your comment and with any
disk or CD–ROM you submit. If the EPA
cannot read your comment due to
technical difficulties and cannot contact
you for clarification, the EPA may not
be able to consider your comment.
Electronic files should avoid the use of
special characters, any form of
encryption, and be free of any defects or
viruses. For additional information
about the EPA’s public docket, visit the
EPA Docket Center homepage at https://
www.epa.gov/epahome/dockets.htm.
For additional instructions on
submitting comments, go to section II.C
of the SUPPLEMENTARY INFORMATION
section of this preamble.
Docket: All documents in the docket
are listed in the https://
www.regulations.gov index. Although
listed in the index, some information is
not publicly available, e.g., 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.
Publicly available docket materials are
available either electronically through
https://www.regulations.gov or in hard
copy at the U.S. Environmental
Protection Agency, EPA West (Air
Docket), Room 3334, 1301 Constitution
Ave., NW., Washington, DC 20004. The
Public Reading Room is open from
8:30 a.m. to 4:30 p.m., Monday through
Friday, excluding legal holidays. The
telephone number for the Public
Reading Room is (202) 566–1744, and
the telephone number for the Air Docket
is (202) 566–1742.
FOR FURTHER INFORMATION CONTACT:
Bruce Moore, Sector Policies and
Programs Division, Office of Air Quality
Planning and Standards (E143–01),
Environmental Protection Agency,
Research Triangle Park, North Carolina
27711, telephone number: (919) 541–
5460; facsimile number: (919) 685–3200;
e-mail address: moore.bruce@epa.gov.
SUPPLEMENTARY INFORMATION:
Organization of This Document. The
following outline is provided to aid in
locating information in this preamble.
I. Preamble Acronyms and Abbreviations
II. General Information
A. Does this action apply to me?
B. Where can I get a copy of this document
and other related information?
C. What should I consider as I prepare my
comments for the EPA?
D. When will a public hearing occur?
III. Background Information
A. What are standards of performance and
NSPS?
B. What are NESHAP?
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C. What litigation is related to this
proposed action?
D. What is a sector-based approach?
IV. Oil and Natural Gas Sector
V. Summary of Proposed Decisions and
Actions
A. What are the proposed revisions to the
NSPS?
B. What are the proposed decisions and
actions related to the NESHAP?
C. What are the proposed notification,
recordkeeping and reporting
requirements for this proposed action?
D. What are the innovative compliance
approaches being considered?
E. How does the NSPS relate to permitting
of sources?
VI. Rationale for Proposed Action for NSPS
A. What did we evaluate relative to NSPS?
B. What are the results of our evaluations
and proposed actions relative to NSPS?
VII. Rationale for Proposed Action for
NESHAP
A. What data were used for the NESHAP
analyses?
B. What are the proposed decisions
regarding certain unregulated emissions
sources?
C. How did we perform the risk assessment
and what are the results and proposed
decisions?
D. How did we perform the technology
review and what are the results and
proposed decisions?
E. What other actions are we proposing?
VIII. What are the cost, environmental,
energy and economic impacts of the
proposed 40 CFR part 60, subpart OOOO
and amendments to subparts HH and
HHH of 40 CFR part 63?
A. What are the affected sources?
B. How are the impacts for this proposal
evaluated?
C. What are the air quality impacts?
D. What are the water quality and solid
waste impacts?
E. What are the secondary impacts?
F. What are the energy impacts?
G. What are the cost impacts?
H. What are the economic impacts?
I. What are the benefits?
IX. Request for Comments
X. Submitting Data Corrections
XI. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
G. Executive Order 13045: Protection of
Children From Environmental Health
and Safety Risks
H. Executive Order 13211: Actions
Concerning Regulations 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
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Minority Populations and Low-Income
Populations
I. Preamble Acronyms and
Abbreviations
Several acronyms and terms used to
describe industrial processes, data
inventories and risk modeling are
included in this preamble. While this
may not be an exhaustive list, to ease
the reading of this preamble and for
reference purposes, the following terms
and acronyms are defined here:
ACGIH American Conference of
Governmental Industrial Hygienists
ADAF Age-Dependent Adjustment Factors
AEGL Acute Exposure Guideline Levels
AERMOD The air dispersion model used by
the HEM–3 model
API American Petroleum Institute
BACT Best Available Control Technology
BID Background Information Document
BPD Barrels Per Day
BSER Best System of Emission Reduction
BTEX Benzene, Ethylbenzene, Toluene and
Xylene
CAA Clean Air Act
CalEPA California Environmental
Protection Agency
CBI Confidential Business Information
CEM Continuous Emissions Monitoring
CEMS Continuous Emissions Monitoring
System
CFR Code of Federal Regulations
CIIT Chemical Industry Institute of
Toxicology
CO Carbon Monoxide
CO2 Carbon Dioxide
CO2e Carbon Dioxide Equivalent
DOE Department of Energy
ECHO Enforcement and Compliance
History Online
e-GGRT Electronic Greenhouse Gas
Reporting Tool
EJ Environmental Justice
EPA Environmental Protection Agency
ERPG Emergency Response Planning
Guidelines
ERT Electronic Reporting Tool
GCG Gas Condensate Glycol
GHG Greenhouse Gas
GOR Gas to Oil Ratio
GWP Global Warming Potential
HAP Hazardous Air Pollutants
HEM–3 Human Exposure Model, version 3
HI Hazard Index
HP Horsepower
HQ Hazard Quotient
H2S Hydrogen Sulfide
ICR Information Collection Request
IPCC Intergovernmental Panel on Climate
Change
IRIS Integrated Risk Information System
km Kilometer
kW Kilowatts
LAER Lowest Achievable Emission Rate
lb Pounds
LDAR Leak Detection and Repair
MACT Maximum Achievable Control
Technology
MACT Code Code within the NEI used to
identify processes included in a source
category
Mcf Thousand Cubic Feet
Mg/yr Megagrams per year
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MIR Maximum Individual Risk
MIRR Monitoring, Inspection,
Recordkeeping and Reporting
MMtCO2e Million Metric Tons of Carbon
Dioxide Equivalents
NAAQS National Ambient Air Quality
Standards
NAC/AEGL National Advisory Committee
for Acute Exposure Guideline Levels for
Hazardous Substances
NAICS North American Industry
Classification System
NAS National Academy of Sciences
NATA National Air Toxics Assessment
NEI National Emissions Inventory
NEMS National Energy Modeling System
NESHAP National Emissions Standards for
Hazardous Air Pollutants
NGL Natural Gas Liquids
NIOSH National Institutes for Occupational
Safety and Health
NOX Oxides of Nitrogen
NRC National Research Council
NSPS New Source Performance Standards
NSR New Source Review
NTTAA National Technology Transfer and
Advancement Act
OAQPS Office of Air Quality Planning and
Standards
OMB Office of Management and Budget
PB–HAP Hazardous air pollutants known to
be persistent and bio-accumulative in the
environment
PFE Potential for Flash Emissions
PM Particulate Matter
PM2.5 Particulate Matter (2.5 microns and
less)
POM Polycyclic Organic Matter
PPM Parts Per Million
PPMV Parts Per Million by Volume
PSIG Pounds per square inch gauge
PTE Potential to Emit
QA Quality Assurance
RACT Reasonably Available Control
Technology
RBLC RACT/BACT/LAER Clearinghouse
REC Reduced Emissions Completions
REL CalEPA Reference Exposure Level
RFA Regulatory Flexibility Act
RfC Reference Concentration
RfD Reference Dose
RIA Regulatory Impact Analysis
RICE Reciprocating Internal Combustion
Engines
RTR Residual Risk and Technology Review
SAB Science Advisory Board
SBREFA Small Business Regulatory
Enforcement Fairness Act
SCC Source Classification Codes
SCFH Standard Cubic Feet Per Hour
SCFM Standard Cubic Feet Per Minute
SCM Standard Cubic Meters
SCMD Standard Cubic Meters Per Day
SCOT Shell Claus Offgas Treatment
SIP State Implementation Plan
SISNOSE Significant Economic Impact on a
Substantial Number of Small Entities
S/L/T State and Local and Tribal Agencies
SO2 Sulfur Dioxide
SSM Startup, Shutdown and Malfunction
STEL Short-term Exposure Limit
TLV Threshold Limit Value
TOSHI Target Organ-Specific Hazard Index
TPY Tons per Year
TRIM Total Risk Integrated Modeling System
TRIM.FaTE A spatially explicit,
compartmental mass balance model that
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describes the movement and
transformation of pollutants over time,
through a user-defined, bounded system
that includes both biotic and abiotic
compartments
TSD Technical Support Document
UF Uncertainty Factor
UMRA Unfunded Mandates Reform Act
URE Unit Risk Estimate
VCS Voluntary Consensus Standards
VOC Volatile Organic Compounds
VRU Vapor Recovery Unit
proposal are listed in Table 1 of this
preamble. These standards and any
changes considered in this rulemaking
would be directly applicable to sources
as a Federal program. Thus, Federal,
state, local and tribal government
entities are not affected by this proposed
action.
II. General Information
A. Does this action apply to me?
The regulated industrial source
categories that are the subject of this
TABLE 1—INDUSTRIAL SOURCE CATEGORIES AFFECTED BY THIS PROPOSED ACTION
Category
NAICS
code 1
Industry .....................................................................
211111
211112
221210
486110
486210
....................
....................
Federal government .................................................
State/local/tribal government ....................................
1 North
Crude Petroleum and Natural Gas Extraction.
Natural Gas Liquid Extraction.
Natural Gas Distribution.
Pipeline Distribution of Crude Oil.
Pipeline Transportation of Natural Gas.
Not affected.
Not affected.
American Industry Classification System.
This table is not intended to be
exhaustive, but rather provides a guide
for readers regarding entities likely to be
affected by this action. To determine
whether your facility would be
regulated by this action, you should
examine the applicability criteria in the
regulations. If you have any questions
regarding the applicability of this action
to a particular entity, contact the person
listed in the preceding FOR FURTHER
INFORMATION CONTACT section.
B. Where can I get a copy of this
document and other related
information?
In addition to being available in the
docket, an electronic copy of this
proposal will also be available on the
EPA’s Web site. Following signature by
the EPA Administrator, a copy of this
proposed action will be posted on the
EPA’s Web site at the following address:
https://www.epa.gov/airquality/
oilandgas.
Additional information is available on
the EPA’s Residual Risk and Technology
Review (RTR) Web site at https://
www.epa.gov/ttn/atw/rrisk/oarpg.html.
This information includes the most
recent version of the rule, source
category descriptions, detailed
emissions and other data that were used
as inputs to the risk assessments.
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Examples of regulated entities
C. What should I consider as I prepare
my comments for the EPA?
Submitting CBI. Do not submit
information containing CBI to the EPA
through https://www.regulations.gov or
e-mail. Clearly mark the part or all of
the information that you claim to be
CBI. For CBI information on a disk or
CD ROM that you mail to the EPA, mark
the outside of the disk or CD ROM as
CBI and then identify electronically
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within the disk or CD ROM the specific
information that is claimed as CBI. In
addition to one complete version of the
comment that includes information
claimed as CBI, a copy of the comment
that does not contain the information
claimed as CBI must be submitted for
inclusion in the public docket. If you
submit a CD ROM or disk that does not
contain CBI, mark the outside of the
disk or CD ROM clearly that it does not
contain CBI. Information not marked as
CBI will be included in the public
docket and the EPA’s electronic public
docket without prior notice. Information
marked as CBI will not be disclosed
except in accordance with procedures
set forth in 40 CFR part 2. Send or
deliver information identified as CBI
only to the following address: Roberto
Morales, OAQPS Document Control
Officer (C404–02), Environmental
Protection Agency, Office of Air Quality
Planning and Standards, Research
Triangle Park, North Carolina 27711,
Attention Docket ID Number EPA–HQ–
OAR–2010–0505.
D. When will a public hearing occur?
We will hold three public hearings,
one in the Dallas, Texas area, one in
Pittsburgh, Pennsylvania, and one in
Denver, Colorado. If you are interested
in attending or speaking at one of the
public hearings, contact Ms. Joan Rogers
at (919) 541–4487 by September 6, 2011.
Details on the public hearings will be
provided in a separate notice and we
will specify the time and date of the
public hearings on https://www.epa.gov/
airquality/oilandgas. If no one requests
to speak at one of the public hearings by
September 6, 2011, then that public
hearing will be cancelled without
further notice.
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III. Background Information
A. What are standards of performance
and NSPS?
1. What is the statutory authority for
standards of performance and NSPS?
Section 111 of the Clean Air Act
(CAA) requires the EPA Administrator
to list categories of stationary sources, if
such sources cause or contribute
significantly to air pollution, which may
reasonably be anticipated to endanger
public health or welfare. The EPA must
then issue performance standards for
such source categories. A performance
standard reflects the degree of emission
limitation achievable through the
application of the ‘‘best system of
emission reduction’’ (BSER) which the
EPA determines has been adequately
demonstrated. The EPA may consider
certain costs and nonair quality health
and environmental impact and energy
requirements when establishing
performance standards. Whereas CAA
section 112 standards are issued for
existing and new stationary sources,
standards of performance are issued for
new and modified stationary sources.
These standards are referred to as new
source performance standards (NSPS).
The EPA has the authority to define the
source categories, determine the
pollutants for which standards should
be developed, identify the facilities
within each source category to be
covered and set the emission level of the
standards.
CAA section 111(b)(1)(B) requires the
EPA to ‘‘at least every 8 years review
and, if appropriate, revise’’ performance
standards unless the ‘‘Administrator
determines that such review is not
appropriate in light of readily available
information on the efficacy’’ of the
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standard. When conducting a review of
an existing performance standard, the
EPA has discretion to revise that
standard to add emission limits for
pollutants or emission sources not
currently regulated for that source
category.
In setting or revising a performance
standard, CAA section 111(a)(1)
provides that performance standards are
to ‘‘reflect the degree of emission
limitation achievable through the
application of the best system of
emission reduction which (taking into
account the cost of achieving such
reduction and any nonair quality health
and environmental impact and energy
requirements) the Administrator
determines has been adequately
demonstrated.’’ In this notice, we refer
to this level of control as the BSER. In
determining BSER, we typically conduct
a technology review that identifies what
emission reduction systems exist and
how much they reduce air pollution in
practice. Next, for each control system
identified, we evaluate its costs,
secondary air benefits (or disbenefits)
resulting from energy requirements and
nonair quality impacts such as solid
waste generation. Based on our
evaluation, we would determine BSER.
The resultant standard is usually a
numerical emissions limit, expressed as
a performance level (i.e., a rate-based
standard or percent control), that
reflects the BSER. Although such
standards are based on the BSER, the
EPA may not prescribe a particular
technology that must be used to comply
with a performance standard, except in
instances where the Administrator
determines it is not feasible to prescribe
or enforce a standard of performance.
Typically, sources remain free to elect
whatever control measures that they
choose to meet the emission limits.
Upon promulgation, an NSPS becomes
a national standard to which all new,
modified or reconstructed sources must
comply.
2. What is the regulatory history
regarding performance standards for the
oil and natural gas sector?
In 1979, the EPA listed crude oil and
natural gas production on its priority
list of source categories for
promulgation of NSPS (44 FR 49222,
August 21, 1979). On June 24, 1985 (50
FR 26122), the EPA promulgated an
NSPS for the source category that
addressed volatile organic compound
(VOC) emissions from leaking
components at onshore natural gas
processing plants (40 CFR part 60,
subpart KKK). On October 1, 1985 (50
FR 40158), a second NSPS was
promulgated for the source category that
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regulates sulfur dioxide (SO2) emissions
from natural gas processing plants (40
CFR part 60, subpart LLL). Other than
natural gas processing plants, EPA has
not previously set NSPS for a variety of
oil and natural gas operations.
B. What are NESHAP?
1. What is the statutory authority for
NESHAP?
Section 112 of the CAA establishes a
two-stage regulatory process to address
emissions of hazardous air pollutants
(HAP) from stationary sources. In the
first stage, after the EPA has identified
categories of sources emitting one or
more of the HAP listed in section 112(b)
of the CAA, section 112(d) of the CAA
calls for us to promulgate national
emission standards for hazardous air
pollutants (NESHAP) for those sources.
‘‘Major sources’’ are those that emit or
have the potential to emit (PTE) 10 tons
per year (tpy) or more of a single HAP
or 25 tpy or more of any combination of
HAP. For major sources, these
technology-based standards must reflect
the maximum degree of emission
reductions of HAP achievable (after
considering cost, energy requirements
and nonair quality health and
environmental impacts) and are
commonly referred to as maximum
achievable control technology (MACT)
standards.
MACT standards are to reflect
application of measures, processes,
methods, systems or techniques,
including, but not limited to, measures
which, (1) reduce the volume of or
eliminate pollutants through process
changes, substitution of materials or
other modifications, (2) enclose systems
or processes to eliminate emissions, (3)
capture or treat pollutants when
released from a process, stack, storage or
fugitive emissions point, (4) are design,
equipment, work practice or operational
standards (including requirements for
operator training or certification) or (5)
are a combination of the above. CAA
section 112(d)(2)(A)–(E). The MACT
standard may take the form of a design,
equipment, work practice or operational
standard where the EPA first determines
either that, (1) a pollutant cannot be
emitted through a conveyance designed
and constructed to emit or capture the
pollutant or that any requirement for or
use of such a conveyance would be
inconsistent with law or (2) the
application of measurement
methodology to a particular class of
sources is not practicable due to
technological and economic limitations.
CAA sections 112(h)(1)–(2).
The MACT ‘‘floor’’ is the minimum
control level allowed for MACT
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standards promulgated under CAA
section 112(d)(3), and may not be based
on cost considerations. For new sources,
the MACT floor cannot be less stringent
than the emission control that is
achieved in practice by the bestcontrolled similar source. The MACT
floors for existing sources can be less
stringent than floors for new sources,
but they cannot be less stringent than
the average emission limitation
achieved by the best-performing 12
percent of existing sources in the
category or subcategory (or the bestperforming five sources for categories or
subcategories with fewer than 30
sources). In developing MACT
standards, we must also consider
control options that are more stringent
than the floor. We may establish
standards more stringent than the floor
based on the consideration of the cost of
achieving the emissions reductions, any
nonair quality health and environmental
impacts and energy requirements.
The EPA is then required to review
these technology-based standards and to
revise them ‘‘as necessary (taking into
account developments in practices,
processes, and control technologies)’’ no
less frequently than every 8 years, under
CAA section 112(d)(6). In conducting
this review, the EPA is not obliged to
completely recalculate the prior MACT
determination. NRDC v. EPA, 529 F.3d
1077, 1084 (D.C. Cir. 2008).
The second stage in standard-setting
focuses on reducing any remaining
‘‘residual’’ risk according to CAA
section 112(f). This provision requires,
first, that the EPA prepare a Report to
Congress discussing (among other
things) methods of calculating risk
posed (or potentially posed) by sources
after implementation of the MACT
standards, the public health significance
of those risks, and the EPA’s
recommendations as to legislation
regarding such remaining risk. The EPA
prepared and submitted this report
(Residual Risk Report to Congress, EPA–
453/R–99–001) in March 1999. Congress
did not act in response to the report,
thereby triggering the EPA’s obligation
under CAA section 112(f)(2) to analyze
and address residual risk.
CAA section 112(f)(2) requires us to
determine for source categories subject
to MACT standards, whether the
emissions standards provide an ample
margin of safety to protect public health.
If the MACT standards for HAP
‘‘classified as a known, probable, or
possible human carcinogen do not
reduce lifetime excess cancer risks to
the individual most exposed to
emissions from a source in the category
or subcategory to less than 1-in-1
million,’’ the EPA must promulgate
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residual risk standards for the source
category (or subcategory), as necessary,
to provide an ample margin of safety to
protect public health. In doing so, the
EPA may adopt standards equal to
existing MACT standards if the EPA
determines that the existing standards
are sufficiently protective. NRDC v.
EPA, 529 F.3d 1077, 1083 (D.C. Cir.
2008). (‘‘If EPA determines that the
existing technology-based standards
provide an ‘‘ample margin of safety,’’
then the Agency is free to readopt those
standards during the residual risk
rulemaking.’’) The EPA must also adopt
more stringent standards, if necessary,
to prevent an adverse environmental
effect,1 but must consider cost, energy,
safety and other relevant factors in
doing so.
Section 112(f)(2) of the CAA expressly
preserves our use of a two-step process
for developing standards to address any
residual risk and our interpretation of
‘‘ample margin of safety’’ developed in
the National Emission Standards for
Hazardous Air Pollutants: Benzene
Emissions from Maleic Anhydride
Plants, Ethylbenzene/Styrene Plants,
Benzene Storage Vessels, Benzene
Equipment Leaks, and Coke By-Product
Recovery Plants (Benzene NESHAP) (54
FR 38044, September 14, 1989). The
first step in this process is the
determination of acceptable risk. The
second step provides for an ample
margin of safety to protect public health,
which is the level at which the
standards are set (unless a more
stringent standard is required to
prevent, taking into consideration costs,
energy, safety, and other relevant
factors, an adverse environmental
effect).
The terms ‘‘individual most exposed,’’
‘‘acceptable level,’’ and ‘‘ample margin
of safety’’ are not specifically defined in
the CAA. However, CAA section
112(f)(2)(B) preserves the interpretation
set out in the Benzene NESHAP, and the
United States Court of Appeals for the
District of Columbia Circuit in NRDC v.
EPA, 529 F.3d 1077, concluded that the
EPA’s interpretation of subsection
112(f)(2) is a reasonable one. See NRDC
v. EPA, 529 F.3d at 1083 (D.C. Cir.,
‘‘[S]ubsection 112(f)(2)(B) expressly
incorporates EPA’s interpretation of the
Clean Air Act from the Benzene
standard, complete with a citation to the
Federal Register’’). (D.C. Cir. 2008). See
1 ‘‘Adverse environmental effect’’ is defined in
CAA section 112(a)(7) as any significant and
widespread adverse effect, which may be
reasonably anticipated to wildlife, aquatic life or
natural resources, including adverse impacts on
populations of endangered or threatened species or
significant degradation of environmental qualities
over broad areas.
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also, A Legislative History of the Clean
Air Act Amendments of 1990, volume 1,
p. 877 (Senate debate on Conference
Report). We notified Congress in the
Residual Risk Report to Congress that
we intended to use the Benzene
NESHAP approach in making CAA
section 112(f) residual risk
determinations (EPA–453/R–99–001, p.
ES–11).
In the Benzene NESHAP, we stated as
an overall objective:
* * * in protecting public health with an
ample margin of safety, we strive to provide
maximum feasible protection against risks to
health from hazardous air pollutants by, (1)
protecting the greatest number of persons
possible to an individual lifetime risk level
no higher than approximately 1-in-1 million;
and (2) limiting to no higher than
approximately 1-in-10 thousand [i.e., 100-in1 million] the estimated risk that a person
living near a facility would have if he or she
were exposed to the maximum pollutant
concentrations for 70 years.
The Agency also stated that, ‘‘The
EPA also considers incidence (the
number of persons estimated to suffer
cancer or other serious health effects as
a result of exposure to a pollutant) to be
an important measure of the health risk
to the exposed population. Incidence
measures the extent of health risk to the
exposed population as a whole, by
providing an estimate of the occurrence
of cancer or other serious health effects
in the exposed population.’’ The Agency
went on to conclude that ‘‘estimated
incidence would be weighed along with
other health risk information in judging
acceptability.’’ As explained more fully
in our Residual Risk Report to Congress,
the EPA does not define ‘‘rigid line[s] of
acceptability,’’ but considers rather
broad objectives to be weighed with a
series of other health measures and
factors (EPA–453/R–99–001, p. ES–11).
The determination of what represents an
‘‘acceptable’’ risk is based on a
judgment of ‘‘what risks are acceptable
in the world in which we live’’
(Residual Risk Report to Congress, p.
178, quoting the Vinyl Chloride
decision at 824 F.2d 1165) recognizing
that our world is not risk-free.
In the Benzene NESHAP, we stated
that ‘‘EPA will generally presume that if
the risk to [the maximum exposed]
individual is no higher than
approximately 1-in-10 thousand, that
risk level is considered acceptable.’’ 54
FR 38045. We discussed the maximum
individual lifetime cancer risk (or
maximum individual risk (MIR)) as
being ‘‘the estimated risk that a person
living near a plant would have if he or
she were exposed to the maximum
pollutant concentrations for 70 years.’’
Id. We explained that this measure of
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risk ‘‘is an estimate of the upper bound
of risk based on conservative
assumptions, such as continuous
exposure for 24 hours per day for 70
years.’’ Id. We acknowledge that
maximum individual lifetime cancer
risk ‘‘does not necessarily reflect the
true risk, but displays a conservative
risk level which is an upper-bound that
is unlikely to be exceeded.’’ Id.
Understanding that there are both
benefits and limitations to using
maximum individual lifetime cancer
risk as a metric for determining
acceptability, we acknowledged in the
1989 Benzene NESHAP that
‘‘consideration of maximum individual
risk * * * must take into account the
strengths and weaknesses of this
measure of risk.’’ Id. Consequently, the
presumptive risk level of 100-in-1
million (1-in-10 thousand) provides a
benchmark for judging the acceptability
of maximum individual lifetime cancer
risk, but does not constitute a rigid line
for making that determination.
The Agency also explained in the
1989 Benzene NESHAP the following:
‘‘In establishing a presumption for MIR,
rather than a rigid line for acceptability,
the Agency intends to weigh it with a
series of other health measures and
factors. These include the overall
incidence of cancer or other serious
health effects within the exposed
population, the numbers of persons
exposed within each individual lifetime
risk range and associated incidence
within, typically, a 50-kilometer (km)
exposure radius around facilities, the
science policy assumptions and
estimation uncertainties associated with
the risk measures, weight of the
scientific evidence for human health
effects, other quantified or unquantified
health effects, effects due to co-location
of facilities and co-emission of
pollutants.’’ Id.
In some cases, these health measures
and factors taken together may provide
a more realistic description of the
magnitude of risk in the exposed
population than that provided by
maximum individual lifetime cancer
risk alone. As explained in the Benzene
NESHAP, ‘‘[e]ven though the risks
judged ‘‘acceptable’’ by the EPA in the
first step of the Vinyl Chloride inquiry
are already low, the second step of the
inquiry, determining an ‘‘ample margin
of safety,’’ again includes consideration
of all of the health factors, and whether
to reduce the risks even further.’’ In the
ample margin of safety decision process,
the Agency again considers all of the
health risks and other health
information considered in the first step.
Beyond that information, additional
factors relating to the appropriate level
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of control will also be considered,
including costs and economic impacts
of controls, technological feasibility,
uncertainties and any other relevant
factors. Considering all of these factors,
the Agency will establish the standard
at a level that provides an ample margin
of safety to protect the public health, as
required by CAA section 112(f). 54 FR
38046.
2. How do we consider the risk results
in making decisions?
As discussed in the previous section
of this preamble, we apply a two-step
process for developing standards to
address residual risk. In the first step,
the EPA determines if risks are
acceptable. This determination
‘‘considers all health information,
including risk estimation uncertainty,
and includes a presumptive limit on
maximum individual lifetime [cancer]
risk (MIR) 2 of approximately 1-in-10
thousand [i.e., 100-in-1 million].’’ 54 FR
38045. In the second step of the process,
the EPA sets the standard at a level that
provides an ample margin of safety ‘‘in
consideration of all health information,
including the number of persons at risk
levels higher than approximately 1-in-1
million, as well as other relevant factors,
including costs and economic impacts,
technological feasibility, and other
factors relevant to each particular
decision.’’ Id.
In past residual risk determinations,
the EPA presented a number of human
health risk metrics associated with
emissions from the category under
review, including: The MIR; the
numbers of persons in various risk
ranges; cancer incidence; the maximum
noncancer hazard index (HI); and the
maximum acute noncancer hazard. In
estimating risks, the EPA considered
source categories under review that are
located near each other and that affect
the same population. The EPA provided
estimates of the expected difference in
actual emissions from the source
category under review and emissions
allowed pursuant to the source category
MACT standard. The EPA also
discussed and considered risk
estimation uncertainties. The EPA is
providing this same type of information
in support of these actions.
The Agency acknowledges that the
Benzene NESHAP provides flexibility
regarding what factors the EPA might
consider in making our determinations
and how they might be weighed for each
source category. In responding to
2 Although
defined as ‘‘maximum individual
risk,’’ MIR refers only to cancer risk. MIR, one
metric for assessing cancer risk, is the estimated
risk were an individual exposed to the maximum
level of a pollutant for a lifetime.
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comment on our policy under the
Benzene NESHAP, the EPA explained
that: ‘‘The policy chosen by the
Administrator permits consideration of
multiple measures of health risk. Not
only can the MIR figure be considered,
but also incidence, the presence of
noncancer health effects, and the
uncertainties of the risk estimates. In
this way, the effect on the most exposed
individuals can be reviewed as well as
the impact on the general public. These
factors can then be weighed in each
individual case. This approach complies
with the Vinyl Chloride mandate that
the Administrator ascertain an
acceptable level of risk to the public by
employing [her] expertise to assess
available data. It also complies with the
Congressional intent behind the CAA,
which did not exclude the use of any
particular measure of public health risk
from the EPA’s consideration with
respect to CAA section 112 regulations,
and, thereby, implicitly permits
consideration of any and all measures of
health risk which the Administrator, in
[her] judgment, believes are appropriate
to determining what will ‘protect the
public health.’ ’’
For example, the level of the MIR is
only one factor to be weighed in
determining acceptability of risks. The
Benzene NESHAP explains ‘‘an MIR of
approximately 1-in-10 thousand should
ordinarily be the upper end of the range
of acceptability. As risks increase above
this benchmark, they become
presumptively less acceptable under
CAA section 112, and would be
weighed with the other health risk
measures and information in making an
overall judgment on acceptability. Or,
the Agency may find, in a particular
case, that a risk that includes MIR less
than the presumptively acceptable level
is unacceptable in the light of other
health risk factors.’’ Similarly, with
regard to the ample margin of safety
analysis, the Benzene NESHAP states
that: ‘‘EPA believes the relative weight
of the many factors that can be
considered in selecting an ample margin
of safety can only be determined for
each specific source category. This
occurs mainly because technological
and economic factors (along with the
health-related factors) vary from source
category to source category.’’
3. What is the regulatory history
regarding NESHAP for the oil and
natural gas sector?
On July 16, 1992 (57 FR 31576), the
EPA published a list of major and area
sources for which NESHAP are to be
published (i.e., the source category list).
Oil and natural gas production facilities
were listed as a category of major
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52743
sources. On February 12, 1998 (63 FR
7155), the EPA amended the source
category list to add Natural Gas
Transmission and Storage as a major
source category.
On June 17, 1999 (64 FR 32610), the
EPA promulgated MACT standards for
the Oil and Natural Gas Production and
Natural Gas Transmission and Storage
major source categories. The Oil and
Natural Gas Production NESHAP (40
CFR part 63, subpart HH) contains
standards for HAP emissions from
glycol dehydration process vents,
storage vessels and natural gas
processing plant equipment leaks. The
Natural Gas Transmission and Storage
NESHAP (40 CFR part 63, subpart HHH)
contains standards for glycol
dehydration process vents.
In addition to these NESHAP for
major sources, the EPA also
promulgated NESHAP for the Oil and
Natural Gas Production area source
category on January 3, 2007 (72 FR 26).
These area source standards, which are
based on generally available control
technology, are also contained in 40
CFR part 63, subpart HH. This proposed
action does not impact these area source
standards.
C. What litigation is related to this
proposed action?
On January 14, 2009, pursuant to
section 304(a)(2) of the CAA, WildEarth
Guardians and the San Juan Citizens
Alliance filed a Complaint alleging that
the EPA failed to meet its obligations
under CAA sections 111(b)(1)(B),
112(d)(6) and 112(f)(2) to take actions
relative to the review/revision of the
NSPS and the NESHAP with respect to
the Oil and Natural Gas Production
source category. On February 4, 2010,
the Court entered a consent decree
requiring the EPA to sign by July 28,
2011,3 proposed standards and/or
determinations not to issue standards
pursuant to CAA sections 111(b)(1)(B),
112(d)(6) and 112(f)(2) and to take final
action by February 28, 2012.
D. What is a sector-based approach?
Sector-based approaches are based on
integrated assessments that consider
multiple pollutants in a comprehensive
and coordinated manner to manage
emissions and CAA requirements. One
of the many ways we can address sectorbased approaches is by reviewing
multiple regulatory programs together
whenever possible, consistent with all
3 On April 27, 2011, pursuant to paragraph 10(a)
of the Consent Decree, the parties filed with the
Court a written stipulation that changes the
proposal date from January 31, 2011, to July 28,
2011, and the final action date from November 30,
2011, to February 28, 2012.
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applicable legal requirements. This
approach essentially expands the
technical analyses on costs and benefits
of particular technologies, to consider
the interactions of rules that regulate
sources. The benefit of multi-pollutant
and sector-based analyses and
approaches includes the ability to
identify optimum strategies, considering
feasibility, cost impacts and benefits
across the different pollutant types
while streamlining administrative and
compliance complexities and reducing
conflicting and redundant requirements,
resulting in added certainty and easier
implementation of control strategies for
the sector under consideration. In order
to benefit from a sector-based approach
for the oil and gas industry, the EPA
analyzed how the NSPS and NESHAP
under consideration relate to each other
and other regulatory requirements
currently under review for oil and gas
facilities. In this analysis, we looked at
how the different control requirements
that result from these requirements
interact, including the different
regulatory deadlines and control
equipment requirements that result, the
different reporting and recordkeeping
requirements and opportunities for
states to account for reductions resulting
from this rulemaking in their State
Implementation Plans (SIP). The
requirements analyzed affect criteria
pollutant, HAP and methane emissions
from oil and natural gas processes and
cover the NSPS and NESHAP reviews.
As a result of the sector-based approach,
this rulemaking will reduce conflicting
and redundant requirements. Also, the
sector-based approach facilitated the
streamlining of monitoring,
recordkeeping and reporting
requirements, thus, reducing
administrative and compliance
complexities associated with complying
with multiple regulations. In addition,
the sector-based approach promotes a
comprehensive control strategy that
maximizes the co-control of multiple
regulated pollutants while obtaining
emission reductions as co-benefits.
IV. Oil and Natural Gas Sector
The oil and natural gas sector
includes operations involved in the
extraction and production of oil and
natural gas, as well as the processing,
transmission and distribution of natural
gas. Specifically for oil, the sector
includes all operations from the well to
the point of custody transfer at a
petroleum refinery. For natural gas, the
sector includes all operations from the
well to the customer. The oil and
natural gas operations can generally be
separated into four segments: (1) Oil and
natural gas production, (2) natural gas
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processing, (3) natural gas transmission
and (4) natural gas distribution. Each of
these segments is briefly discussed
below.
Oil and natural gas production
includes both onshore and offshore
operations. Production operations
include the wells and all related
processes used in the extraction,
production, recovery, lifting,
stabilization, separation or treating of oil
and/or natural gas (including
condensate). Production components
may include, but are not limited to,
wells and related casing head, tubing
head and ‘‘Christmas tree’’ piping, as
well as pumps, compressors, heater
treaters, separators, storage vessels,
pneumatic devices and dehydrators.
Production operations also include the
well drilling, completion and workover
processes and includes all the portable
non-self-propelled apparatus associated
with those operations. Production sites
include not only the ‘‘pads’’ where the
wells are located, but also include
stand-alone sites where oil, condensate,
produced water and gas from several
wells may be separated, stored and
treated. The production sector also
includes the low pressure, small
diameter, gathering pipelines and
related components that collect and
transport the oil, gas and other materials
and wastes from the wells to the
refineries or natural gas processing
plants. None of the operations upstream
of the natural gas processing plant are
covered by the existing NSPS. Offshore
oil and natural gas production occurs on
platform structures that house
equipment to extract oil and gas from
the ocean or lake floor and that process
and/or transfer the oil and gas to
storage, transport vessels or onshore.
Offshore production can also include
secondary platform structures
connected to the platform structure,
storage tanks associated with the
platform structure and floating
production and offloading equipment.
There are three basic types of wells:
Oil wells, gas wells and associated gas
wells. Oil wells can have ‘‘associated’’
natural gas that is separated and
processed or the crude oil can be the
only product processed. Once the crude
oil is separated from the water and other
impurities, it is essentially ready to be
transported to the refinery via truck,
railcar or pipeline. We consider the oil
refinery sector separately from the oil
and natural gas sector. Therefore, at the
point of custody transfer at the refinery,
the oil leaves the oil and natural gas
sector and enters the petroleum refining
sector.
Natural gas is primarily made up of
methane. However, whether natural gas
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is associated gas from oil wells or nonassociated gas from gas or condensate
wells, it commonly exists in mixtures
with other hydrocarbons. These
hydrocarbons are often referred to as
natural gas liquids (NGL). They are sold
separately and have a variety of
different uses. The raw natural gas often
contains water vapor, hydrogen sulfide
(H2S), carbon dioxide (CO2), helium,
nitrogen and other compounds. Natural
gas processing consists of separating
certain hydrocarbons and fluids from
the natural gas to produced ‘‘pipeline
quality’’ dry natural gas. While some of
the processing can be accomplished in
the production segment, the complete
processing of natural gas takes place in
the natural gas processing segment.
Natural gas processing operations
separate and recover NGL or other nonmethane gases and liquids from a stream
of produced natural gas through
components performing one or more of
the following processes: Oil and
condensate separation, water removal,
separation of NGL, sulfur and CO2
removal, fractionation of natural gas
liquid and other processes, such as the
capture of CO2 separated from natural
gas streams for delivery outside the
facility. Natural gas processing plants
are the only operations covered by the
existing NSPS.
The pipeline quality natural gas
leaves the processing segment and
enters the transmission segment.
Pipelines in the natural gas transmission
segment can be interstate pipelines that
carry natural gas across state boundaries
or intrastate pipelines, which transport
the gas within a single state. While
interstate pipelines may be of a larger
diameter and operated at a higher
pressure, the basic components are the
same. To ensure that the natural gas
flowing through any pipeline remains
pressurized, compression of the gas is
required periodically along the pipeline.
This is accomplished by compressor
stations usually placed between 40 and
100 mile intervals along the pipeline. At
a compressor station, the natural gas
enters the station, where it is
compressed by reciprocating or
centrifugal compressors.
In addition to the pipelines and
compressor stations, the natural gas
transmission segment includes
underground storage facilities.
Underground natural gas storage
includes subsurface storage, which
typically consists of depleted gas or oil
reservoirs and salt dome caverns used
for storing natural gas. One purpose of
this storage is for load balancing
(equalizing the receipt and delivery of
natural gas). At an underground storage
site, there are typically other processes,
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including compression, dehydration
and flow measurement.
The distribution segment is the final
step in delivering natural gas to
customers. The natural gas enters the
distribution segment from delivery
points located on interstate and
intrastate transmission pipelines to
business and household customers. The
delivery point where the natural gas
leaves the transmission segment and
enters the distribution segment is often
called the ‘‘citygate.’’ Typically, utilities
take ownership of the gas at the citygate.
Natural gas distribution systems consist
of thousands of miles of piping,
including mains and service pipelines
to the customers. Distribution systems
sometimes have compressor stations,
although they are considerably smaller
than transmission compressor stations.
Distribution systems include metering
stations, which allow distribution
companies to monitor the natural gas in
the system. Essentially, these metering
stations measure the flow of gas and
allow distribution companies to track
natural gas as it flows through the
system.
Emissions can occur from a variety of
processes and points throughout the oil
and natural gas sector. Primarily, these
emissions are organic compounds such
as methane, ethane, VOC and organic
HAP. The most common organic HAP
are n-hexane and BTEX compounds
(benzene, toluene, ethylbenzene and
xylenes). Hydrogen sulfide (H2S) and
sulfur dioxide (SO2) are emitted from
production and processing operations
that handle and treat ‘‘sour gas.’’ Sour
gas is defined as natural gas with a
maximum H2S content of 0.25 gr/100 scf
(4ppmv) along with the presence of CO2.
In addition, there are significant
emissions associated with the
reciprocating internal combustion
engines and combustion turbines that
power compressors throughout the oil
and natural gas sector. However,
emissions from internal combustion
engines and combustion turbines are
covered by regulations specific to
engines and turbines and, thus, are not
addressed in this action.
V. Summary of Proposed Decisions and
Actions
Pursuant to CAA sections 111(b),
112(d)(2), 112(d)(6) and 112(f), we are
proposing to revise the NSPS and
NESHAP relative to oil and gas to
include the standards and requirements
summarized in this section. More
details of the rationale for these
proposed standards and requirements
are provided in sections VI and VII of
this preamble. In addition, as part of
these rationale discussions, we solicit
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public comment and data relevant to
several issues. The comments we
receive during the public comment
period will help inform the rule
development process as we work toward
promulgating a final action.
A. What are the proposed revisions to
the NSPS?
We reviewed the two NSPS that apply
to the oil and natural gas industry.
Based on our review, we believe that the
requirements at 40 CFR part 60, subpart
KKK, should be updated to reflect
requirements in 40 CFR part 60, subpart
VVa for controlling VOC equipment
leaks at processing plants. We also
believe that the requirements at 40 CFR
part 60, subpart LLL, for controlling SO2
emissions from natural gas processing
plants should be strengthened for
facilities with the highest sulfur feed
rates and the highest H2S
concentrations. For a more detailed
discussion, please see section VI.B.1 of
this preamble.
In addition, there are significant VOC
emissions from oil and natural gas
operations that are not covered by the
two existing NSPS, including other
emissions at processing plants and
emissions from upstream production, as
well as transmission and storage
facilities. In the 1984 notice that listed
source categories (including Oil and
Natural Gas) for promulgation of NSPS,
we noted that there were discrepancies
between the source category names on
the list and those in the background
document, and we clarified our intent to
address all sources under an industry
heading at the same time. See 44 FR
49222, 49224–49225.4 We, therefore,
believe that the currently listed Oil and
Natural Gas source category covers all
operations in this industry (i.e.,
production, processing, transmission,
storage and distribution). To the extent
there are oil and gas operations not
covered by the currently listed Oil and
Natural Gas source category, pursuant to
CAA section 111(b), we hereby modify
the category list to include all
operations in the oil and natural gas
sector. Section 111(b) of the CAA gives
the EPA broad authority and discretion
to list and establish NSPS for a category
that, in the Administrator’s judgment,
causes or contributes significantly to air
pollution which may reasonably be
anticipated to endanger public health or
welfare. Pursuant to CAA section
111(b), we are modifying the source
category list to include any oil and gas
4 The Notice further states that ‘‘The
Administrator may also concurrently develop
standards for sources which are not on the priority
list.’’ 44 FR at 49225.
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operation not covered by the current
listing and evaluating emissions from all
oil and gas operations at the same time.
We are also proposing standards for
several new oil and natural gas affected
facilities. The proposed standards
would apply to affected facilities that
commence construction, reconstruction
or modification after August 23, 2011.
These standards, which include
requirements for VOC, would be
contained in a new subpart, 40 CFR part
60, subpart OOOO. Subpart OOOO
would incorporate 40 CFR part 60,
subpart KKK and 40 CFR part 60,
subpart LLL, thereby having in this one
subpart, all standards that are applicable
to the new and modified affected
facilities described above. We also
propose to amend the title of subparts
KKK and LLL, accordingly, to apply
only to affected facilities already subject
to those subparts. Those operations
would not become subject to subpart
OOOO unless they triggered
applicability based on new or modified
affected facilities under subpart OOOO.
We are proposing operational
standards for completions of
hydraulically fractured gas wells. Based
on our review, we identified two
subcategories of fractured gas wells for
which well completions are conducted.
For non-exploratory and nondelineation wells, the proposed
operational standards would require
reduced emission completion (REC),
commonly referred to as ‘‘green
completion,’’ in combination with pitflaring of gas not suitable for entering
the gathering line. For exploratory and
delineation wells (these wells generally
are not in close proximity to a gathering
line), we proposed an operational
standard that would require pit flaring.
Well completions subject to the
standards would be limited to gas well
completions following hydraulic
fracturing operations. These
completions include those conducted at
newly drilled and fractured wells, as
well as completions conducted
following refracturing operations at
various times over the life of the well.
We have determined that a completion
associated with refracturing performed
at an existing well (i.e., a well existing
prior to August 23, 2011) is considered
a modification under CAA section
111(a), because physical change occurs
to the existing well resulting in
emissions increase during the
refracturing and completion operation.
A detailed discussion of this
determination is presented in the
Technical Support Document (TSD) in
the docket. Therefore, the proposed
standards would apply to completions
at new gas wells that are fractured or
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refractured along with completions
associated with fracturing or
refracturing of existing gas wells. The
modification determination and
resultant applicability of NSPS to the
completion operation following
fracturing or refracturing of existing gas
wells (i.e., wells existing before August
23, 2011 would be limited strictly to the
wellhead, well bore, casing and tubing,
and any conveyance through which gas
is vented to the atmosphere and not be
extended beyond the wellhead to other
ancillary components that may be at the
well site such as existing storage
vessels, process vessels, separators,
dehydrators or any other components or
apparatus.
We are also proposing VOC standards
to reduce emissions from gas-driven
pneumatic devices. We are proposing
that each pneumatic device is an
affected facility. Accordingly, the
proposed standards would apply to each
newly installed pneumatic device
(including replacement of an existing
device). At gas processing plants, we are
proposing a zero emission limit for each
individual pneumatic controller. The
proposed emission standards would
reflect the emission level achievable
from the use of non-gas-driven
pneumatic controllers. At other
locations, we are proposing a bleed limit
of 6 standard cubic feet of gas per hour
for an individual pneumatic controller,
which would reflect the emission level
achievable from the use of low bleed
gas-driven pneumatic controllers. In
both cases, the standards provide
exemptions for certain applications
based on functional considerations.
In addition, the proposed rule would
require measures to reduce VOC
emissions from centrifugal and
reciprocating compressors. As explained
in more detail below in section VI.B.4,
we are proposing equipment standards
for centrifugal compressors. The
proposed standards would require the
use of dry seal systems. However, we
are aware that some owners and
operators may need to use centrifugal
compressors with wet seals, and we are
soliciting comment on the suitability of
a compliance option allowing the use of
wet seals combined with routing of
emissions from the seal liquid through
a closed vent system to a control device
as an acceptable alternative to installing
dry seals.
Our review of reciprocating
compressors found that piston rod
packing wear produces fugitive
emissions that cannot be captured and
conveyed to a control device. As a
result, we are proposing operational
standards for reciprocating compressors,
such that the proposed rule would
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require replacement of the rod packing
based on hours of usage. The owner or
operator of a reciprocating compressor
affected facility would be required to
monitor the duration (in hours) that the
compressor is operated. When the hours
of operation reaches 26,000 hours, the
owner or operator would be required to
change the rod packing immediately.
However, to avoid unscheduled
shutdowns when 26,000 hours is
reached, owners and operators could
track hours of operation such that
packing replacement could be
coordinated with planned maintenance
shutdowns before hours of operation
reached 26,000. Some operators may
prefer to replace the rod packing on a
fixed schedule to ensure that the hours
of operation would not reach 26,000
hours. We solicit comment on the
appropriateness of a fixed replacement
frequency and other considerations that
would be associated with regular
replacement.
We are also proposing VOC standards
for new or modified storage vessels. The
proposed rule, which would apply to
individual vessels, would require that
vessels meeting certain specifications
achieve at least 95-percent reduction in
VOC emissions. Requirements would
apply to vessels with a throughput of 1
barrel of condensate per day or 20
barrels of crude oil per day. These
thresholds are equivalent to VOC
emissions of about 6 tpy.
For gas processing plants, we are
updating the requirements for leak
detection and repair (LDAR) to reflect
procedures and leak thresholds
established by 40 CFR 60, subpart VVa.
The existing NSPS requires 40 CFR part
60, subpart VV procedures and
thresholds.
For 40 CFR part 60, subpart LLL,
which regulates SO2 emissions from
natural gas processing plants, we
determined that affected facilities with
sulfur feed rate of at least 5 long tons
per day or H2S concentration in the acid
gas stream of at least 50 percent can
achieve up to 99.9-percent SO2 control,
which is greater than the existing
standard. Therefore, we are proposing
revision to the performance standards in
subpart LLL as a result of this review.
For a more detailed discussion of this
proposed determination, please see
section VI.B.1 of this preamble.
We are proposing to address
compliance requirements for periods of
startup, shutdown and malfunction
(SSM) for 40 CFR part 60, subpart
OOOO. The SSM changes are discussed
in detail in section VI.B.5 below. In
addition, we are proposing to
incorporate the requirements in 40 CFR
part 60, subpart KKK and 40 CFR part
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60, subpart LLL into the new subpart
OOOO so that all requirements
applicable to the new and modified
facilities would be in one subpart. This
would simplify and streamline
compliance efforts on the part of the oil
and natural gas industry and could
minimize duplication of notification,
recordkeeping and reporting.
B. What are the proposed decisions and
actions related to the NESHAP?
This section summarizes the results of
our RTR for the Oil and Natural Gas
Production and the Natural Gas
Transmission and Storage source
categories and our proposed decisions
concerning these two 1999 NESHAP.
1. Addressing Unregulated Emissions
Sources
Pursuant to CAA sections 112(d)(2)
and (3), we are proposing MACT
standards for subcategories of glycol
dehydrators for which standards were
not previously developed (hereinafter
referred to as the ‘‘small dehydrators’’).
In the Oil and Natural Gas Production
source category, the subcategory
consists of glycol dehydrators with an
actual annual average natural gas
flowrate less than 85,000 standard cubic
meters per day (scmd) or actual average
benzene emissions less than 0.9
megagrams per year (Mg/yr). In the
Natural Gas Transmission and Storage
source category, the subcategory
consists of glycol dehydrators with an
actual annual average natural gas
flowrate less than 283,000 scmd or
actual average benzene emissions less
than 0.9 Mg/yr.
The proposed MACT standards for the
subcategory of small dehydrators at oil
and gas production facilities would
require that existing affected sources
meet a unit-specific BTEX limit of 1.10
× 10¥4 grams BTEX/standard cubic
meters (scm)-parts per million by
volume (ppmv) and that new affected
sources meet a BTEX limit of 4.66 ×
10¥6 grams BTEX/scm-ppmv. At
natural gas transmission and storage
affected sources, the proposed MACT
standard for the subcategory of small
dehydrators would require that existing
affected sources meet a unit-specific
BTEX emission limit of 6.42 × 10¥5
grams BTEX/scm-ppmv and that new
affected sources meet a BTEX limit of
1.10 × 10¥5 grams BTEX/scm-ppmv.
We are also proposing MACT
standards for storage vessels that are
currently not regulated under the Oil
and Natural Gas Production NESHAP.
The current MACT standards apply only
to storage vessels with the potential for
flash emissions (PFE). As explained in
section VII, the original MACT analysis
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accounted for all storage vessels. We
are, therefore, proposing to apply the
current MACT standards of 95-percent
emission reduction to every storage
vessel at major source oil and natural
gas production facilities. In conjunction
with this change, we are proposing to
amend the definition of associated
equipment to exclude all storage
vessels, and not just those with the PFE,
from being considered ‘‘associated
equipment.’’ This means that emissions
from all storage vessels, and not just
those from storage vessels with the PFE,
are to be included in the major source
determination.
2. What are the proposed decisions and
actions related to the risk review?
For both the Oil and Natural Gas
Production and the Natural Gas
Transmission and Storage source
categories, we find that the current
levels of emissions allowed by the
MACT reflect acceptable levels of risk;
however, the level of emissions allowed
by the alternative compliance option for
glycol dehydrator MACT (i.e., the
option of reducing benzene emissions to
less than 0.9 Mg/yr in lieu of the MACT
standard of 95-percent control) reflects
an unacceptable level of risk. We are,
therefore, proposing to eliminate the 0.9
Mg/yr alternative compliance option.
In addition, we are proposing that the
MACT for these two oil and gas source
categories, as revised per above, provide
an ample margin of safety to protect
public health and prevent adverse
environmental effects.
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3. What are the proposed decisions and
actions related to the technology
reviews of the existing NESHAP?
For both the Oil and Natural Gas
Production and the Natural Gas
Transmission and Storage source
categories, we are proposing no
revisions to the existing NESHAP
pursuant to section 112(d)(6) of the
CAA.
4. What other actions are we proposing?
We are proposing an alternative
performance test for non-flare,
combustion control devices. This test is
to be conducted by the combustion
control device manufacturer to
demonstrate the destruction efficiency
achieved by a specific model of
combustion control device. This would
allow a source to purchase a
performance tested device for
installation at their site without being
required to conduct a site-specific
performance test. A definition for
‘‘flare’’ is being proposed in the
NESHAP to clarify which combustion
control devices fall under the
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manufacturers’ performance testing
alternative, and to clarify which devices
must be performance tested.
We are also proposing to: Revise the
parametric monitoring calibration
provisions; require periodic
performance testing where applicable;
remove the allowance of a design
analysis for all control devices other
than condensers; remove the
requirement for a minimum residence
time for an enclosed combustion device;
and add recordkeeping and reporting
requirements to document carbon
replacement intervals. These changes
are being proposed to bring the
NESHAP up-to-date based on what we
have learned regarding control devices
and compliance since the original
promulgation date.
In addition, we are proposing the
elimination of the SSM exemption in
the Oil and Natural Gas Production and
the Natural Gas Transmission and
Storage NESHAP. As discussed in more
detail below in section VII, consistent
with Sierra Club v. EPA, 551 F.3d 1019
(D.C. Cir. 2010), the EPA is proposing
that the established standards in these
two NESHAP apply at all times. We are
proposing to revise Table 2 to both 40
CFR part 63, subpart HH and 40 CFR
part 63, subpart HHH to indicate that
certain 40 CFR part 63 general
provisions relative to SSM do not apply,
including: 40 CFR 63.6 (e)(1)(i) 5 and
(ii), 40 CFR 63.6(e)(3) (SSM plan
requirement), 40 CFR 63.6(f)(1); 40 CFR
63.7(e)(1), 40 CFR 63.8(c)(1)(i) and (iii),
and the last sentence of 40 CFR
63.8(d)(3); 40 CFR 63.10(b)(2)(i),(ii), (iv)
and (v); 40 CFR 63.10(c)(10), (11) and
(15); and 40 CFR 63.10(d)(5). We are
also proposing to: (1) Revise 40 CFR
63.771(d)(4)(i) and 40 CFR
63.1281(d)(4)(i) regarding operation of
the control device to be consistent with
the SSM compliance requirements; and
(2) revise the SSM-associated reporting
and recordkeeping requirements in 40
CFR 63.774, 40 CFR 63.775, 40 CFR
63.1284 and 40 CFR 63.1285 to require
reporting and recordkeeping for periods
of malfunction. In addition, as
explained below, we are proposing to
add an affirmative defense to civil
penalties for exceedances of emission
limits caused by malfunctions, as well
5 40 CFR 63.6(e)(1)(i) requires owners or operators
to act according to the general duty to ‘‘operate and
maintain any affected source, including associated
air pollution control equipment and monitoring
equipment, in a manner consistent with safety and
good air pollution control practices for minimizing
emissions.’’ This general duty to minimize is
included in our proposed standard at 40 CFR
63.783(b)(1).
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as criteria for establishing the
affirmative defense.
The EPA has attempted to ensure that
we have neither overlooked nor failed to
propose to remove from the existing text
any provisions that are inappropriate,
unnecessary or redundant in the
absence of the SSM exemption, nor
included any such provisions in the
proposed new regulatory language. We
are specifically seeking comment on
whether there are any such provisions
that we have inadvertently overlooked
or incorporated.
We are also revising the applicability
provisions of 40 CFR part 63, subpart
HH to clarify requirements regarding
PTE determination and the scope of a
facility subject to subpart HH. Lastly, we
are proposing several editorial
corrections and plain language revisions
to improve these rules.
C. What are the proposed notification,
recordkeeping and reporting
requirements for this proposed action?
1. What are the proposed notification,
recordkeeping and reporting
requirements for the proposed NSPS?
The proposed 40 CFR part 60, subpart
OOOO includes new requirements for
several operations for which there are
no existing Federal standards. Most
notably, as discussed in sections V.A
and VI.B of this preamble, the proposed
NSPS will cover completions and
recompletions of hydraulically fractured
gas wells. We estimate that over 20,000
completions and recompletions
annually will be subject to the proposed
requirements. Given the number of
these operations, we believe that
notification and reporting must be
streamlined to the extent possible to
minimize undue burden on owners and
operators, as well as state, local and
tribal agencies. In section V.D of this
preamble, we discuss some innovative
implementation approaches being
considered and seek comment on these
and other potential methods of
streamlining notification and reporting
for well completions covered by the
proposed rule.
Owners or operators are required to
submit initial notifications and annual
reports, and to retain records to assist in
documenting that they are complying
with the provisions of the NSPS. These
notification, recordkeeping and
reporting activities include both
requirements of the 40 CFR part 60
General Provisions, as well as
requirements specific to 40 CFR part 60,
subpart OOOO.
Owners or operators of affected
facilities (except for pneumatic
controller and gas wellhead affected
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sources) must submit an initial
notification within 1 year after
becoming subject to 40 CFR part 60,
subpart OOOO or by 1 year after the
publication of the final rule in the
Federal Register, whichever is later. For
pneumatic controllers, owners and
operators are not required to submit an
initial notification, but instead are
required to report the installation of
these affected facilities in their facility’s
annual report. Owners or operators of
wellhead affected facilities (well
completions) would also be required to
submit a 30-day advance notification of
each well completion subject to the
NSPS. In addition, annual reports are
due 1 year after initial startup date for
your affected facility or 1 year after the
date of publication of the final rule in
the Federal Register, whichever is later.
The notification and annual reports
must include information on all affected
facilities owned or operated that were
new, modified or reconstructed sources
during the reporting period. A single
report may be submitted covering
multiple affected facilities, provided
that the report contains all the
information required by 40 CFR
60.5420(b). This information includes
general information on the facility (i.e.,
company name and address, etc.), as
well as information specific to
individual affected facilities.
For wellhead affected facilities, this
information includes details of each
well completion during the period,
including duration of periods of gas
recovery, flaring and venting. For
centrifugal compressor affected
facilities, information includes
documentation that the compressor is
fitted with dry seals. For reciprocating
compressors, information includes the
cumulative hours of operation of each
compressor and records of rod packing
replacement.
Information for pneumatic device
affected facilities includes location and
manufacturer specifications of each
pneumatic controller installed during
the period and documentation that
supports any exemption claimed
allowing use of high bleed controllers.
For controllers installed at gas
processing plants, the owner or operator
would document the use of non-gas
driven devices. For controllers installed
in locations other than at gas processing
plants, owners or operators would
provide manufacturer’s specifications
that document bleed rate not exceeding
6 cubic feet per hour.
For storage vessel affected facilities,
required report information includes
information that documents control
device compliance, if applicable. For
vessels with throughputs below 1 barrel
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of condensate per day and 21 barrels of
crude oil per day, required information
also includes calculations or other
documentation of the throughput. For
onshore gas processing plants, semiannual reports are required, and include
information on number of pressure
relief devices, number of pressure relief
devices for which leaks were detected
and pressure relief devices for which
leaks were not repaired, as required in
40 CFR 60.5396 of subpart OOOO.
Records must be retained for 5 years
and generally consist of the same
information required in the initial
notification and annual and semiannual
reports.
2. What are the proposed amendments
to notification, recordkeeping and
reporting requirements for the
NESHAP?
We are proposing to revise certain
recordkeeping requirements of 40 CFR
part 63, subpart HH and 40 CFR part 63,
subpart HHH. Specifically, we are
proposing that facilities using carbon
adsorbers as a control device keep
records of their carbon replacement
schedule and records for each carbon
replacement. In addition, owners and
operators are required to keep records of
the occurrence and duration of each
malfunction or operation of the air
pollution control equipment and
monitoring equipment.
In addition, in conjunction with the
proposed MACT standards for small
glycol dehydration units and storage
vessels that do not have the PFE in the
proposed amendment to 40 CFR part 63,
subpart HH, we are proposing that
owners and operators of affected small
glycol dehydration units and storage
vessels submit an initial notification
within 1 year after becoming subject to
subpart HH or by 1 year after the
publication of the final rule in the
Federal Register, whichever is later.
Similarly, in conjunction with the
proposed MACT standards for small
glycol dehydration units in the
proposed 40 CFR part 63, subpart HHH
amendments, we are proposing that
owners and operators of small glycol
dehydration units submit an initial
notification within 1 year after
becoming subject to subpart HHH or by
1 year after the publication of the final
rule in the Federal Register, whichever
is later. Affected sources under either 40
CFR part 63, subpart HH or subpart
HHH that plan to be area sources by the
compliance dates will be required to
submit a notification describing their
schedule for the actions planned to
achieve area source status.
The proposed amendments to the
NESHAP also include additional
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requirements for the contents of the
periodic reports. For both 40 CFR part
63, subpart HH and 40 CFR part 63,
subpart HHH, we are proposing that the
periodic reports also include periodic
test results and information regarding
any carbon replacement events that
occurred during the reporting period.
3. How is information submitted using
the Electronic Reporting Tool (ERT)?
Performance test data are an
important source of information that the
EPA uses in compliance determinations,
developing and reviewing standards,
emission factor development, annual
emission rate determinations and other
purposes. In these activities, the EPA
has found it ineffective and time
consuming, not only for owners and
operators, but also for regulatory
agencies, to locate, collect and submit
performance test data because of varied
locations for data storage and varied
data storage methods. In recent years,
though, stack testing firms have
typically collected performance test data
in electronic format, making it possible
to move to an electronic data submittal
system that would increase the ease and
efficiency of data submittal and improve
data accessibility.
Through this proposal, the EPA is
taking a step to increase the ease and
efficiency of data submittal and improve
data accessibility. Specifically, the EPA
is proposing that owners and operators
of oil and natural gas sector facilities
submit electronic copies of required
performance test reports to the EPA’s
WebFIRE database. The WebFIRE
database was constructed to store
performance test data for use in
developing emission factors. A
description of the WebFIRE database is
available at https://cfpub.epa.gov/
oarweb/index.cfm?action=fire.main.
As proposed above, data entry would
be through an electronic emissions test
report structure called the Electronic
Reporting Tool (ERT). The ERT will be
able to transmit the electronic report
through the EPA’s Central Data
Exchange network for storage in the
WebFIRE database making submittal of
data very straightforward and easy. A
description of the ERT can be found at
https://www.epa.gov/ttn/chief/ert/
ert_tool.html.
The proposal to submit performance
test data electronically to the EPA
would apply only to those performance
tests conducted using test methods that
will be supported by the ERT. The ERT
contains a specific electronic data entry
form for most of the commonly used
EPA reference methods. A listing of the
pollutants and test methods supported
by the ERT is available at https://
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www.epa.gov/ttn/chief/ert/ert_tool.html.
We believe that industry would benefit
from this proposed approach to
electronic data submittal. Having these
data, the EPA would be able to develop
improved emission factors, make fewer
information requests, and promulgate
better regulations.
One major advantage of the proposed
submittal of performance test data
through the ERT is a standardized
method to compile and store much of
the documentation required to be
reported by this rule. Another advantage
is that the ERT clearly states testing
information that would be required.
Another important benefit of submitting
these data to the EPA at the time the
source test is conducted is that it should
substantially reduce the effort involved
in data collection activities in the
future. When the EPA has performance
test data in hand, there will likely be
fewer or less substantial data collection
requests in conjunction with
prospective required residual risk
assessments or technology reviews. This
would result in a reduced burden on
both affected facilities (in terms of
reduced manpower to respond to data
collection requests) and the EPA (in
terms of preparing and distributing data
collection requests and assessing the
results).
State, local and tribal agencies could
also benefit from more streamlined and
accurate review of electronic data
submitted to them. The ERT would
allow for an electronic review process
rather than a manual data assessment
making review and evaluation of the
source provided data and calculations
easier and more efficient. Finally,
another benefit of the proposed data
submittal to WebFIRE electronically is
that these data would greatly improve
the overall quality of existing and new
emissions factors by supplementing the
pool of emissions test data for
establishing emissions factors and by
ensuring that the factors are more
representative of current industry
operational procedures. A common
complaint heard from industry and
regulators is that emission factors are
outdated or not representative of a
particular source category. With timely
receipt and incorporation of data from
most performance tests, the EPA would
be able to ensure that emission factors,
when updated, represent the most
current range of operational practices. In
summary, in addition to supporting
regulation development, control strategy
development and other air pollution
control activities having an electronic
database populated with performance
test data would save industry, state,
local, tribal agencies and the EPA
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significant time, money and effort while
also improving the quality of emission
inventories and, as a result, air quality
regulations.
D. What are the innovative compliance
approaches being considered?
Given the potential number and
diversity of sources affected by this
action, we are exploring optional
approaches to provide the regulated
community, the regulators and the
public a more effective mechanism that
maximizes compliance and
transparency while minimizing burden.
Under a traditional approach, owners
or operators would provide notifications
and keep records of information
required by the NSPS. In addition, they
would certify compliance with the
NSPS as part of a required annual report
that would include compliance-related
information, such as details of each well
completion event and information
documenting compliance with other
requirements of the NSPS. The EPA,
state or local agency would then
physically inspect the affected facilities
and/or audit the records retained by the
owner or operator. As an alternative to
the traditional approach, we are seeking
an innovative way to provide for more
transparency to the public and less
burden on the regulatory agencies and
owners and operators, especially as it
relates to modification of existing
sources through recompletions of
hydraulically fractured gas wells. These
innovative approaches would provide
compliance assurance in light of the
absence of requirements for CAA title V
permitting of non-major sources.
Section V.E of this preamble discusses
permitting implications associated with
the NSPS and presents a proposed
rationale for exempting non-major
sources subject to the NSPS from title V
permitting requirements. As discussed
in sections V.A, V.C and VI.B of this
preamble, the proposed NSPS will cover
completions and recompletions of
hydraulically fractured gas wells. We
estimate that over 20,000 completions
and recompletions annually will be
subject to the proposed requirements.
As a result, we believe that notification
and reporting associated with well
completions must be streamlined to the
extent possible to minimize undue
burden on owners and operators, as well
as state, local and tribal agencies.
Though the requirements being
proposed here are based on the
traditional approach to compliance and
do not include specific regulatory
provisions for innovative compliance
tools, we have included discussions
below that describe how some of these
optional tools could work, and we will
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consider providing for such options in
the final action. Further, we request
comments and suggestions on all
aspects of the innovative compliance
approaches discussed below and how
they may be implemented
appropriately. We are seeking comment
regarding the scope of application of
one or more of these approaches, i.e.,
which provisions of the standards being
proposed here would be suitable for
specific compliance approaches, and
whether the approaches should be
alternatives to the requirements in the
regulations.
The guiding principles we are
following in considering these
approaches to compliance are: (1)
Simplicity and ease of understanding
and implementation; (2) transparency
and public accessibility; (3) electronic
implementation where appropriate; and
(4) encouragement of compliance by
making compliance easier than
noncompliance. Below are some tools
that, when used in tandem with
emissions limits and operational
standards, the Agency believes could
both assure compliance and
transparency, while minimizing burden
on affected sources and regulatory
agencies.
1. Registration of Wells and Advance
Notification of Planned Completions
Although the proposed NSPS will not
require approval to drill or complete
wells, it is important that regulatory
agencies know when completions of
hydraulically fractured wells are to be
performed. Notification should occur
sufficiently in advance to allow for
inspections or audits to certify or verify
that the operator will have in place and
use the appropriate controls during the
completion. To that end, the proposed
NSPS requires a 30-day advance
notification of each completion or
recompletion of a hydraulically
fractured gas well. The advance
notification would require that owners
or operators provide the anticipated
date of the completion, the geographic
coordinates of the well and identifying
information concerning the owner or
operator and responsible company
official. We believe this notification
requirement serves as the registration
requirement and could be streamlined
through optional electronic reporting
with web-based public access or other
methods. We seek comment on potential
methodologies that would minimize
burden on operators, while providing
timely and useful information for
regulators and the public. We also
solicit comment on provisions for a
follow-up notification one or two days
before an impending completion via
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telephone or by electronic means, since
it is difficult to predict exactly when a
well will be ready for completion a
month in advance. However, we would
expect an owner or operator to provide
the follow-up notification only in cases
where the completion date was
expected to deviate from the original
date provided. We ask for suggestions
regarding how much advance
notification is needed and the most
effective method of providing sufficient
and accurate advance notification of
well completions.
2. Third Party Verification
To complement the annual
compliance certification required under
the proposed NSPS, we are considering
and seeking comment on the potential
use of third party verification to assure
compliance. Since the emission sources
in the oil and natural gas sector,
especially well completions, are widely
geographically dispersed (often in very
remote locations), compliance assurance
can be very difficult and burdensome
for state, local and tribal agencies and
EPA permitting staff, inspectors and
compliance officers. Additionally, we
believe that verification of the data
collection, compilation and calculations
by an independent and impartial third
party could facilitate the demonstration
of compliance for the public.
Verification of emissions data can also
be beneficial to owners and operators by
providing certainty of compliance
status.
As mentioned above, notification and
reporting requirements associated with
well completions are likely applications
for third party verification used in
tandem with the required annual
compliance certification. The third
party verification program could be
used in a variety of ways to ease
regulatory burden on the owners and
operators and to leverage compliance
assurance efforts of the EPA and state,
local and tribal agencies. The third party
agent could serve as a clearinghouse for
notifications, records and annual
compliance certifications submitted by
owners and operators. This would
provide online access to completion
information by regulatory agencies and
the public. Having notifications
submitted to the clearinghouse would
relieve state, local and tribal agencies of
the burden of receiving thousands of
paper or e-mail well completion
notifications each year, yet still provide
them quick access to the information.
Using a third party agent, it is possible
that notifications of well completions
could be submitted with an advance
period much less than 30 days that
could make a 2 day follow-up
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notification unnecessary. The
clearinghouse could also house
information on past completions and
copies of compliance certifications. We
seek comment on whether annual
reports for well completions would be
needed if a suitable third party
verification program was in place and
already housed that same information.
We also solicit comment on the range of
potential activities the third party
verification program could handle with
regard to well completions.
In this proposed action, there are also
provisions for applying third party
verification to the required electronic
reporting using the ERT (see section
V.C.3 above for a discussion of the ERT).
As stated above, all sources must use
the ERT to submit all performance test
reports (required in 40 CFR parts 60, 61
and 63) to the EPA. There is an option
in the ERT for state, local and tribal
agencies to review and verify that the
information submitted to the EPA is
truthful, accurate and complete. Third
party verifiers could be contractors or
other personnel familiar with oil and
natural gas exploration and production.
We are seeking comment on appropriate
third party reviewers and qualifications
and registration requirements under
such a program. We want to state clearly
here that third party verification would
not supersede or substitute for
inspections or audit of data and
information by state, local and tribal
agencies and the EPA.
Potential issues with third party
verification include costs incurred by
industry and approval of third party
verifiers. The cost of third party
verification would be borne by the
affected industries. We are seeking
comment on whether third party
verification paid for by industry would
result in impartial, accurate and
complete data information. The EPA,
working with state, local and tribal
agencies and industry, would expect to
develop guidance for third party
verifiers. We are seeking comment on
whether or not the EPA should approve
third party verifiers.
3. Electronic Reporting Using Existing
Mechanisms
The proposed 40 CFR part 60, subpart
OOOO and final Greenhouse Gas (GHG)
Mandatory Reporting Rule, 40 CFR part
98, subpart W, provide details on flare
and vented emission sources and how to
estimate their emissions. We solicit
comment on requiring sources to
electronically submit their emissions
data for the oil and gas rules proposed
here. The EPA’s Electronic Greenhouse
Gas Reporting Tool (e-GGRT) for 40 CFR
part 98, subpart W, while used to report
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emissions at the emissions source level
(e.g., well completions, well unloading,
compressors, gas plant leaks, etc.), will
aggregate emissions at the basin level for
e-reporting purposes. As a result, it may
be difficult to merge reporting under
NSPS subpart OOOO with GHG
Reporting Rule subpart W methane
reporting, especially if manual reporting
is used. However, since the operator
would have these emissions details at
the individual well level (because that
will be how they would develop their
basin-wide estimates), we do not believe
it would be a significant burden to
require owners or operators to report the
data they already have for subpart W in
an ERT for NSPS and NESHAP
compliance purposes. However, if the eGGRT is not structured to provide for
reporting of other pollutants besides
GHG (e.g., VOC and HAP), then there
may be some modification of the
database required to accommodate the
other pollutants.
4. Provisions for Encouraging Innovative
Technology
The oil and natural gas industry has
a long history of innovation in
developing new exploration and
production methods, along with
techniques to minimize product losses
and reduce adverse environmental
impacts. These efforts are often
undertaken with tremendous amounts
of research, including pilot applications
at operating facilities in the field.
Absent regulation, these developmental
activities, some of which ultimately are
not successful, can proceed without risk
of violation of any standards. However,
as more emission sources in this source
category are covered by regulation, as in
the case of the action being proposed
here, there likely will be situations
where innovation and development of
new control techniques potentially
could be stifled by risk of violation.
We believe it is important to facilitate,
not hinder, innovation and continued
development of new technology that can
result in enhanced environmental
performance of facilities and sources
affected by the EPA’s regulations.
However, any approaches to
accommodate technology development
must be designed and implemented in
accordance with the CAA and other
statutes. We seek comment on
approaches that may be suitable for
allowing temporary field testing of
technology in development. These
approaches could include not only
established procedures under the CAA
and its implementing regulations, but
new ways to apply or interpret these
provisions to avoid impeding
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environmentally responsible and legal.
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E. How does the NSPS relate to
permitting of sources?
1. How does this action affect permitting
requirements?
The proposed rules do not change the
Federal requirements for determining
whether oil and gas sources are major
sources for purposes of nonattainment
major New Source Review (NSR),
prevention of significant deterioration,
CAA title V, or HAP major sources
pursuant to CAA section 112.
Specifically, if an owner or operator is
not currently required to get a major
NSR or title V permit for oil and gas
sources, including well completions, it
would not be required to get a major
NSR or title V permit as a result of these
proposed standards. EPA-approved state
and local major source permitting
programs would not be affected. That is,
state and local agencies with EPAapproved programs will still make caseby-case major source determinations for
purposes of major NSR and title V,
relying on the regulatory criteria, as
explained in the McCarthy Memo.6
Consistent with the McCarthy Memo,
whether or not a permitting authority
should aggregate two or more pollutantemitting activities into a single major
stationary source for purposes of NSR
and title V remains a case-by-case
decision in which permitting authorities
retain the discretion to consider the
factors relevant to the specific
circumstances of the permitted
activities.
In addition, the proposed standards
would not change the requirements for
determining whether oil and gas sources
are subject to minor NSR. Nor would the
proposed standards affect existing EPAapproved state and local minor NSR
rules, as well as policies and practices
implementing those rules. Many state
and local agencies have already adopted
minor NSR permitting programs that
provide for control of emissions from
relatively small emission sources,
including various pieces of equipment
used in oil and gas fields. State and
local agencies would be able to continue
to use any EPA-approved General
Permits, Permits by Rule, and other
similar streamlining mechanisms to
permit oil and gas sources such as wells.
We recently promulgated the final
Tribal Minor NSR rules for use in
issuing minor issue permits on tribal
6 Withdrawal of Source Determinations for Oil
and Gas Industries, September 22, 2009. This memo
continues to articulate the Agency’s interpretation
for major NSR and title V permitting of oil and gas
sources.
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lands, where many oil and gas sources
are located.
The proposed standards will lead to
better control of and reduced emissions
from oil and gas production, gas
processing and transmission and
storage, including wells. In some
instances, we anticipate that complying
with the NSPS would reduce emissions
from these smaller sources to below the
minor source applicability thresholds.
In those cases, sources that would
otherwise have been subject to minor
NSR would not need to get minor NSR
permits as a result of being subject to
the NSPS. Accordingly, the number of
minor NSR permits, as well as the
Agency resources needed to issue them,
would be reduced.
We expect the emission reductions
achieved from the proposed standards
to significantly improve ozone
nonattainment problems in areas where
oil and gas production occurs. Strategies
for attaining and maintaining the
national ambient air quality standards
(NAAQS) are a function of SIP (or, in
some instances, Federal Implementation
Plans and Tribal Implementation Plans)
pursuant to CAA section 110. In
developing plans to attain and maintain
the NAAQS, EPA works with state, local
or Tribal agencies to account for growth
and develop overall control strategies
that address existing and expected
emissions. The reductions achieved by
the standards will make it easier for
state and local agencies to plan for and
to attain and maintain the ozone
NAAQS.
2. How does this action affect
applicability of CAA title V?
Under section 502(a) of the CAA, the
EPA may exempt one or more non-major
sources 7 subject to CAA section 111
(NSPS) standards from the requirements
of title V if the EPA finds that
compliance with such requirements is
‘‘impracticable, infeasible, or
unnecessarily burdensome’’ on such
sources. The EPA determine whether to
exempt a non-major source from title V
at the time we issue the relevant CAA
section 111 standards (40 CFR
70.3(b)(2)). We are proposing in this
action to exempt from the requirements
of title V non-major sources that would
be subject to the proposed NSPS for
well completions, pneumatic devices,
compressors, and/or storage vessels.
These non-major sources (hereinafter
referred to as the ‘‘oil and gas NSPS
non-major sources’’) would not be
required to obtain title V permits solely
7 CAA section 502(a) prohibits title V exemption
for any major source, which is defined in CAA
section 501(2) and 40 CFR 70.2.
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as a result of being subject to one or
more of the proposed NSPS identified
above (hereinafter referred to as the
‘‘proposed NSPS’’); however, if they
were otherwise required to obtain title
V permits, such requirement(s) would
not be affected by the proposed
exemption.
Consistent with the statute, the EPA
believes that compliance with title V
permitting is ‘‘unnecessarily
burdensome’’ for the oil and gas NSPS
non-major sources. The EPA’s inquiry
into whether this criterion was satisfied
is based primarily upon consideration of
the following four factors: (1) Whether
title V would result in significant
improvements to the compliance
requirements that we are proposing for
the oil and gas NSPS affected non-major
sources; (2) whether title V permitting
would impose a significant burden on
these non-major sources and whether
that burden would be aggravated by any
difficulty these sources may have in
obtaining assistance from permitting
agencies; (3) whether the costs of title V
permitting for these non-major sources
would be justified, taking into
consideration any potential gains in
compliance likely to occur for such
sources; and (4) whether there are
implementation and enforcement
programs in place that are sufficient to
assure compliance with the proposed
Oil and Natural Gas NSPS without
relying on title V permits. Not all of the
four factors must weigh in favor of an
exemption. See 70 FR 75320, 75323
(Title V Exemption Rule). Instead, the
factors are to be considered in
combination and the EPA determines
whether the factors, taken together,
support an exemption from title V for
the oil and gas non-major sources.
Additionally, consistent with the
guidance provided by the legislative
history of CAA section 502(a),8 we
considered whether exempting the Oil
and Natural Gas NSPS non-major
sources would adversely affect public
health, welfare or the environment. The
first factor is whether title V would
result in significant improvements to
the compliance requirements in the
proposed NSPS. A finding that title V
would not result in significant
improvements to the compliance
requirements in the proposed NSPS
would support a conclusion that title V
permitting is ‘‘unnecessary’’ for non8 The legislative history of section 502(a) suggests
that EPA should not grant title V exemptions where
doing so would adversely affect public health,
welfare or the environment. (See Chafee-Baucus
Statement of Senate Managers, Environment and
Natural Resources Policy Division 1990 CAA Leg.
Hist. 905, Compiled November 1993.)
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major sources subject to the Oil and
Natural Gas Production NSPS.
One way that title V may improve
compliance is by requiring monitoring
(including recordkeeping designed to
serve as monitoring) to assure
compliance with permit terms and
conditions reflecting the emission
limitations and control technology
requirements imposed in the standard.
See 40 CFR 70.6(c)(1) and 40 CFR
71.6(c)(1). The ‘‘periodic monitoring’’
provisions of 40 CFR 70.6(a)(3)(i)(B) and
40 CFR 71.6(a)(3)(i)(B) require new
monitoring to be added to the permit
when the underlying standard does not
already require ‘‘periodic testing or
instrumental or noninstrumental
monitoring (which may consist of
recordkeeping designed to serve as
monitoring).’’ In addition, title V
imposes a number of recordkeeping and
reporting requirements that may be
important for assuring compliance.
These include requirements for a
monitoring report at least every 6
months, prompt reports of deviations,
and an annual compliance certification.
See 40 CFR 70.6(a)(3) and 40 CFR
71.6(a)(3), 40 CFR 70.6(c)(1) and 40 CFR
71.6(c)(1), and 40 CFR 70.6(c)(5) and 40
CFR 71.6(c)(5). To determine whether
title V permits would add significant
compliance requirements to the
proposed NSPS, we compared the title
V monitoring, recordkeeping and
reporting requirements mentioned
above to those requirements proposed
for the Oil and Natural Gas NSPS
affected facilities.
For wellhead affected facilities (well
completions), the proposed NSPS would
require (1) 30-day advance notification
of each well completion to be
performed; (2) noninstrumental
monitoring, which is achieved through
documentation and recordkeeping of
procedures followed during each
completion, including total duration of
the completion event, amount of time
gas is recovered using reduced emission
completion techniques, amount of time
gas is combusted, amount of time gas is
vented to the atmosphere and
justification for periods when gas is
combusted or vented rather than being
recovered; (3) reports of cases where
well completions were not performed in
compliance with the NSPS; (4) annual
reports that document all completions
performed during the reporting period
(a single report may be used to
document multiple completions
conducted by a single owner or operator
during the reporting period); and (5)
annual compliance certifications
submitted with the annual report.
These monitoring, recordkeeping and
reporting requirements in the proposed
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NSPS for well completions are sufficient
to ensure that the Administrator, the
state, local and tribal agencies and the
public are aware of completion events
before they are performed to provide
opportunity for inspection. Sufficient
documentation would also be required
to be retained and reported to the
Administrator to assure compliance
with the NSPS for well completions. In
light of the above, we have determined
that additional monitoring through title
V is not needed and that the monitoring,
recordkeeping and reporting
requirements described above are
sufficient to assure compliance with the
proposed requirements for well
completions.
With respect to storage vessels, the
proposed NSPS would require 95percent control of VOC emissions. The
proposed standard could be met by a
vapor recovery unit, a flare control
device or other control device. The
proposed NSPS would require an initial
performance test followed by
continuous monitoring of the control
device used to meet the 95-percent
control. We believe that the monitoring
requirements described above are
sufficient to assure compliance with the
proposed NSPS for storage vessels and,
therefore, additional monitoring through
title V is not needed. In addition to
monitoring, as part of the first factor, we
have considered the extent to which
title V could potentially enhance
compliance through recordkeeping or
reporting requirements. The proposed
NSPS would require (1) construction,
startup and modification notifications,
as required by 40 CFR 60.7(a); and (2)
annual reports that identify all storage
vessel affected facilities of the owner or
operator and documentation of periods
of non-compliance. The proposed NSPS
would also require records documenting
liquid throughput of condensate or
crude oil (to determine applicability), as
provided for in the proposed rule.
Recordkeeping would also include
records of the initial performance test
and other information that document
compliance with applicable emission
limit. These requirements are similar to
those under title V. In light of the above,
we believe that the monitoring,
recordkeeping and reporting
requirements described above are
sufficient to assure compliance with the
proposed NSPS for storage vessels.
For pneumatic controllers, centrifugal
compressors and reciprocating
compressors, the proposed NSPS are in
the form of operational, work practice or
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equipment standards.9 For each of these
affected facilities, the proposed NSPS
would require: (1) Construction, startup
and modification notifications, as
required by 40 CFR 60.7(a); (2) annual
reports; (3) for each pneumatic
controller installed or modified
(including replacement of an existing
controller), records of location and date
of installation and documentation that
each controller emits no more than the
applicable emission limit or is exempt
(with rationale for the exemption); (4)
for each centrifugal compressor, records
that document that each new or
modified compressor is equipped with
dry seals; and (5) for each new or
modified reciprocating compressor,
records of rod packing replacement,
including elapsed operating hours since
the previous rod packing installation.
For these other affected sources
described above, the proposed NSPS
provide monitoring in the form of
recordkeeping (as described above) that
would assure compliance with the
proposed operational, work practice or
equipment standards. Monitoring by
means other than recordkeeping would
not be practical or appropriate for these
standards. Records are required to
ensure that these standards and
practices are followed. We believe that
the monitoring, recordkeeping and
reporting requirements described above
are sufficient to assure compliance with
the proposed NSPS for pneumatic
controllers and compressors.
We acknowledge that title V might
provide for additional compliance
requirements for these non-major
sources, but we have determined, as
explained above, that the monitoring,
recordkeeping and reporting
requirements in this proposed NSPS are
sufficient to assure compliance with the
proposed standards for well
completions, storage vessels, pneumatic
controllers and compressors. Further,
given the nature of some of the
operations and the types of the
requirements at issue, the additional
compliance requirements under title V
would not significantly improve the
compliance requirements in this
proposed NSPS. For instance, well
completions occur over a very short
period (generally 3 to 10 days), and the
proposed NSPS for pneumatic
controllers and centrifugal compressors
can be met by simply installing the
equipment that meet the proposed
emission limit; therefore, the semiannual reporting requirement under title
V would not improve compliance with
9 The proposed numeric standards for pneumatic
controllers reflect the use of specific equipment
(either non-gas driven device or low-bleed device).
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these proposed NSPS and, in fact, may
seem inappropriate for such short term
operations.
For the reasons stated above, we
believe that title V would not result in
significant improvements to the
compliance requirements that are
provided in this proposed NSPS.
Therefore, the first factor supports a
conclusion that title V permitting is
‘‘unnecessary’’ for non-major sources
subject to the Oil and Natural Gas NSPS.
The second factor we considered is
whether title V permitting would
impose significant burdens on the oil
and natural gas NSPS non-major sources
and whether that burden would be
aggravated by any difficulty these
sources may have in obtaining
assistance from permitting agencies.
Subjecting any source to title V
permitting imposes certain burdens and
costs that do not exist outside of the title
V program. EPA estimated that the
average cost of obtaining and complying
with a title V permit was $65,700 per
source for a 5-year permit period,
including fees. See Information
Collection Request (ICR) for Part 70
Operating Permit Regulations, January
2007, EPA ICR Number 1587.07. EPA
does not have specific estimates for the
burdens and costs of permitting the oil
and gas NSPS non-major sources;
however, there are certain activities
associated with the 40 CFR part 70 and
40 CFR part 71 rules. These activities
are mandatory and impose burdens on
any facility subject to title V. They
include reading and understanding
permit program regulations; obtaining
and understanding permit application
forms; answering follow-up questions
from permitting authorities after the
application is submitted; reviewing and
understanding the permit; collecting
records; preparing and submitting
monitoring reports; preparing and
submitting prompt deviation reports, as
defined by the state, which may include
a combination of written, verbal and
other communication methods;
collecting information, preparing and
submitting the annual compliance
certification; preparing applications for
permit revisions every 5 years; and, as
needed, preparing and submitting
applications for permit revisions. In
addition, although not required by the
permit rules, many sources obtain the
contractual services of consultants to
help them understand and meet the
permitting program’s requirements. The
ICR for 40 CFR part 70 provides
additional information on the overall
burdens and costs, as well as the
relative burdens of each activity
described here. Also, for a more
comprehensive list of requirements
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imposed on 40 CFR part 70 sources
(hence, burden on sources), see the
requirements of 40 CFR 70.3, 40 CFR
70.5, 40 CFR 70.6, and 40 CFR 70.7. The
activities described above, which are
quite extensive and time consuming,
would be a significant burden on the
non-major sources that would be subject
to the proposed NSPS, in particular for
well completion and/or pneumatic
devices, considering the short duration
of a well completion and the one time
equipment installation of a pneumatic
controller for meeting the proposed
NSPS. Furthermore, some of the nonmajor sources that would be subject to
the proposed NSPS may be small
entities that may lack the technical
resources and, therefore, need assistance
from the permitting authorities to
comply with the title V permitting
requirements. Based on our projections,
over 20,000 well completions (for both
new hydraulically fractured gas wells
and for existing gas wells that are
subsequently fractured or re-fractured)
will be performed each year. For
pneumatic controller affected facilities,
we estimate that approximately 14,000
new controllers would be subject to the
NSPS each year. Our estimated numbers
of affected facilities that would be
subject to the proposed NSPS for storage
vessels and compressors are smaller
(around 500 compressors and 300
storage vessels). Although we do not
know the total number of non-major
sources that would be subject to the
proposed NSPS, based on the estimated
numbers of affected facilities, we
anticipate a significant increase in the
number of permit applications that
permitting authorities would have to
process each year. This significant
burden on the permitting authorities
raises a concern with the potential
difficulty or delay that the small entities
may face in obtaining sufficient
assistance from the permitting
authorities.
The third factor we considered is
whether the costs of title V permitting
for these area sources would be
justified, taking into consideration any
potential gains in compliance likely to
occur for such sources. We concluded,
in considering the first factor, that the
monitoring, recordkeeping and
reporting requirements in this proposed
NSPS assure compliance with the
proposed standards, that title V would
not result in significant improvement to
these compliance requirements and,
that, in some instances, certain title V
compliance requirements may not be
appropriate. In addition, as discussed
above in our consideration of the second
factor, we have concerns with the
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potential burdens that title V may
impose on these sources. In addition,
below in our consideration of the fourth
factor, we find that there are adequate
implementation and enforcement
programs in place to assure compliance
with the proposed NSPS. In light of the
above, we find that the costs of title V
permitting are not justified for the
sources we propose to exempt.
Accordingly, the third factor supports
title V exemption for the oil and gas
NSPS non-major sources.
The fourth factor we considered is
whether there are implementation and
enforcement programs in place that are
sufficient to assure compliance with the
proposed NSPS for oil and gas sources
without relying on title V permits. The
CAA provides States the opportunity to
take delegation of NSPS. Before the EPA
will delegate the program, the EPA will
evaluate the state programs to ensure
that states have adequate capability to
enforce the CAA section 111 regulations
and provide assurances that they will
enforce the NSPS. In addition, EPA
retains authority to enforce this NSPS
anytime under CAA sections 111, 113
and 114. Accordingly, we can enforce
the monitoring, recordkeeping and
reporting requirements, which, as
discussed under the first factor, are
adequate to assure compliance with this
NSPS. Also, states and the EPA often
conduct voluntary compliance
assistance, outreach and education
programs (compliance assistance
programs), which are not required by
statute. We determined that these
additional programs will supplement
and enhance the success of compliance
with these proposed standards. We
believe that the statutory requirements
for implementation and enforcement of
this NSPS by the delegated states, the
EPA and the additional assistance
programs described above together are
sufficient to assure compliance with
these proposed standards without
relying on title V permitting.
Our balance of the four factors
strongly supports a finding that title V
is unnecessarily burdensome for the oil
and gas non-major sources. While title
V might add additional compliance
requirements if imposed, we believe
that there would not be significant
improvements to the compliance
requirements in this proposed rule
because the proposed rule requirements
are specifically designed to assure
compliance with the proposed NSPS
and, as explained above, some of the
title V requirements may not be
appropriate for certain operations and/
or proposed standards. We are also
concerned with the potential burden
that title V may impose on some of these
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sources. In light of little or no potential
gain in compliance if title V were
required, we do not believe that the
costs of title V permitting is justified in
this case. Finally, there are adequate
implementation and enforcement
programs in place to assure compliance
with these proposed standards. Thus,
we propose that title V permitting is
‘‘unnecessarily burdensome’’ for the oil
and gas non-major sources.
In addition to evaluating whether
compliance with title V requirements is
‘‘unnecessarily burdensome,’’ EPA also
considered, consistent with guidance
provided by the legislative history of
section 502(a), whether exempting oil
and gas NSPS non-major sources from
title V requirements would adversely
affect public health, welfare or the
environment. The title V permit
program does not impose new
substantive air quality control
requirements on sources, but instead
requires that certain procedural
measures be followed, particularly with
respect to determining compliance with
applicable requirements. As stated in
our consideration of factor one, title V
would not lead to significant
improvements in the compliance
requirements for the proposed NSPS.
For the reason stated above, we believe
that exempting these non-major sources
from title V permitting requirements
would not adversely affect public
health, welfare or the environment.
On the contrary, we are concerned
that requiring title V in this case could
potentially adversely affect public
health, welfare or the environment. As
mentioned above, we anticipate a
significant increase in the number of
permit applications that permitting
authorities would have to process each
year. Depending on the number of nonmajor sources that would be subject to
this rule, requiring permits for those
sources, at least in the first few years of
implementation, could potentially
adversely affect public health, welfare
or the environment by shifting state
agencies resources away from assuring
compliance for major sources (which
cannot be exempt from title V) to
issuing new permits for these non-major
sources, potentially reducing overall air
program effectiveness.
Based on the above analysis, we
conclude that title V permitting would
be ‘‘unnecessarily burdensome’’ for oil
and gas NSPS non-major sources. We
are, therefore, proposing that these nonmajor sources be exempt from title V
permitting requirements.
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VI. Rationale for Proposed Action for
NSPS
A. What did we evaluate relative to
NSPS?
As noted above, there are two existing
NSPS that address emissions from the
Oil and Natural Gas source category.
These NSPS are relatively narrow in
scope, as they address emissions only at
natural gas processing plants.
Specifically, 40 CFR part 60, subpart
KKK addresses VOC emissions from
leaking equipment at onshore natural
gas processing plants and 40 CFR part
60, subpart LLL addresses SO2
emissions from natural gas processing
plants.
CAA section 111(b)(1)(B) requires the
EPA to review and revise, if appropriate,
NSPS standards. Accordingly, we
evaluated whether the existing NSPS
reflect the BSER for the emission
sources that they address. This review
was conducted by examining currently
used, new and emerging control systems
and assessing whether they represent
advances in emission reduction
techniques from those upon which the
existing NSPS are based, including
advances in LDAR approaches and SO2
control at natural gas processing plants.
For each new or emerging control
option identified, we then evaluated
emission reductions, costs, energy
requirements and non-air quality
impacts, such as solid waste generation.
In this package, we have also
evaluated whether there were additional
pollutants emitted by facilities in the
Oil and Natural Gas source category that
warrant regulation and for which we
have adequate information to
promulgate standards of performance.
Finally, we have identified additional
processes in the Oil and Natural Gas
source category for which it may be
appropriate to develop performance
standards. This would include
processes that emit the currently
regulated pollutants, VOC and SO2, as
well as any additional pollutants for
which we determined regulation to be
appropriate.
B. What are the results of our
evaluations and proposed actions
relative to NSPS?
1. Do the existing NSPS reflect the BSER
for sources covered?
Consistent with our obligations under
CAA section 111(b), we evaluated
whether the control options reflected in
the current NSPS for the Oil and Natural
Gas source category still represent
BSER. To evaluate the BSER options for
equipment leaks, we reviewed EPA’s
current LDAR programs, the Reasonably
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Available Control Technology (RACT)/
Best Available Control Technology
(BACT)/Lowest Achievable Emission
Rate (LAER) Clearinghouse (RBLC)
database, and emerging technologies
that have been identified by partners in
the Natural Gas STAR program.
The current NSPS for equipment leaks
of VOC at natural gas processing plants
(40 CFR part 60, subpart KKK) requires
compliance with specific provisions of
40 CFR part 60, subpart VV, which is a
LDAR program, based on the use of EPA
Method 21 to identify equipment leaks.
In addition to the subpart VV
requirements, we reviewed the LDAR
requirements in 40 CFR part 60, subpart
VVa. This LDAR program is considered
to be more stringent than the subpart VV
requirements, because it has lower
component leak threshold definitions
and more frequent monitoring, in
comparison to the subpart VV program.
Furthermore, subpart VVa requires
monitoring of connectors, while subpart
VV does not. We also reviewed options
based on optical gas imaging.
As mentioned above, the currently
required LDAR program for natural gas
processing plants (40 CFR part 60,
subpart KKK) is based on EPA Method
21, which requires the use of an organic
vapor analyzer to monitor components
and to measure the concentration of the
emissions in identifying leaks. We
recognize that there have been
advancements in the use of optical gas
imaging to detect leaks from these same
types of components. These instruments
do not yet provide a direct measure of
leak concentrations. The instruments
instead provide a measure of a leak
relative to an instrument specific
calibration point. Since the
promulgation of 40 CFR part 60, subpart
KKK (which requires Method 21 leak
measurement monthly), the EPA has
updated the 40 CFR part 60 General
Provisions to allow the use of advanced
leak detection tools, such as optical gas
imaging and ultrasound equipment as
an alternative to the LDAR protocol
based on Method 21 leak measurements
(see 40 CFR 60.18(g)). The alternative
work practice allowing use of these
advanced technologies includes a
provision for conducting a Method 21based LDAR check of the regulated
equipment annually to verify good
performance.
In our review, we evaluated 4 options
in considering BSER for VOC equipment
leaks at natural gas processing plants.
One option we evaluated consists of
changing from a 40 CFR part 60, subpart
VV-level program, which is what 40
CFR part 60, subpart KKK currently
requires, to a 40 CFR part 60, subpart
VVa program, which applies to new
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synthetic organic chemical plants after
2006. Subpart VVa lowers the leak
definition for valves from 10,000 parts
per million (ppm) to 500 ppm, and
requires the monitoring of connectors.
In our analysis of these impacts, we
estimated that, for a typical natural gas
processing plant, the incremental cost
effectiveness of changing from the
current subpart VV-level program to a
subpart VVa-level program using
Method 21 is $3,352 per ton of VOC
reduction.
In evaluating 40 CFR part 60, subpart
VVa-level LDAR at processing plants,
we also analyzed separately the
individual types of components (valves,
connectors, pressure relief devices and
open-ended lines) to determine cost
effectiveness for individual
components. Detailed discussions of
these component-by-component
analyses are included in the TSD in the
docket. Cost effectiveness ranged from
$144 per ton of VOC (for valves) to
$4,360 per ton of VOC (for connectors),
with no change in requirements for
pressure relief devices and open-ended
lines.
Another option we evaluated for gas
processing plants was the use of optical
gas imaging combined with an annual
EPA Method 21 check (i.e., the
alternative work practice for monitoring
equipment for leaks at 40 CFR 60.18(g)).
We had previously determined that the
VOC reduction achieved by this
combination of optical gas imaging and
Method 21 would be equivalent to
reductions achieved by the 40 CFR part
60, subpart VVa-level program. Based
on that emission reduction level, we
determined the cost effectiveness of this
option to be $6,462 per ton of VOC
reduction. This analysis is based on the
facility purchasing an optical gas
imaging system costing $85,000.
However, we identified at least one
manufacturer who rents the optical gas
imaging systems. That manufacturer
rents the optical gas imaging system for
$3,950 per week. Using this rental cost
in place of the purchase cost, the VOC
cost effectiveness of the monthly optical
gas imaging combined with annual
Method 21 checks is $4,638 per ton of
VOC reduction.10 A third option we
evaluated consisted of monthly optical
gas imaging without an annual Method
21 check. We estimated the annual cost
of the monthly optical gas imaging
LDAR program to be $76,581, based on
camera purchase, or $51,999, based on
camera rental. However, because we
10 Because optical gas imaging is used to view
several pieces of equipment at a facility at once to
survey for leaks, options involving imaging are not
amenable to a component by component analysis.
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were unable to estimate the VOC
emissions achieved by an optical
imaging program alone, we were unable
to estimate the cost effectiveness of this
option.
Finally, we evaluated a fourth option
similar to the third option, except that
the optical gas imaging would be
performed annually rather than
monthly. For this option, we estimated
the annual cost to be $43,851, based on
camera purchase, or $18,479, based on
camera rental.
We request comment on the
applicability of an LDAR program based
solely on the use of optical gas imaging.
Of most use to us would be information
on the effectiveness of this and,
potentially, other advanced
measurement technologies, to detect
and repair small leaks on the same order
or smaller than specified in the 40 CFR
part 60, subpart VVa equipment leak
requirements and the effects of
increased frequency of and associated
leak detection, recording and repair
practices.
Because we could not estimate the
cost effectiveness of options 3 and 4, we
could not identify either of these two
options as BSER for reducing VOC leaks
at gas processing plants. Because
options 1 and 2 have achieved
equivalent VOC reduction and are both
cost effective, we believe that both
options 1 and 2 reflect BSER for LDAR
for natural gas processing plants. As
mentioned above, option 1 is the LDAR
in 40 CFR part 60, subpart VVa and
option 2 is the alternative work practice
at 40 CFR 60.18(g) and is already
available to use as an alternative to
subpart VVa LDAR. Therefore, we
propose that the NSPS for equipment
leaks of VOC at gas processing plants be
revised to require compliance with the
subpart VVa equipment leak
requirements.
For 40 CFR part 60, subpart LLL, we
reviewed control systems for SO2
emissions from sweetening units located
at natural gas processing plants,
including those followed by a sulfur
recovery unit. Subpart LLL provides
specific standards for SO2 emission
reduction efficiency, on the basis of
sulfur feed rate and the sulfur content
of the natural gas.
According to available literature, the
most widely used process for converting
H2S in acid gases (i.e., H2S and CO2)
separated from natural gas by a
sweetening process (such as amine
treating) into elemental sulfur is the
Claus process. Sulfur recovery
efficiencies are higher with higher
concentrations of H2S in the feed stream
due to the thermodynamic equilibrium
limitation of the Claus process. The
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Claus sulfur recovery unit produces
elemental sulfur from H2S in a series of
catalytic stages, recovering up to 97percent recovery of the sulfur from the
acid gas from the sweetening process.
Further, sulfur recovery is accomplished
by making process modifications or by
employing a tail gas treatment process
to convert the unconverted sulfur
compounds from the Claus unit.
We evaluated process modifications
and tail gas treatment options when we
proposed 40 CFR part 60, subpart LLL.
49 FR 2656, 2659–2660 (1984). As we
explained in the preamble to the
proposed subpart LLL, control through
sulfur recovery with tail gas treatment
may not always be cost effective,
depending on sulfur feed rate and inlet
H2S concentrations. Therefore, other
methods of increasing sulfur recovery
via process modifications were
evaluated. As shown in the original
evaluation, the performance capabilities
and costs of each of these technologies
are highly dependent on the ratio of H2S
and CO2 in the gas stream and the total
quantity of sulfur in the gas stream
being treated. The most effective means
of control was selected as BSER for the
different stream characteristics. As a
result, separate emissions limitations
were developed in the form of equations
that calculate the required initial and
continuous emission reduction
efficiency for each plant. The equations
were based on the design performance
capabilities of the technologies selected
as BSER relative to the gas stream
characteristics. 49 FR 2656, 2663–2664
(1984). The emission limit for sulfur
feed rates at or below 5 long tons per
day, regardless of H2S content, was 79
percent. For facilities with sulfur feed
rates above 5 long tons per day, the
emission limits ranged from 79 percent
at an H2S content below 10 percent to
99.8 percent for H2S contents at or
above 50 percent.
To review these emission limitations,
we performed a search of the RBLC
database and state regulations. No state
regulations identified had emission
limitations more stringent than 40 CFR
part 60, subpart LLL. However, the
RBLC database search identified two
entries with SO2 emission reductions of
99.9 percent. One entry is for a facility
in Bakersfield, California, with a 90 long
ton per day sulfur recovery unit
followed by an amine-based tail-gas
treating unit. The second entry is for a
facility in Coden, Alabama, with a
sulfur recovery unit with a sulfur feed
rate of 280 long tons per day, followed
by selective catalytic reduction and a
tail gas incinerator. However, neither of
these entries contained information
regarding the H2S contents of the feed
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stream. Because the sulfur recovery
efficiency of these large sized plants was
greater than 99.8 percent, we
reevaluated the original data. Based on
the available cost information, it
appears that a 99.9-percent efficiency is
cost effective for facilities with a sulfur
feed rate greater than 5 long tons per
day and H2S content equal to or greater
than 50 percent. Based on our review,
we are proposing that the maximum
initial and continuous efficiency for
facilities with a sulfur feed rate greater
than 5 long tons per day and an H2S
content equal to or greater than 50
percent be raised to 99.9 percent. We are
not proposing to make changes to the
equations.
Our search of the RBLC database did
not uncover information regarding costs
and achievable emission reductions to
suggest that the emission limitations for
facilities with a sulfur feed rate less than
5 long tons per day or H2S content less
than 50 percent should be modified.
Therefore, we are not proposing any
changes to the emissions limitations for
facilities with sulfur feed rate and H2S
content less than 5 long tons per day
and 50 percent, respectively.
2. What pollutants are being evaluated
in this Oil and Natural Gas NSPS
package?
The two current NSPS for the Oil and
Natural Gas source category address
emissions of VOC and SO2. In addition
to these pollutants, sources in this
source category also emit a variety of
other pollutants, most notably, air
toxics. As discussed elsewhere in this
notice, there are NESHAP that address
air toxics from the oil and natural gas
sector.
In addition, processes in the Oil and
Natural Gas source category emit
significant amounts of methane. The
1990–2009 U.S. GHG Inventory
estimates 2009 methane emissions from
Petroleum and Natural Gas Systems (not
including petroleum refineries) to be
251.55 MMtCO2e (million metric tons of
CO2-equivalents (CO2e)).11 The
emissions estimated from well
completions and recompletions exclude
a significant number of wells completed
in tight sand plays, such as the
Marcellus, due to availability of data
when the 2009 Inventory was
developed. The estimate in this
proposal includes an adjustment for
tight sand plays (being considered as a
planned improvement in development
of the 2010 Inventory). This adjustment
11 U.S. EPA. Inventory of U.S. Greenhouse Gas
Inventory and Sinks. 1990–2009. https://
www.epa.gov/climatechange/emissions/
downloads10/US-GHG-Inventory2010_ExecutiveSummary.pdf.
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would increase the 2009 Inventory
estimate by 76.74 MMtCO2e. The total
methane emissions from Petroleum and
Natural Gas Systems, based on the 2009
Inventory, adjusted for tight sand plays
and the Marcellus, is 328.29 MMtCO2e.
Although this proposed rule does not
include standards for regulating the
GHG emissions discussed above, we
continue to assess these significant
emissions and evaluate appropriate
actions for addressing these concerns.
Because many of the proposed
requirements for control of VOC
emissions also control methane
emissions as a co-benefit, the proposed
VOC standards would also achieve
significant reduction of methane
emissions.
Significant emissions of oxides of
nitrogen (NOX) also occur at oil and
natural gas sites due to the combustion
of natural gas in reciprocating engines
and combustion turbines used to drive
the compressors that move natural gas
through the system, and from
combustion of natural gas in heaters and
boilers. While these engines, turbines,
heaters and boilers are co-located with
processes in the oil and natural gas
sector, they are not in the Oil and
Natural Gas source category and are not
being addressed in this action. The NOX
emissions from engines and turbines are
covered by the Standards of
Performance for Stationary Spark
Internal Combustion Engines (40 CFR
part 60, subpart JJJJ) and Standards of
Performance for Stationary Combustion
Turbines (40 CFR part 60, subpart
KKKK), respectively.
An additional source of NOX
emissions would be pit flaring of VOC
emissions from well completions during
periods where REC is not feasible, as
would be required under our proposed
operational standards for wellhead
affected facilities. As discussed below in
section VI.B.4 (well completion), pit
flaring is the only way we identified of
controlling VOC emissions during these
periods. Because there is no way of
directly measuring the NOX produced,
nor is there any way of applying
controls other than minimizing flaring,
we propose to allow flaring only when
REC is not feasible. We have included
our estimates of NOX formation from pit
flaring in our discussion of secondary
impacts in section VI.B.4.
3. What emission sources are being
evaluated in this Oil and Natural Gas
NSPS package?
The current NSPS only cover
emissions of VOC and SO2 from one
type of facility in the oil and natural gas
sector, which is the natural gas
processing plant. This is the only type
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of facility in the Oil and Natural Gas
source category where we would expect
SO2 to be emitted directly, although H2S
contained in sour gas, when oxidized in
the atmosphere or combusted in boilers
and heaters in the field, forms SO2 as a
product of oxidation. These field boilers
and heaters are not part of the Oil and
Natural Gas source category and are
generally too small to be regulated by
the NSPS covering boilers (i.e., they
have a heat input of less than 10 million
British Thermal Units per hour).
However, we may consider addressing
them as part of a future sector-based
strategy for the oil and natural gas
sector.
In addition to VOC emissions from
gas processing plants, there are
numerous sources of VOC throughout
the oil and natural gas sector that are
not addressed by the current NSPS. As
explained above in section V.A,
pursuant to CAA section 111(b), to the
extent necessary, we are modifying the
listed category to include all segments
of the oil and natural gas industry for
regulation. We are also proposing VOC
standards to cover additional processes
at oil and natural gas operations. These
include NSPS for VOC from gas well
completions, pneumatic controllers,
compressors and storage vessels.
We believe that produced water
ponds are also a potentially significant
source of emissions, but we have only
limited information. We, therefore,
solicit comments on produced water
ponds, particularly in the following
subject areas:
(a) We are requesting comments
pertaining to methods for calculating
emissions. The State of Colorado
currently uses a mass balance that
assumes 100 percent of the VOC content
is emitted to the atmosphere. Water9, an
air emissions model, is another option
that has some limitations, including
poor methanol estimation.
(b) We are requesting additional
information on typical VOC content in
produced water and any available
chemical analyses, including data that
could help clarify seasonal variations or
differences among gas fields.
Additionally, we request data that
increase our understanding of how
changing process variables or age of
wells affect produced water output and
VOC content.
(c) We solicit information on the size
and throughput capacity of typical
evaporation pond facilities and request
suggestions on parameters that could be
used to define affected facilities or
affected sources. We also seek
information on impacts of smaller
evaporation pits that are co-located with
drilling operations, whether those
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warrant control and, if so, how controls
should be developed.
(d) An important factor is cost of
emission reduction technologies,
including recovery credits or cost
savings realized from recovered salable
product. We are seeking information on
these considerations as well.
(e) We are also seeking information on
any limitations for emission reduction
technologies such as availability of
electricity, waste generation and
disposal and throughput and
concentration constraints.
(f) Finally, we solicit information on
separator technologies that are able to
improve the oil-water separation
efficiency.
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4. What are the rationales for the
proposed NSPS?
We have provided below our
rationales for the proposed BSER
determinations and performance
standards for a number of VOC emission
sources in the Oil and Natural Gas
source category that are not covered by
the existing NSPS. Our general process
for evaluating systems of emission
reduction for the emission sources
discussed below included: (1)
Identification of available control
measures; (2) evaluation of these
measures to determine emission
reductions achieved, associated costs,
nonair environmental impacts, energy
impacts and any limitations to their
application; and (3) selection of the
control techniques that represent BSER
based on the information we
considered.
We identified the control options
discussed in this package through our
review of relevant state and local
requirements and mitigation measures
developed and reported by the EPA’s
Natural Gas STAR program. The EPA’s
Natural Gas STAR program has worked
with industry partners since 1993 to
identify cost effective measures to
reduce emissions of methane and other
pollutants from natural gas operations.
We relied heavily on this wealth of
information in conducting this review.
We also identified state regulations,
primarily in Colorado and Wyoming,
which require mitigation measures for
some emission sources in the Oil and
Natural Gas source category.
a. NSPS for Well Completions
Well completion activities are a
significant source of VOC emissions,
which occur when natural gas and nonmethane hydrocarbons are vented to the
atmosphere during flowback of a
hydraulically fractured gas well.
Flowback emissions are short-term in
nature and occur over a period of
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several days following fracturing of a
new well or refracturing of an existing
well. Well completions include multiple
steps after the well bore hole has
reached the target depth. These steps
include inserting and cementing-in well
casing, perforating the casing at one or
more producing horizons, and often
hydraulically fracturing one or more
zones in the reservoir to stimulate
production. Well recompletions may
also include hydraulic fracturing.
Hydraulic fracturing is one technique
for improving gas production where the
reservoir rock is fractured with very
high pressure fluid, typically water
emulsion with a proppant (generally
sand) that ‘‘props open’’ the fractures
after fluid pressure is reduced.
Emissions are a result of the backflow of
the fracture fluids and reservoir gas at
high volume and velocity necessary to
lift excess proppant and fluids to the
surface. This multi-phase mixture is
often directed to a surface
impoundment where natural gas and
VOC vapors escape to the atmosphere
during the collection of water, sand and
hydrocarbon liquids. As the fracture
fluids are depleted, the backflow
eventually contains more volume of
natural gas from the formation. Wells
that are fractured generally have great
amounts of emissions because of the
extended length of the flowback period
required to purge the well of the fluids
and sand that are associated with the
fracturing operation. Along with the
fluids and sand from the fracturing
operation, the 3- to 10-day flowback
period also results in emissions of
natural gas and VOC that would not
occur in large quantities at oil wells or
at natural gas wells that are not
fractured. Thus, we estimate that gas
well completions involving hydraulic
fracturing vent substantially more VOC,
approximately 200 times more, than
completions not involving hydraulic
fracturing. Specifically, we estimate that
uncontrolled well completion emissions
for a hydraulically fractured gas well are
approximately 23 tons of VOC, where
emissions for a conventional gas well
completion are around 0.12 tons VOC.
These estimates are explained in detail
in the TSD available in the docket.
Based on our review, we believe that
emissions from recompletions of
previously completed wells that are
fractured or refractured to stimulate
production or to begin production from
a new production horizon are of similar
magnitude and composition as
emissions from completions of new
wells that have been hydraulically
fractured.
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EPA has based the NSPS impacts
analysis on best available emission data.
However, we recognize that there is
uncertainty associated with our
estimates. For both new completions
and recompletions, there are a variety of
factors that will determine the length of
the flowback period and actual volume
of emissions such as the number of
zones, depth, pressure of the reservoir,
gas composition, etc. This variability
means there will be some wells which
emit more than the estimated emission
factor and some wells that emit less.
During our review, we examined
information from the Natural Gas STAR
program and the Colorado and
Wyoming state rules covering well
completions. We identified two
subcategories of fractured gas wells: (1)
Non-exploratory and non-delineation
wells; and (2) exploratory and
delineation wells. An exploratory well
is the first well drilled to determine the
presence of a producing reservoir and
the well’s commercial viability. A
delineation well is a well drilled to
determine the boundary of a field or
producing reservoir. Because
exploratory and delineation wells are
generally isolated from existing
producing wells, there are no gathering
lines available for collection of gas
recovered during completion
operations. In contrast, non-exploratory
and non-delineation wells are located
where existing, producing wells are
connected to gathering lines and are,
therefore, able to be connected to a
gathering line to collect recovered
salable natural gas product that would
otherwise be vented to the atmosphere
or combusted.
For subcategory 1, we identified
‘‘green’’ completion, which we refer to
as REC, as an option for reducing VOC
emissions during well completions. REC
are performed by separating the
flowback water, sand, hydrocarbon
condensate and natural gas to reduce
the portion of natural gas and VOC
vented to the atmosphere, while
maximizing recovery of salable natural
gas and VOC condensate. In some cases,
for a portion of the completion
operation, such as when CO2 or nitrogen
is injected with the fracture water,
initial gas produced is not of suitable
quality to introduce into the gathering
line due to CO2 or nitrogen content or
other undesirable characteristic. In such
cases, for a portion of the flowback
period, gas cannot be recovered, but
must be either vented or combusted. In
practice, REC are often combined with
combustion to minimize the amount of
gas and condensate being vented. This
combustion process is rather crude,
consisting of a horizontal pipe
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downstream of the REC equipment,
fitted with a continuous ignition source
and discharging over a pit near the
wellhead. Because of the nature of the
flowback (i.e., with periods of water,
condensate, and gas in slug flow),
conveying the entire portion of this
stream to a traditional flare control
device or other control device, such as
a vapor recovery unit, is not feasible.
These control devices are not designed
to accommodate the multiphase flow
consisting of water, sand and
hydrocarbon liquids, along with the gas
and vapor being controlled. Although
‘‘pit flaring’’ does not employ a
traditional flare control device, and is
not capable of being tested or monitored
for efficiency due to the multiphase slug
flow and intermittent nature of the
discharge of gas, water and sand over
the pit, it does provide a means of
minimizing vented gas and is preferable
to venting. Because of the rather large
exposed flame, open pit flaring can
present a fire hazard or other
undesirable impacts in some situations
(e.g., dry, windy conditions, proximity
to residences, etc.). As a result, we are
aware that owners and operators may
not be able to pit flare unrecoverable gas
safely in every case. In some cases, pit
flaring may be prohibited by local
ordinance.
Equipment required to conduct REC
may include tankage, special gas-liquidsand separator traps and gas
dehydration. Equipment costs
associated with REC will vary from well
to well. Typical well completions last
between 3 and 10 days and costs of
performing REC are projected to be
between $700 and $6,500 per day,
including a cost of approximately
$3,523 per completion event for the pit
flaring equipment. However, there are
savings associated with the use of REC
because the gas recovered can be
incorporated into the production stream
and sold. In fact, we estimate that REC
will result in an overall net cost savings
in many cases.
The emission reductions for a
hydraulically fractured well are
estimated to be around 22 tons of VOC.
Based on an average incremental cost of
$33,237 per completion, the cost
effectiveness of REC, without
considering any cost savings, is around
$1,516 per ton of VOC (which we have
previously found to be cost effective on
average). When the value of the gas
recovered (approximately 150 tons of
methane per completion) is considered,
the cost effectiveness is estimated as an
average net savings of $99 per ton VOC
reduced, using standard discount rates.
We believe that these costs are very
reasonable, given the emission
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reduction that would be achieved. Aside
from the potential hazards associated
with pit flaring, in some cases, we did
not identify any nonair environmental
impacts, health or energy impacts
associated with REC combined with
combustion. However, pit flaring would
produce NOX emissions. Because we
believe that these emissions cannot be
controlled or measured directly due to
the open combustion process
characteristic of pit flaring, we used
published emission factors (EPA
Emission Guidelines AP–42) to estimate
the NOX emissions for purposes of
assessing secondary impacts. For
category 1 well completions, we
estimated that 0.02 tons of NOX are
produced per event. This is based on the
assumption that 5 percent of the
flowback gas is combusted by the
combustion device. The 1.2 tons of VOC
controlled during the pit flaring portion
of category 1 well completions is
approximately 57 times greater than the
NOX produced by pit flaring. Thus, we
believe that the benefit of the VOC
reduction far outweighs the secondary
impact of NOX formation during pit
flaring.
We believe that, based on the analysis
above, REC in combination with
combustion is BSER for subcategory 1
wells. We considered setting a
numerical performance standard for
subcategory 1 wells. However, it is not
practicable to measure the emissions
during pit flaring or venting because the
gas is discharged over the pit along with
water and sand in multiphase slug flow.
Therefore, we believe it is not feasible
to set a numerical performance
standard. Pursuant to section 111(h)(2)
of the CAA, we are proposing an
operational standard for subcategory 1
wells that would require a combination
of REC and pit flaring to minimize
venting of gas and condensate vapors to
the atmosphere, with provisions for
venting in lieu of pit flaring for
situations in which pit flaring would
present safety hazards or for periods
when the flowback gas is
noncombustible due to high
concentrations of nitrogen or CO2. The
proposed operational standard would be
accompanied by requirements for
documentation of the overall duration of
the completion event, duration of
recovery using REC, duration of
combustion, duration of venting, and
specific reasons for venting in lieu of
combustion.
We recognize that there is
heterogeneity in well operations and
costs, and that while RECs may be costeffective on average, they may not be for
all operators. Nonetheless, EPA is
proposing to require an operational
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standard rather than a performancebased standard (e.g., requiring that some
percentage of emissions be flared or
captured), because we believe there are
no feasible ways for operators to
measure emissions with enough
certainty to demonstrate compliance
with a performance-based standard for
REC in combination with pit flaring.
The EPA requests comment on this and
seeks input on whether alternative
approaches to requiring REC for all
operators with access to pipelines may
exist that would allow operators to meet
a performance-based standard if they
can demonstrate that an REC is not cost
effective.
We have discussed above certain
situations where unrecoverable gas
would be vented because pit flaring
would present a fire hazard or is
infeasible because gas is
noncombustible due to high
concentrations of nitrogen or CO2. We
solicit comment on whether there are
other such situations where flaring
would be unsafe or infeasible, and
potential criteria that would support
venting in lieu of pit flaring. In addition,
we learned that coalbed methane
reservoirs may have low pressure,
which would present a technical barrier
for performing a REC because the well
pressure may not be substantial enough
to overcome gathering line pressure. In
addition, we identified that coalbed
methane wells often have low to almost
no VOC emissions, even following the
hydraulic fracturing process. We solicit
comment on criteria and thresholds that
could be used to exempt some well
completion operations occurring in
coalbed methane reservoirs from the
requirements for subcategory 1 wells.
Of the 25,000 new and modified
fractured gas wells completed each year,
we estimate that approximately 3,000 to
4,000 currently employ reduced
emission completion. We expect this
number to increase to over 21,000 REC
annually as operators comply with the
proposed NSPS. We estimate that
approximately 9,300 new wells and
12,000 existing wells will be fractured
or refractured annually that would be
subject to subcategory 1 requirements
under the NSPS. We believe that there
will be a sufficient supply of REC
equipment available by the time the
NSPS becomes effective. However,
energy availability could be affected if a
shortage of REC equipment was allowed
to cause delays in well completions. We
request comment on whether sufficient
supply of this equipment and personnel
to operate it will be available to
accommodate the increased number of
REC by the effective date of the NSPS.
We also request specific estimates of
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how much time would be required to
get enough equipment in operation to
accommodate the full number of REC
performed annually.
In the event that public comments
indicate that available equipment would
likely be insufficient to accommodate
the increase in number of REC
performed, we are considering phasing
in requirements for well completions
that would achieve an overall
comparable level of environmental
benefit. For example, operators
performing completions of fractured or
refractured existing wells (i.e., modified
wells) could be allowed to control
emissions through pit flaring instead of
REC for some period of time. After some
date certain, all modified wells would
be subject to REC. We solicit comment
on the phasing of requirements for REC
along with suggestions for other ways to
address a potential short-term REC
equipment shortage that may hinder
operators’ compliance with the
proposed NSPS, while also achieving a
comparable level of reduced emissions
to the air.
Although we have determined that,
on average, reduced emission
completions are cost effective, well and
reservoir characteristics could vary,
such that some REC are more cost
effective than others. Unlike most
stationary source controls, REC
equipment is used only for a 3 to 10 day
period. Our review found that most
operators contract with service
companies to perform REC rather than
purchase the equipment themselves,
which was reflected in our economic
analysis. It is also possible that the
contracting costs of supplying and
operating REC equipment may rise in
the short term with the increased
demand for those services. We request
comment and any available technical
information to judge whether our
assumption of $33,237 per well
completion for this service given the
projected number of wells in 2015
subject to this requirement is accurate.
We believe that the proposed rule
regulates only significant emission
sources for which controls are costeffective. Nevertheless, we solicit
comment and supporting data on
appropriate thresholds (e.g., pressure,
flowrate) that we should consider in
specifying which well completions are
subject to the REC requirements for
subcategory 1 wells. Comments
specifying thresholds should include an
analysis of why sources below these
thresholds are not cost effective to
control.
In addition, there may be economic,
technical or other opportunities or
barriers associated with performing cost
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effective REC that we have not
identified in our review. For example,
some small regulated entities may have
an increased source of revenue due to
the captured product. On the other
hand, some small regulated entities may
have less access to REC than larger
regulated entities might have. We
request information on such
opportunities and barriers that we
should consider and suggestions for
how we may take them into account in
structuring the NSPS.
The second subcategory of fractured
gas wells includes exploratory wells or
delineation wells. Because these types
of wells generally are not in proximity
to existing gathering lines, REC is not an
option, since there is no infrastructure
in place to get the recovered gas to
market or further processing. For these
wells, the only potential control option
we were able to identify is pit flaring,
described above. As explained above,
because of the slug flow nature of the
flowback gas, water and sand, control by
a traditional flare control device or other
control devices, such as vapor recovery
units, is infeasible, which leaves pit
flaring as the only practicable control
system for subcategory 2 wells. As also
discussed above, open pit flaring can
present a fire hazard or other
undesirable impacts in some situations.
Aside from the potential hazards
associated with pit flaring, in some
cases, we did not identify any nonair
environmental impacts, health or energy
impacts associated with pit flaring.
However, pit flaring would produce
NOX emissions. As in the case of
category 1 wells, we believe that these
emissions cannot be controlled or
measured directly due to the open
combustion process characteristic of pit
flaring. We again used published
emission factors to estimate the NOX
emissions for purposes of assessing
secondary impacts. For category 2 well
completions, we estimated that 0.32
tons of NOX are produced as secondary
emissions per completion event. This is
based on the assumption that 95 percent
of flowback gas is combusted by the
combustion device. The 22 tons of VOC
reduced during the pit flaring used to
control category 2 well completions is
approximately 69 times greater than the
NOX produced. Thus, we believe that
the benefit of the VOC reduction far
outweighs the secondary impact of NOX
formation during pit flaring.
In light of the above, we propose to
determine that BSER for subcategory 2
wells would be pit flaring. As we
explained above, it is not practicable to
measure the emissions during pit flaring
or venting because the gas is discharged
during flowback mixed with water and
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sand in multiphase slug flow. It is,
therefore, not feasible to set a numerical
performance standard.
Pursuant to CAA section 111(h)(2), we
are proposing an operational standard
for subcategory 2 wells that requires
minimization of venting of gas and
hydrocarbon vapors during the
completion operation through the use of
pit flaring, with provisions for venting
in lieu of pit flaring for situations in
which flaring would present safety
hazards or for periods when the
flowback gas is noncombustible due to
high concentrations of nitrogen or
carbon dioxide.
Consistent with requirements for
subcategory 1 wells, owners or operators
of subcategory 2 wells would be
required to document completions and
provide justification for periods when
gas was vented in lieu of combustion.
We solicit comment on whether there
are other such situations where flaring
would be unsafe or infeasible and
potential criteria that would support
venting in lieu of pit flaring.
For controlling completion emissions
at oil wells and conventional (nonfractured) gas wells, we have identified
and evaluated the following control
options: REC in conjunction with pit
flaring and pit flaring alone. Due to the
low uncontrolled VOC emissions of
approximately 0.007 ton per completion
and, therefore, low potential emission
reductions from these events, the cost
per ton of reduction based on REC
would be extremely high (over $700,000
per ton of VOC reduced). We evaluated
the use of pit flaring alone as a system
for controlling emissions from oil wells
and conventional gas wells and
determined that the cost costeffectiveness would be approximately
$520,000 per ton for oil wells and
approximately $32,000 per ton for
conventional gas wells. In light of the
high cost per ton of VOC reduction, we
do not consider either of these control
options to be BSER for oil wells and
conventional wells.
We propose that fracturing (or
refracturing) and completion of an
existing well (i.e., a well existing prior
to August 23, 2011) is considered a
modification under CAA section 111(a),
because physical change occurs to the
existing well, which includes the
wellbore, casing and tubing, resulting in
an emissions increase during the
completion operation. The physical
change, in this case, would be caused by
the reperforation of the casing and
tubing, along with the refracturing of the
wellbore. The increased VOC emissions
would occur during the flowback period
following the fracturing or refracturing
operation. Therefore, the proposed
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standards for category 1 and category 2
wells would apply to completions at
existing fractured or refractured wells.
EPA seeks comment on the 10 percent
per year rate of refracturing for natural
gas wells assumed in the impacts
analysis found in the TSD. EPA has
received anecdotal information
suggesting that refracturing could be
occurring much less frequently, while
others suggest that the percent of wells
refractured in a given year could be
greater. We seek comment and
comprehensive data and information on
the rate of refracturing and key factors
that influence or determine refracturing
frequency.
In addition to well completions, we
considered VOC emissions occurring at
the wellhead affected facility during
subsequent day-to-day operations
during well production. As discussed
below in section VI.B.1.e, VOC
emissions from wellheads are very small
during production and account for
about 2.6 tons VOC per year. We are not
aware of any cost effective controls that
can be used to address these relatively
small emissions.
b. NSPS for Pneumatic Controllers
Pneumatic controllers are automated
instruments used for maintaining a
process condition, such as liquid level,
pressure, pressure differential and
temperature. Pneumatic controllers are
widely used in the oil and natural gas
sector. In many situations across all
segments of the oil and gas industry,
pneumatic controllers make use of the
available high-pressure natural gas to
operate. In these ‘‘gas-driven’’
pneumatic controllers, natural gas may
be released with every valve movement
or continuously from the valve control
pilot. The rate at which this release
occurs is referred to as the device bleed
rate. Bleed rates are dependent on the
design of the device. Similar designs
will have similar steady-state rates
when operated under similar
conditions. Gas-driven pneumatic
controllers are typically characterized as
‘‘high-bleed’’ or ‘‘low-bleed,’’ where a
high-bleed device releases more than 6
standard cubic feet per hour (scfh) of
gas, with 18 scfh bleed rate being what
we used in our analyses below. There
are three basic designs: (1) Continuous
bleed devices (high or low-bleed) are
used to modulate flow, liquid level or
pressure and gas is vented at a steadystate rate; (2) actuating/intermittent
devices (high or low-bleed) perform
quick control movements and only
release gas when they open or close a
valve or as they throttle the gas flow;
and (3) self-contained devices release
gas to a downstream pipeline instead of
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to the atmosphere. We are not aware of
any add-on controls that are or can be
used to reduce VOC emissions from gasdriven pneumatic devices.
For an average high-bleed pneumatic
controller located in production (where
the content of VOC in the raw product
stream is relatively high), the difference
in VOC emissions between a high-bleed
controller and a low-bleed controller is
around 1.8 tpy. For the transmission
and storage segment (where the content
of VOC in the pipeline quality gas is
relatively low), the difference in VOC
emissions between a high-bleed
controller and a low-bleed controller is
around 0.89 tpy. We have developed
projections that estimate that
approximately 13,600 new gas-driven
units in the production segment and 67
new gas-driven units in the
transmission and storage segment will
be installed each year, including
replacement of old units. Not all
pneumatic controllers are gas driven.
These ‘‘non-gas driven’’ pneumatic
controllers use sources of power other
than pressurized natural gas, such as
compressed ‘‘instrument air.’’ Because
these devices are not gas driven, they do
not release natural gas or VOC
emissions, but they do have energy
impacts because electrical power is
required to drive the instrument air
compressor system. Electrical service of
at least 13.3 kilowatts (kW) is required
to power a 10 horsepower (hp)
instrument air compressor, which is a
relatively small capacity compressor. At
sites without available electrical service
sufficient to power an instrument air
compressor, only gas driven pneumatic
devices can be used. During our review,
we determined that gas processing
plants are the only facilities in the oil
and natural gas sector highly likely to
have electrical service sufficient to
power an instrument air system, and
that approximately half of existing gas
processing plants are using non-gas
driven devices.
For devices at gas processing plants,
we evaluated the use of non-gas driven
controllers and low-bleed controllers as
options for reducing VOC emissions,
with high-bleed controllers being the
baseline. As mentioned above, non-gas
driven devices themselves have zero
emissions, but they do have energy
impacts because electrical power is
required to drive the instrument air
compressor system. In our cost analysis,
we determined that the annualized cost
of installing and operating a fully
redundant 10 hp (13.3 kW) instrument
air system (systems generally are
designed with redundancy to allow for
system maintenance and failure without
loss of air pressure), including duplicate
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compressors, air tanks and dryers,
would be $11,090. A system of this size
is capable of serving 15 control loops
and reducing VOC emissions by 4.2 tpy,
for a cost effectiveness of $2,659 per ton
of VOC reduced. If the savings of the
salable natural gas that would have been
emitted is considered, the value of the
gas not emitted would help offset the
cost for this control, bringing the cost
per ton of VOC down to $1,824.
We also evaluated the use of lowbleed controllers in place of high-bleed
controllers at processing plants. We
evaluated the impact of bleeding 6
standard cubic feet of natural gas per
hour, which is the maximum bleed rate
from low-bleed controllers, according to
manufacturers of these devices. We
chose natural gas as a surrogate for VOC,
because manufacturers’ technical
specifications for pneumatic controllers
are stated in terms of natural gas bleed
rate rather than VOC. The capital cost
difference between a new high-bleed
controller and a new low-bleed
controller is estimated to be $165.
Without taking into account the savings
due to the natural gas losses avoided,
the annual costs are estimated to be
around $23 per year, which is a cost of
$13 per ton of VOC reduced for the
production segment. If the savings of the
salable natural gas that would have been
emitted is considered, there is a net
savings of $1,519 per ton of VOC
reduced.
Although the non-gas-driven
controller system is more expensive
than the low-bleed controller system, it
is still reasonably cost-effective.
Furthermore, the non-gas-driven
controller system achieves a 100-percent
VOC reduction in contrast to a 66percent reduction achieved by a lowbleed controller. Moreover, we believe
the collateral emissions from electrical
power generation needed to run the
compressor are very low. Finally, nongas-driven pneumatic controllers avoid
potentially explosive concentrations of
natural gas which can occur as a result
of normal bleeding from groups of gasdriven pneumatic controllers located in
close proximity, as they often are at gas
processing plants. Based on our review
described above, we believe that a nongas-driven controller is BSER for
reducing VOC emissions from
pneumatic devices at gas processing
plants. Accordingly, the proposed
standard for pneumatic devices at gas
processing plants is a zero VOC
emission limit.
For the production (other than
processing plants) and transmission and
storage segments, where electrical
service sufficient to power an
instrument air system is likely
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unavailable and, therefore, only gasdriven devices can be used, we
evaluated the use of low-bleed
controllers in place of high-bleed
controllers. Just as in our analysis of
low-bleed controllers as an option for
gas processing plants, we evaluated the
impact of bleeding 6 standard cubic feet
per minute (scfm) of natural gas per
hour contrasted with 18 scfm from a
high-bleed unit. Again, the capital cost
difference between a new high-bleed
controller and a new low-bleed
controller is estimated to be $165.
Without taking into account the savings
due to the natural gas losses avoided,
the annual costs are estimated to be
around $23 per year, which is a cost of
$13 per ton of VOC reduced for the
production segment. If the savings of the
salable natural gas that would have been
emitted is considered, there is a net
savings for this control. In the
transmission and storage segment,
where the VOC content of the vented
gas is much lower than in the
production segment, the cost
effectiveness of a low-bleed pneumatic
device is estimated to be around $262
per ton of VOC reduced. However, there
are no potential offsetting savings to be
realized in the transmission and storage
segment, since the operators of
transmission and storage stations
typically do not own the gas they are
handling. Based on our evaluation of the
emissions and costs, we believe that
low-bleed controllers represent BSER
for pneumatic controllers in the
production (other than processing
plants) and transmission and storage
segments. Therefore, for pneumatic
devices at these locations, we propose a
natural gas bleed rate limit of 6.0 scfh
to reflect the VOC limit with the use of
a low-bleed controller.
There may be situations where highbleed controllers and the attendant gas
bleed rate greater than 6 cubic feet per
hour, are necessary due to functional
requirements, such as positive actuation
or rapid actuation. An example would
be controllers used on large emergency
shutdown valves on pipelines entering
or exiting compression stations. For
such situations, we have provided in the
proposed rule an exemption where
pneumatic controllers meeting the
emission standards discussed above
would pose a functional limitation due
to their actuation response time or other
operating characteristics. We are
requesting comments on whether there
are other situations that should be
considered for this exemption. If you
provide such comment, please specify
the criteria for such situations that
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would help assure that only appropriate
exemptions are claimed.
The proposed standards would apply
to installation of a new pneumatic
device (including replacing an existing
device with a new device). We consider
that a pneumatic device, an apparatus,
is an affected facility and each
installation is construction subject to
the proposed NSPS. See definitions of
‘‘affected facility’’ and ‘‘construction’’ at
40 CFR 60.2.
c. NSPS for Compressors
There are many locations throughout
the oil and natural gas sector where
compression of natural gas is required to
move it along the pipeline. This is
accomplished by compressors powered
by combustion turbines, reciprocating
internal combustion engines or electric
motors. Turbine-powered compressors
use a small portion of the natural gas
that they compress to fuel the turbine.
The turbine operates a centrifugal
compressor, which compresses the
natural gas for transit through the
pipeline. Sometimes an electric motor is
used to turn a centrifugal compressor.
This type of compressor does not
require the use of any of the natural gas
from the pipeline, but it does require a
substantial source of electricity.
Reciprocating spark ignition engines are
also used to power many compressors,
referred to as reciprocating compressors,
since they compress gas using pistons
that are driven by the engine. Like
combustion turbines, these engines are
fueled by natural gas from the pipeline.
Both centrifugal and reciprocating
compressors are sources of VOC
emissions and were evaluated for
coverage under the NSPS.
Centrifugal Compressors. Centrifugal
compressors require seals around the
rotating shaft to minimize gas leakage
and fugitive VOC emissions from where
the shaft exits the compressor casing.
There are two types of seal systems: Wet
seal systems and mechanical dry seal
systems.
Wet seal systems use oil, which is
circulated under high pressure between
three or more rings around the
compressor shaft, forming a barrier to
minimize compressed gas leakage. Very
little gas escapes through the oil barrier,
but considerable gas is absorbed by the
oil. The amount of gas absorbed and
entrained by the oil barrier is affected by
the operating pressure of the gas being
handled; higher operating pressures
result in higher absorption of gas into
the oil. Seal oil is purged of the
absorbed and entrained gas (using
heaters, flash tanks and degassing
techniques) and recirculated to the seal
area for reuse. Gas that is purged from
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the seal oil is commonly vented to the
atmosphere. Degassing of the seal oil
emits an average of 47.7 scfm of gas,
depending on the operating pressure of
the compressor. An uncontrolled wet
seal system can emit, on average,
approximately 20.5 tpy of VOC during
the venting process (production
segment) or about 3.5 tpy (transmission
and storage segment). We identified two
potential control techniques for
reducing emissions from degassing of
wet seal systems: (1) Routing the gas
back to a low pressure fuel stream to be
combusted as fuel gas and (2) routing
the gas to a flare. We know only of
anecdotal, undocumented information
on routing of the gas back to a fuel
stream and, therefore, were unable to
assess costs and cost effectiveness of the
first option. Although we do not have
specific examples of routing emissions
from wet seal degassing to a flare, we
were able to estimate the cost, emission
reductions and cost effectiveness of the
second option using uncontrolled wet
seals as a baseline.
Based on the average uncontrolled
emissions of wet seal systems discussed
above and a flare efficiency of 95
percent, we determined that VOC
emission reductions from a wet seal
system would be an average of 19.5 tpy
(production segment) or 3.3 tpy
(transmission and storage segment).
Using an annualized cost of flare
installation and operation of $103,373,
we estimated the incremental cost
effectiveness of this option (from
uncontrolled wet seals to controlled wet
seals using a flare) to be approximately
$5,300/ton and $31,000/ton for the
production segment and transmission
and storage segment, respectively. With
this option, there would be secondary
air impacts from combustion. However
we did not identify any nonair quality
or energy impacts associated with this
control technique.
Dry seal systems do not use any
circulating seal oil. Dry seals operate
mechanically under the opposing force
created by hydrodynamic grooves and
springs. Fugitive emissions occur from
dry seals around the compressor shaft.
Based on manufacturer studies and
engineering design estimates, fugitive
emissions from dry seal systems are
approximately 6 scfm of gas, depending
on the operating pressure of the
compressor. A dry seal system can have
fugitive emissions of, on average,
approximately 2.6 tpy of VOC
(production segment) or about 0.4 tpy
(transmission and storage segment). We
did not identify any control device
suitable to capture and control the
fugitive emissions from dry seals around
the compressor shaft.
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Using uncontrolled wet seals as a
baseline, we evaluated the reductions
and incremental cost effectiveness of
dry seal systems. Based on the average
fugitive emissions, we determined that
VOC emission reductions achieved by
dry seal systems compared to
uncontrolled wet seal systems would be
18 tpy (production segment) and 3.1 tpy
(transmission and storage segment).
Combined with an annualized cost of
dry seal systems of $10,678, the
incremental cost effectiveness compared
to uncontrolled wet seal systems would
be $595/ton and $3,495/ton for the
production segment and transmission
and storage segment, respectively. We
identified neither nonair quality nor any
energy impacts associated with this
option.
In performing our analysis, we
estimated the incremental cost of a dry
seal compressor over that of an
equivalent wet seal compressor to be
$75,000. This value was obtained from
a vendor who represents a large share of
the market for centrifugal compressors.
However, this number likely represents
a conservatively high value because wet
seal units have a significant amount of
ancillary equipment, namely the seal oil
system and, thus, additional capital
expenses. Dry seal systems have some
ancillary equipment (the seal gas
filtration system), but the costs are less
than the wet seal oil system. We were
not able to directly confirm this
assumption with the vendor, however, a
search of product literature showed that
seal oil systems and seal gas filtration
systems are typically listed separate
from the basic compressor package.
Using available data on the cost of this
equipment, it is very likely that the cost
of purchasing a dry seal compressor
may actually be lower that a wet seal
compressor. We seek comment on
available cost data of a dry seal versus
wet seal compressor, including all
ancillary equipment costs.
In light of the above analyses, we
propose to determine that dry seal
systems are BSER for reducing VOC
emissions from centrifugal compressors.
We evaluated the possibility of setting a
performance standard that reflects the
emission limitation achievable through
the use of a dry seal system. However,
as mentioned above, VOC from
centrifugal compressors with dry seals
are fugitive emissions from around the
compressor shafts. There is no device to
capture and control these fugitive
emissions, nor can reliable
measurement of these emissions be
conducted due to difficulty in accessing
the leakage area and danger of
contacting the shaft rotating at
approximately 30,000 revolutions per
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minute. This not only poses a likely
hazard that would destroy test
equipment on contact, it poses a safety
hazard to personnel, as well. Therefore,
pursuant to section 111(h)(2) of the
CAA, we are proposing an equipment
standard that would require the use of
dry seals to limit the VOC emissions
from new centrifugal compressors. We
consider that a centrifugal compressor,
an apparatus, is an affected facility and
each installation is construction subject
to the proposed NSPS. See definitions of
‘‘affected facility’’ and ‘‘construction’’ at
40 CFR 60.2. Accordingly, the proposed
standard would apply to installation of
new centrifugal compressors at new
locations, as well as replacement of old
compressors.
Although we are proposing to
determine dry seal systems to be BSER
for centrifugal compressors, we are
soliciting comments on the emission
reduction potential, cost and any
limitations for the option of routing the
gas back to a low pressure fuel stream
to be combusted as fuel gas. In addition,
we solicit comments on whether there
are situations or applications where wet
seal is the only option, because a dry
seal system is infeasible or otherwise
inappropriate.
Reciprocating Compressors.
Reciprocating compressors in the
natural gas industry leak natural gas
fugitive VOC during normal operation.
The highest volumes of gas loss and
fugitive VOC emissions are associated
with piston rod packing systems.
Packing systems are used to maintain a
tight seal around the piston rod,
preventing the high pressure gas in the
compressor cylinder from leaking, while
allowing the rod to move freely. This
leakage rate is dependent on a variety of
factors, including physical size of the
compressor piston rod, operating speed
and operating pressure. Under the best
conditions, new packing systems
properly installed on a smooth, wellaligned shaft can be expected to leak a
minimum of 11.5 scfh. Higher leak rates
are a consequence of fit, alignment of
the packing parts and wear.
We evaluated the possibility of
reducing VOC emissions from reciprocal
compressors through a control device.
However, VOC from reciprocating
compressors are fugitive emissions from
around the compressor shafts. Although
it is possible to construct an enclosure
around the rod packing area and vent
the emissions outside for safety
purposes, connection to a closed vent
system and control device would create
back pressure on the leaking gas. This
back pressure would cause the leaked
gas instead to be forced inside the
crankcase of the engine, which would
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dilute lubricating oil, causing premature
failure of engine bearings, pose an
explosion hazard and eventually be
vented from the crankcase breather,
defeating the purpose of a control
device.
As mentioned above, as packing
wears and deteriorates, leak rates can
increase. We, therefore, evaluate
replacement of compressor rod packing
systems as an option for reducing VOC
emissions. Conventional bronzemetallic packing rings wear out and
need to be replaced every 3 to 5 years,
depending on the compressor’s rate of
usage (i.e., the percentage of time that a
compressor is in pressurized mode).
Based on industry experience in the
Natural Gas STAR program and other
sources, we evaluated the rod packing
replacement costs for reciprocating
compressors at different segments of
this industry. Usage rates vary by
segment. Usage rates for compressors at
wellheads, gathering/boosting stations,
processing plants, transmission stations
and storage facilities are 100, 79, 90, 79
and 68 percent, respectively.
Reciprocating compressors at wellheads
are small and operate at lower
pressures, which limit VOC emissions
from these sources. Due to the low VOC
emissions from these compressors,
about 0.044 tpy, combined with an
annual cost of approximately $3,700,
the cost per ton of VOC reduction is
rather high. We estimated that the cost
effectiveness of controlling wellhead
compressors is over $84,000 per ton of
VOC reduced, which we believe to be
too high and, therefore, not reasonable.
Because the cost effectiveness of
replacing packing wellhead compressor
rod systems is not reasonable, and
absent other emission reduction
measures, we did not find a BSER for
reducing VOC emissions from reciprocal
compressors at wellheads.
For reciprocating compressors located
at other oil and gas operations, we
estimated that the cost effectiveness of
controlling compressor VOC emissions
by rod packing replacement would be
$870 per ton of VOC for reciprocating
compressors at gathering and boosting
stations, $270 per ton of VOC for
reciprocating compressors at processing
stations, $2,800 per ton of VOC for
reciprocating compressors at
transmission stations and $3,700 per ton
of VOC for reciprocating compressors at
underground storage facilities. We
consider these costs to be reasonable.
We did not identify any nonair quality
health or environmental impacts or
energy impacts associated with rod
packing replacement. In light of the
above, we propose to determine that
such control is the BSER for reducing
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VOC emission from compressors at
these other oil and gas operations.
Because VOC emitted from reciprocal
compressors are fugitive emissions,
there is no device to capture and control
the emissions. Therefore, pursuant to
section 111(h) of the CAA, we are
proposing an operational standard.
Based on industry experience reported
to the Natural Gas STAR program, we
determined that packing rods should be
replaced every 3 years of operation.
However, to account for segments of the
industry in which reciprocating
compressors operate in pressurized
mode a fraction of the calendar year
(ranging from approximately 68 percent
up to approximately 90 percent), the
proposed rule expresses the
replacement requirement in terms of
hours of operation rather than on a
calendar year basis. One year of
continuous operation would be 8,760
hours. Three years of continuous
operation would be 26,280 hours, or
rounded to the nearest thousand, 26,000
hours. Accordingly, the proposed rule
would require the replacement of the
rod packing every 26,000 hours of
operation. The owner or operator would
be required to monitor the hours of
operation beginning with the
installation of the reciprocating
compressor affected facility. Cumulative
hours of operation would be reported
each year in the facility’s annual report.
Once the hours of operation reached
26,000 hours, the owner or operator
would be required to change the rod
packing immediately, although
unexpected shutdowns could be
avoided by tracking hours of operation
and planning for packing replacement at
scheduled maintenance shutdowns
before the hours of operation reached
26,000.
Some industry partners of the Natural
Gas STAR program currently conduct
periodic testing to determine the leakage
rates that would identify economically
beneficial replacement of rod packing
based on natural gas savings. Therefore,
we are soliciting comments on
incorporating a method similar to that
in the Natural Gas STAR’s Lessons
Learned document entitled, Reducing
Methane Emissions from Compressor
Rod Packing Systems (https://
www.epa.gov/gasstar/documents/
ll_rodpack.pdf), to be incorporated in
the NSPS. We are soliciting comments
on how to determine a suitable leak
threshold above which rod packing
replacement would be cost effective for
VOC emission reduction. We are also
soliciting comment on the appropriate
replacement frequency and other
considerations that would be associated
with regular replacement periods.
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d. NSPS for Storage Vessels
Crude oil, condensate and produced
water are typically stored in fixed-roof
storage vessels. Some vessels used for
storing produced water may be open-top
tanks. These vessels, which are operated
at or near atmospheric pressure
conditions, are typically located as part
of a tank battery. A tank battery refers
to the collection of process equipment
used to separate, treat and store crude
oil, condensate, natural gas and
produced water. The extracted products
from productions wells enter the tank
battery through the production header,
which may collect product from many
wells.
Emissions from storage vessels are a
result of working, breathing and flash
losses. Working losses occur due to the
emptying and filling of storage tanks.
Breathing losses are the release of gas
associated with daily temperature
fluctuations and other equilibrium
effects. Flash losses occur when a liquid
with dissolved gases is transferred from
a vessel with higher pressure to a vessel
with lower pressure, thus, allowing
dissolved gases and a portion of the
liquid to vaporize or flash. In the oil and
natural gas production segment, flashing
losses occur when live crude oils or
condensates flow into a storage tank
from a processing vessel operated at a
higher pressure. Typically, the larger the
pressure drop, the more flash emissions
will occur in the storage stage.
Temperature of the liquid also
influences the amount of flash
emissions. The amount of liquid
entering the tank during a given time,
commonly known as throughput, also
affects the emission rate, with higher
throughput tanks having higher annual
emissions, given that other parameters
are the same.
In analyzing controls for storage
vessels, we reviewed control techniques
identified in the Natural Gas STAR
program and state regulations. We
identified two ways of controlling
storage vessel emissions, both of which
can reduce VOC emissions by 95
percent. One option would be to install
a vapor recovery unit (VRU) and recover
all the vapors from the tanks. The other
option would be to route the emissions
from the tanks to a flare control device.
These devices could be ‘‘candlestick’’
flares that are found at gas processing
plants or other larger facilities or
enclosed combustors which are
commonly found at smaller field
facilities. We estimated the total annual
cost for a VRU to be approximately
$18,900/yr and for a flare to be
approximately $8,900/yr. Cost
effectiveness of these control options
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depend on the amount of vapor
produced by the storage vessels being
controlled. A VRU has a potential
advantage over flaring, in that it
recovers hydrocarbon vapors that
potentially can be used as supplemental
burner fuel, or the vapors can be
condensed and collected as condensate
that can be sold. If natural gas is
recovered, it can be sold, as well, as
long as a gathering line is available to
convey the recovered salable gas
product to market or to further
processing. A VRU also does not have
secondary air impacts that flaring does,
as described below. However, a VRU
cannot be used in all instances. Some
conditions that affect the feasibility of
VRU are: Availability of electrical
service sufficient to power the VRU;
fluctuations in vapor loading caused by
surges in throughput and flash
emissions from the tank; potential for
drawing air into condensate tanks
causing an explosion hazard; and lack of
appropriate destination or use for the
vapor recovered.
Like a VRU, a flare control device can
also achieve a control efficiency of 95
percent. There are no technical
limitations on the use of flares to control
vapors from condensate and crude oil
tanks. However, flaring has a secondary
impact from emissions of NOX and other
pollutants. In light of the technical
limitations with the use of a VRU, we
are unable to conclude that a VRU is
better than flaring. We, therefore,
propose to determine that both a VRU
and flare are BSER for reducing VOC
emission from storage vessels. We
propose an NSPS of 95-percent
reduction for storage vessels to reflect
the level of emission reduction
achievable by VRU and flares.
VOC emissions from storage vessels
vary significantly, depending on the rate
of liquid entering and passing through
the vessel (i.e., its throughput), the
pressure of the liquid as it enters the
atmospheric pressure storage vessel, the
liquid’s volatility and temperature of the
liquid. Some storage vessels have
negligible emissions, such as those with
very little throughput and/or handling
heavy liquids entering at atmospheric
pressure. We do not believe that it is
cost effective to control these vessels.
We believe it is important to control
tanks with significant VOC emissions
under the proposed NSPS.
In our analysis, we evaluated storage
tanks with varying condensate or crude
oil throughput. We used emission
factors developed for the Texas
Environmental Research Consortium in
a study that evaluated VOC emissions
from crude oil and condensate storage
tanks by performing direct
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measurements. The study found that the
average VOC emission factor for crude
oil storage tanks was 1.6 pounds (lb)
VOC per barrel of crude oil throughput.
The average VOC emission factor for
condensate tanks was determined to be
33.3 lb VOC per barrel of condensate
throughput. Applying these emission
factors and evaluating condensate
throughput rates of 0.5, 1, 2 and 5
barrels per day (bpd), we determined
that VOC emissions at these condensate
throughput rates would be
approximately 3, 6, 12 and 30 tpy,
respectively. Similarly, we evaluated
crude oil throughput rates of 1, 5, 20
and 50 bpd. Based on the Texas study,
these crude oil throughput rates would
result in VOC emissions of 0.3, 1.5, 5.8
and 14.6 tpy, respectively. We believe
that it is important to control tanks with
significant VOC emissions.
Furthermore, we believe it would be
easier and less costly for owners and
operators to determine applicability by
using a throughput threshold instead of
an emissions threshold. As a result of
the above analyses, we believe that
storage vessels with at least 1 bpd of
condensate or 20 bpd of crude oil
should be controlled. These throughput
rates are equivalent to VOC emissions of
approximately 6 tpy. Based on an
estimated annual cost of $18,900 for the
control device, controlling storage
vessels with these condensate or crude
oil throughputs would result in a cost
effectiveness of $3,150 per ton of VOC
reduced.
Based on our evaluation, we propose
to determine that both a VRU and flare
are BSER for reducing VOC emission
from storage vessels with throughput of
at least 1 barrel of condensate per day
or 20 barrels of crude oil per day. We
propose an NSPS of 95-percent
reduction for these storage vessels to
reflect the level of emission reduction
achievable by VRU and flare control
devices.
For storage vessels below the
throughput levels described above
(‘‘small throughput tanks’’), for which
we do not consider flares or VRU to be
cost effective controls, we evaluated
other measures to reduce VOC
emissions. Standard practices for such
tanks include requiring a cover that is
well designed, maintained in good
condition and kept closed. Crude oil
and condensate storage tanks in the oil
and natural gas sector are designed to
operate at or just slightly above or below
atmospheric pressure. Accordingly, they
are provided with vents to prevent tank
destruction under rapid pressure
increases due to flash emissions
conditions. Studies by the Natural Gas
STAR program and by others have
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shown that working losses (i.e., those
emissions absent flash emission
conditions) are very low, approaching
zero. During times of flash emissions,
tanks are designed such that the flash
emissions are released through a vent on
the fixed roof of the tank when pressure
reaches just a few ounces to prevent
pressure buildup and resulting tank
damage. At those times, vapor readily
escapes through the vent to protect the
tank. Tests have shown that open
hatches or leaking hatch gaskets have
little effect on emissions from
uncontrolled tanks due to the
functioning roof vent. However, in the
case of controlled tanks, the control
requirements include provisions for
maintaining integrity of the closed vent
system that conveys emissions to the
control device, including hatches and
other tank openings. As a result, hatches
are required to be kept closed and
gaskets kept in good repair to meet
control requirements of controlled
storage vessels. Because the measures
we evaluated, including maintenance of
hatch integrity, do not provide
appreciable emission reductions for
storage vessels with throughputs under
1 barrel of condensate per day and 21
barrels of crude oil per day, we believe
that the control options we evaluated do
not reflect BSER for the small
throughput tanks and we are not
proposing standards for these tanks.
As discussed in section VII of this
preamble, we are proposing to amend
the NESHAP for oil and natural gas
production facilities at 40 CFR part 63,
subpart HH to require that all storage
vessels at production facilities reduce
HAP emissions by 95 percent. Because
the controls used to achieve the 95percent HAP reduction are the same as
the proposed BSER for VOC reduction
for storage vessels (i.e., VRU and flare),
sources that are achieving the 95percent HAP reduction would also be
meeting the proposed NSPS of 95percent VOC reduction. In light of the
above, and to avoid duplicate
monitoring, recordkeeping and
reporting, we propose that storage
vessels subject to the requirements of
subpart HH are exempt from the
proposed NSPS for storage vessel in 40
CFR part 60, subpart OOOO.
e. NSPS for VOC Equipment Leaks
Equipment leaks are fugitive
emissions emanating from valves, pump
seals, flanges, compressor seals,
pressure relief valves, open-ended lines
and other process and operation
components. There are several potential
reasons for equipment leak emissions.
Components such as pumps, valves,
pressure relief valves, flanges, agitators
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and compressors are potential sources
that can leak due to seal failure. Other
sources, such as open-ended lines and
sampling connections may leak for
reasons other than faulty seals. In
addition, corrosion of welded
connections, flanges, and valves may
also be a cause of equipment leak
emissions. Because of the large number
of valves, pumps and other components
within an oil and gas production,
processing and transmission facility,
equipment leak volatile emissions from
these components can be significant.
Natural gas processing plants, especially
those using refrigerated absorption and
transmission stations tend to have a
large number of components.
Equipment leaks from processing plants
are addressed in our review of 40 CFR
part 60, subpart KKK, which is
discussed above in section VI.B.1.
In addition to gas processing plants,
these types of equipment also exist at oil
and gas production sites and gas
transmission and storage facilities.
While the number of components at
individual transmission and storage
facilities is relatively smaller than at
processing plants, collectively, there are
many components that can result in
significant emissions.
Therefore, we evaluated applying
NSPS for equipment leaks to facilities in
the production segment of the industry,
which includes everything from the
wellhead to the point that the gas enters
the processing plant, transmission
pipeline or distribution pipeline.
Production facilities can vary
significantly in the operations
performed and the processes, all of
which impact the number of
components and potential emissions
from leaking equipment and, thus,
impact the annual costs related to
implementing a LDAR program. We
used data collected by the Gas Research
Institute to develop model production
facilities. Baseline emissions, along with
emission reductions and costs of
regulatory alternatives, were estimated
using these model production facilities.
We considered production facilities
where separation, storage, compression
and other processes occur. These
facilities may not have a wellhead onsite, but would be associated with a
wellhead. We also evaluated gathering
and boosting facilities, where gas and/
or oil are collected from a number of
wells, then processed and transported
downstream to processing plants or
transmission stations. We evaluated the
impacts at these production facilities
with varying number of operations and
equipment. We also developed a model
plant for the transmission and storage
segment using data from the Gas
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Research Institute. Details of these
evaluations may be found in the TSD in
the docket.
For an average production site at or
associated with a wellhead, we
estimated annual VOC emissions from
equipment leaks of around 2.6 tpy. For
an average gathering/boosting facility,
we estimated the annual VOC emissions
from equipment leaks to be around 9.8
tpy. The average transmission and
storage facility emits 2.7 tpy of VOC.
For facilities in each non-gas
processing plant segment, we evaluated
the same four options as we did for gas
processing plants in section VI.B.1
above. These four options are as follows:
(1) 40 CFR part 60, subpart VVa-level
LDAR (which is based on conducting
Method 21 monthly, defining ‘‘leak’’ at
500 ppm threshold, and adding
connectors to the VV list of components
to be monitored); (2) monthly optical
gas imaging with annual Method 21
check (the alternative work practice for
monitoring equipment for leaks at 40
CFR 60.18(g)); (3) monthly optical gas
imaging alone; and (4) annual optical
gas imaging alone.
For option 1, we evaluated subpart
VVa-LDAR as a whole. We also
analyzed separately the individual types
of components (valves, connectors,
pressure relief devices and open-ended
lines). Detailed discussions of these
component by component analyses are
included in the TSD in the docket.
Based on our evaluation, subpart VValevel LDAR (Option 1) results in more
VOC reduction than the subpart VVlevel LDAR currently required for gas
processing plants, because more leaks
are found based on the lower definition
of ‘‘leak’’ under subpart VVa (10,000
ppm for subpart VV and 500 ppm for
subpart VVa). In addition, our
evaluation shows that the cost per ton
of VOC reduced for subpart VVa level
controls is less than the cost per ton of
VOC reduced for the less stringent
subpart VV level of control. Although
the cost of repairing more leaks is
higher, the increased VOC control
afforded by subpart VVa level controls
more than offsets the increased costs.
For the subpart VVa level of control
at the average production site associated
with a wellhead, average facility-wide
cost-effectiveness would be $16,084 per
ton of VOC. Component-specific costeffectiveness ranged from $15,063 per
ton of VOC (for valves) to $211,992 per
ton of VOC (for pressure relief devices),
with connectors and open-ended lines
being $74,283 and $180,537 per ton of
VOC, respectively. We also looked at
component costs for a modified subpart
VVa level of control with less frequent
monitoring for valves and connectors at
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production sites associated with a
wellhead.12 The cost-effectiveness for
valves was calculated to be $17,828 per
ton of VOC by reducing the monitoring
frequency from monthly to annually.
The cost-effectiveness for connectors
was calculated to be $87,277 per ton of
VOC by reducing the monitoring
frequency from every 4 years to every 8
years after the initial compliance period.
We performed a similar facility-wide
and component-specific analysis of
option 1 LDAR for gathering and
boosting stations. For the subpart VVa
level of control at the average gathering
and boosting station, facility-wide costeffectiveness was estimated to be $9,344
per ton of VOC. Component-specific
cost-effectiveness ranged from $6,079
per ton of VOC (for valves) to $77,310
per ton of VOC (for open-ended lines),
with connectors and pressure relief
devices being $23,603 and $72,523 per
ton, respectively. For the modified
subpart VVa level of control at gathering
and boosting stations, cost-effectiveness
ranged from $5,221 per ton of VOC (for
valves) to $77,310 per ton of VOC (for
open-ended lines), with connectors and
pressure relief devices being $27,274
and $72,523 per ton, respectively. The
modified subpart VVa level controls
were more cost-effective than the
subpart VVa level controls for valves,
but not for connectors. This is due to the
low cost of monitoring connectors and
the low VOC emissions from leaking
connectors.
We also performed a similar analysis
of option 1 subpart VVa-level LDAR for
gas transmission and storage facilities.
For the subpart VVa level of control at
the average transmission and storage
facility, facility-wide cost-effectiveness
was $20,215. Component-specific costeffectiveness ranged from $24,762 per
ton of VOC (for open-ended lines) to
$243,525 per ton of VOC (for pressure
relief devices), with connectors and
valves being $36,527 and $43,111 per
ton of VOC, respectively. For the
modified subpart VVa level of control at
transmission and storage facilities, costeffectiveness ranged from $24,762 per
ton of VOC (for open-ended lines) to
$243,525 per ton of VOC (for pressure
relief devices), with connectors and
valves being $42,140 and $40,593 per
ton of VOC, respectively. Again, the
modified subpart VVa level controls
were more cost-effective for valves and
less cost effective for connectors than
the subpart VVa level controls. This is
due to the low cost of monitoring
connectors and the low VOC emissions
from leaking connectors.
For each of the non-gas processing
segments, we also evaluated monthly
optical gas imaging with annual Method
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21 check (Option 2). As discussed in
secton VI.B.1, we had previously
determined that the VOC reductions
achieved under this option would be the
same as for option 1 subpart VVa-level
LDAR. In our evaluation of Option 2, we
estimated that a single optical imaging
instrument could be used for 160 well
sites and 13 gathering and boosting
stations, which means that the cost of
the purchase or rental of the camera
would be spread across 173 facilities.
For production sites, gathering and
boosting stations, and transmission and
storage facilities, we estimated that
option 2 monthly optical gas imaging
with annual Method 21 check would
have cost-effectiveness of $16,123,
$10,095, and $19,715 per ton of VOC,
respectively.13
The annual costs for option 1 and
option 2 leak detection and repair
programs for production sites associated
with a wellhead, gathering and boosting
stations and transmission and storage
facilities were higher than those
estimated for natural gas processing
plants because natural gas processing
plant annual costs are based on the
incremental cost of implementing
subpart VVa-level standards, whereas
the other facilities are not currently
regulated under an LDAR program. The
currently unregulated sites would be
required to set up a new LDAR program;
perform initial monitoring, tagging,
logging and repairing of components; as
well as planning and training personnel
to implement the new LDAR program.
In addition to options 1 and 2, we
evaluated a third option that consisted
of monthly optical gas imaging without
an annual Method 21 check. Because we
were unable to estimate the VOC
emissions achieved by an optical
imaging program alone, we were unable
to estimate the cost-effectiveness of this
option. However, we estimated the
annual cost of the monthly optical gas
imaging LDAR program at production
sites, gathering and boosting stations,
and transmission and storage facilities
to be $37,049, $86,135, and $45,080,
respectively, based on camera purchase,
or $32,693, $81,780, and $40,629,
respectively, based on camera rental.
Finally, we evaluated a fourth option
similar to the third option except that
the optical gas imaging would be
performed annually rather than
monthly. For this option, we estimated
the annual cost for production sites,
gathering and boosting stations, and
transmission and storage facilities to be
13 Because optical gas imaging is used to view
several pieces of equipment at a facility at once to
survey for leaks, options involving imaging are not
amenable to a component by component analysis.
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$30,740, $64,416, and $24,031,
respectively, based on camera purchase,
or $26,341, $60,017, and $19,493,
respectively, based on camera rental.
We request comment on the
applicability of a leak detection and
repair program based solely on the use
of optical imaging or other technologies.
Of most use to us would be information
on the effectiveness of advanced
measurement technologies to detect and
repair small leaks on the same order or
smaller as specified in the VVa
equipment leak requirements and the
effects of increased frequency of and
associated leak detection, recording, and
repair practices.
Based on the evaluation described
above, we believe that neither option 1
nor option 2 is cost effective for
reducing fugitive VOC emissions from
equipment leaks at sites, gathering and
boosting stations, and transmission and
storage facilities. For options 3 and 4,
we were unable to estimate their cost
effectiveness and, therefore, could not
identify either of these two options as
BSER for addressing equipment leak of
VOC at production facilities associated
with wellheads, at gathering and
boosting stations or at gas transmission
and storage facilities. We are, therefore,
not proposing NSPS for addressing VOC
emissions from equipment leaks at these
facilities.
5. What are the SSM provisions?
The EPA is proposing standards in
this rule that apply at all times,
including during periods of startup or
shutdown, and periods of malfunction.
In proposing the standards in this rule,
the EPA has taken into account startup
and shutdown periods.
The General Provisions in 40 CFR part
60 require facilities to keep records of
the occurrence and duration of any
startup, shutdown or malfunction (40
CFR 60.7(b)) and either report to the
EPA any period of excess emissions that
occurs during periods of SSM (40 CFR
60.7(c)(2)) or report that no excess
emissions occurred (40 CFR 60.7(c)(4)).
Thus, any comments that contend that
sources cannot meet the proposed
standard during startup and shutdown
periods should provide data and other
specifics supporting their claim.
Periods of startup, normal operations
and shutdown are all predictable and
routine aspects of a source’s operations.
However, by contrast, malfunction is
defined as a ‘‘sudden, infrequent, and
not reasonably preventable failure of air
pollution control and monitoring
equipment, process equipment or a
process to operate in a normal or usual
manner * * *’’ (40 CFR 60.2.) The EPA
has determined that malfunctions
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should not be viewed as a distinct
operating mode and, therefore, any
emissions that occur at such times do
not need to be factored into
development of CAA section 111
standards. Further, nothing in CAA
section 111 or in case law requires that
the EPA anticipate and account for the
innumerable types of potential
malfunction events in setting emission
standards. See, Weyerhaeuser v Costle,
590 F.2d 1011, 1058 (D.C. Cir. 1978)
(‘‘In the nature of things, no general
limit, individual permit, or even any
upset provision can anticipate all upset
situations. After a certain point, the
transgression of regulatory limits caused
by ‘uncontrollable acts of third parties,’
such as strikes, sabotage, operator
intoxication or insanity, and a variety of
other eventualities, must be a matter for
the administrative exercise of case-bycase enforcement discretion, not for
specification in advance by
regulation.’’), and, therefore, any
emissions that occur at such times do
not need to be factored into
development of CAA section 111
standards.
Further, it is reasonable to interpret
CAA section 111 as not requiring the
EPA to account for malfunctions in
setting emissions standards. For
example, we note that CAA section 111
provides that the EPA set standards of
performance which reflect the degree of
emission limitation achievable through
‘‘the application of the best system of
emission reduction’’ that the EPA
determines is adequately demonstrated.
Applying the concept of ‘‘the
application of the best system of
emission reduction’’ to periods during
which a source is malfunctioning
presents difficulties. The ‘‘application of
the best system of emission reduction’’
is more appropriately understood to
include operating units in such a way as
to avoid malfunctions.
Moreover, even if malfunctions were
considered a distinct operating mode,
we believe it would be impracticable to
take malfunctions into account in
setting CAA section 111 standards for
affected facilities under 40 CFR part 60,
subpart OOOO. As noted above, by
definition, malfunctions are sudden and
unexpected events and it would be
difficult to set a standard that takes into
account the myriad different types of
malfunctions that can occur across all
sources in the category. Moreover,
malfunctions can vary in frequency,
degree and duration, further
complicating standard setting.
In the event that a source fails to
comply with the applicable CAA section
111 standards as a result of a
malfunction event, the EPA would
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determine an appropriate response
based on, among other things, the good
faith efforts of the source to minimize
emissions during malfunction periods,
including preventative and corrective
actions, as well as root cause analyses
to ascertain and rectify excess
emissions. The EPA would also
consider whether the source’s failure to
comply with the CAA section 111
standard was, in fact, ‘‘sudden,
infrequent, not reasonably preventable’’
and was not instead ‘‘caused in part by
poor maintenance or careless
operation.’’ 40 CFR 60.2 (definition of
malfunction).
Finally, the EPA recognizes that even
equipment that is properly designed and
maintained can sometimes fail. Such
failure can sometimes cause an
exceedance of the relevant emission
standard (See, e.g., State
Implementation Plans: Policy Regarding
Excessive Emissions During
Malfunctions, Startup, and Shutdown
(September 20, 1999); Policy on Excess
Emissions During Startup, Shutdown,
Maintenance, and Malfunctions
(February 15, 1983)). The EPA is,
therefore, proposing to add an
affirmative defense to civil penalties for
exceedances of emission limits that are
caused by malfunctions. See 40 CFR
60.41Da (defining ‘‘affirmative defense’’
to mean, in the context of an
enforcement proceeding, a response or
defense put forward by a defendant,
regarding which the defendant has the
burden of proof and the merits of which
are independently and objectively
evaluated in a judicial or administrative
proceeding). We also are proposing
other regulatory provisions to specify
the elements that are necessary to
establish this affirmative defense; the
source must prove by a preponderance
of the evidence that it has met all of the
elements set forth in 40 CFR 60.46Da.
(See 40 CFR 22.24). These criteria
ensure that the affirmative defense is
available only where the event that
causes an exceedance of the emission
limit meets the narrow definition of
malfunction in 40 CFR 60.2 (sudden,
infrequent, not reasonably preventable
and not caused by poor maintenance
and or careless operation). For example,
to successfully assert the affirmative
defense, the source must prove by a
preponderance of the evidence that
excess emissions ‘‘[w]ere caused by a
sudden, infrequent, and unavoidable
failure of air pollution control and
monitoring equipment, process
equipment, or a process to operate in a
normal or usual manner * * *’’ The
criteria also are designed to ensure that
steps are taken to correct the
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malfunction, to minimize emissions in
accordance with 40 CFR 60.40Da and to
prevent future malfunctions. For
example, the source would have to
prove by a preponderance of the
evidence that ‘‘[r]epairs were made as
expeditiously as possible when the
applicable emission limitations were
being exceeded * * *’’ and that ‘‘[a]ll
possible steps were taken to minimize
the impact of the excess emissions on
ambient air quality, the environment
and human health * * *’’ In any
judicial or administrative proceeding,
the Administrator may challenge the
assertion of the affirmative defense and,
if the respondent has not met the
burden of proving all of the
requirements in the affirmative defense,
appropriate penalties may be assessed
in accordance with CAA section 113
(see also 40 CFR part 22.77).
VII. Rationale for Proposed Action for
NESHAP
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
A. What data were used for the NESHAP
analyses?
To perform the technology review and
residual risk analysis for the two
NESHAP, we created a comprehensive
dataset (i.e., the MACT dataset). This
dataset was based on the EPA’s 2005
National Emissions Inventory (NEI). The
NEI database contains information about
sources that emit criteria air pollutants
and their precursors and HAP. The
database includes estimates of annual
air pollutant emissions from point,
nonpoint and mobile sources in the 50
states, the District of Columbia, Puerto
Rico and the Virgin Islands. The EPA
collects information about sources and
releases an updated version of the NEI
database every 3 years.
The NEI database is compiled from
these primary sources:
• Emissions inventories compiled by
state and local environmental
agencies
• Databases related to the EPA’s MACT
programs
• Toxics Release Inventory data
• For electric generating units, the
EPA’s Emission Tracking System/
CEM data and United States
Department of Energy (DOE) fuel use
data
• For onroad sources, the United States
Federal Highway Administration’s
estimate of vehicle miles traveled and
emission factors from the EPA’s
MOBILE computer model
• For nonroad sources, the EPA’s
NONROAD computer model
• Emissions inventories from previous
years, if states do not submit current
data
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To concentrate on only records
pertaining to the oil and natural gas
industry sector, data were extracted
using two criteria. First, we specified
that all facilities containing codes
identifying the Oil and Natural Gas
Production and the Natural Gas
Transmission and Storage MACT source
categories (MACT codes 0501 and 0504,
respectively). Second, we extracted
facilities identified with the following
NAICS codes: 211 * * * (Oil and Gas
Extraction), 221210 (Natural Gas
Distribution), 4861 * * * (Pipeline
Transportation of Crude Oil), and 4862
* * * (Pipeline Transportation of
Natural Gas). Once the data were
extracted, we reviewed the Source
Classification Codes (SCC) to assess
whether there were any records
included in the dataset that were clearly
not a part of the oil and natural gas
sector. Our review of the SCC also
included assigning each SCC to an
‘‘Emission Process Group’’ that
represents emission point types within
the oil and natural gas sector.
Since these MACT standards only
apply to major sources, only facilities
designated as major sources in the NEI
were extracted. In the NEI, sources are
identified as major if the facility-wide
emissions are greater than 10 tpy for any
single HAP or 25 tpy for any
combination of HAP. We believe that
this may overestimate the number of
major sources in the oil and natural gas
sector because it does not take into
account the limitations set forth in the
CAA regarding aggregation of emissions
from wells and associated equipment in
determining major source status.
The final dataset contained a total of
1,311 major sources in the oil and
natural gas sector; 990 in Oil and
Natural Gas Production, and 321 in
Natural Gas Transmission and Storage.
To assess how representative this
number of facilities was, we obtained
information on the number of subject
facilities for both MACT standards from
the Enforcement and Compliance
History Online (ECHO) database. The
ECHO database is a web-based tool
(https://www.epa-echo.gov/echo/
index.html) that provides public access
to compliance and enforcement
information for approximately 800,000
EPA-regulated facilities. The ECHO
database allows users to find permit,
inspection, violation, enforcement
action and penalty information covering
the past 3 years. The site includes
facilities regulated as CAA stationary
sources, as well as Clean Water Act
direct dischargers, and Resource
Conservation and Recovery Act
hazardous waste generators/handlers.
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The data in the ECHO database are
updated monthly.
We performed a query on the ECHO
database requesting records for major
sources, with NAICS codes 211*,
221210, 4861* and 4862*, with
information for MACT. The ECHO
database query identified records for a
total of 555 facilities, 269 in the Oil and
Natural Gas Production source category
(NAICS 211* and 221210) and 286 in
the Natural Gas Transmission and
Storage source category (NAICS 4861*
and 4862*). This comparison leads us to
conclude that, for the Natural Gas
Transmission and Storage segment, the
NEI database is representative of the
number of sources subject to the rule.
For the Oil and Natural Gas Production
source category, it confirms our
assumption that the NEI dataset
contains more facilities than are subject
to the rule. However, this provides a
conservative overestimate of the number
of sources, which we believe is
appropriate for our risk analyses.
We are requesting that the public
provide a detailed review of the
information in this dataset and provide
comments and updated information
where appropriate. Section X of this
preamble provides an explanation of
how to provide updated information for
these datasets.
B. What are the proposed decisions
regarding certain unregulated emissions
sources?
In addition to actions relative to the
technology review and risk reviews
discussed below, we are proposing,
pursuant to CAA sections 112(d)(2) and
(3), MACT standards for glycol
dehydrators and storage vessels for
which standards were not previously
developed. We are also proposing
changes that affect the definition of
‘‘associated equipment’’ which could
apply these MACT standards to
previously unregulated sources.
1. Glycol Dehydrators
Once natural gas has been separated
from any liquid materials or products
(e.g., crude oil, condensate or produced
water), residual entrained water is
removed from the natural gas by
dehydration. Dehydration is necessary
because water vapor may form hydrates,
which are ice-like structures, and can
cause corrosion in or plug equipment
lines. The most widely used natural gas
dehydration processes are glycol
dehydration and solid desiccant
dehydration. Solid desiccant
dehydration, which is typically only
used for lower throughputs, uses
adsorption to remove water and is not
a source of HAP emissions.
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Glycol dehydration is an absorption
process in which a liquid absorbent,
glycol, directly contacts the natural gas
stream and absorbs any entrained water
vapor in a contact tower or absorption
column. The majority of glycol
dehydration units use triethylene glycol
as the absorbent, but ethylene glycol
and diethylene glycol are also used. The
rich glycol, which has absorbed water
vapor from the natural gas stream,
leaves the bottom of the absorption
column and is directed either to (1) a
gas condensate glycol (GCG) separator
(flash tank) and then a reboiler or (2)
directly to a reboiler where the water is
boiled off of the rich glycol. The
regenerated glycol (lean glycol) is
circulated, by pump, into the absorption
tower. The vapor generated in the
reboiler is directed to the reboiler vent.
The reboiler vent is a source of HAP
emissions. In the glycol contact tower,
glycol not only absorbs water, but also
absorbs selected hydrocarbons,
including BTEX and n-hexane. The
hydrocarbons are boiled off along with
the water in the reboiler and vented to
the atmosphere or to a control device.
The most commonly used control
device is a condenser. Condensers not
only reduce emissions, but also recover
condensable hydrocarbon vapors that
can be recovered and sold. In addition,
the dry non-condensable off-gas from
the condenser may be used as fuel or
recycled into the production process or
directed to a flare, incinerator or other
combustion device.
If present, the GCG separator (flash
tank) is also a potential source of HAP
emissions. Some glycol dehydration
units use flash tanks prior to the reboiler
to separate entrained gases, primarily
methane and ethane from the glycol.
The flash tank off-gases are typically
recovered as fuel or recycled to the
natural gas production header.
However, the flash tank may also be
vented directly to the atmosphere. Flash
tanks typically enhance the reboiler
condenser’s emission reduction
efficiency by reducing the concentration
of non-condensable gases present in the
stream prior to being introduced into
the condenser.
In the development of the MACT
standards for the two oil and natural gas
source categories, the EPA created two
subcategories of glycol dehydrators
based on actual annual average natural
gas flowrate and actual average benzene
emissions. Under 40 CFR part 63,
subpart HH, (the Oil and Natural Gas
Production NESHAP), the EPA
established MACT standards for glycol
dehydration units with an actual annual
average natural gas flowrate greater than
or equal to 85,000 scmd and actual
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average benzene emissions greater than
or equal to 0.90 Mg/yr (40 CFR
63.765(a)). The EPA did not establish
standards for the other subcategory,
which consists of glycol dehydration
units that are below the flowrate and
emission thresholds specified in subpart
HH. Similarly, under 40 CFR part 63,
subpart HHH (the Natural Gas
Transmission and Storage NESHAP), the
EPA established MACT standards for
the subcategory of glycol dehydration
units with an actual annual average
natural gas flowrate greater than or
equal to 283,000 scmd and actual
average benzene emissions greater than
or equal to 0.90 Mg/yr, but did not
establish standards for the other
subcategory, which consists of glycol
dehydration units that are below the
flowrate and emission thresholds
specified in subpart HHH. As
mentioned above, we refer to these
unregulated dehydration units in both
subparts HH and HHH as ‘‘small
dehydrators’’ in this proposed rule.
The EPA is proposing emission
standards for these subcategories of
small dehydrators (i.e., those
dehydrators with an actual annual
average natural gas flowrate less than
85,000 scmd at production sites or
283,000 scmd at natural gas
transmission and storage sites, or actual
average benzene emissions less than 0.9
Mg/yr). Because we do not have any
new emissions data concerning these
emission points, we evaluated the
dataset collected from industry during
the development of the original MACT
standards (legacy docket A–94–04, item
II–B–01, disk 1 for oil and natural gas
production facilities; and items IV–G–
24, 26, 27, 30 and 31 for natural gas
transmission and storage facilities). We
believe this dataset is representative of
currently operating glycol dehydrators
because it contains information for a
varied group of sources (i.e., units
owned by different companies, located
in different states, representing a range
of gas compositions and emission
controls) and that the processes have
not changed significantly since the data
were collected.
In the Oil and Natural Gas Production
source category, there were 91 glycol
dehydration units with throughput and
emissions data identified that would be
classified as small glycol dehydration
units. We evaluated the possibility of
establishing a MACT floor as a Mg/yr
limit. However, due to variability of gas
throughput and inlet gas composition,
we could not properly identify the best
performing units by only considering
emissions. To allow us to normalize the
emissions for a more accurate
determination of the best performing
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sources, we created an emission factor
in terms of grams BTEX/scm-ppmv for
each facility. The emission factor
reflects the facility’s emission level,
taking into consideration its natural gas
throughput and inlet natural gas BTEX
concentration. To determine the MACT
floor for the existing dehydrators, we
ranked each unit from lowest to highest,
based on their emission factor, to
determine the facilities in the top 12
percent of the dataset. The MACT floor
was an emission factor of 1.10 × 10¥4
grams BTEX/scm-ppmv. To meet this
level of emissions, we anticipate that
sources will use a variety of options,
including, but not limited to, routing
emissions to a condenser or to a
combustion device.
We also considered beyond-the-floor
options for the existing sources, as
required by section 112(d)(2) of the
CAA. To achieve further reductions
beyond the MACT floor level of control,
sources would have to install an
additional add-on control device, most
likely a combustion device. Assuming
the MACT floor control device is a
combustion device, which generally
achieves at least a 95-percent HAP
reduction, then less than 5 percent of
the initial HAP emissions remain.
Installing a second device would
involve the same costs as the first
control, but would only achieve 1⁄20 of
the reduction (i.e., reducing the
remaining 5 percent by another 95
percent represents a 4.49-percent
reduction of the initial, uncontrolled
emissions, which is 1⁄20 of the 95percent reduction achieved with the
first control). Based on the $8,360/Mg
cost effectiveness of the floor level of
control, we estimate that the
incremental cost effectiveness of the
second control to be $167,200/Mg. We
do not believe this cost to be reasonable
given the level of emission reduction.
We are, therefore, proposing an
emission standard for existing small
dehydrators that reflects the MACT
floor.
For new small glycol dehydrators in
the Oil and Natural Gas Production
source category, based on our
performance ranking, the best
performing source has an emission
factor of 4.66 × 10¥6 grams BTEX/scmppmv. To meet this level of emissions,
we anticipate that sources will use a
variety of options, including, but not
limited to, routing emissions to a
condenser or to a combustion device.
The consideration of beyond-the-floor
options for new small dehydrators
would be the same as for existing small
dehydrators, and, as stated above, we do
not believe a cost of $167,200/Mg to be
reasonable given the level of emission
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reduction. We are, therefore, proposing
a MACT standard for new small
dehydrators that reflects the MACT floor
level of control.
Under our proposal, a small
dehydrator’s actual MACT emission
limit would be determined by
multiplying the MACT floor emission
factor in g BTEX/scm-ppmv by its unitspecific incoming natural gas
throughput and BTEX concentration for
the dehydrator. A formula is provided
in 40 CFR 63.765(b)(1)(iii) to calculate
the MACT limit as an annual value.
In the Natural Gas Transmission and
Storage source category, there were 16
facilities for which throughput and
emissions data were available that
would be classified as small glycol
dehydration units. Since the number of
units was less than 30, the MACT floor
for existing sources was based on the
top five performing units. Using the
same emission factor concept, we
determined that the MACT floor for
existing sources is an emission factor
equal to 6.42 × 10¥5 grams BTEX/scmppmv. To meet this level of emissions,
we anticipate that sources will use a
variety of options, including, but not
limited to, routing emissions to a
condenser or to a combustion device.
We also considered beyond-the-floor
options for the existing small
dehydrators as required by section
112(d)(2) of the CAA. To achieve further
reductions beyond the MACT floor level
of control, sources would have to install
an additional add-on control device,
most likely a combustion device.
Assuming the MACT floor control
device is a combustion device, which
generally achieves at least a 95-percent
HAP reduction, then less than 5 percent
of the initial HAP emissions remain.
Installing a second device would
involve the same costs as the first
control device, but would only achieve
1⁄20 of the reduction (i.e., reducing the
remaining 5 percent by another 95
percent represents a 4.49-percent
reduction of the initial, uncontrolled
emissions, which is 1⁄20 of the 95percent reduction achieved with the
first control). Based on the $1,650/Mg
cost effectiveness of the floor level of
control, we estimate that the
incremental cost effectiveness of the
second control to be $33,000/Mg. We do
not believe this cost to be reasonable
given the level of emission reduction.
We are, therefore, proposing an
emission standard for existing small
dehydrators that reflects the MACT
floor.
For new small glycol dehydrators,
based on our performance ranking, the
best performing source has an emission
factor of 1.10 × 10¥5 grams BTEX/scm-
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ppmv. To meet this level of emissions,
we anticipate that sources will use a
variety of options, including, but not
limited to, routing emissions to a
condenser or to a combustion device.
The consideration of beyond-the-floor
options for new small dehydrators
would be the same as for existing small
dehydrators, and, as stated above, we do
not believe a cost of $33,000/Mg to be
reasonable given the level of emission
reduction. We are, therefore, proposing
an emission standard for new sources
that reflects the MACT floor level of
control.
Under our proposal, a source’s actual
MACT emissions limit would be
determined by multiplying this
emission factor by their unit-specific
incoming natural gas throughput and
BTEX concentration for the dehydrator.
A formula is provided in 40 CFR
63.1275(b)(1)(iii) to calculate the limit
as an annual value.
As discussed below, we are proposing
that, with the removal of the 1-ton
alternative compliance option from the
existing standards for glycol
dehydrators, the MACT for these two
source categories would provide an
ample margin of safety to protect public
health. We, therefore, maintain that,
after the implementation of the small
dehydrator standards discussed above,
these MACT will continue to provide an
ample margin of safety to protect public
health. Consequently, we do not believe
it will be necessary to conduct another
residual risk review under CAA section
112(f) for these two source categories 8
years following promulgation of the
small dehydrator standards merely due
to the addition of these new MACT
requirements.
2. Storage Vessels
Crude oil, condensate and produced
water are typically stored in fixed-roof
storage vessels. Some vessels used for
storing produced water may be open-top
tanks. These vessels, which are operated
at or near atmospheric pressure
conditions, are typically located at tank
batteries. A tank battery refers to the
collection of process components used
to separate, treat and store crude oil,
condensate, natural gas and produced
water. The extracted products from
productions wells enter the tank battery
through the production header, which
may collect product from many wells.
Emissions from storage vessels are a
result of working, breathing and flash
losses. Working losses occur due to the
emptying and filling of storage tanks.
Breathing losses are the release of gas
associated with daily temperature
fluctuations and other equilibrium
effects. Flash losses occur when a liquid
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with entrained gases is transferred from
a vessel with higher pressure to a vessel
with lower pressure, thus, allowing
entrained gases or a portion of the liquid
to vaporize or flash. In the oil and
natural gas production segment, flashing
losses occur when live crude oils or
condensates flow into a storage tank
from a processing vessel operated at a
higher pressure. Typically, the larger the
pressure drop, the more flashing
emission will occur in the storage stage.
Temperature of the liquid may also
influence the amount of flash emissions.
In the Oil and Natural Gas Production
NESHAP (40 CFR part 63, subpart HH),
the MACT standards for storage vessels
apply only to those with the PFE.
Storage vessels with the PFE are defined
as storage vessels that contain
hydrocarbon liquids that meet the
following criteria:
• A stock tank gas to oil ratio (GOR)
greater than or equal to 0.31 cubic
meters per liter (m3/liter); and
• An American Petroleum Institute
(API) gravity greater than or equal to 40
degrees; and
• An actual annual average
hydrocarbon liquid throughput greater
than or equal to 79,500 liters per day
(liter/day).
Accordingly, there is no emission
limit in the existing MACT for storage
vessels without the PFE. However, the
MACT analysis performed at the time
indicates that the MACT floor was based
on all storage vessels, not just those
vessels with flash emissions. See,
Recommendation of MACT Floor Levels
for HAP Emission Points at Major
Sources in the Oil and Natural Gas
Production Source Category, (September
23, 1997, Docket A–94–04, Item II–A–
07). We, therefore, propose to apply the
existing MACT for storage vessels with
PFE to all storage vessels (i.e., storage
vessels with the PFE, as well as those
without the PFE).
3. Definition of Associated Equipment
CAA section 112(n)(4)(A) provides:
Notwithstanding the provisions of
subsection (a), emissions from any oil or gas
exploration or production well (with its
associated equipment) and emission from
any pipeline compressor or pump station
shall not be aggregated with emissions from
other similar units, whether or not such units
are in contiguous area or under common
control, to determine whether such units or
stations are major sources.
As stated above, the CAA prevents
aggregation of HAP emissions from
wells and associated equipment in
making major source determinations. In
the absence of clear guidance in the
statute on what constitutes ‘‘associated
equipment,’’ the EPA sought to define
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‘‘associated equipment’’ in a way that
recognizes the need to implement relief
for this industry as Congress intended
and that also allow for the appropriate
regulation of significant emission
points. 64 FR at 32619. Accordingly, in
the existing Oil and Natural Gas
Production NESHAP (1998 and 1999
NESHAP), the EPA defined ‘‘associated
equipment’’ to exclude glycol
dehydration units and storage vessels
with PFE (thus allowing their emissions
to be included in determining major
source status) because EPA identified
these sources as substantial contributors
to HAP emissions. Id. EPA explained in
that NESHAP that, because a single
storage vessel with flash emissions may
emit several Mg of HAP per year and
individual glycol dehydrators may emit
above the major source level, storage
vessels with PFE and glycol dehydrators
are large individual sources of HAP, 63
FR 6288, 6301 (1998). The EPA
therefore considered these emission
sources substantial contributors to HAP
emissions and excluded them from the
definition of ‘‘associated equipment.’’
64 FR at 32619. We have recently
examined HAP emissions from storage
vessels without flash emissions and
found that these emissions are
significant and comparable to those
vessels with flash emissions. For
example, one storage vessel with an API
gravity of 30 degrees and a GOR of 2.09
× 10¥3 m3/liter with a throughput of
79,500 liter/day had HAP emissions of
9.91 Mg/yr, including 9.45 Mg/yr of nhexane.
Because storage vessels without the
PFE can have significant emissions at
levels that are comparable to emissions
from storage vessels with the PFE, there
is no appreciable difference between
storage vessels with the PFE and those
without the PFE for purposes of
defining ‘‘associated equipment.’’ We
are, therefore, proposing to amend the
associated equipment definition to
exclude all storage vessels and not just
storage vessels with the PFE.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
C. How did we perform the risk
assessment and what are the results and
proposed decisions?
1. How did we estimate risks posed by
the source categories?
The EPA conducted risk assessments
that provided estimates for each source
in a category of the MIR posed by the
HAP emissions, the HI for chronic
exposures to HAP with the potential to
cause noncancer health effects, and the
hazard quotient (HQ) for acute
exposures to HAP with the potential to
cause noncancer health effects. The
assessments also provided estimates of
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the distribution of cancer risks within
the exposed populations, cancer
incidence and an evaluation of the
potential for adverse environmental
effects for each source category. The risk
assessments consisted of seven primary
steps, as discussed below. The docket
for this rulemaking contains the
following document which provides
more information on the risk assessment
inputs and models: Draft Residual Risk
Assessment for the Oil and Gas
Production and Natural Gas
Transmission and Storage Source
Categories. The methods used to assess
risks (as described in the seven primary
steps below) are consistent with those
peer-reviewed by a panel of the EPA’s
Science Advisory Board (SAB) in 2009
and described in their peer review
report issued in 2010 14; they are also
consistent with the key
recommendations contained in that
report.
a. Establishing the Nature and
Magnitude of Actual Emissions and
Identifying the Emissions Release
Characteristics
As discussed in section VII.A of this
preamble, we used a dataset based on
the 2005 NEI as the basis for the risk
assessment. In addition to the quality
assurance (QA) of the facilities
contained in the dataset, we also
checked the coordinates of every facility
in the dataset through visual
observations using tools such as
GoogleEarth and ArcView. Where
coordinates were found to be incorrect,
we identified and corrected them to the
extent possible. We also performed QA
of the emissions data and release
characteristics to ensure there were no
outliers.
We discussed the use of both MACTallowable and actual emissions in the
final Coke Oven Batteries residual risk
rule (70 FR 19998–19999, April 15,
2005) and in the proposed and final
Hazardous Organic NESHAP residual
risk rules (71 FR 34428, June 14, 2006,
and 71 FR 76609, December 21, 2006,
respectively). In those previous actions,
we noted that assessing the risks at the
MACT-allowable level is inherently
reasonable since these risks reflect the
maximum level sources could emit and
still comply with national emission
standards. But we also explained that it
is reasonable to consider actual
emissions, where such data are
available, in both steps of the risk
analysis, in accordance with the
Benzene NESHAP. (54 FR 38044,
September 14, 1989.)
To estimate emissions at the MACTallowable level, we developed a ratio of
MACT-allowable to actual emissions for
each emissions source type in each
source category, based on the level of
control required by the MACT standards
compared to the level of reported actual
emissions and available information on
the level of control achieved by the
emissions controls in use.
b. Establishing the Relationship
Between Actual Emissions and MACTAllowable Emissions Levels
The available emissions data in the
MACT dataset represent the estimates of
mass of emissions actually emitted
during the specified annual time period.
These ‘‘actual’’ emission levels are often
lower than the emission levels that a
facility might be allowed to emit and
still comply with the MACT standards.
The emissions level allowed to be
emitted by the MACT standards is
referred to as the ‘‘MACT-allowable’’
emissions level. This represents the
highest emissions level that could be
emitted by the facility without violating
the MACT standards.
c. Conducting Dispersion Modeling,
Determining Inhalation Exposures and
Estimating Individual and Population
Inhalation Risks
Both long-term and short-term
inhalation exposure concentrations and
health risks from each source in the
source categories addressed in this
proposal were estimated using the
Human Exposure Model (HEM)
(Community and Sector HEM–3 version
1.1.0). The HEM–3 performs three
primary risk assessment activities:
(1) Conducting dispersion modeling to
estimate the concentrations of HAP in
ambient air, (2) estimating long-term
and short-term inhalation exposures to
individuals residing within 50 km of the
modeled sources and (3) estimating
individual and population-level
inhalation risks using the exposure
estimates and quantitative doseresponse information.
The dispersion model used by HEM–
3 is AERMOD, which is one of the
EPA’s preferred models for assessing
pollutant concentrations from industrial
facilities.15 To perform the dispersion
modeling and to develop the
preliminary risk estimates, HEM–3
draws on three data libraries. The first
is a library of meteorological data,
14 U.S. EPA SAB. Risk and Technology Review
(RTR) Risk Assessment Methodologies: For Review
by the EPA’s Science Advisory Board with Case
Studies—MACT I Petroleum Refining Sources and
Portland Cement Manufacturing, May 2010.
15 U.S. EPA. Revision to the Guideline on Air
Quality Models: Adoption of a Preferred General
Purpose (Flat and Complex Terrain) Dispersion
Model and Other Revisions (70 FR 68218,
November 9, 2005).
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which is used for dispersion
calculations. This library includes
1 year of hourly surface and upper air
observations for more than 158
meteorological stations, selected to
provide coverage of the United States
and Puerto Rico. A second library of
United States Census Bureau census
block 16 internal point locations and
populations provides the basis of
human exposure calculations (Census,
2000). In addition, for each census
block, the census library includes the
elevation and controlling hill height,
which are also used in dispersion
calculations. A third library of pollutant
unit risk factors and other health
benchmarks is used to estimate health
risks. These risk factors and health
benchmarks are the latest values
recommended by the EPA for HAP and
other toxic air pollutants. These values
are available at https://www.epa.gov/ttn/
atw/toxsource/summary.html and are
discussed in more detail later in this
section.
In developing the risk assessment for
chronic exposures, we used the
estimated annual average ambient air
concentration of each of the HAP
emitted by each source for which we
have emissions data in the source
category. The air concentrations at each
nearby census block centroid were used
as a surrogate for the chronic inhalation
exposure concentration for all the
people who reside in that census block.
We calculated the MIR for each facility
as the cancer risk associated with a
continuous lifetime (24 hours per day,
7 days per week, and 52 weeks per year
for a 70-year period) exposure to the
maximum concentration at the centroid
of an inhabited census block. Individual
cancer risks were calculated by
multiplying the estimated lifetime
exposure to the ambient concentration
of each of the HAP (in micrograms per
cubic meter) by its unit risk estimate
(URE), which is an upper bound
estimate of an individual’s probability
of contracting cancer over a lifetime of
exposure to a concentration of 1
microgram of the pollutant per cubic
meter of air. For residual risk
assessments, we generally use URE
values from the EPA’s Integrated Risk
Information System (IRIS). For
carcinogenic pollutants without the EPA
IRIS values, we look to other reputable
sources of cancer dose-response values,
often using California EPA (CalEPA)
URE values, where available. In cases
where new, scientifically credible doseresponse values have been developed in
16 A census block is generally the smallest
geographic area for which census statistics are
tabulated.
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a manner consistent with the EPA
guidelines and have undergone a peer
review process similar to that used by
the EPA, we may use such doseresponse values in place of or in
addition to other values, if appropriate.
Formaldehyde is a unique case. In
2004, the EPA determined that the
Chemical Industry Institute of
Toxicology (CIIT) cancer dose-response
value for formaldehyde (5.5 × 10¥9 per
μg/m3) was based on better science than
the IRIS cancer dose-response value
(1.3 × 10¥5 per μg/m3) and we switched
from using the IRIS value to the CIIT
value in risk assessments supporting
regulatory actions. However, subsequent
research published by the EPA suggests
that the CIIT model was not appropriate
and in 2010 the EPA returned to using
the 1991 IRIS value, which is more
health protective.17 The EPA has been
working on revising the formaldehyde
IRIS assessment and the National
Academy of Sciences (NAS) completed
its review of the EPA’s draft in May of
2011. EPA is reviewing the public
comments and the NAS independent
scientific peer review, and the draft IRIS
assessment will be revised and the final
assessment will be posted on the IRIS
database. In the interim, we will present
findings using the 1991 IRIS value as a
primary estimate, and may also consider
other information as the science
evolves.
In the case of benzene, the high end
of the reported cancer URE range was
used in our assessments to provide a
conservative estimate of potential
cancer risks. Use of the high end of the
range provides risk estimates that are
approximately 3.5 times higher than use
of the equally-plausible low end value.
We also evaluated the impact of using
the low end of the URE range on our
risk results.
We also note that polycyclic organic
matter (POM), a carcinogenic HAP with
a mutagenic mode of action, is emitted
by some of the facilities in these two
categories.18 For this compound
group,19 the age-dependent adjustment
factors (ADAF) described in the EPA’s
Supplemental Guidance for Assessing
Susceptibility from Early-Life Exposure
17 For details on the justification for this decision,
see the memorandum in the docket from Peter
Preuss to Steve Page entitled, Recommendation for
Formaldehyde Inhalation Cancer Risk Values,
January 22, 2010.
18 U.S. EPA. Performing risk assessments that
include carcinogens described in the Supplemental
Guidance as having a mutagenic mode of action.
Science Policy Council Cancer Guidelines
Implementation Work Group Communication II:
Memo from W.H. Farland, dated October 4, 2005.
19 See the Risk Assessment for Source Categories
document available in the docket for a list of HAP
with a mutagenic mode of action.
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to Carcinogens 20 were applied. This
adjustment has the effect of increasing
the estimated lifetime risks for POM by
a factor of 1.6. In addition, although
only a small fraction of the total POM
emissions were not reported as
individual compounds, the EPA
expresses carcinogenic potency for
compounds in this group in terms of
benzo[a]pyrene equivalence, based on
evidence that carcinogenic POM has the
same mutagenic mechanism of action as
benzo[a]pyrene. For this reason, the
EPA’s Science Policy Council 21
recommends applying the Supplemental
Guidance to all carcinogenic polycyclic
aromatic hydrocarbons for which risk
estimates are based on relative potency.
Accordingly, we have applied the ADAF
to the benzo[a]pyrene equivalent
portion of all POM mixtures.
Incremental individual lifetime
cancer risks associated with emissions
from the source category were estimated
as the sum of the risks for each of the
carcinogenic HAP (including those
classified as carcinogenic to humans,
likely to be carcinogenic to humans and
suggestive evidence of carcinogenic
potential 22) emitted by the modeled
source. Cancer incidence and the
distribution of individual cancer risks
for the population within 50 km of any
source were also estimated for the
source category as part of these
assessments by summing individual
risks. A distance of 50 km is consistent
with both the analysis supporting the
1989 Benzene NESHAP (54 FR 38044)
and the limitations of Gaussian
dispersion models, including AERMOD.
To assess risk of noncancer health
effects from chronic exposures, we
summed the HQ for each of the HAP
that affects a common target organ
system to obtain the HI for that target
organ system (or target organ-specific
HI, TOSHI). The HQ for chronic
exposures is the estimated chronic
20 U.S. EPA. Supplemental Guidance for
Assessing Early-Life Exposure to Carcinogens. EPA/
630/R–03/003F, 2005. https://www.epa.gov/ttn/atw/
childrens_supplement_final.pdf.
21 U.S. EPA. Science Policy Council Cancer
Guidelines Implementation Workgroup
Communication II: Memo from W.H. Farland, dated
June 14, 2006.
22 These classifications also coincide with the
terms ‘‘known carcinogen, probable carcinogen and
possible carcinogen,’’ respectively, which are the
terms advocated in the EPA’s previous Guidelines
for Carcinogen Risk Assessment, published in 1986
(51 FR 33992, September 24, 1986). Summing the
risks of these individual compounds to obtain the
cumulative cancer risks is an approach that was
recommended by the EPA’s SAB in their 2002 peer
review of EPA’s NATA entitled, NATA—Evaluating
the National-scale Air Toxics Assessment 1996
Data—an SAB Advisory, available at: https://
yosemite.epa.gov/sab/sabproduct.nsf/
214C6E915BB04E14852570CA007A682C/$File/
ecadv02001.pdf.
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exposure divided by the chronic
reference level, which is either the EPA
reference concentration (RfC), defined
as ‘‘an estimate (with uncertainty
spanning perhaps an order of
magnitude) of a continuous inhalation
exposure to the human population
(including sensitive subgroups) that is
likely to be without an appreciable risk
of deleterious effects during a lifetime,’’
or, in cases where an RfC from the
EPA’s IRIS database is not available, the
EPA will utilize the following
prioritized sources for our chronic doseresponse values: (1) The Agency for
Toxic Substances and Disease Registry
Minimum Risk Level, which is defined
as ‘‘an estimate of daily human
exposure to a substance that is likely to
be without an appreciable risk of
adverse effects (other than cancer) over
a specified duration of exposure’’; (2)
the CalEPA Chronic Reference Exposure
Level (REL), which is defined as ‘‘the
concentration level at or below which
no adverse health effects are anticipated
for a specified exposure duration’’; and
(3), as noted above, in cases where
scientifically credible dose-response
values have been developed in a manner
consistent with the EPA guidelines and
have undergone a peer review process
similar to that used by the EPA, we may
use those dose-response values in place
of or in concert with other values.
Screening estimates of acute
exposures and risks were also evaluated
for each of the HAP at the point of
highest off-site exposure for each facility
(i.e., not just the census block
centroids), assuming that a person is
located at this spot at a time when both
the peak (hourly) emission rate and
worst-case dispersion conditions (1991
calendar year data) occur. The acute HQ
is the estimated acute exposure divided
by the acute dose-response value. In
each case, acute HQ values were
calculated using best available, shortterm dose-response values. These acute
dose-response values, which are
described below, include the acute REL,
acute exposure guideline levels (AEGL)
and emergency response planning
guidelines (ERPG) for 1-hour exposure
durations. As discussed below, we used
conservative assumptions for emission
rates, meteorology and exposure
location for our acute analysis.
As described in the CalEPA’s Air
Toxics Hot Spots Program Risk
Assessment Guidelines, Part I, The
Determination of Acute Reference
Exposure Levels for Airborne Toxicants,
an acute REL value (https://
www.oehha.ca.gov/air/pdf/acuterel.pdf)
is defined as ‘‘the concentration level at
or below which no adverse health
effects are anticipated for a specified
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exposure duration.’’ Acute REL values
are based on the most sensitive,
relevant, adverse health effect reported
in the medical and toxicological
literature. Acute REL values are
designed to protect the most sensitive
individuals in the population by the
inclusion of margins of safety. Since
margins of safety are incorporated to
address data gaps and uncertainties,
exceeding the acute REL does not
automatically indicate an adverse health
impact.
AEGL values were derived in
response to recommendations from the
National Research Council (NRC). As
described in Standing Operating
Procedures (SOP) of the National
Advisory Committee on Acute Exposure
Guideline Levels for Hazardous
Substances (https://www.epa.gov/
opptintr/aegl/pubs/sop.pdf),23 ‘‘the
NRC’s previous name for acute exposure
levels—community emergency exposure
levels—was replaced by the term AEGL
to reflect the broad application of these
values to planning, response, and
prevention in the community, the
workplace, transportation, the military,
and the remediation of Superfund
sites.’’ This document also states that
AEGL values ‘‘represent threshold
exposure limits for the general public
and are applicable to emergency
exposures ranging from 10 minutes to
eight hours.’’ The document lays out the
purpose and objectives of AEGL by
stating (page 21) that ‘‘the primary
purpose of the AEGL program and the
National Advisory Committee for Acute
Exposure Guideline Levels for
Hazardous Substances is to develop
guideline levels for once-in-a-lifetime,
short-term exposures to airborne
concentrations of acutely toxic, highpriority chemicals.’’ In detailing the
intended application of AEGL values,
the document states (page 31) that ‘‘[i]t
is anticipated that the AEGL values will
be used for regulatory and
nonregulatory purposes by U.S. Federal
and state agencies and possibly the
international community in conjunction
with chemical emergency response,
planning, and prevention programs.
More specifically, the AEGL values will
be used for conducting various risk
assessments to aid in the development
of emergency preparedness and
prevention plans, as well as real-time
emergency response actions, for
accidental chemical releases at fixed
facilities and from transport carriers.’’
The AEGL–1 value is then specifically
defined as ‘‘the airborne concentration
of a substance above which it is
predicted that the general population,
including susceptible individuals, could
experience notable discomfort,
irritation, or certain asymptomatic
nonsensory effects. However, the effects
are not disabling and are transient and
reversible upon cessation of exposure.’’
The document also notes (page 3) that,
‘‘Airborne concentrations below AEGL–
1 represent exposure levels that can
produce mild and progressively
increasing but transient and
nondisabling odor, taste, and sensory
irritation or certain asymptomatic,
nonsensory effects.’’ Similarly, the
document defines AEGL–2 values as
‘‘the airborne concentration (expressed
as ppm or mg/m3) of a substance above
which it is predicted that the general
population, including susceptible
individuals, could experience
irreversible or other serious, long-lasting
adverse health effects or an impaired
ability to escape.’’
ERPG values are derived for use in
emergency response, as described in the
American Industrial Hygiene
Association’s document entitled,
Emergency Response Planning
Guidelines (ERPG) Procedures and
Responsibilities (https://www.aiha.org/
1documents/committees/
ERPSOPs2006.pdf) which states that,
‘‘Emergency Response Planning
Guidelines were developed for
emergency planning and are intended as
health based guideline concentrations
for single exposures to chemicals.’’ 24
The ERPG–1 value is defined as ‘‘the
maximum airborne concentration below
which it is believed that nearly all
individuals could be exposed for up to
1 hour without experiencing other than
mild transient adverse health effects or
without perceiving a clearly defined,
objectionable odor.’’ Similarly, the
ERPG–2 value is defined as ‘‘the
maximum airborne concentration below
which it is believed that nearly all
individuals could be exposed for up to
1 hour without experiencing or
developing irreversible or other serious
health effects or symptoms which could
impair an individual’s ability to take
protective action.’’
As can be seen from the definitions
above, the AEGL and ERPG values
include the similarly-defined severity
levels 1 and 2. For many chemicals, a
severity level 1 value AEGL or ERPG has
not been developed; in these instances,
higher severity level AEGL–2 or ERPG–
2 values are compared to our modeled
23 NAS, 2001. Standing Operating Procedures for
Developing Acute Exposure Levels for Hazardous
Chemicals, page 2.
24 ERP Committee Procedures and
Responsibilities. November 1, 2006. American
Industrial Hygiene Association.
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exposure levels to screen for potential
acute concerns.
Acute REL values for 1-hour exposure
durations are typically lower than their
corresponding AEGL–1 and ERPG–1
values. Even though their definitions are
slightly different, AEGL–1 values are
often the same as the corresponding
ERPG–1 values, and AEGL–2 values are
often equal to ERPG–2 values.
Maximum HQ values from our acute
screening risk assessments typically
result when basing them on the acute
REL value for a particular pollutant. In
cases where our maximum acute HQ
value exceeds 1, we also report the HQ
value based on the next highest acute
dose-response value (usually the AEGL–
1 and/or the ERPG–1 value).
To develop screening estimates of
acute exposures, we developed
estimates of maximum hourly emission
rates by multiplying the average actual
annual hourly emission rates by a factor
to cover routinely variable emissions.
We chose the factor based on process
knowledge and engineering judgment
and with awareness of a Texas study of
short-term emissions variability, which
showed that most peak emission events,
in a heavily-industrialized 4-county area
(Harris, Galveston, Chambers and
Brazoria Counties, Texas) were less than
twice the annual average hourly
emission rate. The highest peak
emission event was 74 times the annual
average hourly emission rate, and the
99th percentile ratio of peak hourly
emission rate to the annual average
hourly emission rate was 9.25 This
analysis is provided in Appendix 4 of
the Draft Residual Risk Assessment for
the Oil and Gas Production and Natural
Gas Transmission and Storage Source
Categories, which is available in the
docket for this action. Considering this
analysis, unless specific process
knowledge or data are available to
provide an alternate value, to account
for more than 99 percent of the peak
hourly emissions, we apply a
conservative screening multiplication
factor of 10 to the average annual hourly
emission rate in these acute exposure
screening assessments. The factor of 10
was used for both the Oil and Natural
Gas Production and the Natural Gas
Transmission and Storage source
categories.
In cases where acute HQ values from
the screening step were less than or
equal to 1, acute impacts were deemed
negligible and no further analysis was
performed. In cases where an acute HQ
from the screening step was greater than
25 See https://www.tceq.state.tx.us/compliance/
field_ops/eer/ or docket to access the
source of these data.
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1, additional site-specific data were
considered to develop a more refined
estimate of the potential for acute
impacts of concern. The data
refinements employed for these source
categories consisted of using the sitespecific facility layout to distinguish
facility property from an area where the
public could be exposed. These
refinements are discussed in the draft
risk assessment document, which is
available in the docket for each of these
source categories. Ideally, we would
prefer to have continuous measurements
over time to see how the emissions vary
by each hour over an entire year. Having
a frequency distribution of hourly
emission rates over a year would allow
us to perform a probabilistic analysis to
estimate potential threshold
exceedances and their frequency of
occurrence. Such an evaluation could
include a more complete statistical
treatment of the key parameters and
elements adopted in this screening
analysis. However, we recognize that
having this level of data is rare, hence
our use of the multiplier approach.
To better characterize the potential
health risks associated with estimated
acute exposures to HAP, and in
response to a key recommendation from
the SAB’s peer review of the EPA’s RTR
risk assessment methodologies,26 we
generally examine a wider range of
available acute health metrics than we
do for our chronic risk assessments.
This is in response to the SAB’s
acknowledgement that there are
generally more data gaps and
inconsistencies in acute reference
values than there are in chronic
reference values. Comparisons of the
estimated maximum off-site 1-hour
exposure levels are not typically made
to occupational levels for the purpose of
characterizing public health risks in
RTR assessments. This is because they
are developed for working age adults
and are not generally considered
protective for the general public. We
note that occupational ceiling values
are, for most chemicals, set at levels
higher than a 1-hour AEGL–1.
As discussed in section VII.C.2 of this
preamble, the maximum estimated
worst-case 1-hour exposure to benzene
outside the facility fence line for a
facility in either source category is 12
mg/m3. This estimated exposure
exceeds the 6-hour REL by a factor of 9
(HQREL = 9), but is significantly below
the 1-hour AEGL–1 (HQAEGL–1 = 0.07).
Although this worst-case exposure
26 The SAB peer review of RTR Risk Assessment
Methodologies is available at: https://yosemite.epa.
gov/sab/sabproduct.nsf/4AB3966E263D943A852
5771F00668381/$File/EPA-SAB-10-007unsigned.pdf.
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estimate does not exceed the AEGL–1,
we note here that it slightly exceeds
workplace ceiling level guidelines
designed to protect the worker
population for short duration (<15
minute) increases in exposure to
benzene, as discussed below. The
occupational short-term exposure limit
(STEL) standard for benzene developed
by the Occupational Safety and Health
Administration is 16 mg/m3, ‘‘as
averaged over any 15-minute period.’’ 27
Occupational guideline STEL for
exposures to benzene have also been
developed by the American Conference
of Governmental Industrial Hygienists
(ACGIH) 28 for less than 15 minutes 29
(ACGIH threshold limit value (TLV)STEL value of 8.0 mg/m3), and by the
National Institute for Occupational
Safety and Health (NIOSH) 30 ‘‘for any
15 minute period in a work day’’
(NIOSH REL–STEL of 3.2 mg/m3). These
shorter duration occupational values
indicate potential concerns regarding
health effects at exposure levels below
the 1-hour AEGL–1 value. We solicit
comment on the use of the occupational
values described above in the
interpretation of these worst-case acute
screening exposure estimates.
d. Conducting Multi-Pathway Exposure
and Risk Modeling
The potential for significant human
health risks due to exposures via routes
other than inhalation (i.e., multipathway exposures) and the potential
for adverse environmental impacts were
evaluated in a three-step process. In the
first step, we determined whether any
facilities emitted any HAP known to be
PB–HAP (HAP known to be persistent
and bio-accumulative) in the
environment. There are 14 PB–HAP
compounds or compound classes
identified for this screening in the EPA’s
Air Toxics Risk Assessment Library
(available at https://www.epa.gov/ttn/
fera/risk_atra_vol1.html). They are
cadmium compounds, chlordane,
chlorinated dibenzodioxins and furans,
27 29 CFR 1910.1028, Benzene. Available online
at https://www.osha.gov/pls/oshaweb/owadisp.
show_document?p_table=STANDARDS&p_
id=10042.
28 ACGIH (2001) Benzene. In Documentation of
the TLVs® and BEIs® with Other Worldwide
Occupational Exposure Values. ACGIH, 1300
Kemper Meadow Drive, Cincinnati, OH 45240
(ISBN: 978–1–882417–74–2) and available online at
https://www.acgih.org.
29 The ACGIH definition of a TLV–STEL states
that ‘‘Exposures above the TLV–TWA up to the
TLV–STEL should be less than 15 minutes, should
occur no more than four times per day, and there
should be at least 60 minutes between successive
exposures in this range.’’
30 NIOSH. Occupational Safety and Health
Guideline for Benzene; https://www.cdc.gov/niosh/
74-137.html.
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dichlorodiphenyldichloroethylene,
heptachlor, hexachlorobenzene,
hexachlorocyclohexane, lead
compounds, mercury compounds,
methoxychlor, polychlorinated
biphenyls, POM, toxaphene and
trifluralin.
Since one or more of these PB–HAP
are emitted by at least one facility in
both source categories, we proceeded to
the second step of the evaluation. In this
step, we determined whether the
facility-specific emission rates of each of
the emitted PB–HAP were large enough
to create the potential for significant
non-inhalation human or environmental
risks under reasonable worst-case
conditions. To facilitate this step, we
have developed emission rate
thresholds for each PB–HAP using a
hypothetical worst-case screening
exposure scenario developed for use in
conjunction with the EPA’s TRIM.FaTE
model. The hypothetical screening
scenario was subjected to a sensitivity
analysis to ensure that its key design
parameters were established such that
environmental media concentrations
were not underestimated (i.e., to
minimize the occurrence of false
negatives or results that suggest that
risks might be acceptable when, in fact,
actual risks are high) and to also
minimize the occurrence of false
positives for human health endpoints.
We call this application of the
TRIM.FaTE model TRIM–Screen. The
facility-specific emission rates of each of
the PB–HAP in each source category
were compared to the TRIM–Screen
emission threshold values for each of
the PB–HAP identified in the source
category datasets to assess the potential
for significant human health risks or
environmental risks via non-inhalation
pathways.
There was only one facility in the
Natural Gas Transmission and Storage
source category with reported emissions
of PB–HAP, and the emission rates were
less than the emission threshold values.
There were 29 facilities in the Oil and
Natural Gas Production source category
with reported emissions of PB–HAP,
and one of these had emission rates
greater than the emission threshold
values. In this case, the emission
threshold value for POM was exceeded
by a factor of 6. For POM, dairy,
vegetables and fruits were the three
most dominant exposure pathways
driving human exposures in the
hypothetical screening exposure
scenario. The single facility with
emissions exceeding the emission
threshold value for POM is located in a
highly industrialized area. Therefore,
since the exposure pathways which
would drive high human exposure are
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not locally available, multi-pathway
exposures and environmental risks were
deemed negligible, and no further
analysis was performed. For further
information on the multi-pathway
analysis approach, see the residual risk
documentation.
e. Assessing Risks Considering
Emissions Control Options
In addition to assessing baseline
inhalation risks and screening for
potential multi-pathway risks, where
appropriate, we also estimated risks
considering the potential emission
reductions that would be achieved by
the particular control options under
consideration. In these cases, the
expected emissions reductions were
applied to the specific HAP and
emissions sources in the source category
dataset to develop corresponding
estimates of risk reductions.
f. Conducting Other Risk-Related
Analyses: Facility-Wide Assessments
To put the source category risks in
context, we also examined the risks
from the entire ‘‘facility,’’ where the
facility includes all HAP-emitting
operations within a contiguous area and
under common control. In other words,
for each facility that includes one or
more sources from one of the source
categories under review, we examined
the HAP emissions not only from the
source category of interest, but also from
all other emission sources at the facility.
The emissions data for generating these
‘‘facility-wide’’ risks were also obtained
from the 2005 NEI. For every facility
included in the MACT database, we also
retrieved emissions data and release
characteristics for all other emission
sources at the same facility. We
estimated the risks due to the inhalation
of HAP that are emitted ‘‘facility-wide’’
for the populations residing within 50
km of each facility, consistent with the
methods used for the source category
analysis described above. For these
facility-wide risk analyses, the modeled
source category risks were compared to
the facility-wide risks to determine the
portion of facility-wide risks that could
be attributed to the source categories
addressed in this proposal. We
specifically examined the facilities
associated with the highest estimates of
risk and determined the percentage of
that risk attributable to the source
category of interest. The risk
documentation available through the
docket for this action provides the
methodology and the results of the
facility-wide analyses for each source
category.
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g. Conducting Other Analyses:
Demographic Analysis
To examine the potential for any
environmental justice (EJ) issues that
might be associated with each source
category, we performed a demographic
analysis of population risk. In this
analysis, we evaluated the distributions
of HAP-related cancer and noncancer
risks across different social,
demographic and economic groups
within the populations living near the
facilities where these source categories
are located. The development of
demographic analyses to inform the
consideration of EJ issues in the EPA
rulemakings is an evolving science. The
EPA offers the demographic analyses in
this rulemaking to inform the
consideration of potential EJ issues and
invites public comment on the
approaches used and the interpretations
made from the results, with the hope
that this will support the refinement
and improve the utility of such analyses
for future rulemakings.
For the demographic analyses, we
focus on the populations within 50 km
of any facility estimated to have
exposures to HAP which result in
cancer risks of 1-in-1 million or greater,
or noncancer HI of 1 or greater (based
on the emissions of the source category
or the facility, respectively). We
examine the distributions of those risks
across various demographic groups,
comparing the percentages of particular
demographic groups to the total number
of people in those demographic groups
nationwide. The results, including other
risk metrics, such as average risks for
the exposed populations, are
documented in source-category-specific
technical reports in the docket for both
source categories covered in this
proposal.
The basis for the risk values used in
these analyses were the modeling
results based on actual emissions levels
obtained from the HEM–3 model
described above. The risk values for
each census block were linked to a
database of information from the 2000
Decennial census that includes data on
race and ethnicity, age distributions,
poverty status, household incomes and
education level. The Census Department
Landview® database was the source of
the data on race and ethnicity and the
data on age distributions, poverty status,
household incomes and education level
were obtained from the 2000 Census of
Population and Housing Summary File
3 Long Form. While race and ethnicity
census data are available at the census
block level, the age and income census
data are only available at the census
block group level (which includes an
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average of 26 blocks or an average of
1,350 people). Where census data are
available at the block group level, but
not the block level, we assumed that all
census blocks within the block group
have the same distribution of ages and
incomes as the block group.
For each source category, we focused
on those census blocks where source
category risk results show estimated
lifetime inhalation cancer risks above
1-in-1 million or chronic noncancer
indices above 1 and determined the
relative percentage of different racial
and ethnic groups, different age groups,
adults with and without a high school
diploma, people living in households
below the national median income and
for people living below the poverty line
within those census blocks. The specific
census population categories studied
include:
• Total population
• White
• African American (or Black)
• Native Americans
• Other races and multiracial
• Hispanic or Latino
• Children 18 years of age and under
• Adults 19 to 64 years of age
• Adults 65 years of age and over
• Adults without a high school diploma
• Households earning under the
national median income
• People living below the poverty line
It should be noted that these
categories overlap in some instances,
resulting in some populations being
counted in more than one category (e.g.,
other races and multiracial and
Hispanic). In addition, while not a
specific census population category, we
also examined risks to ‘‘Minorities,’’ a
classification which is defined for these
purposes as all race population
categories except white.
For further information about risks to
the populations located near the
facilities in these source categories, we
also evaluated the estimated
distribution of inhalation cancer and
chronic noncancer risks associated with
the HAP emissions from all the
emissions sources at the facility (i.e.,
facility-wide). This analysis used the
facility-wide RTR modeling results and
the census data described above.
The methodology and the results of
the demographic analyses for each
source category are included in a
source-category-specific technical report
for each of the categories, which are
available in the docket for this action.
h. Considering Uncertainties in Risk
Assessment
Uncertainty and the potential for bias
are inherent in all risk assessments,
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including those performed for the
source categories addressed in this
proposal. Although uncertainty exists,
we believe that our approach, which
used conservative tools and
assumptions, ensures that our decisions
are health-protective. A brief discussion
of the uncertainties in the emissions
datasets, dispersion modeling,
inhalation exposure estimates and doseresponse relationships follows below. A
more thorough discussion of these
uncertainties is included in the risk
assessment documentation (referenced
earlier) available in the docket for this
action.
i. Uncertainties in the Emissions
Datasets
Although the development of the
MACT dataset involved QA/quality
control processes, the accuracy of
emissions values will vary depending
on the source of the data, the degree to
which data are incomplete or missing,
the degree to which assumptions made
to complete the datasets are inaccurate,
errors in estimating emissions values
and other factors. The emission
estimates considered in this analysis
generally are annual totals for certain
years that do not reflect short-term
fluctuations during the course of a year
or variations from year to year.
The estimates of peak hourly emission
rates for the acute effects screening
assessment were based on a
multiplication factor of 10 applied to
the average annual hourly emission rate,
which is intended to account for
emission fluctuations due to normal
facility operations. Additionally,
although we believe that we have data
for most facilities in these two source
categories in our RTR dataset, our
dataset may not include data for all
existing facilities. Moreover, there are
uncertainties with regard to the
identification of sources as major or area
in the NEI for these source categories.
ii. Uncertainties in Dispersion Modeling
While the analysis employed the
EPA’s recommended regulatory
dispersion model, AERMOD, we
recognize that there is uncertainty in
ambient concentration estimates
associated with any model, including
AERMOD. In circumstances where we
had to choose between various model
options, where possible, model options
(e.g., rural/urban, plume depletion,
chemistry) were selected to provide an
overestimate of ambient air
concentrations of the HAP rather than
underestimates. However, because of
practicality and data limitation reasons,
some factors (e.g., meteorology, building
downwash) have the potential in some
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situations to overestimate or
underestimate ambient impacts. For
example, meteorological data were
taken from a single year (1991) and
facility locations can be a significant
distance from the site where these data
were taken. Despite these uncertainties,
we believe that at off-site locations and
census block centroids, the approach
considered in the dispersion modeling
analysis should generally yield
overestimates of ambient HAP
concentrations.
iii. Uncertainties in Inhalation Exposure
The effects of human mobility on
exposures were not included in the
assessment. Specifically, short-term
mobility and long-term mobility
between census blocks in the modeling
domain were not considered.31 The
assumption of not considering short or
long-term population mobility does not
bias the estimate of the theoretical MIR,
nor does it affect the estimate of cancer
incidence since the total population
number remains the same. It does,
however, affect the shape of the
distribution of individual risks across
the affected population, shifting it
toward higher estimated individual
risks at the upper end and reducing the
number of people estimated to be at
lower risks, thereby increasing the
estimated number of people at specific
risk levels.
In addition, the assessment predicted
the chronic exposures at the centroid of
each populated census block as
surrogates for the exposure
concentrations for all people living in
that block. Using the census block
centroid to predict chronic exposures
tends to over-predict exposures for
people in the census block who live
further from the facility, and underpredict exposures for people in the
census block who live closer to the
facility. Thus, using the census block
centroid to predict chronic exposures
may lead to a potential understatement
or overstatement of the true maximum
impact, but is an unbiased estimate of
average risk and incidence.
The assessments evaluate the cancer
inhalation risks associated with
continuous pollutant exposures over a
70-year period, which is the assumed
lifetime of an individual. In reality, both
the length of time that modeled
emissions sources at facilities actually
operate (i.e., more or less than 70 years),
and the domestic growth or decline of
the modeled industry (i.e., the increase
31 Short-term mobility is movement from one
micro-environment to another over the course of
hours or days. Long-term mobility is movement
from one residence to another over the course of a
lifetime.
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or decrease in the number or size of
United States facilities), will influence
the risks posed by a given source
category. Depending on the
characteristics of the industry, these
factors will, in most cases, result in an
overestimate both in individual risk
levels and in the total estimated number
of cancer cases. However, in rare cases,
where a facility maintains or increases
its emission levels beyond 70 years,
residents live beyond 70 years at the
same location, and the residents spend
most of their days at that location, then
the risks could potentially be
underestimated. Annual cancer
incidence estimates from exposures to
emissions from these sources would not
be affected by uncertainty in the length
of time emissions sources operate.
The exposure estimates used in these
analyses assume chronic exposures to
ambient levels of pollutants. Because
most people spend the majority of their
time indoors, actual exposures may not
be as high, depending on the
characteristics of the pollutants
modeled. For many of the HAP, indoor
levels are roughly equivalent to ambient
levels, but for very reactive pollutants or
larger particles, these levels are
typically lower. This factor has the
potential to result in an overstatement of
25 to 30 percent of exposures.32
In addition to the uncertainties
highlighted above, there are several
factors specific to the acute exposure
assessment that should be highlighted.
The accuracy of an acute inhalation
exposure assessment depends on the
simultaneous occurrence of
independent factors that may vary
greatly, such as hourly emissions rates,
meteorology, and human activity
patterns. In this assessment, we assume
that individuals remain for 1 hour at the
point of maximum ambient
concentration as determined by the cooccurrence of peak emissions and worstcase meteorological conditions. These
assumptions would tend to overestimate
actual exposures since it is unlikely that
a person would be located at the point
of maximum exposure during the time
of worst-case impact.
iv. Uncertainties in Dose-Response
Relationships
There are uncertainties inherent in
the development of the dose-response
values used in our risk assessments for
cancer effects from chronic exposures
and noncancer effects from both chronic
and acute exposures. Some
uncertainties may be considered
32 U.S. EPA. National-Scale Air Toxics
Assessment for 1996. (EPA 453/R–01–003; January
2001; page 85.)
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quantitatively, and others generally are
expressed in qualitative terms. We note
as a preface to this discussion a point on
dose-response uncertainty that is
brought out in the EPA 2005 Cancer
Guidelines; namely, that ‘‘the primary
goal of the EPA actions is protection of
human health; accordingly, as an
Agency policy, risk assessment
procedures, including default options
that are used in the absence of scientific
data to the contrary, should be health
protective.’’ (EPA 2005 Cancer
Guidelines, pages 1–7.) This is the
approach followed here as summarized
in the next several paragraphs. A
complete detailed discussion of
uncertainties and variability in doseresponse relationships is given in the
residual risk documentation, which is
available in the docket for this action.
Cancer URE values used in our risk
assessments are those that have been
developed to generally provide an upper
bound estimate of risk. That is, they
represent a ‘‘plausible upper limit to the
true value of a quantity’’ (although this
is usually not a true statistical
confidence limit).33 In some
circumstances, the true risk could be as
low as zero; however, in other
circumstances, the risk could also be
greater.34 When developing an upper
bound estimate of risk and to provide
risk values that do not underestimate
risk, health-protective default
approaches are generally used. To err on
the side of ensuring adequate healthprotection, the EPA typically uses the
upper bound estimates rather than
lower bound or central tendency
estimates in our risk assessments, an
approach that may have limitations for
other uses (e.g., priority-setting or
expected benefits analysis).
Chronic noncancer reference (RfC and
reference dose (RfD)) values represent
chronic exposure levels that are
intended to be health-protective levels.
Specifically, these values provide an
estimate (with uncertainty spanning
perhaps an order of magnitude) of daily
oral exposure (RfD) or of a continuous
inhalation exposure (RfC) to the human
population (including sensitive
subgroups) that is likely to be without
an appreciable risk of deleterious effects
during a lifetime. To derive values that
are intended to be ‘‘without appreciable
risk,’’ the methodology relies upon an
uncertainty factor (UF) approach (U.S.
EPA, 1993, 1994) which includes
33 IRIS glossary (https://www.epa.gov/NCEA/iris/
help_gloss.htm).
34 An exception to this is the URE for benzene,
which is considered to cover a range of values, each
end of which is considered to be equally plausible
and which is based on maximum likelihood
estimates.
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consideration of both uncertainty and
variability. When there are gaps in the
available information, UF are applied to
derive reference values that are
intended to protect against appreciable
risk of deleterious effects. The UF are
commonly default values,35 e.g., factors
of 10 or 3, used in the absence of
compound-specific data; where data are
available, UF may also be developed
using compound-specific information.
When data are limited, more
assumptions are needed and more UF
are used. Thus, there may be a greater
tendency to overestimate risk in the
sense that further study might support
development of reference values that are
higher (i.e., less potent) because fewer
default assumptions are needed.
However, for some pollutants, it is
possible that risks may be
underestimated. While collectively
termed ‘‘uncertainty factor,’’ these
factors account for a number of different
quantitative considerations when using
observed animal (usually rodent) or
human toxicity data in the development
of the RfC. The UF are intended to
account for: (1) Variation in
susceptibility among the members of the
human population (i.e., inter-individual
variability); (2) uncertainty in
extrapolating from experimental animal
data to humans (i.e., interspecies
differences); (3) uncertainty in
extrapolating from data obtained in a
study with less-than-lifetime exposure
(i.e., extrapolating from sub-chronic to
chronic exposure); (4) uncertainty in
extrapolating the observed data to
obtain an estimate of the exposure
associated with no adverse effects; and
(5) uncertainty when the database is
incomplete or there are problems with
the applicability of available studies.
Many of the UF used to account for
variability and uncertainty in the
development of acute reference values
35 According to the NRC report, Science and
Judgment in Risk Assessment (NRC, 1994)
‘‘[Default] options are generic approaches, based on
general scientific knowledge and policy judgment,
that are applied to various elements of the risk
assessment process when the correct scientific
model is unknown or uncertain.’’ The 1983 NRC
report, Risk Assessment in the Federal Government:
Managing the Process, defined default option as
‘‘the option chosen on the basis of risk assessment
policy that appears to be the best choice in the
absence of data to the contrary’’ (NRC, 1983a, p. 63).
Therefore, default options are not rules that bind
the Agency; rather, the Agency may depart from
them in evaluating the risks posed by a specific
substance when it believes this to be appropriate.
In keeping with EPA’s goal of protecting public
health and the environment, default assumptions
are used to ensure that risk to chemicals is not
underestimated (although defaults are not intended
to overtly overestimate risk). See EPA, 2004, An
Examination of EPA Risk Assessment Principles
and Practices, EPA/100/B–04/001 available at:
https://www.epa.gov/osa/pdfs/ratf-final.pdf.
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are quite similar to those developed for
chronic durations, but they more often
use individual UF values that may be
less than 10. UF are applied based on
chemical-specific or health effectspecific information (e.g., simple
irritation effects do not vary appreciably
between human individuals, hence a
value of 3 is typically used), or based on
the purpose for the reference value (see
the following paragraph). The UF
applied in acute reference value
derivation include: (1) Heterogeneity
among humans; (2) uncertainty in
extrapolating from animals to humans;
(3) uncertainty in lowest observed
adverse effect (exposure) level to no
observed adverse effect (exposure) level
adjustments; and (4) uncertainty in
accounting for an incomplete database
on toxic effects of potential concern.
Additional adjustments are often
applied to account for uncertainty in
extrapolation from observations at one
exposure duration (e.g., 4 hours) to
derive an acute reference value at
another exposure duration (e.g., 1 hour).
Not all acute reference values are
developed for the same purpose and
care must be taken when interpreting
the results of an acute assessment of
human health effects relative to the
reference value or values being
exceeded. Where relevant to the
estimated exposures, the lack of shortterm dose-response values at different
levels of severity should be factored into
the risk characterization as potential
uncertainties.
Although every effort is made to
identify peer-reviewed reference values
for cancer and noncancer effects for all
pollutants emitted by the sources
included in this assessment, some HAP
continue to have no reference values for
cancer or chronic noncancer or acute
effects. Since exposures to these
pollutants cannot be included in a
quantitative risk estimate, an
understatement of risk for these
pollutants at environmental exposure
levels is possible. For a group of
compounds that are either unspeciated
or do not have reference values for every
individual compound (e.g., glycol
ethers), we conservatively use the most
protective reference value to estimate
risk from individual compounds in the
group of compounds.
Additionally, chronic reference values
for several of the compounds included
in this assessment are currently under
the EPA IRIS review and revised
assessments may determine that these
pollutants are more or less potent than
the current value. We may re-evaluate
residual risks for the final rulemaking if
these reviews are completed prior to our
taking final action for these source
categories and a dose-response metric
changes enough to indicate that the risk
assessment supporting this notice may
significantly understate human health
risk.
v. Uncertainties in the Multi-Pathway
and Environmental Effects Assessment
We generally assume that when
exposure levels are not anticipated to
adversely affect human health, they also
are not anticipated to adversely affect
the environment. For each source
category, we generally rely on the sitespecific levels of PB–HAP emissions to
determine whether a full assessment of
the multi-pathway and environmental
effects is necessary. As discussed above,
we conclude that the potential for these
types of impacts is low for these source
categories.
vi. Uncertainties in the Facility-Wide
Risk Assessment
Given that the same general analytical
approach and the same models were
used to generate facility-wide risk
results as were used to generate the
source category risk results, the same
types of uncertainties discussed above
52777
for our source category risk assessments
apply to the facility-wide risk
assessments. Additionally, the degree of
uncertainty associated with facilitywide emissions and risks is likely
greater because we generally have not
conducted a thorough engineering
review of emissions data for source
categories not currently undergoing an
RTR review.
vii. Uncertainties in the Demographic
Analysis
Our analysis of the distribution of
risks across various demographic groups
is subject to the typical uncertainties
associated with census data (e.g., errors
in filling out and transcribing census
forms), as well as the additional
uncertainties associated with the
extrapolation of census-block group data
(e.g., income level and education level)
down to the census block level.
2. What are the results and proposed
decisions from the risk review for the
Oil and Natural Gas Production source
category?
a. Results of the Risk Assessments and
Analyses
We conducted an inhalation risk
assessment for the Oil and Natural Gas
Production source category. We also
conducted an assessment of facilitywide risk. Details of the risk
assessments and analyses can be found
in the residual risk documentation,
which is available in the docket for this
action. For informational purposes and
to examine the potential for any EJ
issues that might be associated with
each source category, we performed a
demographic analysis of population
risks.
i. Inhalation Risk Assessment Results
Table 2 provides an overall summary
of the results of the inhalation risk
assessment.
TABLE 2—OIL AND NATURAL GAS PRODUCTION INHALATION RISK ASSESSMENT RESULTS
Number of
facilities 1
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990
Maximum individual cancer risk
(in 1 million) 2
Actual emissions level
Allowable emissions level
40
100–400 3
Estimated population at risk ≥
1-in-1 million
Estimated
annual cancer
incidence
(cases per
year)
Maximum chronic noncancer
TOSHI 4
Actual emissions level
Allowable emissions level
160,000 3
0.007–0.02 3
0.1
0.7
1 Number
Maximum
off-site acute
noncancer HQ 5
HQREL = 9
(benzene)
HQAEGL–1 =
0.07 (benzene)
of facilities evaluated in the risk analysis.
maximum individual excess lifetime cancer risk.
EPA IRIS assessment for benzene provides a range of equally-plausible URE (2.2E–06 to 7.8E–06 per ug/m3), giving rise to ranges for
the estimates of cancer MIR and cancer incidence. Estimated population values are not scalable with benzene URE range, but would be lower
using the lower end of the URE range.
4 Maximum TOSHI. The target organ with the highest TOSHI for the Oil and Natural Gas Production source category is the respiratory system.
5 The maximum estimated acute exposure concentration was divided by available short-term dose-response values to develop an array of HQ
values.
2 Estimated
3 The
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As shown in Table 2, the results of the
inhalation risk assessment performed
using actual emissions data indicate the
maximum lifetime individual cancer
risk could be as high as 40-in-1 million,
with POM driving the highest risk, and
benzene driving risks overall. The total
estimated cancer incidence from this
source category is 0.02 excess cancer
cases per year (0.007 excess cancer cases
per year based on the lower end of the
benzene URE range), or one case in
every 50 years. Approximately 160,000
people are estimated to have cancer
risks at or above 1-in-1 million as a
result of the emissions from 89 facilities
(use of the lower end of the benzene
URE range would further reduce this
population estimate). The maximum
chronic non-cancer TOSHI value for the
source category could be up to 0.1 from
emissions of naphthalene, indicating no
significant potential for chronic
noncancer impacts.
As explained above, our analysis of
potential differences between actual
emission levels and emissions allowable
under the oil and natural gas production
MACT standard indicate that MACTallowable emission levels may be up to
50 times greater than actual emission
levels. Considering this difference, the
risk results from the inhalation risk
assessment indicate the maximum
lifetime individual cancer risk could be
as high as 400-in-1 million (100-in-1
million based on the lower end of the
benzene URE range) and the maximum
chronic noncancer TOSHI value could
be as high as 0.7 at the MACT-allowable
emissions level.
ii. Facility-Wide Risk Assessment
Results
A facility-wide risk analysis was also
conducted based on actual emissions
levels. Table 3 displays the results of the
facility-wide risk assessment. For
detailed facility-specific results, see
Table 2 of Appendix 6 of the risk
document in the docket for this
rulemaking.
TABLE 3—OIL AND NATURAL GAS PRODUCTION FACILITY-WIDE RISK ASSESSMENT RESULTS
Number of facilities analyzed ..................................................................................................................................................................
Cancer Risk:
Estimated maximum facility-wide individual cancer risk (in 1 million) .............................................................................................
Number of facilities with estimated facility-wide individual cancer risk of 100-in-1 million or more ................................................
Number of facilities at which the Oil and Natural Gas Production source category contributes 50 percent or more to the facility-wide individual cancer risks of 100-in-1 million or more .........................................................................................................
Number of facilities with facility-wide individual cancer risk of 1-in-1 million or more .....................................................................
Number of facilities at which the Oil and Natural Gas Production source category contributes 50 percent or more to the facility-wide individual cancer risk of 1-in-1 million or more ...............................................................................................................
Chronic Noncancer Risk:
Maximum facility-wide chronic noncancer TOSHI ...........................................................................................................................
Number of facilities with facility-wide maximum noncancer TOSHI greater than 1 ........................................................................
Number of facilities at which the Oil and Natural Gas Production source category contributes 50 percent or more to the facility-wide maximum noncancer TOSHI of 1 or more ......................................................................................................................
The facility-wide MIR from all HAP
emissions at a facility that contains
sources subject to the oil and natural gas
production MACT standards is
estimated to be 100-in-1 million, based
on actual emissions. Of the 990 facilities
included in this analysis, only one has
a facility-wide MIR of 100-in-1 million.
At this facility, oil and natural gas
production accounts for less than 2
percent of the total facility-wide risk.
Nickel emissions from oil-fired boilers
and formaldehyde emissions from
reciprocating internal combustion
engines (RICE) contribute essentially all
the facility-wide risks at this facility,
with over 80 percent of the risk
attributed to the nickel emissions.36
There are 140 facilities with facility-
wide MIR of 1-in-1 million or greater. Of
these facilities, 85 have oil and natural
gas production operations that
contribute greater than 50 percent to the
facility-wide risks. As discussed above,
we are proposing MACT standards for
BTEX emissions from small glycol
dehydrators in this action. These
standards would reduce the risk from
benzene emissions at facilities with oil
and gas production. Formaldehyde
emissions will be assessed under future
RTR for RICE.
The facility-wide maximum
individual chronic noncancer TOSHI is
estimated to be 9 based on actual
emissions. Of the 990 facilities included
in this analysis, 10 have facility-wide
maximum chronic noncancer TOSHI
990
100
1
0
140
85
9
10
0
values greater than 1. Of these facilities,
none had oil and natural gas production
operations that contributed greater than
50 percent to these facility-wide risks.
The chronic noncancer risks at these 10
facilities are primarily driven by
acrolein emissions from RICE.
iii. Demographic Risk Analysis Results
The results of the demographic
analyses performed to investigate the
distribution of cancer risks at or above
1-in-1 million among the surrounding
population are summarized in Table 4
below. These results, for various
demographic groups, are based on
actual emissions levels for the
population living within 50 km of the
facilities.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
TABLE 4—OIL AND NATURAL GAS PRODUCTION DEMOGRAPHIC RISK ANALYSIS RESULTS
Population with cancer risk at or
above 1-in-1 million due to
Nationwide
Source category
HAP emissions
Total Population .........................................................................................................
36 We note that there is an ongoing IRIS
reassessment for formaldehyde, and that future RTR
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285,000,000
risk assessments will use the cancer potency for
formaldehyde that results from that reassessment.
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160,000
Facility-wide HAP
emissions
597,000
As a result, the current results may not match those
of future assessments.
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
TABLE 4—OIL AND NATURAL GAS PRODUCTION DEMOGRAPHIC RISK ANALYSIS RESULTS—Continued
Population with cancer risk at or
above 1-in-1 million due to
Nationwide
Source category
HAP emissions
Facility-wide HAP
emissions
Race by Percent
White ..........................................................................................................................
All Other Races .........................................................................................................
75
25
62
38
61
39
75
12
0.9
12
62
12
0.7
25
61
8
1.3
30
14
86
22
78
34
66
13
87
14
86
19
81
13
87
10
90
16
84
Race by Percent
White ..........................................................................................................................
African American .......................................................................................................
Native American ........................................................................................................
Other and Multiracial .................................................................................................
Ethnicity by Percent
Hispanic .....................................................................................................................
Non-Hispanic .............................................................................................................
Income by Percent
Below Poverty Level ..................................................................................................
Above Poverty Level ..................................................................................................
Education by Percent
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
Over 25 and without High School Diploma ...............................................................
Over 25 and with a High School Diploma .................................................................
The results of the Oil and Natural Gas
Production source category
demographic analysis indicate that there
are approximately 160,000 people
exposed to a cancer risk at or above 1in-1 million due to emissions from the
source category, including an estimated
38 percent that are classified as minority
(listed as ‘‘All Other Races’’ in the table
above). Of the 160,000 people with
estimated cancer risks at or above 1-in1 million from the source category, 25
percent are in the ‘‘Other and
Multiracial’’ demographic group, 22
percent are in the ‘‘Hispanic or Latino’’
demographic group, and 14 percent are
in the ‘‘Below Poverty Level’’
demographic group, results which are
13, 8 and 1 percentage points higher,
respectively, than the respective
percentages for these demographic
groups across the United States. The
percentages for the other demographic
groups are lower than their respective
nationwide percentages. The table also
shows that there are approximately
597,000 people exposed to an estimated
cancer risk at or above 1-in-1 million
due to facility-wide emissions,
including 30 percent in the ‘‘Other and
Multiracial’’ demographic group, 34
percent in the ‘‘Hispanic or Latino’’
demographic group, 1.3 percent in the
‘‘Native American’’ demographic group
and 16 percent in the ‘‘Over 25 and
without High School Diploma’’
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demographic group, results which are
18, 2, 0.4 and 3 percentage points higher
than the percentages for these
demographic groups across the United
States, respectively. The percentages for
the other demographic groups are lower
than their respective nationwide
percentages.
b. What are the proposed risk decisions
for the Oil and Natural Gas Production
source category?
i. Risk Acceptability
In the risk analysis we performed for
this source category, pursuant to CAA
section 112(f)(2), we considered the
available health information—the MIR;
the numbers of persons in various risk
ranges; cancer incidence; the maximum
noncancer HI; the maximum acute
noncancer hazard; the extent of
noncancer risks; the potential for
adverse environmental effects; and
distribution of risks in the exposed
population; and risk estimation
uncertainty (54 FR 38044, September
14, 1989).
For the Oil and Natural Gas
Production source category, the risk
analysis we performed indicates that the
cancer risks to the individual most
exposed could be as high as 40-in-1
million due to actual emissions and as
high as 400-in-1 million due to MACTallowable emissions (100-in-1 million,
based on the lower end of the benzene
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URE range). While the 40-in-1 million
risk due to actual emissions is
considerably less than 100-in-1 million,
which is the presumptive limit of
acceptability, the 400-in-1 million risk
due to allowable emissions is
considerably higher and is considered
unacceptable. We do note, however, that
the risk analysis shows low cancer
incidence (1 case in every 50 years), low
potential for adverse environmental
effects or human health multi-pathway
effects and that chronic noncancer
health impacts are unlikely.
We also conclude that acute
noncancer health impacts are unlikely.
As discussed above, screening estimates
of acute exposures and risks were
evaluated for each of the HAP at the
point of highest off-site exposure for
each facility (i.e., not just the census
block centroids) assuming that a person
is located at this spot at a time when
both the peak emission rate and worstcase dispersion conditions occur. Under
these worst-case conditions, we estimate
benzene acute HQ values (based on the
REL) could be as high as 9. Although the
REL (which indicates the level below
which adverse effects are not
anticipated) is exceeded in this case, we
believe the potential for acute effects is
low for several reasons. First, the acute
modeling scenario is worst-case because
of the confluence of peak emission rates
and worst-case dispersion conditions.
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Second, the benzene REL is based on a
6-hour exposure duration because a
1-hour exposure duration value was
unavailable. An REL based on a 6-hour
exposure duration is generally lower
than an REL based on a 1-hour exposure
duration and, consequently, easier to
exceed. Also, although there are
exceedances of the REL, the highest
estimated 1-hour exposure is less than
10 percent of the AEGL–1 value, which
is a level at which effects could be
experienced. Finally, the generally
sparse populations near these facilities
make it less likely that a person would
be near the plant to be exposed. For
example, in the two cases where the
acute HQ value is as high as 9, there are
only 30 people associated with the
census blocks within 2 miles of the two
facilities.
While our additional analysis of
facility-wide risks showed that there is
one facility with maximum facility-wide
cancer risk of 100-in-1 million or greater
and 10 facilities with a maximum
chronic noncancer TOSHI greater than
1, it also showed that oil and natural gas
production operations did not drive
these risks.
In determining whether risk is
acceptable, we considered the available
health information, as described above.
In this case, although a number of
factors we considered indicate relatively
low risk concern, we are proposing to
determine that the risks are
unacceptable, in large part, because the
MIR is 400-in-1 million due to MACTallowable emissions, which greatly
exceeds the ‘‘presumptive limit on
maximum individual lifetime risk of
approximately 1-in-10 thousand [100-in1 million] recognized in the Benzene
NESHAP (54 FR 38045).’’ The MIR,
based on MACT-allowable emissions, is
driven by the allowable emissions of 0.9
Mg/yr benzene under the MACT as a
compliance option. We are, therefore,
proposing to eliminate the alternative
compliance option of 0.9 Mg/yr benzene
from the existing glycol dehydrator
MACT requirements. With this change,
the source category MIR, based on
MACT-allowable emissions, would be
reduced to 40-in-1 million, which we
find acceptable in light of all the other
factors considered. Thus, we are
proposing that the risks from the Oil
and Natural Gas Production source
category are acceptable, with the
removal of the alternative compliance
option of 0.9 Mg/yr benzene limit from
the current glycol dehydrator MACT
requirements.
Pursuant to CAA section 112(f)(4), we
are proposing that this change (i.e.,
removal of the 0.9 Mg/yr compliance
alternative) apply 90 days after its
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effective date. We are requesting
comment on whether or not this is
sufficient time for the large dehydrators
that have been relying on this
compliance alternative to come into
compliance with the 95-percent control
requirement or if additional time is
needed. See CAA section 112(f)(4)(A).
We recognize that our proposal to
remove the 0.9 Mg/yr compliance
alternative for the 95-percent control
glycol dehydrator MACT standard could
have negative impacts on some sources
that have come to rely on the flexibility
this alternative provides. We solicit
comment on any such impacts and
whether such impacts warrant adding a
different compliance alternative that
would result in less risk than the 0.9
Mg/yr benzene limit compliance option.
If a commenter suggests a different
compliance alternative, the commenter
should explain, in detail, what that
alternative would be, how it would
work and how it would reduce risk.
ii. Ample Margin of Safety
We next considered whether this
revised standard (existing MACT plus
removal of 0.9 Mg/yr benzene
compliance option) provides an ample
margin of safety. In this analysis, we
investigated available emissions control
options that might reduce the risk
associated with emissions from the
source category and considered this
information along with all of the health
risks and other health information
considered in the risk acceptability
determination.
For glycol dehydrators, we considered
the addition of a second control device
in the same manner that was discussed
in the floor evaluation in section VII.B.1
above. The cost effectiveness associated
with that option would be $167,200/Mg,
which we believe is too high to require
additional controls on glycol
dehydrators.
Similarly, we considered the addition
of a second control device to the
required MACT floor control device
(cost effectiveness of $18,300/Mg).
Similar to our discussion of beyond-theMACT-floor controls for glycol
dehydrators in section VII.B.1 of this
preamble, the incremental cost to add a
second control device for storage vessels
would be approximately 20 times higher
than the MACT floor cost effectiveness,
or $366,000/Mg. We do not believe this
cost effectiveness is reasonable.
For leak detection, we considered
implementation of LDAR programs that
are more stringent than the current
standards. An assessment performed for
various LDAR options under the NSPS
in section VI.B.4.b of this preamble
yielded the lowest cost effectiveness of
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$5,170/Mg ($4,700/ton) for control of
VOC for the options evaluated. A LDAR
program to control HAP would involve
similar costs for equipment, labor, etc.,
to those considered in the NSPS
assessment, but since there is
approximately 20 times less HAP than
VOC present in material handled in
regulated equipment, the cost
effectiveness to control HAP would be
approximately 20 times greater (i.e.,
$100,000/Mg) for HAP, which we
believe is not reasonable.
In accordance with the approach
established in the Benzene NESHAP,
the EPA weighed all health risk
measures and information considered in
the risk acceptability determination,
along with the costs and economic
impacts of emissions controls,
technological feasibility, uncertainties
and other relevant factors in making our
ample margin of safety determination.
Considering the health risk information
and the high cost effectiveness of the
options identified, we propose that the
existing MACT standards, with the
removal of the 1 tpy benzene limit
compliance option from the glycol
dehydrator standards, provide an ample
margin of safety to protect public health.
While we are proposing that the oil
and natural gas production MACT
standards (with the removal of the
alternative compliance option of 1 tpy
benzene limit) provide an ample margin
of safety to protect public health, we are
concerned about the estimated facilitywide risks identified through these
screening analyses. As described
previously, the highest estimated
facility-wide cancer risks are mostly due
to emissions from oil fired boilers and
RICE. Both of these sources are
regulated under other source categories
and we anticipate that emission
reductions from those sources will
occur as standards for those source
categories are implemented.
3. What are the results and proposed
decisions from the risk review for the
Natural Gas Transmission and Storage
source category?
a. Results of the Risk Assessments and
Analyses
We conducted an inhalation risk
assessment for the Natural Gas
Transmission and Storage source
category. We also conducted an
assessment of facility-wide risk and
performed a demographic analysis of
population risks. Details of the risk
assessments and analyses can be found
in the residual risk documentation,
which is available in the docket for this
action.
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i. Inhalation Risk Assessment Results
Table 5 provides an overall summary
of the results of the inhalation risk
assessment. For informational purposes
and to examine the potential for any EJ
issues that might be associated with
each source category, we performed a
demographic analysis of population
risks.
TABLE 5—NATURAL GAS TRANSMISSION AND STORAGE INHALATION RISK ASSESSMENT RESULTS
Maximum individual cancer risk
(in 1 million) 2
Number of
Facilities 1
3 30–90
321
Allowable emissions level
3 30–90
Estimated
annual cancer
incidence
(cases per
year)
Actual
emissions level
Allowable emissions level
3 2,500
Actual
emissions level
Estimated
population at
risk ≥ 1-in-1
million
Maximum chronic noncancer
TOSHI 4
3 0.0003–0.001
0.4
0.8
Maximum
off-site acute
noncancer HQ 5
HQREL = 5
(benzene)
HQAEGL–1 = 0.2
(chlorobenzene)
1 Number
of facilities evaluated in the risk analysis.
maximum individual excess lifetime cancer risk.
3 The EPA IRIS assessment for benzene provides a range of equally-plausible URE (2.2E–06 to 7.8E–06 per ug/m3), giving rise to ranges for
the estimates of cancer MIR and cancer incidence. Estimated population values are not scalable with benzene URE range, but would be lower
using the lower end of the URE range.
4 Maximum TOSHI. The target organ with the highest TOSHI for the Natural Gas Transmission and Storage source category is the immune
system.
5 The maximum estimated acute exposure concentration was divided by available short-term dose-response values to develop an array of HQ
values.
2 Estimated
As shown in Table 5 above, the
results of the inhalation risk assessment
performed using actual emissions data
indicate the maximum lifetime
individual cancer risk could be as high
as 90-in-1 million, (30-in-1 million
based on the lower end of the benzene
URE range), with benzene as the major
contributor to the risk. The total
estimated cancer incidence from the
source category is 0.001 excess cancer
cases per year (0.0003 excess cancer
cases per year based on the lower end
of the benzene URE range), or one case
in every polycyclic organic matter 1,000
years. Approximately 2,500 people are
estimated to have cancer risks at or
above 1-in-1 million as a result of the
emissions from 15 facilities (use of the
lower end of the benzene URE range
would further reduce this population
estimate). The maximum chronic
noncancer TOSHI value for the source
category could be up to 0.4 from
emissions of benzene, indicating no
significant potential for chronic
noncancer impacts.
As explained above in section
VII.C.1.b, our analysis of potential
differences between actual emission
levels and emissions allowable under
the natural gas transmission and storage
MACT standard indicate that MACTallowable emission levels may be up to
50 times greater than actual emission
levels at some sources. However,
because some sources are emitting at the
level allowed under the current
NESHAP, the risk results from the
inhalation risk assessment indicate the
maximum lifetime individual cancer
risk would still be 90-in-1 million (30in-1 million based on the lower end of
the benzene URE range), based on both
actual and allowable emission levels,
and the maximum chronic noncancer
TOSHI value could be as high as 0.8 at
the MACT-allowable emissions level.
ii. Facility-Wide Risk Assessment
Results
A facility-wide risk analysis was also
conducted based on actual emissions
levels. Table 6 below displays the
results of the facility-wide risk
assessment. For detailed facility-specific
results, see Table 2 of Appendix 6 of the
risk document in the docket for this
rulemaking.
TABLE 6—NATURAL GAS TRANSMISSION AND STORAGE FACILITY-WIDE RISK ASSESSMENT RESULTS
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
Number of Facilities Analyzed .................................................................................................................................................................
Cancer Risk:
Estimated maximum facility-wide individual cancer risk (in 1 million) .............................................................................................
Number of facilities with estimated facility-wide individual cancer risk of 100-in-1 million or more ................................................
Number of facilities at which the Natural Gas Transmission and Storage source category contributes 50 percent or more to
the facility-wide individual cancer risks of 100-in-1 million or more .............................................................................................
Number of facilities with facility-wide individual cancer risk of 1-in-1 million or more .....................................................................
Number of facilities at which the Natural Gas Transmission and Storage source category contributes 50 percent or more to
the facility-wide individual cancer risk of 1-in-1 million or more ...................................................................................................
Chronic Noncancer Risk:
Maximum facility-wide chronic noncancer TOSHI ...........................................................................................................................
Number of facilities with facility-wide maximum noncancer TOSHI greater than 1 ........................................................................
Number of facilities at which the Natural Gas Transmission and Storage source category contributes 50 percent or more to
the facility-wide maximum noncancer TOSHI of 1 or more .........................................................................................................
1 We
321
1 200
3
1
74
10
80
30
0
note that the MIR would be 100-in-1 million if the CIIT URE for formaldehyde were used instead of the IRIS URE.
The facility-wide MIR from all HAP
emissions at any facility that contains
sources subject to the natural gas
transmission and storage MACT
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standards is estimated to be 200-in-1
million, based on actual emissions. Of
the 321 facilities included in this
analysis, three have facility-wide MIR of
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100-in-1 million or greater. The facilitywide MIR is 200-in-1 million at two of
these facilities, driven by formaldehyde
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from RICE.37 Another facility has a
facility-wide risk of 100-in-1 million,
with 90 percent of the risk attributed to
natural gas transmission and storage.
There are 74 facilities with facility-wide
MIR of 1-in-1 million or greater. Of
these facilities, 10 have natural gas
transmission and storage operations that
contribute greater than 50 percent to the
facility-wide risks. As discussed above,
we are proposing MACT standards for
benzene emissions from small glycol
dehydrators in this action. These
standards would reduce the risk from
benzene emissions at facilities with
natural gas transmission and storage
operations. The facility-wide cancer
risks at the facilities with risks of 1-in1 million or more are primarily driven
by formaldehyde emissions from RICE,
which will be assessed in a future RTR
for that category.
The facility-wide maximum
individual chronic noncancer TOSHI is
estimated to be 80, based on actual
emissions. Of the 321 facilities included
in this analysis, 30 have facility-wide
maximum chronic noncancer TOSHI
values greater than 1. Of these facilities,
none had natural gas transmission and
storage operations that contributed
greater than 50 percent to these facility-
wide risks. The chronic noncancer risks
at these facilities are primarily driven by
acrolein emissions from RICE.
iii. Demographic Risk Analysis Results
The results of the demographic
analyses performed to investigate the
distribution of cancer risks at or above
1-in-1 million among the surrounding
population are summarized in Table 7
below. These results, for various
demographic groups, are based on
actual emissions levels for the
population living within 50 km of the
facilities.
TABLE 7—NATURAL GAS TRANSMISSION AND STORAGE DEMOGRAPHIC RISK ANALYSIS RESULTS
Population with cancer risk at or
above 1-in-1 million due to . . .
Nationwide
Source category
HAP emissions
Total Population .........................................................................................................
Facility-wide HAP
emissions
285,000,000
2,500
99,000
75
25
92
8
58
42
75
12
0.9
12
92
6
0.1
1
58
40
0.2
2
14
86
1
99
2
98
13
87
17
83
20
80
13
87
20
80
15
85
Race by Percent
White ..........................................................................................................................
All Other Races .........................................................................................................
Race by Percent
White ..........................................................................................................................
African American .......................................................................................................
Native American ........................................................................................................
Other and Multiracial .................................................................................................
Ethnicity by Percent
Hispanic .....................................................................................................................
Non-Hispanic .............................................................................................................
Income by Percent
Below Poverty Level ..................................................................................................
Above poverty level ...................................................................................................
Education by Percent
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
Over 25 and without High School Diploma ...............................................................
Over 25 and with a High School Diploma .................................................................
The results of the Natural Gas
Transmission and Storage source
category demographic analysis indicate
that there are approximately 2,500
people exposed to a cancer risk at or
above 1-in-1 million due to emissions
from the source category, including an
estimated 8 percent that are classified as
minority (listed as ‘‘All Other Races’’ in
Table 7 above). Of the 2,500 people with
estimated cancer risks at or above 1-in1 million from the source category, 17
percent are in the ‘‘Below Poverty
Level’’ demographic group, and 20
percent are in the ‘‘Over 25 and without
High School Diploma’’ demographic
group, results which are 4 and 7
percentage points higher, respectively,
than the percentages for these
demographic groups across the United
States. The percentages for the other
demographic groups are lower than
their respective nationwide percentages.
The table also shows that there are
approximately 99,000 people exposed to
an estimated cancer risk at or above 1in-1 million due to facility-wide
emissions, including an estimated 42
percent that are classified as minority
(‘‘All Other Races’’ in Table 7 above). Of
the 99,000 people with estimated cancer
risk at or above 1-in-1 million from
facility-wide emissions, 40 percent are
in the ‘‘African American’’ demographic
group, 20 percent are in the ‘‘Below
Poverty Level’’ demographic group, and
15 percent are in the ‘‘Over 25 and
without High School Diploma’’
demographic group, results which are
28, 7 and 2 percentage points higher,
respectively, than the percentages for
these demographic groups across the
United States. The percentages for the
other demographic groups are equal to
37 We note that there is an ongoing IRIS
reassessment for formaldehyde, and that future RTR
risk assessments will use the cancer potency for
formaldehyde that results from that reassessment.
As a result, the current results may not match those
of future assessments.
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
or lower than their respective
nationwide percentages.
proposing to determine that the risks are
acceptable.
b. What are the proposed risk decisions
for the Natural Gas Transmission and
Storage source category?
ii. Ample Margin of Safety
We next considered whether the
existing MACT standard provides an
ample margin of safety. In this analysis,
we investigated available emissions
control options that might reduce the
risk associated with emissions from the
source category and considered this
information, along with all of the health
risks and other health information
considered in the risk acceptability
determination. The estimated MIR of 90in-1 million discussed above is driven
by the 0.9 Mg/year benzene limit
compliance alternative for the glycol
dehydrator MACT standard in the
current NESHAP. Removal of this
compliance alternative would lower the
MIR for the source category to 20-in-1
million. We, therefore, considered
removing this compliance alternative as
an option for reducing risk and assessed
the cost of such alternative. Without the
compliance alternative, affected glycol
dehydrators (i.e., those units with
annual average benzene emissions of 0.9
Mg/yr or greater and an annual average
natural gas throughput of 283,000 scmd
or greater) must demonstrate
compliance with the 95-percent control
requirement, which we believe can be
shown with their existing control
devices in most cases, although, in some
instances, installation of a different or
an additional control may be necessary.
In section VII.B.1 above, we discuss
the costs for requiring controls on
currently unregulated ‘‘small glycol
dehydrators,’’ which are similar, in
operation and type of emission controls,
to the dehydrators subject to the current
MACT (‘‘large dehydrators’’). The HAP
cost effectiveness determined for small
dehydrators at the floor level of control
was $1,650/Mg. Although control
methodologies are similar for large and
small dehydrators, we expect that the
costs for controls on large units could be
as much as twice as high as for small
units because of the large gas flow being
processed. However, we also expect that
the amount of HAP emission reduction
for the large dehydrators, in general, to
be as much as, or more than, the amount
achieved by small dehydrators. In light
of the above, we do not expect the cost
effectiveness of the control device
needed to meet the 95-percent control
requirement for large dehydrators to
exceed $3,300/Mg (i.e., twice the cost
effectiveness for small dehydrators),
which we consider to be reasonable.
In accordance with the approach
established in the Benzene NESHAP,
the EPA weighed all health risk
measures and information considered in
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
i. Risk Acceptability
In the risk analysis we performed for
this source category, pursuant to CAA
section 112(f)(2), we considered the
available health information—the MIR;
the numbers of persons in various risk
ranges; cancer incidence; the maximum
noncancer HI; the maximum acute
noncancer hazard; the extent of
noncancer risks; the potential for
adverse environmental effects;
distribution of risks in the exposed
population; and risk estimation
uncertainty (54 FR 38044, September
14, 1989).
For the Natural Gas Transmission and
Storage source category, the risk
analysis we performed indicates that the
cancer risks to the individual most
exposed could be as high as 90-in-1
million due to actual and allowable
emissions (30-in-1 million, based on the
lower end of the benzene URE range).
These risks are near 100-in-1 million,
which is the presumptive limit of
acceptability. On the other hand, the
risk analysis shows low cancer
incidence (1 case in every 1,000 years),
low potential for adverse environmental
effects or human health multi-pathway
effects and that chronic and acute
noncancer health impacts are unlikely.
We conclude that acute noncancer
health impacts are unlikely for reasons
similar to those described in section
VII.C.2.b.i of this preamble.
Our additional analysis of facilitywide risks showed that, among three
facilities with maximum facility-wide
cancer risk of 100-in-1 million or
greater, one facility has a facility-wide
cancer risk of 100-in-1 million, with 90
percent of the risk attributed to natural
gas and transmission and storage. There
are 30 facilities with a maximum
chronic noncancer TOSHI greater than
1, but natural gas transmission and
storage operations did not drive this
risk.
In determining whether risk is
acceptable, we considered the available
health information, as described above.
In this case, because the MIR is
approaching, but still less than 100-in1 million risk, and because a number of
other factors indicate relatively low risk
concern (e.g., low cancer incidence, low
potential for adverse environmental
effects or human health multi-pathway
effects, chronic and acute noncancer
health impacts unlikely), we are
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the risk acceptability determination,
along with the costs and economic
impacts of emissions controls,
technological feasibility, uncertainties
and other relevant factors in making our
ample margin of safety determination.
Considering the health risk information
and the reasonable cost effectiveness of
the option identified, we propose that
the existing MACT standards, with the
removal of the 0.9 Mg benzene limit
compliance option from the glycol
dehydrator standards, provide an ample
margin of safety to protect public health.
Pursuant to CAA section 112(f)(4), we
are proposing that this change (i.e.,
removal of the 0.9 Mg/yr compliance
alternative) apply 90 days after its
effective date. We are requesting
comment on whether or not there is
sufficient time for the large dehydrators
that have been relying on this
compliance alternative to come into
compliance with the 95-percent control
requirement or if additional time is
needed. See CAA section 112(f)(4)(A).
We recognize that our proposal to
remove the one-ton compliance
alternative for the 95-percent control
glycol dehydrator MACT standard could
have negative impacts on some sources
that have come to rely on the flexibility
this alternative provides. We solicit
comment on any such impacts and
whether such impacts warrant adding a
different compliance alternative that
would result in less risk than the 0.9
Mg/yr benzene limit compliance option.
If a commenter suggests a different
compliance alternative, the commenter
should explain, in detail, what that
alternative would be, how it would
work, and how it would reduce risk.
As described above, we are proposing
that the natural gas transmission and
storage MACT standards (with the
removal of the 0.9 Mg/yr benzene limit
compliance option) provide an ample
margin of safety to protect public health.
We recognize that one facility has a
facility-wide cancer risk of 100-in-1
million, with 90 percent of the risk
attributed to natural gas transmission
and storage. This risk is driven by
benzene emissions from glycol
dehydrators and is being addressed by
our proposed revision to the Natural Gas
Transmission and Storage NESHAP
(removal of the 0.9 Mg/yr benzene limit
compliance option). As previously
mentioned, two facilities have facilitywide MIR of 200-in-1 million, driven by
formaldehyde from RICE. Emissions
from RICE are regulated under another
source category and will be assessed
under a future RTR for that category.
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D. How did we perform the technology
review and what are the results and
proposed decisions?
1. What was the methodology for the
technology review?
Our technology review is focused on
the identification and evaluation of
‘‘developments in practices, processes,
and control technologies’’ since the
promulgation of the MACT standards
for the two oil and gas source categories.
If a review of available information
identifies such developments, then we
conduct an analysis of the technical
feasibility of requiring the
implementation of these developments,
along with the impacts (costs, emission
reductions, risk reductions, etc.). We
then make a decision on whether it is
necessary to amend the regulation to
require these developments.
Based on specific knowledge of each
source category, we began by identifying
known developments in practices,
processes and control technologies. For
the purpose of this exercise, we
considered any of the following to be a
‘‘development’’:
• Any add-on control technology or
other equipment that was not identified
and considered during MACT
development;
• Any improvements in add-on
control technology or other equipment
(that was identified and considered
during MACT development) that could
result in significant additional emission
reduction;
• Any work practice or operational
procedure that was not identified and
considered during MACT development;
and
• Any process change or pollution
prevention alternative that could be
broadly applied that was not identified
and considered during MACT
development.
In addition to looking back at
practices, processes or control
technologies reviewed at the time we
developed the MACT standards, we
reviewed a variety of sources of data to
aid in our evaluation of whether there
were additional practices, processes or
controls to consider. One of these
sources of data was subsequent air
toxics rules. Since the promulgation of
the MACT standards for the source
categories addressed in this proposal,
the EPA has developed air toxics
regulations for a number of additional
source categories. We reviewed the
regulatory requirements and/or
technical analyses associated with these
subsequent regulatory actions to
identify any practices, processes and
control technologies considered in these
efforts that could possibly be applied to
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emission sources in the source
categories under this current RTR
review.
We also consulted the EPA’s RBLC.
The terms ‘‘RACT,’’ ‘‘BACT,’’ and
‘‘LAER’’ are acronyms for different
program requirements under the CAA
provisions addressing the NAAQS.
Control technologies classified as RACT,
BACT or LAER apply to stationary
sources depending on whether the
source exists or is new and on the size,
age and location of the facility. The
BACT and LAER (and sometimes RACT)
are determined on a case-by-case basis,
usually by state or local permitting
agencies. The EPA established the RBLC
to provide a central database of air
pollution technology information
(including technologies required in
source-specific permits) to promote the
sharing of information among
permitting agencies and to aid in
identifying future possible control
technology options that might apply
broadly to numerous sources within a
category or apply only on a source-bysource basis. The RBLC contains over
5,000 air pollution control permit
determinations that can help identify
appropriate technologies to mitigate
many air pollutant emission streams.
We searched this database to determine
whether any practices, processes or
control technologies are included for the
types of processes used for emission
sources (e.g., spray booths) in the source
categories under consideration in this
proposal.
We also consulted information from
the Natural Gas STAR program. The
Natural Gas STAR program is a flexible,
voluntary partnership that encourages
oil and natural gas companies to adopt
cost effective technologies and practices
that improve operational efficiency and
reduce pollutant emissions. The
program provides the oil and gas
industry with information on new
techniques and developments to reduce
pollutant emissions from the various
processes.
2. What are the results and proposed
decisions from the technology review?
There are three types of emission
sources covered by the two oil and gas
NESHAP. These sources and the control
technologies (including add-on control
devices and process modifications)
considered during the development of
the MACT standards are: Glycol
dehydrators (combustion devices,
recovery devices, process
modifications), storage vessels with the
PFE (combustion devices, recovery
devices) and equipment leaks (LDAR
programs, specific equipment
modifications). Dehydrators are
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addressed by both 40 CFR part 63,
subpart HH and 40 CFR part 63, subpart
HHH, while equipment leaks and
storage vessels with the PFE are only
covered by subpart HH.
Since the promulgation of 40 CFR part
63, subpart HH, which established
MACT standards to address HAP
emissions from equipment leaks at gas
processing plants, the EPA has
developed LDAR programs that are
more stringent than what is required in
subpart HH. The most prevalent
differences between these more
stringent programs and subpart HH
relate to the frequency of monitoring
and the concentration which constitutes
a ‘‘leak.’’ We do consider these
programs to represent a development in
practices and evaluated whether to
revise the MACT standards for
equipment leaks at natural gas
processing plants under subpart HH in
light of this development.
An analysis was performed above in
section VI.B.1 to assess the VOC
reduction, costs and other impacts
associated with these more stringent
LDAR program options at natural gas
processing plants. One option
considered was to require compliance
with 40 CFR part 60, subpart VVa
instead of 40 CFR part 60, subpart VV
(the current NSPS requirement for
equipment leaks of VOC at natural gas
processing plants), which changes the
leak definition (based on methane) from
10,000 ppm to 500 ppm and requires
monitoring of connectors. Because the
current leak definition under NESHAP
40 CFR part 63, subpart HH is the same
as that in NSPS subpart VV, and the
ratio of VOC to HAP is approximately
20 to 1, we expect that the HAP
reduction would be 1/20th of the VOC
reduction under subpart VVa. The
estimated incremental cost for that
option was determined to be $3,340 per
ton of VOC. Based on the 20-to-1 ratio,
we estimate the incremental cost to
control HAP at the subpart VVa level
would be approximately $66,800 per ton
of HAP ($73,480/Mg). Other options
considered in section VI.B.1 of this
preamble (and the incremental cost of
each option for reducing HAP) are as
follows: The use of an optical gas
imaging camera monthly with an annual
EPA Method 21 check ($129,000 per ton
of HAP/$143,600 per Mg, if purchasing
the camera; $93,000 per ton of HAP/
$103,300 per Mg, if renting the camera);
monthly optical gas imagining alone;
and annual optical gas imaging.38 In
38 As stated above in section VI.B.1, emissions for
the two options using the optical gas imaging
camera alone cannot be quantified and, therefore,
no cost effectiveness values were determined.
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light of the above, we do not believe that
the additional costs of these programs
are justified.
In addition to the plant-wide
evaluations, a component analysis was
also evaluated at gas processing plants
for the 40 CFR part 60, subpart VValevel of control (option 1 considered in
section VI.B.1).39 That assessment
shows that the subpart VVa-level of
control for connectors has an
incremental cost effectiveness of $4,360
per ton for VOC for connectors and $144
per ton for VOC for valves. This means
the incremental cost to control HAP
would be approximately $87,200 per ton
($96,900/Mg) for connectors and $2,880
per ton ($3,200/Mg) for valves. We do
not believe the additional cost for the
more stringent requirement for
connectors is justified, but the
additional cost for valves is justified.
Therefore, we are proposing to revise
the equipment leak requirements in 40
CFR part 63, subpart HH to lower the
leak definition for valves to an
instrument reading of at least 500 ppm
as a result of our technology review.
Some of the practices, processes or
control technologies listed by the
Natural Gas STAR program applicable
to the emission sources in these
categories were not identified and
evaluated during the original MACT
development. While the Natural Gas
STAR program does contain information
regarding new innovative techniques
that are available to reduce HAP
emissions, they are not considered to
have emission reductions higher than
what is set by the original MACT. One
control technology identified in the
Natural Gas STAR program that would
result in no HAP emissions from glycol
dehydration units would be the
replacement of a glycol dehydration
unit with a desiccant dehydrator. This
technology cannot be used for natural
gas operations with gas streams having
high temperature, high volume, and low
pressure. Due to the limitations posed
by these conditions, we do not consider
desiccant dehydrators as MACT.
For storage vessels, the applicable
technologies identified by the Gas STAR
program, which are evaluated above for
proposal under NSPS in section VI.B.4,
are similar to the cover and control
technologies currently required for
storage vessels under the existing
MACT. Therefore, these technologies
would not result in any further
emissions reductions than what is
achieved by the original MACT.
39 Because optical gas imaging is used to view
several pieces of equipment at a facility at once to
survey for leaks, options involving imaging are not
amenable to a component by component analysis.
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Our review of the RBLC did not
identify any practices, processes and
control technologies applicable to the
emission sources in these categories that
were not identified and evaluated
during the original MACT development.
In light of the above, we are not
proposing any revisions to the existing
MACT standards for storage vessels
pursuant to section 112(d)(6) of the
CAA.
E. What other actions are we proposing?
1. Combustion Control Device Testing
As explained below in section VII.E.2,
under our proposal, performance testing
would be required initially and every 5
years for non-condenser control devices.
However, for certain enclosed
combustion control devices, we are
proposing to allow, as an alternative to
on-site testing, a performance test
conducted by a control device
manufacturer in accordance with the
procedures provided in this proposal.
We propose to allow a unit whose
model meets the proposed performance
criteria to claim a BTEX or HAP
destruction efficiency of 98 percent at
the facility. This value is lower than the
99.9-percent destruction efficiency
required in the manufacturers’ test due
to variations between the test fuel
specified and the gas streams combusted
at the actual facility. A source subject to
the small dehydrator BTEX limit would
use the 98-percent destruction
efficiency to calculate their dehydrator’s
BTEX emissions for the purpose of
demonstrating compliance. For the
95-percent control MACT standard, a
control device matching the tested
model would be considered to meet that
requirement. Once a device has been
demonstrated to meet the proposed
performance criteria (and, therefore, is
assigned a 98-percent destruction
efficiency), installation of a unit
matching the tested model at a facility
would require no further performance
testing (i.e., periodic tests would not be
required every 5 years).
We are proposing this alternative to
minimize issues associated with
performance testing of certain
combustion control devices. We believe
that testing units that are not configured
with a distinct combustion chamber
present several technical issues that are
more optimally addressed through
manufacturer testing, and once these
units are installed at a facility, through
periodic inspection and maintenance in
accordance with manufacturers’
recommendations. One issue is that an
extension above certain existing
combustion control device enclosures
will be necessary to get adequate
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clearance above the flame zone. Such
extensions can more easily be
configured by the manufacturer of the
control device rather than having to
modify an extension in the field to fit
devices at every site. Issues related to
transporting, installing and supporting
the extension in the field are also
eliminated through manufacturer
testing. Another concern is that the pitot
tube used to measure flow can be
altered by radiant heat from the flame
such that gas flow rates are not accurate.
This issue is best overcome by having
the manufacturer select and use the
pitot tube best suited to their specific
unit. For these reasons, we believe the
manufacturers’ test is appropriate for
these control devices with ongoing
performance ensured by periodic
inspection and maintenance.
This proposed alternative does not
apply to flares, as defined in 40 CFR
63.761 and 40 CFR 63.1271, which must
demonstrate compliance by meeting the
design and operation requirements in 40
CFR 63.11(b), 40 CFR 63.772(e)(2) and
40 CFR 63.1282(d)(2). It also would not
apply to thermal oxidizers having a
combustion chamber/firebox where
combustion temperature and residence
time can be measured during an on-site
performance test and are valid
indicators of performance. These
thermal oxidizers do not present the
issues described above relative to onsite performance testing and, therefore,
do not need an alternative testing
option. The proposed alternative would,
therefore, apply to enclosed combustion
control devices except for these thermal
oxidizers.
In conjunction with the proposed
manufacturer testing alternative, we are
proposing to add a definition for flare to
clarify that flares, as referenced in the
NESHAP (and to which the proposed
testing alternative does not apply),
refers to a thermal oxidation system
with an open flame (i.e., without
enclosure). Accordingly, any thermal
oxidation system that does not meet the
proposed flare definition would be
considered an enclosed combustion
control device.
We estimate that there are many
existing facilities currently using
enclosed combustion control devices
that would be required to either conduct
an on-site performance test or install
and operate a control device tested by
the manufacturer under our proposal.
Given the estimated number of these
combustion control devices in use, the
time required for manufacturers to test
and manufacture such units, we are
proposing that existing sources have up
to 3 years from the date of the final
rules’ publication date to comply with
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requirements.
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2. Monitoring, Recordkeeping and
Reporting
We are proposing to make changes to
the monitoring requirements described
below to address issues we have
identified through a monitoring
sufficiency review performed during the
RTR process. First, we are including
calibration procedures associated with
parametric monitoring requirements in
the existing NESHAP. The NESHAP
require parametric monitoring of control
device parameters (e.g., temperatures or
flowrate monitoring), but did not
include information on calibration or
included inadequate information on
calibration of monitoring devices.
Therefore, we are specifying the
calibration requirements for temperature
and flow monitors that the NESHAP
currently lacks.
In addition, under the current
NESHAP, a design analysis can be used
in lieu of performance testing to
demonstrate compliance and establish
operating parameter limits. We are
proposing to allow the use of the design
evaluation alternative only when the
control device being used is a
condenser. The design evaluation
option is appropriate for condensers
because their emissions can be
accurately predicted using readily
available physical property information
(e.g., vapor pressure data and
condensation calculations). In those
cases, one would not need to conduct
emissions testing to determine actual
emissions to demonstrate compliance
with the MACT standard. For example,
a requirement that ‘‘the temperature at
the outlet of the condenser shall be
maintained at 50° Fahrenheit below the
condensation temperature calculated for
the compound of interest using the
reference equation’’ (e.g., National
Institute of Standards and Technology
Chemistry WebBook at https://
webbook.nist.gov/chemistry/) is
adequate to assure proper operation of
the condenser and, therefore,
compliance with the required emission
standard.
For other types of control
technologies, such as carbon adsorption
systems and enclosed combustion
devices,40 the ability to predict
emissions depends on data developed
by the vendor and such data may not
reliably result in an accurate prediction
of emissions from a specific facility.
40 The design analysis alternative in the existing
MACT does not apply to flares. As previously
mentioned, the existing MACT provides separate
design and operation requirements for flares.
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There are variables (e.g., air to fuel
ratios and waste constituents for
combustion; varying organic
concentrations, constituents and
capacity issues, including break-through
for carbon adsorption) that make
theoretical predictions less reliable. The
effects of these site-specific variables on
emissions are not easily predictable and
establishing monitoring conditions (e.g.,
combustion temperature, vacuum
regeneration) based on vendor data will
likely not account for those variables.
Therefore, we propose to eliminate the
design evaluation alternative for noncondenser controls.
For non-condenser controls (and
condensers not using the design
analysis option), in addition to the
initial compliance testing, we are
proposing that performance tests be
conducted at least once every 5 years
and whenever sources desire to
establish new operating limits. Under
the current NESHAP, a performance test
is only conducted in two instances: (1)
As an alternative to a design analysis for
their compliance demonstration and
identification of operating parameter
ranges and (2) as a requirement to
resolve a disagreement between the EPA
and the owner or operator regarding the
design analysis. The current NESHAP
do not require additional performance
testing beyond these two cases (i.e.,
there is no periodic testing
requirement). As mentioned above, we
are proposing to remove the design
evaluation option for non-condenser
controls. For non-condenser controls
(and condensers not using the design
analysis option), the proposed periodic
testing would ensure compliance with
the emission standards by verifying that
the control device is meeting the
necessary HAP destruction efficiency
determined in the initial performance
test. As discussed above in section
VII.E.1, we are proposing that
combustion control devices tested under
the manufacturers’ procedure are not
required to conduct periodic testing. In
addition, we are also proposing that
combustion control devices that can
demonstrate a uniform combustion zone
temperature meeting the required
control efficiency during the initial
performance test are exempt from
periodic testing. The requirement for
continuous monitoring of combustion
zone temperature is an accurate
indicator of control device performance
and eliminates the need for future
testing.
The current NESHAP (40 CFR
63.771(d) and 40 CFR 63.1281(d))
require operating an enclosed
combustion device at a minimum
residence time of 0.5 seconds at a
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minimum temperature of 760 degrees
Celsius. We are proposing to remove the
residence time requirement. The
residence time requirement is not
needed because the compliance
demonstration made during the
performance test is sufficient to ensure
that the combustion device has adequate
residence time to ensure the needed
destruction efficiency. Therefore, we are
proposing to remove the residence time
requirement.
We are also clarifying at 40 CFR
63.773(d)(3)(i) and 40 CFR
63.1283(d)(3)(i) for thermal vapor
incinerators, boilers and process
heaters, that the temperature sensor
shall be installed at a location
representative of the combustion zone
temperature. Currently, the regulation
requires that the temperature sensor be
installed at a location ‘‘downstream of
the combustion zone’’ because we had
thought that the temperature
downstream would be representative of
combustion zone temperature. We have
now learned that may or may not be the
case. We are, therefore, proposing to
amend this provision to more accurately
reflect the intended requirement.
Next, consistent with revisions for
SSM, we’ve revised 40 CFR
63.771(d)(4)(i) and 40 CFR
63.1281(d)(4)(i), except when
maintenance or repair on a unit cannot
be completed without a shutdown of the
control device.
Also, we’ve updated the criteria for
prior performance test results that can
be used to demonstrate compliance in
lieu of conducting a performance test.
These updates ensure that data for
determining compliance are accurate,
up-to-date, and truly representative of
actual operating conditions.
In addition, we are proposing to
revise the temperature monitoring
device minimum accuracy criteria in 40
CFR 63.773(d)(3)(i) to better reflect the
level of performance that is required of
the temperature monitoring devices. We
believe that temperature monitoring
devices currently used to meet the
requirements of the NESHAP can meet
the proposed revised criteria without
modification.
Also, we are proposing to revise the
calibration gas concentration for the no
detectable emissions procedure
applicable to closed vent systems in 40
CFR 63.772(c)(4)(ii) from 10,000 ppmv
to 500 ppmv methane to be consistent
with the leak threshold of 500 ppmv in
40 CFR part 63, subpart HH. The current
calibration level is inconsistent with
achieving accurate readings at the level
necessary to demonstrate there are no
detectable emissions.
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Also, we are proposing recordkeeping
and reporting requirements for carbon
adsorption systems. The current
NESHAP require the replacement of all
carbon in the carbon adsorption system
with fresh carbon on a regular,
predetermined time interval that is no
longer than the carbon service life
established for the carbon system, but
provide no recordkeeping or reporting
requirement to document and assure
compliance with this standard. We
believe that maintaining some sort of log
book is a reasonable alternative
combined with a requirement to report
instances when specified practices are
not followed. Therefore, the proposed
rule adds reporting and recordkeeping
requirements for establishing a schedule
and maintaining logs of carbon
replacement.
Finally, as noted above in section
VII.B.1, we are proposing a BTEX
emissions limit for small glycol
dehydration unit process vents. For the
compliance demonstration, we propose
that parametric monitoring of the
control device be performed. We believe
that parametric monitoring is adequate
for glycol dehydrators in these two
source categories because temperature
monitoring, whether it be to verify
proper condenser or combustion device
operation, is a reliable indicator of
performance for reducing organic HAP
emissions. We also considered the use
of a continuous emissions monitoring
system (CEMS) to monitor compliance.
However, for glycol dehydrators in the
oil and natural gas sector, the necessary
electricity, weather-protective
enclosures and daily staffing are not
usually available. We, therefore,
question the technical feasibility of
operating a CEMS correctly in this
sector. We request comment on the
practicality of including provisions in
the final rule for a CEMS to monitor
BTEX emissions for small glycol
dehydration units.
3. Startup, Shutdown, Malfunction
The United States Court of Appeals
for the District of Columbia Circuit
vacated portions of two provisions in
the EPA’s CAA section 112 regulations
governing the emissions of HAP during
periods of SSM. Sierra Club v. EPA, 551
F.3d 1019 (D.C. Cir. 2008), cert. denied,
130 S. Ct. 1735 (U.S. 2010). Specifically,
the Court vacated the SSM exemption
contained in 40 CFR 63.6(f)(1) and 40
CFR 63.6(h)(1), that is part of a
regulation, commonly referred to as the
General Provisions Rule, that the EPA
promulgated under section 112 of the
CAA. When incorporated into CAA
section 112(d) regulations for specific
source categories, these two provisions
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exempt sources from the requirement to
comply with the otherwise applicable
CAA section 112(d) emission standard
during periods of SSM.
We are proposing the elimination of
the SSM exemption in the two oil and
gas NESHAP. Consistent with Sierra
Club v. EPA, the EPA is proposing to
apply the standards in these NESHAP at
all times. In addition, we are proposing
to revise 40 CFR 63.771(d)(4)(i) and 40
CFR 63.1281(d)(4)(i) to remove the
provision allowing shutdown of the
control device during maintenance or
repair. We are also proposing several
revisions to the General Provisions
applicability table for the MACT
standard. For example, we are
proposing to eliminate the incorporation
of the General Provisions’ requirement
that the source develop a SSM plan. We
are also proposing to eliminate or revise
certain recordkeeping and reporting
requirements related to the SSM
exemption. The EPA has attempted to
ensure that we have not included in the
proposed regulatory language any
provisions that are inappropriate,
unnecessary or redundant in the
absence of the SSM exemption. We are
specifically seeking comment on
whether there are any such provisions
that we have inadvertently incorporated
or overlooked.
In proposing the MACT standards in
these rules, the EPA has taken into
account startup and shutdown periods.
We believe that operations and
emissions do not differ from normal
operations during these periods such
that it warrants a separate standard.
Therefore, we have not proposed
different standards for these periods.
Periods of startup, normal operations
and shutdown are all predictable and
routine aspects of a source’s operations.
However, by contrast, malfunction is
defined as a ‘‘sudden, infrequent and
not reasonably preventable failure of air
pollution control and monitoring
equipment, process equipment or a
process to operate in a normal or usual
manner * * *’’ (40 CFR 63.2). The EPA
has determined that malfunctions
should not be viewed as a distinct
operating mode and, therefore, any
emissions that occur at such times do
not need to be factored into
development of CAA section 112(d)
standards, which, once promulgated,
apply at all times. In Mossville
Environmental Action Now v. EPA, 370
F.3d 1232, 1242 (D.C. Cir. 2004), the
Court upheld as reasonable, standards
that had factored in variability of
emissions under all operating
conditions. However, nothing in CAA
section 112(d) or in case law requires
that the EPA anticipate and account for
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the innumerable types of potential
malfunction events in setting emission
standards. See Weyerhaeuser v. Costle,
590 F.2d 1011, 1058 (D.C. Cir. 1978),
(‘‘In the nature of things, no general
limit, individual permit, or even any
upset provision can anticipate all upset
situations. After a certain point, the
transgression of regulatory limits caused
by ‘‘uncontrollable acts of third parties,’’
such as strikes, sabotage, operator
intoxication or insanity, and a variety of
other eventualities, must be a matter for
the administrative exercise of case-bycase enforcement discretion, not for
specification in advance by
regulation.’’).
Further, it is reasonable to interpret
CAA section 112(d) as not requiring the
EPA to account for malfunctions in
setting emissions standards. For
example, we note that CAA section 112
uses the concept of ‘‘best performing’’
sources in defining MACT, the level of
stringency that major source standards
must meet. Applying the concept of
‘‘best performing’’ to a source that is
malfunctioning presents significant
difficulties. The goal of best performing
sources is to operate in such a way as
to avoid malfunctions of their units.
Moreover, even if malfunctions were
considered a distinct operating mode,
we believe it would be impracticable to
take malfunctions into account in
setting CAA section 112(d) standards for
oil and natural gas production facility
and natural gas transmission and storage
operations. As noted above, by
definition, malfunctions are sudden and
unexpected events, and it would be
difficult to set a standard that takes into
account the myriad different types of
malfunctions that can occur across all
sources in each source category.
Moreover, malfunctions can also vary in
frequency, degree and duration, further
complicating standard setting.
In the event that a source fails to
comply with the applicable CAA section
112(d) standards as a result of a
malfunction event, the EPA would
determine an appropriate response
based on, among other things, the good
faith efforts of the source to minimize
emissions during malfunction periods,
including preventative and corrective
actions, as well as root cause analyses
to ascertain and rectify excess
emissions. The EPA would also
consider whether the source’s failure to
comply with the CAA section 112(d)
standard was, in fact, ‘‘sudden,
infrequent, not reasonably preventable’’
and was not instead ‘‘caused in part by
poor maintenance or careless
operation.’’ 40 CFR 63.2 (definition of
malfunction).
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Finally, the EPA recognizes that even
equipment that is properly designed and
maintained can sometimes fail and that
such failure can sometimes cause or
contribute to an exceedance of the
relevant emission standard. (See, e.g.,
State Implementation Plans: Policy
Regarding Excessive Emissions During
Malfunctions, Startup, and Shutdown
(September 20, 1999); Policy on Excess
Emissions During Startup, Shutdown,
Maintenance, and Malfunctions
(February 15, 1983)). The EPA is,
therefore, proposing to add to the final
rule an affirmative defense to civil
penalties for exceedances of emission
limits that are caused by malfunctions
in both of the MACT standards
addressed in this proposal. See 40 CFR
63.761 for sources subject to the oil and
natural gas production MACT
standards, or 40 CFR 63.1271 for
sources subject to the natural gas
transmission and storage MACT
standards (defining ‘‘affirmative
defense’’ to mean, in the context of an
enforcement proceeding, a response or
defense put forward by a defendant,
regarding which the defendant has the
burden of proof and the merits of which
are independently and objectively
evaluated in a judicial or administrative
proceeding). We also are proposing
other regulatory provisions to specify
the elements that are necessary to
establish this affirmative defense; a
source subject to the oil and natural gas
production facilities or natural gas
transmission MACT standards must
prove by a preponderance of the
evidence that it has met all of the
elements set forth in 40 CFR 63.762 and
a source subject to the natural gas
transmission and storage facilities
MACT standards must prove by a
preponderance of the evidence that it
has met all of the elements set forth in
40 CFR 63.1272. (See 40 CFR 22.24.)
The criteria ensure that the affirmative
defense is available only where the
event that causes an exceedance of the
emission limit meets the narrow
definition of malfunction in 40 CFR 63.2
(sudden, infrequent, not reasonably
preventable and not caused by poor
maintenance and or careless operation).
For example, to successfully assert the
affirmative defense, the source must
prove by a preponderance of evidence
that excess emissions ‘‘[w]ere caused by
a sudden, infrequent, and unavoidable
failure of air pollution control and
monitoring equipment, process
equipment, or a process to operate in a
normal or usual manner * * *.’’ The
criteria also are designed to ensure that
steps are taken to correct the
malfunction, to minimize emissions in
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accordance with 40 CFR 63.762 for
sources subject to the oil and natural gas
production facilities MACT standards or
40 CFR 63.1272 for sources subject to
the natural gas transmission and storage
facilities MACT standards and to
prevent future malfunctions. For
example, the source must prove by a
preponderance of evidence that
‘‘[r]epairs were made as expeditiously as
possible when the applicable emission
limitations were being exceeded * * *’’
and that ‘‘[a]ll possible steps were taken
to minimize the impact of the excess
emissions on ambient air quality, the
environment and human health * * *.’’
In any judicial or administrative
proceeding, the Administrator may
challenge the assertion of the affirmative
defense and, if the respondent has not
met its burden of proving all of the
requirements in the affirmative defense,
appropriate penalties may be assessed
in accordance with section 113 of the
CAA (see also 40 CFR 22.77).
4. Applicability and Compliance
a. Calculating Potential To Emit (PTE)
We are proposing to amend section 40
CFR 63.760(a)(1)(iii) to clarify that
sources must use a glycol circulation
rate consistent with the definition of
PTE in 40 CFR 63.2 in calculating
emissions for purposes of determining
PTE. Affected parties have
misinterpreted the current language
concerning measured values or annual
average to apply to a broader range of
parameters than was intended. Those
qualifiers were meant to apply to gas
characteristics that are measured, such
as inlet gas composition, pressure and
temperature rather than process
equipment settings. That means that the
circulation rate used in PTE
determinations shall be the maximum
under its physical and operational
design.
In addition to the proposed changes
described above, we are seeking
comment on several PTE related issues.
According to the data available to the
Administrator, when 40 CFR part 63,
subpart HH was promulgated, the level
of HAP emissions was predominantly
driven by natural gas throughput (i.e.,
HAP emissions went up or down in
concert with natural gas throughput).
Since promulgation, we have learned
that there is not always a direct
correlation between HAP emissions and
natural gas throughput. We have
received information suggesting that, in
some cases, HAP emissions can increase
despite decreasing natural gas
throughput due to changes in gas
composition. We are asking for
comment regarding the likelihood of
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this occurrence and data demonstrating
the circumstances where it occurs. In
light of the potential issue, we are
asking for comment regarding the
addition of provisions in the NESHAP
to require area sources to recalculate
their PTE to confirm that they are
indeed area sources and whether that
calculation should be performed on an
annual or biannual basis to verify that
changes in gas composition have not
increased their emissions.
b. Definition of Facility and
Applicability Criteria
Subpart HH of 40 CFR part 63 (section
63.760(a)(2)) currently defines facilities
as those where hydrocarbon liquids are
processed, upgraded or stored prior to
the point of custody transfer or where
natural gas is processed, upgraded or
stored prior to entering the Natural Gas
Transmission and Storage source
category. We are proposing to remove
the references to ‘‘point of custody
transfer’’ and ‘‘transmission and storage
source categories’’ from the definition
because the operations performed at a
site sufficiently define a facility and the
scope of the subpart is specified already
under 40 CFR 63.760. In addition, we
are removing the custody transfer
reference from the applicability criteria
in 40 CFR 63.760(a)(2). Since
hydrocarbon liquids can pass through
several custody transfer points between
the well and the final destination, the
custody transfer criteria is not clear
enough. We are, therefore, proposing to
replace the reference to ‘‘point of
custody transfer’’ with a more specific
description of the point up to which the
subpart applies (i.e., the point where
hydrocarbon liquids enter either the
organic liquids distribution or
petroleum refineries source categories)
and exclude custody transfer from that
criteria. We believe this change
eliminates ambiguity and is consistent
with the oil and natural gas productionspecific provisions in the organic
liquids distribution MACT.
5. Other Proposed Changes To Clarify
These Rules
The following lists additional changes
to the NESHAP we are proposing. This
list includes proposed rule changes that
address editorial corrections and plain
language revisions:
• Revise 40 CFR 63.769(b) to clarify
that the equipment leak provisions in 40
CFR part 63, subpart HH do not apply
to a source if that source is required to
control equipment leaks under either 40
CFR part 63, subpart H or 40 CFR part
60, subpart KKK. The current 40 CFR
63.769(b), which states that subpart HH
does not apply if a source meets the
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requirements in either of the subparts
mentioned above, does not clearly
express our intent that such source must
be implementing the LDAR provisions
in the other 40 CFR part 60 or 40 CFR
part 63 subparts to qualify for the
exemption.
• Revise 40 CFR 63.760(a)(1) to
clarify that an existing area source that
increases its emissions to major source
levels has up to the first substantive
compliance date to either reduce its
emissions below major source levels by
obtaining a practically enforceable
permit or comply with the applicable
major source provisions of 40 CFR part
63, subpart HH. We have revised the
second to last sentence in 40 CFR
63.760(a)(1) by removing the
parenthetical statement because it
simply reiterates the last sentence of
this section and is, therefore,
unnecessary.
• Revise 40 CFR 63.771(d)(1)(ii) and
40 CFR 63.1281(d)(1)(ii) to clarify that
the vapor recovery device and ‘‘other
control device’’ described in those
provisions refer to non-destructive
control devices only.
• Revise the last sentence of 40 CFR
63.764(i) and 40 CFR 63.1274(g) to
clarify the requirements following an
unsuccessful attempt to repair a leak.
• Updated the e-mail and physical
address for area source reporting in 40
CFR 63.775(c)(1).
VIII. What are the cost, environmental,
energy and economic impacts of the
proposed 40 CFR part 60, subpart
OOOO and amendments to subparts HH
and HHH of 40 CFR part 63?
We are presenting a combined
discussion of the estimates of the
impacts for the proposed 40 CFR part
60, subpart OOOO and proposed
amendments to 40 CFR part 63, subpart
HH and 40 CFR part 63, subpart HHH.
The cost, environmental and economic
impacts presented in this section are
expressed as incremental differences
between the impacts of an oil and
natural gas facility complying with the
amendments to subparts HH and HHH
and new standards under 40 CFR 60,
subpart OOOO and the baseline, i.e., the
standards before these amendments.
The impacts are presented for the year
2015, which will be the year that all
existing oil and natural gas facilities
will have to be in compliance, and also
the year that will represent
approximately 5 years of construction of
new oil and natural gas facilities subject
to the NSPS emissions limits. The
analyses and the documents referenced
below can be found in Docket ID
Numbers EPA–HQ–OAR–2007–0877
and EPA–HQ–OAR–2002–0051.
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A. What are the affected sources?
We expect that by 2015, the year
when all existing sources will be
required to come into compliance in the
United States, there will be 97 oil and
natural gas production facilities and 15
natural gas transmission and storage
facilities with one or more existing
glycol dehydration units. We also
estimate that there will be an additional
329 (there are 47 facilities that already
have an affected glycol dehydration
unit) existing oil and natural gas
production facilities with existing
storage vessels that we expect to be
affected by these final amendments.
These facilities operate approximately
134 glycol dehydration units (115 in
production and 19 in transmission and
storage) and 1,970 storage vessels.
Approximately 10 oil and natural gas
production and two transmission and
storage facilities would have new glycol
dehydration units and 38 production
facilities would have new dehydration
units. We expect new production
facilities would operate approximately
12 production glycol dehydration units
and 197 storage vessels and new
transmission and storage would operate
approximately two glycol dehydration
units.
Based on data provided by the United
States Energy Information
Administration, we anticipate that by
2015 there will be approximately 21,800
gas wellhead facilities, 790
reciprocating compressors, 30
centrifugal compressors, 14,000
pneumatic devices and 300 storage
vessels subject to the new NSPS for
VOC. Some of these affected facilities
will be built at existing facilities and
some at new greenfield facilities. Based
on data limitations, we assume impacts
are equal regardless of location.
There are about 21 glycol dehydration
units with high enough HAP emissions
that we believe cannot meet the
emissions limit without using more than
one control technique. In developing the
cost impacts, we assume that they
would require multiple controls. The
controls for which we have detailed cost
data are condensers and VRU, so we
developed costs for both controls to
develop what we consider to be a
reasonable cost estimate for these
facilities. This does not imply that we
believe these facilities will specifically
use a combination of a condenser and
vapor recovery limit, but we do believe
the combination of these control results
is a reasonable estimate of cost.
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52789
B. How are the impacts for this proposal
evaluated?
For these proposed Oil and Natural
Gas Production and Natural Gas
Transmission and Storage NESHAP
amendments and NSPS, the EPA used
two models to evaluate the impacts of
the regulation on the industry and the
economy. Typically, in a regulatory
analysis, the EPA determines the
regulatory options suitable to meet
statutory obligations under the CAA.
Based on the stringency of those
options, the EPA then determines the
control technologies and monitoring
requirements that sources might
rationally select to comply with the
regulation. This analysis is documented
in an engineering analysis. The selected
control technologies and monitoring
requirements are then evaluated in a
cost model to determine the total
annualized control costs. The
annualized control costs serve as inputs
to an Economic Impact Analysis model
that evaluates the impacts of those costs
on the industry and society as a whole.
The Economic Impact Analysis used
the National Energy Modeling System
(NEMS) to estimate the impacts of the
proposed NSPS on the United States
energy system. The NEMS is a
publically-available model of the United
States energy economy developed and
maintained by the Energy Information
Administration of the United States
DOE and is used to produce the Annual
Energy Outlook, a reference publication
that provides detailed forecasts of the
energy economy from the current year to
2035. The impacts we estimated
included changes in drilling activity,
price and quantity changes in the
production and consumption of crude
oil and natural gas and changes in
international trade of crude oil and
natural gas. We evaluated whether and
to what extent the increased production
costs imposed by the NSPS might alter
the mix of fuels consumed at a national
level. Additionally, we combined
estimated emissions co-reductions of
methane from the engineering analysis
with NEMS analysis to estimate the net
change in CO2e GHG from energyrelated sources.
C. What are the air quality impacts?
For the oil and natural gas sector
NESHAP and NSPS, we estimated the
emission reductions that will occur due
to the implementation of the final
emission limits. The EPA estimated
emission reductions based on the
control technologies selected by the
engineering analysis. These emission
reductions associated with the proposed
amendments to 40 CFR part 63, subpart
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HH and 40 CFR part 63, subpart HHH
are based on the estimated population
in 2008. Under the proposed limits for
glycol dehydration units and storage
vessels, we have estimated that the HAP
emissions reductions will be 1,400 tpy
for existing units subject to the
proposed emissions limits.
For the NSPS, we estimated the
emission reductions that will occur due
to the implementation of the final
emission limits. The EPA estimated
emission reductions based on the
control technologies selected by the
engineering analysis. These emission
reductions are based on the estimated
population in 2015. Under the proposed
NSPS, we have estimated that the
emissions reductions will be 540,000
tpy VOC for affected facilities subject to
the NSPS.
The control strategies likely adopted
to meet the proposed NESHAP
amendments and the proposed NSPS
will result in concurrent control of HAP,
methane and VOC emissions. We
estimate that direct reductions in HAP,
methane and VOC for the proposed
rules combined total about 38,000 tpy,
3.4 million tpy and 540,000 tpy,
respectively.
Under the final standards, new
monitoring requirements are being
added.
D. What are the water quality and solid
waste impacts?
We estimated minimal water quality
impacts for the proposed amendments
and proposed NSPS. For the proposed
amendments to the NESHAP, we
anticipate that the water impacts
associated with the installation of a
condenser system for the glycol
dehydration unit process vent would be
minimal. This is because the condensed
water collected with the hydrocarbon
condensate can be directed back into the
system for reprocessing with the
hydrocarbon condensate or, if separated,
combined with produced water for
disposal, usually by reinjection.
Similarly, the water impacts
associated with installation of a vapor
control system either on a glycol
dehydration unit or a storage vessel
would be minimal. This is because the
water vapor collected along with the
hydrocarbon vapors in the vapor
collection and redirect system can be
directed back into the system for
reprocessing with the hydrocarbon
condensate or, if separated, combined
with the produced water for disposal for
reinjection.
There would be no water impacts
expected for facilities subject to the
proposed NSPS. Further, we do not
anticipate any adverse solid waste
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impacts from the implementation of the
proposed NESHAP amendments and the
proposed NSPS.
E. What are the secondary impacts?
Indirect or secondary air quality
impacts include impacts that will result
from the increased electricity usage
associated with the operation of control
devices, as well as water quality and
solid waste impacts (which were just
discussed) that might occur as a result
of these proposed actions. We estimate
the proposed amendments to 40 CFR
part 63, subpart HH and 40 CFR part 63,
subpart HHH will increase emissions of
criteria pollutants due to the potential
use of flares for the control of storage
vessels. We do not estimate an increased
energy demand associated with the
installation of condensers, VRU or
flares. The increases in criteria pollutant
emissions associated with the use of
flares to control storage vessels subject
to existing source standards are
estimated to be 5,500 tpy of CO2, 16 tpy
of carbon monoxide (CO), 3 tpy of NOX,
less than 1 tpy of particulate matter
(PM) and 6 tpy total hydrocarbons. For
storage vessels subject to new source
standards, increases in secondary air
pollutants are estimated to be less than
900 tpy of CO2, 3 tpy of CO, 1 tpy of
NOX, 1 tpy of PM and 1 tpy total
hydrocarbons.
In addition, we estimate that the
secondary impacts associated with the
pneumatic controller requirements to
comply with the proposed NSPS would
be about 22 tpy of CO2, 1 tpy of NOX
and 3 tpy PM. For gas wellhead affected
facilities, we estimate that the use of
flares would result in increases in
criteria pollutant emissions of about
990,000 tons of CO2, 2,800 tpy of CO,
500 tpy of NOX, 5 tpy of PM and 1,000
tpy total hydrocarbons.
F. What are the energy impacts?
Energy impacts in this section are
those energy requirements associated
with the operation of emission control
devices. Potential impacts on the
national energy economy from the rule
are discussed in the economic impacts
section. There would be little national
energy demand increase from the
operation of any of the control options
analyzed under the proposed NESHAP
amendments and proposed NSPS.
The proposed NESHAP amendments
and proposed NSPS encourage the use
of emission controls that recover
hydrocarbon products, such as methane
and condensate that can be used on-site
as fuel or reprocessed within the
production process for sale. We
estimated that the proposed standards
will result in a net cost savings due to
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the recovery of salable natural gas and
condensate. Thus, the final standards
have a positive impact associated with
the recovery of non-renewable energy
resources.
G. What are the cost impacts?
The estimated total capital cost to
comply with the proposed amendments
to 40 CFR part 63, subpart HH for major
sources in the Oil and Natural Gas
Production source category is
approximately $51.5 million. The total
capital cost for the proposed
amendments to 40 CFR part 63, subpart
HHH for major sources in the Natural
Gas Transmission and Storage source
category is estimated to be
approximately $370 thousand. All costs
are in 2008 dollars.
The total estimated net annual cost to
industry to comply with the proposed
amendments to 40 CFR part 63, subpart
HH for major sources in the Oil and
Natural Gas Production source category
is approximately $16 million. The total
net annual cost for proposed
amendments to 40 CFR part 63, subpart
HHH for major sources in the Natural
Gas Transmission and Storage source
category is estimated to be
approximately $360,000. These
estimated annual costs include: (1) The
cost of capital, (2) operating and
maintenance costs, (3) the cost of
monitoring, inspection, recordkeeping
and reporting (MIRR) and (4) any
associated product recovery credits. All
costs are in 2008 dollars.
The estimated total capital cost to
comply with the proposed NSPS is
approximately $740 million in 2008
dollars. The total estimated net annual
cost to industry to comply with the
proposed NSPS is approximately $740
million in 2008 dollars. This annual
cost estimate includes: (1) The cost of
capital, (2) operating and maintenance
costs and (3) the cost of MIRR. This
estimated annual cost does not take into
account any producer revenues
associated with the recovery of salable
natural gas and hydrocarbon
condensates.
When revenues from additional
product recovery are considered, the
proposed NSPS is estimated to result in
a net annual engineering cost savings
overall. When including the additional
natural gas recovery in the engineering
cost analysis, we assume that producers
are paid $4 per thousand cubic feet
(Mcf) for the recovered gas at the
wellhead. The engineering analysis cost
analysis assumes the value of recovered
condensate is $70 per barrel. Based on
the engineering analysis, about
180,000,000 Mcf (180 billion cubic feet)
of natural gas and 730,000 barrels of
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condensate are estimated to be
recovered by control requirements in
2015. Using the price assumptions, the
estimated revenues from natural gas
product recovery are approximately
$780 million in 2008 dollars. This
savings is estimated at $45 million in
2008 dollars.
Using the engineering cost estimates,
estimated natural gas product recovery,
and natural gas product price
assumptions, the net annual engineering
cost savings is estimated for the
proposed NSPS at about $45 million in
2008 dollars. Totals may not sum due to
independent rounding.
As the price assumption is very
influential on estimated annualized
engineering costs, we performed a
simple sensitivity analysis of the
influence of the assumed wellhead price
paid to natural gas producers on the
overall engineering annualized costs
estimate of the proposed NSPS. At
$4.22/Mcf, the price forecast reported in
the 2011 Annual Energy Outlook in
2008 dollars, the annualized costs are
estimated at about ¥$90 million, which
would approximately double the
estimate of net cost savings of the
proposed NSPS. As indicated by this
difference, EPA has chosen a relatively
conservative assumption (leading to an
estimate of few savings and higher net
costs) for the engineering costs analysis.
The natural gas price at which the
proposed NSPS breaks-even from an
estimated engineering costs perspective
is around $3.77/Mcf. A $1/Mcf change
in the wellhead natural gas price leads
to about a $180 million change in the
annualized engineering costs of the
proposed NSPS. Consequently,
annualized engineering costs estimates
would increase to about $140 million
under a $3/Mcf price or decrease to
about ¥$230 million under a $5/Mcf
price. For further details on this
sensitivity analysis, please refer the
regulatory impact analysis (RIA) for this
rulemaking located in the docket.
H. What are the economic impacts?
The NEMS analysis of energy system
impacts for the proposed NSPS option
estimates that domestic natural gas
production is likely to increase slightly
(about 20 billion cubic feet or 0.1
percent) and average natural gas prices
to decrease slightly ($0.04 per Mcf in
2008 dollars or 0.9 percent at the
wellhead for onshore producers in the
lower 48 states) for 2015, the year of
analysis. This increase in production
and decrease in wellhead price is
largely a result of the increased natural
gas and condensate recovery as a result
of complying with the NSPS. Domestic
crude oil production is not expected to
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change, while average crude oil prices
are estimated to decrease slightly
($0.02/barrel in 2008 dollars or less than
0.1 percent at the wellhead for onshore
producers in the lower 48 states) in the
year of analysis, 2015. The NEMS-based
analysis estimates in the year of
analysis, 2015, that net imports of
natural gas and crude will not change
significantly.
Total CO2e emissions from energyrelated sources are expected to increase
about 2.0 million metric tons CO2e or
0.04 percent under the proposed NSPS,
according to the NEMS analysis. This
increase is attributable largely to natural
gas consumption increases. This
estimate does not include CO2e
reductions from the implementation of
the controls; these reductions are
discussed in more detail in the benefits
section that follows.
We did not estimate the energy
economy impacts of the proposed
NESHAP amendments using NEMS, as
the expected costs of the rule are not
likely to have estimable impacts on the
national energy economy.
I. What are the benefits?
The proposed Oil and Natural Gas
NSPS and NESHAP amendments are
expected to result in significant
reductions in existing emissions and
prevent new emissions from expansions
of the industry. These proposed rules
combined are anticipated to reduce
38,000 tons of HAP, 540,000 tons of
VOC and 3.4 million tons of methane.
These pollutants are associated with
substantial health effects, welfare effects
and climate effects. With the data
available, we are not able to provide
credible health benefit estimates for the
reduction in exposure to HAP, ozone
and PM (2.5 microns and less) (PM2.5)
for these rules, due to the differences in
the locations of oil and natural gas
emission points relative to existing
information and the highly localized
nature of air quality responses
associated with HAP and VOC
reductions.
This is not to imply that there are no
benefits of the rules; rather, it is a
reflection of the difficulties in modeling
the direct and indirect impacts of the
reductions in emissions for this
industrial sector with the data currently
available. In addition to health
improvements, there will be
improvements in visibility effects,
ecosystem effects and climate effects, as
well as additional product recovery.
Although we do not have sufficient
information or modeling available to
provide quantitative estimates for this
rulemaking, we include a qualitative
assessment of the health effects
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52791
associated with exposure to HAP, ozone
and PM2.5 in the RIA for this rule. These
qualitative effects are briefly
summarized below, but for more
detailed information, please refer to the
RIA, which is available in the docket.
One of the HAP of concern from the oil
and natural gas sector is benzene, which
is a known human carcinogen, and
formaldehyde, which is a probable
human carcinogen. VOC emissions are
precursors to both PM2.5 and ozone
formation. As documented in previous
analyses (U.S. EPA, 2006 41 and U.S.
EPA, 2010 42), exposure to PM2.5 and
ozone is associated with significant
public health effects. PM2.5 is associated
with health effects such as premature
mortality for adults and infants,
cardiovascular morbidity, such as heart
attacks, hospital admissions and
respiratory morbidity such as asthma
attacks, acute and chronic bronchitis,
hospital and emergency room visits,
work loss days, restricted activity days
and respiratory symptoms, as well as
visibility impairment.43 Ozone is
associated with health effects such as
respiratory morbidity such as asthma
attacks, hospital and emergency
department visits, school loss days and
premature mortality, as well as injury to
vegetation and climate effects.44
In addition to the improvements in air
quality and resulting benefits to human
health and non-climate welfare effects
previously discussed, this proposed rule
is expected to result in significant
climate co-benefits due to anticipated
methane reductions. Methane is a
potent GHG that, once emitted into the
atmosphere, absorbs terrestrial infrared
radiation, which contributes to
increased global warming and
continuing climate change. Methane
reacts in the atmosphere to form ozone
and ozone also impacts global
temperatures. According to the
41 U.S. EPA. RIA. National Ambient Air Quality
Standards for Particulate Matter, Chapter 5. Office
of Air Quality Planning and Standards, Research
Triangle Park, NC. October 2006. Available on the
Internet at https://www.epa.gov/ttn/ecas/regdata/
RIAs/Chapter%205-Benefits.pdf.
42 U.S. EPA. RIA. National Ambient Air Quality
Standards for Ozone. Office of Air Quality Planning
and Standards, Research Triangle Park, NC. January
2010. Available on the Internet at https://
www.epa.gov/ttn/ecas/regdata/RIAs/s1supplemental_analysis_full.pdf.
43 U.S. EPA. Integrated Science Assessment for
Particulate Matter (Final Report). EPA–600–R–08–
139F. National Center for Environmental
Assessment—RTP Division. December 2009.
Available at https://cfpub.epa.gov/ncea/cfm/
recordisplay.cfm?deid=216546.
44 U.S. EPA. Air Quality Criteria for Ozone and
Related Photochemical Oxidants (Final). EPA/600/
R–05/004aF–cF. Washington, DC: U.S. EPA.
February 2006. Available on the Internet at https://
cfpub.epa.gov/ncea/CFM/
recordisplay.cfm?deid=149923.
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
Intergovernmental Panel on Climate
Change (IPCC) 4th Assessment Report
(2007), methane is the second leading
long-lived climate forcer after CO2
globally. Total methane emissions from
the oil and gas industry represent about
40 percent of the total methane
emissions from all sources and account
for about 5 percent of all CO2e
emissions in the United States, with
natural gas systems being the single
largest contributor to United States
anthropogenic methane emissions.45
Methane, in addition to other GHG
emissions, contributes to warming of the
atmosphere, which, over time, leads to
increased air and ocean temperatures,
changes in precipitation patterns,
melting and thawing of global glaciers
and ice, increasingly severe weather
events, such as hurricanes of greater
intensity and sea level rise, among other
impacts.
This rulemaking proposes emission
control technologies and regulatory
alternatives that will significantly
decrease methane emissions from the oil
and natural gas sector in the United
States. The regulatory alternatives
proposed for the NESHAP and the NSPS
are expected to reduce methane
emissions annually by about 3.4 million
short tons or 65 million metric tons
CO2e. After considering the secondary
impacts of this proposal previously
discussed, such as increased CO2
emissions from well completion
combustion and decreased CO2e
emissions because of fuel-switching by
consumers, the methane reductions
become about 62 million metric tons
CO2e. These reductions represent about
26 percent of the baseline methane
emissions for this sector reported in the
EPA’s U.S. Greenhouse Gas Inventory
Report for 2009 (251.55 million metric
tons CO2e when petroleum refineries
and petroleum transportation are
excluded because these sources are not
examined in this proposal). After
considering the secondary impacts of
this proposal, such as increased CO2
emissions from well completion
combustion and decreased CO2
emissions because of fuel-switching by
consumers, the CO2e GHG reductions
are reduced to about 62 million metric
tons CO2e. However, it is important to
note that the emission reductions are
based upon predicted activities in 2015;
the EPA did not forecast sector-level
emissions in 2015 for this rulemaking.
These emission reductions equate to the
45 U.S. EPA (2011), 2011 U.S. Greenhouse Gas
Inventory Report Executive Summary available on
the internet at https://www.epa.gov/
climateexchange/emissions/downloads11/US-GHGInventory-2011-Executive Summary.pdf.
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climate benefits of taking approximately
11 million typical passenger cars off the
road or eliminating electricity use from
about 7 million typical homes each
year.46
The EPA recognizes that the methane
reductions proposed in this rule will
provide for significant economic climate
benefits to society just described.
However, there is no interagencyaccepted methodology to place
monetary values on these benefits. A
‘global warming potential (GWP)
approach’ of converting methane to
CO2e using the GWP of methane
provides an approximation method for
estimating the monetized value of the
methane reductions anticipated from
this rule. This calculation uses the GWP
of the non-CO2 gas to estimate CO2
equivalents and then multiplies these
CO2 equivalent emission reductions by
the social cost of carbon developed by
the Interagency Social Cost of Carbon
Work Group to generate monetized
estimates of the benefits.
The social cost of carbon is an
estimate of the net present value of the
flow of monetized damages from a 1metric ton increase in CO2 emissions in
a given year (or from the alternative
perspective, the benefit to society of
reducing CO2 emissions by 1 ton). For
more information about the social cost
of carbon, see the Support Document:
Social Cost of Carbon for Regulatory
Impact Analysis Under Executive Order
12866 47 and RIA for the Light-Duty
Vehicle GHG rule.48 Applying this
approach to the methane reductions
estimated for the proposed NESHAP
and NSPS of the oil and gas rule, the
2015 climate co-benefits vary by
discount rate and range from about $370
million to approximately $4.7 billion;
the mean social cost of carbon at the 3percent discount rate results in an
estimate of about $1.6 billion in 2015.
The ratio of domestic to global
benefits of emission reductions varies
with key parameter assumptions. For
example, with a 2.5 or 3 percent
discount rate, the U.S. benefit is about
7–10 percent of the global benefit, on
average, across the scenarios analyzed.
46 U.S. EPA. Greenhouse Gas Equivalency
Calculator available at: https://www.epa.gov/
cleanenergy/energy-resources/calculator.html
accessed 07/19/11.
47 Interagency Working Group on Social Cost of
Carbon (IWGSC). 2010. Technical Support
Document: Social Cost of Carbon for Regulatory
Impact Analysis Under Executive Order 12866.
Docket ID EPA–HQ–OAR–2009–0472–114577.
https://www.epa.gov/otaq/climate/regulations/scctsd.pdf; Accessed March 30, 2011.
48 U.S. EPA. Final Rulemaking: Light-Duty
Vehicle Greenhouse Gas Emissions Standards and
Corporate Average Fuel Economy Standards. May
2010. Available on the Internet at https://
www.epa.gov/otaq/climate/regulations.htm#finalR.
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Alternatively, if the fraction of GDP lost
due to climate change is assumed to be
similar across countries, the domestic
benefit would be proportional to the
U.S. share of global GDP, which is
currently about 23 percent. On the basis
of this evidence, values from 7 to 23
percent should be used to adjust the
global SCC to calculate domestic effects.
It is recognized that these values are
approximate, provisional and highly
speculative. There is no a priori reason
why domestic benefits should be a
constant fraction of net global damages
over time.49
These co-benefits equate to a range of
approximately $110 to $1,400 per short
ton of methane reduced, depending
upon the discount rate assumed with a
per ton estimate of $480 at the 3-percent
discount rate. Methane climate cobenefit estimates for additional
regulatory alternatives are included in
the RIA for this proposed rule. These
social cost of methane benefit estimates
are not the same as would be derived
from direct computations (using the
integrated assessment models employed
to develop the Interagency Social Cost
of Carbon estimates) for a variety of
reasons, including the shorter
atmospheric lifetime of methane relative
to CO2 (about 12 years compared to CO2
whose concentrations in the atmosphere
decay on timescales of decades to
millennia). The climate impacts also
differ between the pollutants for reasons
other than the radiative forcing profiles
and atmospheric lifetimes of these
gases.
Methane is a precursor to ozone and
ozone is a short-lived climate forcer that
contributes to global warming. The use
of the IPCC Second Assessment Report
GWP to approximate co-benefits may
underestimate the direct radiative
forcing benefits of reduced ozone levels
and does not capture any secondary
climate co-benefits involved with
ozone-ecosystem interactions. In
addition, a recent EPA National Center
of Environmental Economics working
paper suggests that this quick ‘GWP
approach’ to benefits estimation will
likely understate the climate benefits of
methane reductions in most cases.50
This conclusion is reached using the
100-year GWP for methane of 25 as put
forth in the IPCC Fourth Assessment
Report (AR 4), as opposed to the lower
49 Interagency Working Group on Social Cost of
Carbon (IWGSC). 2010. Technical Support
Document: Social Cost of Carbon for Regulatory
Impact Analysis Under Executive Order 12866.
50 Marten and Newbold (2011), Estimating the
Social Cost of Non-CO2 GHG Emissions: Methane
and Nitrous Oxide, NCEE Working Paper Series
#11–01. https://yosemite.epa.gov/EE/epa/eed.nsf/
WPNumber/2011-01?OpenDocument.
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value of 21 used in this analysis. Using
the higher GWP estimate of 25 would
increase these reported methane climate
co-benefit estimates by about 19
percent. Although the IPCC Assessment
Report (AR4) suggested a GWP of 25 for
methane, the EPA has used GWP of 21
to estimate the methane climate cobenefits for this oil and gas proposal in
order to provide estimates more
consistent with global GHG inventories,
which currently use GWP from the IPCC
Second Assessment Report.
Due to the uncertainties involved
with the ‘GWP approach’ estimates
presented and methane climate cobenefits estimates available in the
literature, the EPA chooses not to
compare these co-benefit estimates to
the costs of the rule for this proposal.
Rather, the EPA presents the ‘GWP
approach’ climate co-benefit estimates
as an interim method to produce these
estimates until the Interagency Social
Cost of Carbon Work Group develops
values for non-CO2 GHG. The EPA
requests comments from interested
parties and the public about this interim
approach specifically and more broadly
about appropriate methods to monetize
the climate benefits of methane
reductions. In particular, the EPA seeks
public comments to this proposed
rulemaking regarding social cost of
methane estimates that may be used to
value the co-benefits of methane
emission reductions anticipated for the
oil and gas industry from this rule.
Comments specific to whether GWP is
an acceptable method for generating a
placeholder value for the social cost of
methane until interagency-modeled
estimates become available are
welcome. Public comments may be
provided in the official docket for this
proposed rulemaking in accordance
with the process outlined earlier in this
notice. These comments will be
considered in developing the final rule
for this rulemaking.
For the proposed NESHAP
amendments, a break-even analysis
suggests that HAP emissions would
need to be valued at $12,000 per ton for
the benefits to exceed the costs if the
health, ecosystem and climate benefits
from the reductions in VOC and
methane emissions are assumed to be
zero. Even though emission reductions
of VOC and methane are co-benefits for
the proposed NESHAP amendments,
they are legitimate components of the
total benefit-cost comparison. If we
assume the health benefits from HAP
emission reductions are zero, the VOC
emissions would need to be valued at
$1,700 per ton or the methane emissions
would need to be valued at $3,300 per
ton for the co-benefits to exceed the
costs. All estimates are in 2008 dollars.
For the proposed NSPS, the revenue
from additional product recovery
exceeds the costs, which renders a
break-even analysis unnecessary when
these revenues are included in the
analysis. Based on the methodology
from Fann, Fulcher, and Hubbell
(2009),51 ranges of benefit-per-ton
estimates for emissions of VOC indicate
that on average in the United States,
VOC emissions are valued from $1,200
to $3,000 per ton as a PM2.5 precursor,
but emission reductions in specific
areas are valued from $280 to $7,000 per
ton in 2008 dollars. As a result, even if
VOC emissions from oil and natural gas
operations result in monetized benefits
that are substantially below the national
average, there is a reasonable chance
that the benefits of the rule would
exceed the costs, especially if we were
able to monetize all of the additional
benefits associated with ozone
formation, visibility, HAP and methane.
IX. Request for Comments
We are soliciting comments on all
aspects of this proposed action. All
comments received during the comment
period will be considered. In addition to
general comments on the proposed
52793
actions, we are also interested in any
additional data that may help to reduce
the uncertainties inherent in the risk
assessments. We are specifically
interested in receiving corrections to the
datasets used for MACT analyses and
risk modeling. Such data should include
supporting documentation in sufficient
detail to allow characterization of the
quality and representativeness of the
data or information. Please see the
following section for more information
on submitting data.
X. Submitting Data Corrections
The facility-specific data used in the
source category risk analyses, facilitywide analyses and demographic
analyses for each source category
subject to this action are available for
download on the RTR Web page at
https://www.epa.gov/ttn/atw/rrisk/
rtrpg.html. These data files include
detailed information for each HAP
emissions release point at each facility
included in the source category and all
other HAP emissions sources at these
facilities (facility-wide emissions
sources). However, it is important to
note that the source category risk
analysis included only those emissions
tagged with the MACT code associated
with the source category subject to the
risk analysis.
If you believe the data are not
representative or are inaccurate, please
identify the data in question, provide
your reason for concern and provide any
‘‘improved’’ data that you have, if
available. When you submit data, we
request that you provide documentation
of the basis for the revised values to
support your suggested changes. To
submit comments on the data
downloaded from the RTR Web page,
complete the following steps:
1. Within this downloaded file, enter
suggested revisions to the data fields
appropriate for that information. The
data fields that may be revised include
the following:
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
Data element
Definition
Control Measure .................................................................
Control Measure Comment ................................................
Delete .................................................................................
Delete Comment ................................................................
Emission Calculation Method Code for Revised Emissions.
Emission Process Group ...................................................
Are control measures in place? (yes or no).
Select control measure from list provided and briefly describe the control measure.
Indicate here if the facility or record should be deleted.
Describes the reason for deletion.
Code description of the method used to derive emissions. For example, CEM, material balance, stack test, etc.
Enter the general type of emission process associated with the specified emission
point.
Enter release angle (clockwise from true North); orientation of the y-dimension relative to true North, measured positive for clockwise starting at 0 degrees (maximum 89 degrees).
Enter dimension of the source in the east-west (x-) direction, commonly referred to
as length (ft).
Fugitive Angle ....................................................................
Fugitive Length ...................................................................
51 Fann, N., C.M. Fulcher, B.J. Hubbell. The
influence of location, source, and emission type in
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estimates of the human health benefits of reducing
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a ton of air pollution. Air Qual Atmos Health (2009)
2:169–176.
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Data element
Definition
Fugitive Width ....................................................................
Enter dimension of the source in the north-south (y-) direction, commonly referred to
as width (ft).
Enter total annual emissions due to malfunctions (TPY).
Enter maximum hourly malfunction emissions here (lb/hr).
Enter datum for latitude/longitude coordinates (NAD27 or NAD83); if left blank,
NAD83 is assumed.
Enter general comments about process sources of emissions.
Enter revised physical street address for MACT facility here.
Enter revised city name here.
Enter revised county name here.
Enter revised Emission Release Point Type here.
Enter revised End Date here.
Enter revised Exit Gas Flowrate here (ft3/sec).
Enter revised Exit Gas Temperature here (OF).
Enter revised Exit Gas Velocity here (ft/sec).
Enter revised Facility Category Code here, which indicates whether facility is a major
or area source.
Enter revised Facility Name here.
Enter revised Facility Registry Identifier here, which is an ID assigned by the EPA
Facility Registry System.
Enter revised HAP Emissions Performance Level here.
Enter revised Latitude here (decimal degrees).
Enter revised Longitude here (decimal degrees).
Enter revised MACT Code here.
Enter revised Pollutant Code here.
Enter revised routine emissions value here (TPY).
Enter revised SCC Code here.
Enter revised Stack Diameter here (ft).
Enter revised Stack Height here (Ft).
Enter revised Start Date here.
Enter revised state here.
Enter revised Tribal Code here.
Enter revised Zip Code here.
Enter total annual emissions due to shutdown events (TPY).
Enter maximum hourly shutdown emissions here (lb/hr).
Enter general comments about emission release points.
Enter total annual emissions due to startup events (TPY).
Enter maximum hourly startup emissions here (lb/hr).
Enter date facility stopped operations.
Malfunction Emissions .......................................................
Malfunction Emissions Max Hourly ....................................
North American Datum ......................................................
Process Comment ..............................................................
REVISED Address .............................................................
REVISED City ....................................................................
REVISED County Name ....................................................
REVISED Emission Release Point Type ...........................
REVISED End Date ...........................................................
REVISED Exit Gas Flow Rate ...........................................
REVISED Exit Gas Temperature .......................................
REVISED Exit Gas Velocity ...............................................
REVISED Facility Category Code ......................................
REVISED Facility Name ....................................................
REVISED Facility Registry Identifier ..................................
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
REVISED HAP Emissions Performance Level Code ........
REVISED Latitude ..............................................................
REVISED Longitude ...........................................................
REVISED MACT Code ......................................................
REVISED Pollutant Code ...................................................
REVISED Routine Emissions ............................................
REVISED SCC Code .........................................................
REVISED Stack Diameter ..................................................
REVISED Stack Height ......................................................
REVISED Start Date ..........................................................
REVISED State ..................................................................
REVISED Tribal Code ........................................................
REVISED Zip Code ............................................................
Shutdown Emissions ..........................................................
Shutdown Emissions Max Hourly ......................................
Stack Comment ..................................................................
Startup Emissions ..............................................................
Startup Emissions Max Hourly ...........................................
Year Closed .......................................................................
2. Fill in the commenter information
fields for each suggested revision (i.e.,
commenter name, commenter
organization, commenter e-mail address,
commenter phone number and revision
comments).
3. Gather documentation for any
suggested emissions revisions (e.g.,
performance test reports, material
balance calculations, etc.).
4. Send the entire downloaded file
with suggested revisions in Microsoft®
Access format and all accompanying
documentation to Docket ID Number
EPA–HQ–OAR–2010–0505 (through one
of the methods described in the
ADDRESSES section of this preamble). To
expedite review of the revisions, it
would also be helpful if you submitted
a copy of your revisions to the EPA
directly at RTR@epa.gov in addition to
submitting them to the docket.
5. If you are providing comments on
a facility with multiple source
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categories, you need only submit one
file for that facility, which should
contain all suggested changes for all
source categories at that facility. We
request that all data revision comments
be submitted in the form of updated
Microsoft® Access files, which are
provided on the https://www.epa.gov/ttn/
atw/rrisk/rtrpg.html Web page.
XI. Statutory and Executive Order
Reviews
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
Under Executive Order 12866 (58 FR
51735, October 4, 1993), this action is
an ‘‘economically significant regulatory
action’’ because it is likely to have an
annual effect on the economy of $100
million or more. Accordingly, the EPA
submitted this action to OMB for review
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under Executive Order 12866 and
Executive Order 13563 (76 FR 3821,
January 21, 2011) and any changes made
in response to OMB recommendations
have been documented in the docket for
this action.
In addition, the EPA prepared a RIA
of the potential costs and benefits
associated with this action. The RIA
available in the docket describes in
detail the empirical basis for the EPA’s
assumptions and characterizes the
various sources of uncertainties
affecting the estimates below. Table 8
shows the results of the cost and
benefits analysis for these proposed
rules. For more information on the
benefit and cost analysis, as well as
details on the regulatory options
considered, please refer to the RIA for
this rulemaking, which is available in
the docket.
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52795
TABLE 8—SUMMARY OF THE MONETIZED BENEFITS, COSTS AND NET BENEFITS FOR THE PROPOSED OIL AND NATURAL
GAS NSPS AND NEHSAP AMENDMENTS IN 2015
[Millions of 2008$] 1
Proposed NESHAP
amendments
Proposed NSPS
Total Monetized Benefits 2 ...............................................
Total Costs 3 ....................................................................
Net Benefits .....................................................................
Non-monetized Benefits 4 5 ..............................................
N/A
¥$45 million
N/A
37,000 tons of HAP
540,000 tons of VOC
3.4 million tons of methane
N/A
$16 million
N/A
1,400 tons of HAP
9,200 tons of VOC
4,900 tons of methane
Proposed NSPS and
NESHAP amendments
combined
N/A.
¥$29 million.
N/A.
38,000 tons of HAP.
540,000 tons of VOC.
3.4 million tons of methane.
Health effects of HAP exposure.
Health effects of PM2.5 and ozone exposure.
Visibility impairment.
Vegetation effects.
Climate effects.
1 All
estimates are for the implementation year (2015).
we expect that these avoided emissions will result in improvements in air quality and reductions in health effects associated with HAP,
ozone and PM, as well as climate effects associated with methane, we have determined that quantification of those benefits cannot be accomplished for this rule in a defensible way. This is not to imply that there are no benefits of the rules; rather, it is a reflection of the difficulties in
modeling the direct and indirect impacts of the reductions in emissions for this industrial sector with the data currently available.
3 The engineering compliance costs are annualized using a 7-percent discount rate. The negative cost for the proposed NSPS reflects the inclusion of revenues from additional natural gas and hydrocarbon condensate recovery that are estimated as a result of the proposed NSPS.
4 For the NSPS, reduced exposure to HAP and climate effects are co-benefits. For the NESHAP, reduced VOC emissions, PM
2.5 and ozone
exposure, visibility and vegetation effects and climate effects are co-benefits.
5 The specific control technologies for these proposed rules are anticipated to have minor secondary disbenefits. The net CO -equivalent emis2
sion reductions are 93,000 metric tons for the NESHAP and 62 million metric tons for the NSPS.
2 While
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B. Paperwork Reduction Act
The information collection
requirements in this proposed action
have been submitted for approval to
OMB under the Paperwork Reduction
Act, 44 U.S.C. 3501, et seq. The ICR
document prepared by the EPA has been
assigned EPA ICR Numbers 1716.07 (40
CFR part 60, subpart OOOO), 1788.10
(40 CFR part 63, subpart HH), 1789.07
(40 CFR part 63, subpart HHH) and
1086.10 (40 CFR part 60, subparts KKK
and subpart LLL).
The information to be collected for
the proposed NSPS and the proposed
NESHAP amendments are based on
notification, recordkeeping and
reporting requirements in the NESHAP
General Provisions (40 CFR part 63,
subpart A), which are mandatory for all
operators subject to national emission
standards. These recordkeeping and
reporting requirements are specifically
authorized by section 114 of the CAA
(42 U.S.C. 7414). All information
submitted to the EPA pursuant to the
recordkeeping and reporting
requirements for which a claim of
confidentiality is made is safeguarded
according to Agency policies set forth in
40 CFR part 2, subpart B.
These proposed rules would require
maintenance inspections of the control
devices, but would not require any
notifications or reports beyond those
required by the General Provisions. The
recordkeeping requirements require
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only the specific information needed to
determine compliance.
For sources subject to the proposed
NSPS, burden changes associated with
these amendments result from the
respondents’ annual reporting and
recordkeeping burden associated with
this proposed rule for this collection
(averaged over the first 3 years after the
effective date of the standards). The
burden is estimated to be 560,000 labor
hours at a cost of $18 million per year.
This includes the burden previously
estimated for sources subject to 40 CFR
part 60, subpart KKK (which is being
incorporated into 40 CFR part 60,
subpart OOOO). The average hours and
cost per regulated entity subject to the
NSPS for oil and natural gas production
and natural gas transmissions and
distribution facilities would be 110
hours per response and $3,693 per
response, based on an average of 1,459
operators responding per year and 16
responses per year.
The estimated recordkeeping and
reporting burden after the effective date
of the proposed amendments is
estimated for all affected major and area
sources subject to the Oil and Natural
Gas Production NESHAP to be
approximately 63,000 labor hours per
year at a cost of $2.1 million per year.
For the Natural Gas Transmission and
Storage NESHAP, the recordkeeping and
reporting burden is estimated to be
2,500 labor hours per year at a cost of
$86,800 per year. This estimate includes
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the cost of reporting, including reading
instructions and information gathering.
Recordkeeping cost estimates include
reading instructions, planning activities
and conducting compliance monitoring.
The average hours and cost per
regulated entity subject to the Oil and
Natural Gas Production NESHAP would
be 72 hours per year and $2,500 per
year, based on an average of 846
facilities per year and three responses
per facility. For the Natural Gas
Transmission and Storage NESHAP, the
average hours and cost per regulated
entity would be 50 hours per year and
$1,600 per year, based on an average of
53 facilities per year and three
responses per facility. Burden is defined
at 5 CFR 1320.3(b).
An agency may not conduct or
sponsor, and a person is not required to
respond to, a collection of information
unless it displays a currently valid OMB
control number. The OMB control
numbers for the EPA’s regulations in 40
CFR are listed in 40 CFR part 9.
To comment on the Agency’s need for
this information, the accuracy of the
provided burden estimates and any
suggested methods for minimizing
respondent burden, the EPA has
established a public docket for this rule,
which includes this ICR, under Docket
ID Number EPA–HQ–OAR–2010–0505.
Submit any comments related to the ICR
to the EPA and OMB. See the ADDRESSES
section at the beginning of this notice
for where to submit comments to the
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EPA. Send comments to OMB at the
Office of Information and Regulatory
Affairs, Office of Management and
Budget, 725 17th Street, NW.,
Washington, DC 20503, Attention: Desk
Office for the EPA. Since OMB is
required to make a decision concerning
the ICR between 30 and 60 days after
August 23, 2011, a comment to OMB is
best assured of having its full effect if
OMB receives it by September 22, 2011.
The final rule will respond to any OMB
or public comments on the information
collection requirements contained in
this proposal.
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C. Regulatory Flexibility Act
The Regulatory Flexibility Act
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act or any
other statute, unless the agency certifies
that the rule will not have a significant
economic impact on a substantial
number of small entities (SISNOSE).
Small entities include small businesses,
small organizations, and small
governmental jurisdictions. For
purposes of assessing the impact of this
rule on small entities, a small entity is
defined as: (1) A small business whose
parent company has no more than 500
employees (or revenues of less than $7
million for firms that transport natural
gas via pipeline); (2) a small
governmental jurisdiction that is a
government of a city, county, town,
school district, or special district with a
population of less than 50,000; and (3)
a small organization that is any not-forprofit enterprise which is independently
owned and operated and is not
dominant in its field.
Proposed NSPS
After considering the economic
impact of the proposed NSPS on small
entities, I certify that this action will not
have a SISNOSE. The EPA performed a
screening analysis for impacts on a
sample of expected affected small
entities by comparing compliance costs
to entity revenues. Based upon the
analysis in the RIA, which is in the
Docket, EPA concludes the number of
impacted small businesses is unlikely to
be sufficiently large to declare a
SISNOSE. Our judgment in this
determination is informed by the fact
that many affected firms are expected to
receive revenues from the additional
natural gas and condensate recovery
engendered by the implementation of
the controls evaluated in this RIA. As
much of the additional natural gas
recovery is estimated to arise from
completion-related activities, we expect
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the impact on well-related compliance
costs to be significantly mitigated. This
conclusion is enhanced because the
returns to REC activities occur without
a significant time lag between
implementing the control and obtaining
the recovered product, unlike many
control options where the emissions
reductions accumulate over long
periods of time; the reduced emission
completions and recompletions occur
over a short span of time, during which
the additional product recovery is also
accomplished.
Proposed NESHAP Amendments
After considering the economic
impact of the proposed NESHAP
amendments on small entities, I certify
that this action will not have a
SISNOSE. Based upon the analysis in
the RIA, which is in the Docket, we
estimate that 62 of the 118 firms (53
percent) that own potentially affected
facilities are small entities. The EPA
performed a screening analysis for
impacts on all expected affected small
entities by comparing compliance costs
to entity revenues. Among the small
firms, 52 of the 62 (84 percent) are likely
to have impacts of less than 1 percent
in terms of the ratio of annualized
compliance costs to revenues.
Meanwhile, 10 firms (16 percent) are
likely to have impacts greater than 1
percent. Four of these 10 firms are likely
to have impacts greater than 3 percent.
While these 10 firms might receive
significant impacts from the proposed
NESHAP amendments, they represent a
very small slice of the oil and gas
industry in its entirety, less than 0.2
percent of the estimated 6,427 small
firms in NAICS 211. Although this final
rule will not impact a substantial
number of small entities, the EPA,
nonetheless, has tried to reduce the
impact of this rule on small entities by
setting the final emissions limits at the
MACT floor, the least stringent level
allowed by law.
We continue to be interested in the
potential impacts of the proposed rule
on small entities and welcome
comments on issues related to such
impacts.
D. Unfunded Mandates Reform Act
This action contains no Federal
mandates under the provisions of title II
of the Unfunded Mandates Reform Act
of 1995 (UMRA), 2 U.S.C. 1531–1538 for
state, local or tribal governments or the
private sector. This proposed rule does
not contain a Federal mandate that may
result in expenditures of $100 million or
more for state, local and tribal
governments, in the aggregate, or to the
private sector in any one year. Thus,
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this proposed rule is not subject to the
requirements of sections 202 or 205 of
UMRA. This proposed rule is also not
subject to the requirements of section
203 of UMRA because it contains no
regulatory requirements that might
significantly or uniquely affect small
governments. This action contains no
requirements that apply to such
governments nor does it impose
obligations upon them.
E. Executive Order 13132: Federalism
This proposed 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. Thus, Executive
Order 13132 does not apply to this
proposed rule. In the spirit of Executive
Order 13132 and consistent with the
EPA policy to promote communications
between the EPA and state and local
governments, the EPA specifically
solicits comment on this proposed rule
from state and local officials.
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This action does not have tribal
implications, as specified in Executive
Order 13175 (65 FR 67249, November 9,
2000). It will not have substantial direct
effect on tribal governments, on the
relationship between the Federal
government and Indian tribes or on the
distribution of power and
responsibilities between the Federal
government and Indian tribes, as
specified in Executive Order 13175.
Thus, Executive Order 13175 does not
apply to this action.
The EPA specifically solicits
additional comment on this proposed
action from tribal officials.
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
This proposed rule is not subject to
Executive Order 13045 (62 FR 19885,
April 23, 1997) because the Agency does
not believe the environmental health
risks or safety risks addressed by this
action present a disproportionate risk to
children. This actions’ health and risk
assessments are contained in section
VII.C of this preamble.
The public is invited to submit
comments or identify peer-reviewed
studies and data that assess effects of
early life exposure to HAP from oil and
natural gas sector activities.
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H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution or Use
Executive Order 13211, (66 FR 28,355,
May 22, 2001), provides that agencies
shall prepare and submit to the
Administrator of the Office of
Information and Regulatory Affairs,
OMB, a Statement of Energy Effects for
certain actions identified as significant
energy actions. Section 4(b) of Executive
Order 13211 defines ‘‘significant energy
actions’’ as ‘‘any action by an agency
(normally published in the Federal
Register) that promulgates or is
expected to lead to the promulgation of
a final rule or regulation, including
notices of inquiry, advance notices of
proposed rulemaking, and notices of
proposed rulemaking: (1)(i) That is a
significant regulatory action under
Executive Order 12866 or any successor
order and (ii) is likely to have a
significant adverse effect on the supply,
distribution, or use of energy; or (2) that
is designated by the Administrator of
the Office of Information and Regulatory
Affairs as a significant energy action.’’
The proposed rules will result in the
addition of control equipment and
monitoring systems for existing and new
sources within the oil and natural gas
industry. The proposed NESHAP
amendments are unlikely to have a
significant adverse effect on the supply,
distribution or use of energy. As such,
the proposed NESHAP amendments are
not ‘‘significant energy actions’’ as
defined in Executive Order 13211 (66
FR 28355, May 22, 2001).
The proposed NSPS is also unlikely to
have a significant effect on the supply,
distribution or use of energy. As such,
the proposed NSPS is not a ‘‘significant
energy action’’ as defined in Executive
Order 13211 (66 FR 28355, May 22,
2001). The basis for the determination is
as follows.
As discussed in the impacts section of
the Preamble, we use the NEMS to
estimate the impacts of the proposed
NSPS on the United States energy
system. The NEMS is a publically
available model of the United States
energy economy developed and
maintained by the Energy Information
Administration of the United States
DOE and is used to produce the Annual
Energy Outlook, a reference publication
that provides detailed forecasts of the
United States energy economy.
Proposed emission controls for the
NSPS capture VOC emissions that
otherwise would be vented to the
atmosphere. Since methane is coemitted with VOC, a large proportion of
the averted methane emissions can be
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directed into natural gas production
streams and sold. One pollution control
requirement of the proposed NSPS also
captures saleable condensates. The
revenues from additional natural gas
and condensate recovery are expected to
offset the costs of implementing the
proposed NSPS.
The analysis of energy impacts for the
proposed NSPS that includes the
additional product recovery shows that
domestic natural gas production is
estimated to increase (20 billion cubic
feet or 0.1 percent) and natural gas
prices to decrease ($0.04/Mcf or 0.9
percent at the wellhead for producers in
the lower 48 states) in 2015, the year of
analysis. Domestic crude oil production
is not estimated to change, while crude
oil prices are estimated to decrease
slightly ($0.02/barrel or less than 0.1
percent at the wellhead for producers in
the lower 48 states) in 2015, the year of
analysis. All prices are in 2008 dollars.
Additionally, the NSPS establishes
several performance standards that give
regulated entities flexibility in
determining how to best comply with
the regulation. In an industry that is
geographically and economically
heterogeneous, this flexibility is an
important factor in reducing regulatory
burden.
For more information on the
estimated energy effects, please refer to
the economic impact analysis for this
proposed rule. The analysis is available
in the RIA, which is in the public
docket.
I. National Technology Transfer and
Advancement Act
Section 12(d) of the National
Technology Transfer and Advancement
Act of 1995 (NTTAA), Public Law No.
104–113 (15 U.S.C. 272 note) directs the
EPA to use voluntary consensus
standards (VCS) in its regulatory
activities unless to do so would be
inconsistent with applicable law or
otherwise impractical. VCS are
technical standards (e.g., materials
specifications, test methods, sampling
procedures, and business practices) that
are developed or adopted by VCS
bodies. NTTAA directs the EPA to
provide Congress, through OMB,
explanations when the Agency decides
not to use available and applicable VCS.
The proposed rule involves technical
standards. Therefore, the requirements
of the NTTAA apply to this action. We
are proposing to revise 40 CFR part 63,
subpart HH and 40 CFR part 63, subpart
HHH to allow ANSI/ASME PTC 19.10–
1981, Flue and Exhaust Gas Analyses
(Part 10, Instruments and Apparatus) to
be used in lieu of EPA Methods 3B, 6
and 16A. This standard is available from
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the American Society of Mechanical
Engineers (ASME), Three Park Avenue,
New York, NY 10016–5990. Also, we
are proposing to revise subpart HHH to
allow ASTM D6420–99 (2004), Test
Method for Determination of Gaseous
Organic Compounds by Direct Interface
Gas Chromatography/Mass
Spectrometry, to be used in lieu of EPA
Method 18. For a detailed discussion of
this VCS, and its appropriateness as a
substitute for Method 18, see the final
Oil and Natural Gas Production
NESHAP (Area Sources) (72 FR 36,
January 3, 2007).
As a result, the EPA is proposing
ASTM D6420–99 (2004) for use in 40
CFR part 63, subpart HHH. The EPA
also proposes to allow Method 18 as an
option in addition to ASTM D6420–99
(2004). This would allow the continued
use of gas chromatography
configurations other than gas
chromatography/mass spectrometry.
The EPA welcomes comments on this
aspect of the proposed rulemaking and,
specifically, invites the public to
identify potentially-applicable VCS and
to explain why such standards should
be used in this regulation.
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order 12898 (59 FR 7629,
February 16, 1994) establishes Federal
executive policy on EJ. Its main
provision directs Federal agencies, to
the greatest extent practicable and
permitted by law, to make EJ 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 lowincome populations in the United
States.
The EPA has determined that this
proposed 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.
To examine the potential for any EJ
issues that might be associated with
each source category, we evaluated the
distributions of HAP-related cancer and
noncancer risks across different social,
demographic and economic groups
within the populations living near the
facilities where these source categories
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are located. The methods used to
conduct demographic analyses for this
rule are described in section VII.C of the
preamble for this rule. The development
of demographic analyses to inform the
consideration of EJ issues in EPA
rulemakings is an evolving science. The
EPA offers the demographic analyses in
this proposed rulemaking as examples
of how such analyses might be
developed to inform such consideration,
and invites public comment on the
approaches used and the interpretations
made from the results, with the hope
that this will support the refinement
and improve utility of such analyses for
future rulemakings.
For the demographic analyses, we
focused on the populations within 50
km of any facility estimated to have
exposures to HAP which result in
cancer risks of 1-in-1 million or greater,
or noncancer HI of 1 or greater (based
on the emissions of the source category
or the facility, respectively). We
examined the distributions of those
risks across various demographic
groups, comparing the percentages of
particular demographic groups to the
total number of people in those
demographic groups nationwide. The
results, including other risk metrics,
such as average risks for the exposed
populations, are documented in source
category-specific technical reports in the
docket for both source categories
covered in this proposal.
As described in the preamble, our risk
assessments demonstrate that the
regulations for the oil and natural gas
production and natural gas transmission
and storage source categories, are
associated with an acceptable level of
risk and that the proposed additional
requirements will provide an ample
margin of safety to protect public health.
Our analyses also show that, for these
source categories, there is no potential
for an adverse environmental effect or
human health multi-pathway effects,
and that acute and chronic noncancer
health impacts are unlikely. The EPA
has determined that, although there may
be an existing disparity in HAP risks
from these sources between some
demographic groups, no demographic
group is exposed to an unacceptable
level of risk.
List of Subjects
40 CFR Part 60
Environmental protection, Air
pollution control, Reporting and
recordkeeping requirements, Volatile
organic compounds.
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40 CFR Part 63
Environmental protection, Air
pollution control, Reporting and
recordkeeping requirements, Volatile
organic compounds.
Dated: July 28, 2011.
Lisa P. Jackson,
Administrator.
For the reasons set out in the
preamble, title 40, chapter I of the Code
of Federal Regulations is proposed to be
amended as follows:
1. The authority citation for part 60
continues to read as follows:
Authority: 42 U.S.C. 7401, et seq.
2. Section 60.17 is amended by:
a. Revising paragraph (a)(7); and
b. Revising paragraphs (a)(91) and
(a)(92) to read as follows:
Incorporations by reference.
*
*
*
*
*
(a) * * *
(7) ASTM D86–78, 82, 90, 93, 95, 96,
Distillation of Petroleum Products, IBR
approved for §§ 60.562–2(d), 60.593(d),
60.593a(d), 60.633(h) and 60.5401(h).
*
*
*
*
*
(91) ASTM E169–63, 77, 93, General
Techniques of Ultraviolet Quantitative
Analysis, IBR approved for
§§ 60.485a(d)(1), 60.593(b)(2),
60.593a(b)(2), 60.632(f) and 60.5400(f).
(92) ASTM E260–73, 91, 96, General
Gas Chromatography Procedures, IBR
approved for §§ 60.485a(d)(1),
60.593(b)(2), 60.593a(b)(2), 60.632(f),
60.5400(f) and 60.5406(b).
*
*
*
*
*
Subpart KKK—Standards of
Performance for Equipment Leaks of
VOC From Onshore Natural Gas
Processing Plants for Which
Construction, Reconstruction, or
Modification Commenced After
January 20, 1984, and on or Before
August 23, 2011
3. The heading for Subpart KKK is
revised to read as set out above.
4. Section 60.630 is amended by
revising paragraph (b) to read as follows:
§ 60.630 Applicability and designation of
affected facility.
*
*
*
*
*
(b) Any affected facility under
paragraph (a) of this section that
commences construction,
reconstruction, or modification after
January 20, 1984, and on or before
August 23, 2011, is subject to the
requirements of this subpart.
*
*
*
*
*
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5. The heading for Subpart LLL is
revised to read as set out above.
6. Section 60.640 is amended by
revising paragraph (d) to read as
follows:
§ 60.640 Applicability and designation of
affected facilities.
PART 60—[AMENDED]
§ 60.17
Subpart LLL—Standards of
Performance for SO2 Emissions From
Onshore Natural Gas Processing for
Which Construction, Reconstruction,
or Modification Commenced After
January 20, 1984, and on or Before
August 23, 2011
*
*
*
*
*
(d) The provisions of this subpart
apply to each affected facility identified
in paragraph (a) of this section which
commences construction or
modification after January 20, 1984, and
on or before August 23, 2011.
*
*
*
*
*
7. Add subpart OOOO to part 60 to
read as follows:
Subpart OOOO—Standards of Performance
for Crude Oil and Natural Gas Production,
Transmission, and Distribution
Sec.
60.5360 What is the purpose of this
subpart?
60.5365 Am I subject to this subpart?
60.5370 When must I comply with this
subpart?
60.5375 What standards apply to gas
wellhead affected facilities?
60.5380 What standards apply to
centrifugal compressor affected
facilities?
60.5385 What standards apply to
reciprocating compressor affected
facilities?
60.5390 What standards apply to pneumatic
controller affected facilities?
60.5395 What standards apply to storage
vessel affected facilities?
60.5400 What VOC standards apply to
affected facilities at an onshore natural
gas processing plant?
60.5401 What are the exceptions to the VOC
standards for affected facilities at
onshore natural gas processing plants?
60.5402 What are the alternative emission
limitations for equipment leaks from
onshore natural gas processing plants?
60.5405 What standards apply to
sweetening units at onshore natural gas
processing plants?
60.5406 What test methods and procedures
must I use for my sweetening units
affected facilities at onshore natural gas
processing plants?
60.5407 What are the requirements for
monitoring of emissions and operations
from my sweetening unit affected
facilities at onshore natural gas
processing plants?
60.5408 What is an optional procedure for
measuring hydrogen sulfide in acid gas—
Tutwiler Procedure?
60.5410 How do I demonstrate initial
compliance with the standards for my
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gas wellhead affected facility, my
centrifugal compressor affected facility,
my reciprocating compressor affected
facility, my pneumatic controller
affected facility, my storage vessel
affected facility, and my affected
facilities at onshore natural gas
processing plants?
60.5415 How do I demonstrate continuous
compliance with the standards for my
gas wellhead affected facility, my
centrifugal compressor affected facility,
my stationary reciprocating compressor
affected facility, my pneumatic
controller affected facility, my storage
vessel affected facility, and my affected
facilities at onshore natural gas
processing plants?
60.5420 What are my notification,
reporting, and recordkeeping
requirements?
60.5421 What are my additional
recordkeeping requirements for my
affected facility subject to VOC
requirements for onshore natural gas
processing plants?
60.5422 What are my additional reporting
requirements for my affected facility
subject to VOC requirements for onshore
natural gas processing plants?
60.5423 What additional recordkeeping and
reporting requirements apply to my
sweetening unit affected facilities at
onshore natural gas processing plants?
60.5425 What part of the General Provisions
apply to me?
60.5430 What definitions apply to this
subpart?
Table 1 to Subpart OOOO of Part 60—
Required Minimum Initial SO2 Emission
Reduction Efficiency (Zi)
Table 2 to Subpart OOOO of Part 60—
Required Minimum SO2 Emission
Reduction Efficiency (Zc)
Table 3 to Subpart OOOO of Part 60—
Applicability of General Provisions to
Subpart OOOO
Subpart OOOO—Standards of
Performance for Crude Oil and Natural
Gas Production, Transmission, and
Distribution
§ 60.5360
subpart?
What is the purpose of this
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This subpart establishes emission
standards and compliance schedules for
the control of volatile organic
compounds (VOC) and sulfur dioxide
(SO2) emissions from affected facilities
that commenced construction,
modification or reconstruction after
August 23, 2011.
§ 60.5365
Am I subject to this subpart?
If you are the owner or operator of one
or more of the affected facilities listed
in paragraphs (a) through (g) of this
section that commenced construction,
modification, or reconstruction after
August 23, 2011 your affected facility is
subject to the applicable provisions of
this subpart. For the purposes of this
subpart, a well completion operation
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following hydraulic fracturing or
refracturing that occurs at a gas
wellhead facility that commenced
construction, modification, or
reconstruction on or before August 23,
2011 is considered a modification of the
gas wellhead facility, but does not affect
other equipment, process units, storage
vessels, or pneumatic devices located at
the well site.
(a) A gas wellhead affected facility, is
a single natural gas well.
(b) A centrifugal compressor affected
facility, which is defined as a single
centrifugal compressor located between
the wellhead and the city gate (as
defined in § 60.5430), except that a
centrifugal compressor located at a well
site (as defined in § 60.5430) is not an
affected facility under this subpart. For
the purposes of this subpart, your
centrifugal compressor is considered to
have commenced construction on the
date the compressor is installed at the
facility.
(c) A reciprocating compressor
affected facility, which is defined as a
single reciprocating compressor located
between the wellhead and the city gate
(as defined in § 60.5430), except that a
reciprocating compressor located at a
well site (as defined in § 60.5430) is not
an affected facility under this subpart.
For the purposes of this subpart, your
reciprocating compressor is considered
to have commenced construction on the
date the compressor is installed at the
facility.
(d) A pneumatic controller affected
facility, which is defined as a single
pneumatic controller.
(e) A storage vessel affected facility,
which is defined as a single storage
vessel.
(f) Compressors and equipment (as
defined in § 60.5430) located at onshore
natural gas processing plants.
(1) Each compressor in VOC service or
in wet gas service is an affected facility.
(2) The group of all equipment, except
compressors, within a process unit is an
affected facility.
(3) Addition or replacement of
equipment, as defined in § 60.5430, for
the purpose of process improvement
that is accomplished without a capital
expenditure shall not by itself be
considered a modification under this
subpart.
(4) Equipment (as defined in
§ 60.5430) associated with a compressor
station, dehydration unit, sweetening
unit, underground storage tank, field gas
gathering system, or liquefied natural
gas unit is covered by §§ 60.5400,
60.5401, 60.5402, 60.5421 and 60.5422
of this subpart if it is located at an
onshore natural gas processing plant.
Equipment (as defined in § 60.5430) not
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located at the onshore natural gas
processing plant site is exempt from the
provisions of §§ 60.5400, 60.5401,
60.5402, 60.5421 and 60.5422 of this
subpart.
(5) Affected facilities located at
onshore natural gas processing plants
and described in paragraphs (f)(1) and
(f)(2) of this section are exempt from
this subpart if they are subject to and
controlled according to subparts VVa,
GGG or GGGa of this part.
(g) Sweetening units located onshore
that process natural gas produced from
either onshore or offshore wells.
(1) Each sweetening unit that
processes natural gas is an affected
facility; and
(2) Each sweetening unit that
processes natural gas followed by a
sulfur recovery unit is an affected
facility.
(3) Facilities that have a design
capacity less than 2 long tons per day
(LT/D) of hydrogen sulfide (H2S) in the
acid gas (expressed as sulfur) are
required to comply with recordkeeping
and reporting requirements specified in
§ 60.5423(c) but are not required to
comply with §§ 60.5405 through
60.5407 and paragraphs 60.5410(g) and
60.5415(g) of this subpart.
(4) Sweetening facilities producing
acid gas that is completely reinjected
into oil-or-gas-bearing geologic strata or
that is otherwise not released to the
atmosphere are not subject to §§ 60.5405
through 60.5407, and §§ 60.5410(g),
60.5415(g), and § 60.5423 of this
subpart.
§ 60.5370
subpart?
When must I comply with this
(a) You must be in compliance with
the standards of this subpart no later
than the date of publication of the final
rule in the Federal Register or upon
startup, whichever is later.
(b) The provisions for exemption from
compliance during periods of startup,
shutdown, and malfunctions provided
for in 40 CFR 60.8(c) do not apply to
this subpart.
(c) You are exempt from the
obligation to obtain a permit under 40
CFR part 70 or 40 CFR part 71, provided
you are not otherwise required by law
to obtain a permit under 40 CFR 70.3(a)
or 40 CFR 71.3(a). Notwithstanding the
previous sentence, you must continue to
comply with the provisions of this
subpart.
§ 60.5375 What standards apply to gas
wellhead affected facilities?
If you are the owner or operator of a
gas wellhead affected facility, you must
comply with paragraphs (a) through (g)
of this section.
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(a) Except as provided in paragraph (f)
of this section, for each well completion
operation with hydraulic fracturing, as
defined in § 60.5430, you must control
emissions by the operational procedures
found in paragraphs (a)(1) through (a)(3)
of this section.
(1) You must minimize the emissions
associated with venting of hydrocarbon
fluids and gas over the duration of
flowback by routing the recovered
liquids into storage vessels and routing
the recovered gas into a gas gathering
line or collection system.
(2) You must employ sand traps, surge
vessels, separators, and tanks during
flowback and cleanout operations to
safely maximize resource recovery and
minimize releases to the environment.
All salable quality gas must be routed to
the gas gathering line as soon as
practicable.
(3) You must capture and direct
flowback emissions that cannot be
directed to the gathering line to a
completion combustion device, except
in conditions that may result in a fire
hazard or explosion. Completion
combustion devices must be equipped
with a reliable continuous ignition
source over the duration of flowback.
(b) You must maintain a log for each
well completion operation at each gas
wellhead affected facility. The log must
be completed on a daily basis and must
contain the records specified in
§ 60.5420(c)(1)(iii).
(c) You must demonstrate initial
compliance with the standards that
apply to gas wellhead affected facilities
as required by § 60.5410.
(d) You must demonstrate continuous
compliance with the standards that
apply to gas wellhead affected facilities
as required by § 60.5415.
(e) You must perform the required
notification, recordkeeping, and
reporting as required by § 60.5420.
(f) For wells meeting the criteria for
wildcat or delineation wells, each well
completion operation with hydraulic
fracturing at a gas wellhead affected
facility must reduce emissions by using
a completion combustion device
meeting the requirements of paragraph
(a)(3) of this section. You must also
maintain records specified in
§ 60.5420(c)(1)(iii) for wildcat or
delineation wells.
§ 60.5380 What standards apply to
centrifugal compressor affected facilities?
You must comply with the standards
in paragraphs (a) through (d) of this
section, as applicable for each
centrifugal compressor affected facility.
(a) You must equip each rotating
compressor shaft with a dry seal system
upon initial startup.
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(b) You must demonstrate initial
compliance with the standards that
apply to centrifugal compressor affected
facilities as required by § 60.5410.
(c) You must demonstrate continuous
compliance with the standards that
apply to centrifugal compressor affected
facilities as required by § 60.5415.
(d) You must perform the required
notification, recordkeeping, and
reporting as required by § 60.5420.
§ 60.5385 What standards apply to
reciprocating compressor affected
facilities?
You must comply with the standards
in paragraphs (a) through (d) of this
section for each reciprocating
compressor affected facility.
(a) You must replace the reciprocating
compressor rod packing before the
compressor has operated for 26,000
hours. The number of hours of operation
must be continuously monitored
beginning upon initial startup of your
reciprocating compressor affected
facility, or the date of publication of the
final rule in the Federal Register, or the
date of the previous reciprocating
compressor rod packing replacement,
whichever is later.
(b) You must demonstrate initial
compliance with standards that apply to
reciprocating compressor affected
facilities as required by § 60.5410.
(c) You must demonstrate continuous
compliance with standards that apply to
reciprocating compressor affected
facilities as required by § 60.5415.
(d) You must perform the required
notification, recordkeeping, and
reporting as required by § 60.5420.
§ 60.5390 What standards apply to
pneumatic controller affected facilities?
For each pneumatic controller
affected facility you must comply with
the VOC standards, based on natural gas
as a surrogate for VOC, in either
paragraph (b) or (c) of this section, as
applicable. Pneumatic controllers
meeting the conditions in paragraph (a)
are exempt from this requirement.
(a) The requirements of paragraph (b)
or (c) of this section are not required if
you demonstrate, to the Administrator’s
satisfaction, that the use of a high bleed
device is predicated. The demonstration
may include, but is not limited to,
response time, safety and actuation.
(b) Each pneumatic controller affected
facility located at a natural gas
processing plant (as defined in
§ 60.5430) must have zero emissions of
natural gas.
(c) Each pneumatic controller affected
facility not located at a natural gas
processing plant (as defined in
§ 60.5430) must have natural gas
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emissions no greater than 6 standard
cubic feet per hour.
(d) You must demonstrate initial
compliance with standards that apply to
pneumatic controller affected facilities
as required by § 60.5410.
(e) You must demonstrate continuous
compliance with standards that apply to
pneumatic controller affected facilities
as required by § 60.5415.
(f) You must perform the required
notification, recordkeeping, and
reporting as required by § 60.5420,
except that you are not required to
submit the notifications specified in
§ 60.5420(a).
§ 60.5395 What standards apply to storage
vessel affected facilities?
You must comply with the standards
in paragraphs (a) through (e) of this
section for each storage vessel affected
facility.
(a) You must comply with the
standards for storage vessels specified in
§ 63.766(b) and (c) of this chapter,
except as specified in paragraph (b) of
this section. Storage vessels that meet
either one or both of the throughput
conditions specified in paragraphs (a)(1)
or (a)(2) of this section are not subject
to the standards of this section.
(1) The annual average condensate
throughput is less than 1 barrel per day
per storage vessel.
(2) The annual average crude oil
throughput is less than 20 barrels per
day per storage vessel.
(b) This standard does not apply to
storage vessels already subject to and
controlled in accordance with the
requirements for storage vessels in
§ 63.766(b)(1) or (2) of this chapter.
(c) You must demonstrate initial
compliance with standards that apply to
storage vessel affected facilities as
required by § 60.5410.
(d) You must demonstrate continuous
compliance with standards that apply to
storage vessel affected facilities as
required by § 60.5415.
(e) You must perform the required
notification, recordkeeping, and
reporting as required by § 60.5420.
§ 60.5400 What VOC standards apply to
affected facilities at an onshore natural gas
processing plant?
This section applies to each
compressor in VOC service or in wet gas
service and the group of all equipment
(as defined in § 60.5430), except
compressors, within a process unit.
(a) You must comply with the
requirements of § 60.482–1a(a), (b), and
(d), § 60.482–2a, and § 60.482–4a
through 60.482–11a, except as provided
in § 60.5401.
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(b) You may elect to comply with the
requirements of §§ 60.483–1a and
60.483–2a, as an alternative.
(c) You may apply to the
Administrator for permission to use an
alternative means of emission limitation
that achieves a reduction in emissions
of VOC at least equivalent to that
achieved by the controls required in this
subpart according to the requirements of
§ 60.5402 of this subpart.
(d) You must comply with the
provisions of § 60.485a of this part
except as provided in paragraph (f) of
this section.
(e) You must comply with the
provisions of §§ 60.486a and 60.487a of
this part except as provided in
§§ 60.5401, 60.5421, and 60.5422 of this
part.
(f) You must use the following
provision instead of § 60.485a(d)(1):
Each piece of equipment is presumed to
be in VOC service or in wet gas service
unless an owner or operator
demonstrates that the piece of
equipment is not in VOC service or in
wet gas service. For a piece of
equipment to be considered not in VOC
service, it must be determined that the
VOC content can be reasonably
expected never to exceed 10.0 percent
by weight. For a piece of equipment to
be considered in wet gas service, it must
be determined that it contains or
contacts the field gas before the
extraction step in the process. For
purposes of determining the percent
VOC content of the process fluid that is
contained in or contacts a piece of
equipment, procedures that conform to
the methods described in ASTM E169–
63, 77, or 93, E168–67, 77, or 92, or
E260–73, 91, or 96 (incorporated by
reference as specified in § 60.17) must
be used.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
§ 60.5401 What are the exceptions to the
VOC standards for affected facilities at
onshore natural gas processing plants?
(a) You may comply with the
following exceptions to the provisions
of subpart VVa of this part.
(b)(1) Each pressure relief device in
gas/vapor service may be monitored
quarterly and within 5 days after each
pressure release to detect leaks by the
methods specified in § 60.485a(b) except
as provided in § 60.5400(c) and in
paragraph (b)(4) of this section, and
§ 60.482–4a(a) through (c) of subpart
VVa.
(2) If an instrument reading of 5000
ppm or greater is measured, a leak is
detected.
(3)(i) When a leak is detected, it must
be repaired as soon as practicable, but
no later than 15 calendar days after it is
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detected, except as provided in
§ 60.482–9a.
(ii) A first attempt at repair must be
made no later than 5 calendar days after
each leak is detected.
(4)(i) Any pressure relief device that
is located in a nonfractionating plant
that is monitored only by non-plant
personnel may be monitored after a
pressure release the next time the
monitoring personnel are on-site,
instead of within 5 days as specified in
paragraph (b)(1) of this section and
§ 60.482–4a(b)(1) of subpart VVa.
(ii) No pressure relief device
described in paragraph (b)(4)(i) of this
section must be allowed to operate for
more than 30 days after a pressure
release without monitoring.
(c) Sampling connection systems are
exempt from the requirements of
§ 60.482–5a.
(d) Pumps in light liquid service,
valves in gas/vapor and light liquid
service, and pressure relief devices in
gas/vapor service that are located at a
nonfractionating plant with a design
capacity to process 283,200 standard
cubic meters per day (scmd) (10 million
standard cubic feet per day) or more of
field gas are exempt from the routine
monitoring requirements of §§ 60.482–
2a(a)(1) and 60.482–7a(a), and
paragraph (b)(1) of this section.
(e) Pumps in light liquid service,
valves in gas/vapor and light liquid
service, and pressure relief devices in
gas/vapor service within a process unit
that is located in the Alaskan North
Slope are exempt from the routine
monitoring requirements of §§ 60.482–
2a(a)(1), 60.482–7a(a), and paragraph
(b)(1) of this section.
(f) Flares used to comply with this
subpart must comply with the
requirements of § 60.18.
(g) An owner or operator may use the
following provisions instead of
§ 60.485a(e):
(1) Equipment is in heavy liquid
service if the weight percent evaporated
is 10 percent or less at 150 °C (302 °F)
as determined by ASTM Method D86–
78, 82, 90, 95, or 96 (incorporated by
reference as specified in § 60.17).
(2) Equipment is in light liquid
service if the weight percent evaporated
is greater than 10 percent at 150 °C (302
°F) as determined by ASTM Method
D86–78, 82, 90, 95, or 96 (incorporated
by reference as specified in § 60.17).
§ 60.5402 What are the alternative
emission limitations for equipment leaks
from onshore natural gas processing
plants?
(a) If, in the Administrator’s
judgment, an alternative means of
emission limitation will achieve a
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reduction in VOC emissions at least
equivalent to the reduction in VOC
emissions achieved under any design,
equipment, work practice or operational
standard, the Administrator will
publish, in the Federal Register, a
notice permitting the use of that
alternative means for the purpose of
compliance with that standard. The
notice may condition permission on
requirements related to the operation
and maintenance of the alternative
means.
(b) Any notice under paragraph (a) of
this section must be published only
after notice and an opportunity for a
public hearing.
(c) The Administrator will consider
applications under this section from
either owners or operators of affected
facilities, or manufacturers of control
equipment.
(d) The Administrator will treat
applications under this section
according to the following criteria,
except in cases where the Administrator
concludes that other criteria are
appropriate:
(1) The applicant must collect, verify
and submit test data, covering a period
of at least 12 months, necessary to
support the finding in paragraph (a) of
this section.
(2) If the applicant is an owner or
operator of an affected facility, the
applicant must commit in writing to
operate and maintain the alternative
means so as to achieve a reduction in
VOC emissions at least equivalent to the
reduction in VOC emissions achieved
under the design, equipment, work
practice or operational standard.
§ 60.5405 What standards apply to
sweetening units at onshore natural gas
processing plants?
(a) During the initial performance test
required by § 60.8(b), you must achieve
at a minimum, an SO2 emission
reduction efficiency (Zi) to be
determined from Table 1 of this subpart
based on the sulfur feed rate (X) and the
sulfur content of the acid gas (Y) of the
affected facility.
(b) After demonstrating compliance
with the provisions of paragraph (a) of
this section, you must achieve at a
minimum, an SO2 emission reduction
efficiency (Zc) to be determined from
Table 2 of this subpart based on the
sulfur feed rate (X) and the sulfur
content of the acid gas (Y) of the
affected facility.
60.5406 What test methods and
procedures must I use for my sweetening
units affected facilities at onshore natural
gas processing plants?
(a) In conducting the performance
tests required in § 60.8, you must use
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Where:
X = average sulfur feed rate, Mg/D (LT/D).
Qa = average volumetric flow rate of acid gas
from sweetening unit, dscm/day (dscf/
day).
Y = average H2S concentration in acid gas
feed from sweetening unit, percent by
volume, expressed as a decimal.
K = (32 kg S/kg-mole) / ((24.04 dscm/kgmole) (1000 kg S/Mg))
= 1.331 × 10¥3 Mg/dscm, for metric units
= (32 lb S/lb-mole) / ((385.36 dscf/lb-mole)
(2240 lb S/long ton))
= 3.707 × 10¥5 long ton/dscf, for English
units.
(2) You must use the continuous
readings from the process flowmeter to
determine the average volumetric flow
rate (Qa) in dscm/day (dscf/day) of the
acid gas from the sweetening unit for
each run.
(3) You must use the Tutwiler
procedure in § 60.5408 or a
chromatographic procedure following
ASTM E–260 (incorporated by
reference—see § 60.17) to determine the
H2S concentration in the acid gas feed
from the sweetening unit (Y). At least
one sample per hour (at equally spaced
intervals) must be taken during each
4-hour run. The arithmetic mean of all
samples must be the average H2S
concentration (Y) on a dry basis for the
run. By multiplying the result from the
Tutwiler procedure by 1.62 × 10¥3, the
units gr/100 scf are converted to volume
percent.
(4) Using the information from
paragraphs (b)(1) and (b)(3) of this
section, Tables 1 and 2 of this subpart
must be used to determine the required
initial (Zi) and continuous (Zc)
reduction efficiencies of SO2 emissions.
(c) You must determine compliance
with the SO2 standards in § 60.5405(a)
or (b) as follows:
(1) You must compute the emission
reduction efficiency (R) achieved by the
sulfur recovery technology for each run
using the following equation:
(2) You must use the level indicators
or manual soundings to measure the
liquid sulfur accumulation rate in the
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product storage tanks. You must use
readings taken at the beginning and end
of each run, the tank geometry, sulfur
density at the storage temperature, and
sample duration to determine the sulfur
production rate (S) in kg/hr (lb/hr) for
each run.
(3) You must compute the emission
rate of sulfur for each run as follows:
Where:
E = emission rate of sulfur per run, kg/hr.
Ce = concentration of sulfur equivalent (SO2
+ reduced sulfur), g/dscm (lb/dscf).
Qsd = volumetric flow rate of effluent gas,
dscm/hr (dscf/hr).
K1 = conversion factor, 1000 g/kg
(7000 gr/lb).
(4) The concentration (Ce) of sulfur
equivalent must be the sum of the SO2
and TRS concentrations, after being
converted to sulfur equivalents. For
each run and each of the test methods
specified in this paragraph (c) of this
section, you must use a sampling time
of at least 4 hours. You must use
Method 1 of Appendix A to part 60 of
this chapter to select the sampling site.
The sampling point in the duct must be
at the centroid of the cross-section if the
area is less than 5 m2 (54 ft2) or at a
point no closer to the walls than
1 m (39 in) if the cross-sectional area is
5 m2 or more, and the centroid is more
than 1 m (39 in.) from the wall.
(i) You must use Method 6 of
Appendix A to part 60 of this chapter
to determine the SO2 concentration. You
must take eight samples of 20 minutes
each at 30-minute intervals. The
arithmetic average must be the
concentration for the run. The
concentration must be multiplied by
0.5 × 10¥3 to convert the results to
sulfur equivalent.
(ii) You must use Method 15 of
appendix A to part 60 of this chapter to
determine the TRS concentration from
reduction-type devices or where the
oxygen content of the effluent gas is less
than 1.0 percent by volume. The
sampling rate must be at least 3 liters/
min (0.1 ft3/min) to insure minimum
residence time in the sample line. You
must take sixteen samples at 15-minute
intervals. The arithmetic average of all
the samples must be the concentration
for the run. The concentration in ppm
reduced sulfur as sulfur must be
multiplied by 1.333 × 10¥3 to convert
the results to sulfur equivalent.
(iii) You must use Method 16A or
Method 15 of appendix A to part 60 of
this chapter to determine the reduced
sulfur concentration from oxidationtype devices or where the oxygen
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content of the effluent gas is greater than
1.0 percent by volume. You must take
eight samples of 20 minutes each at 30minute intervals. The arithmetic average
must be the concentration for the run.
The concentration in ppm reduced
sulfur as sulfur must be multiplied by
1.333 × 10¥3 to convert the results to
sulfur equivalent.
(iv) You must use Method 2 of
appendix A to part 60 of this chapter to
determine the volumetric flow rate of
the effluent gas. A velocity traverse
must be conducted at the beginning and
end of each run. The arithmetic average
of the two measurements must be used
to calculate the volumetric flow rate
(Qsd) for the run. For the determination
of the effluent gas molecular weight, a
single integrated sample over the 4-hour
period may be taken and analyzed or
grab samples at 1-hour intervals may be
taken, analyzed, and averaged. For the
moisture content, you must take two
samples of at least 0.10 dscm (3.5 dscf)
and 10 minutes at the beginning of the
4-hour run and near the end of the time
period. The arithmetic average of the
two runs must be the moisture content
for the run.
§ 60.5407 What are the requirements for
monitoring of emissions and operations
from my sweetening unit affected facilities
at onshore natural gas processing plants?
(a) If your sweetening unit affected
facility is located at an onshore natural
gas processing plant and is subject to
the provisions of § 60.5405(a) or (b) you
must install, calibrate, maintain, and
operate monitoring devices or perform
measurements to determine the
following operations information on a
daily basis:
(1) The accumulation of sulfur
product over each 24-hour period. The
monitoring method may incorporate the
use of an instrument to measure and
record the liquid sulfur production rate,
or may be a procedure for measuring
and recording the sulfur liquid levels in
the storage tanks with a level indicator
or by manual soundings, with
subsequent calculation of the sulfur
production rate based on the tank
geometry, stored sulfur density, and
elapsed time between readings. The
method must be designed to be accurate
within ± 2 percent of the 24-hour sulfur
accumulation.
(2) The H2S concentration in the acid
gas from the sweetening unit for each
24-hour period. At least one sample per
24-hour period must be collected and
analyzed using the equation specified in
§ 60.5406(b)(1). The Administrator may
require you to demonstrate that the H2S
concentration obtained from one or
more samples over a 24-hour period is
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the test methods in Appendix A of this
part or other methods and procedures as
specified in this section, except as
provided in paragraph § 60.8(b).
(b) During a performance test required
by § 60.8, you must determine the
minimum required reduction
efficiencies (Z) of SO2 emissions as
required in § 60.5405(a) and (b) as
follows:
(1) The average sulfur feed rate (X)
must be computed as follows:
X ¥ KQag
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within ± 20 percent of the average of 12
samples collected at equally spaced
intervals during the 24-hour period. In
instances where the H2S concentration
of a single sample is not within ± 20
percent of the average of the 12 equally
spaced samples, the Administrator may
require a more frequent sampling
schedule.
(3) The average acid gas flow rate
from the sweetening unit. You must
install and operate a monitoring device
to continuously measure the flow rate of
acid gas. The monitoring device reading
must be recorded at least once per hour
during each 24-hour period. The average
acid gas flow rate must be computed
from the individual readings.
(4) The sulfur feed rate (X). For each
24-hour period, you must compute X
using the equation specified in
§ 60.5406(b)(3).
(5) The required sulfur dioxide
emission reduction efficiency for the
24-hour period. You must use the sulfur
feed rate and the H2S concentration in
the acid gas for the 24-hour period, as
applicable, to determine the required
reduction efficiency in accordance with
the provisions of § 60.5405(b).
(b) Where compliance is achieved
through the use of an oxidation control
system or a reduction control system
followed by a continually operated
incineration device, you must install,
calibrate, maintain, and operate
monitoring devices and continuous
emission monitors as follows:
(1) A continuous monitoring system to
measure the total sulfur emission rate
(E) of SO2 in the gases discharged to the
atmosphere. The SO2 emission rate
must be expressed in terms of
equivalent sulfur mass flow rates (kg/hr
(lb/hr)). The span of this monitoring
system must be set so that the
equivalent emission limit of
§ 60.5405(b) will be between 30 percent
and 70 percent of the measurement
range of the instrument system.
(2) Except as provided in paragraph
(b)(3) of this section: A monitoring
device to measure the temperature of
the gas leaving the combustion zone of
the incinerator, if compliance with
§ 60.5405(a) is achieved through the use
of an oxidation control system or a
reduction control system followed by a
continually operated incineration
device. The monitoring device must be
certified by the manufacturer to be
accurate to within ± 1 percent of the
temperature being measured.
(3) When performance tests are
conducted under the provision of § 60.8
to demonstrate compliance with the
standards under § 60.5405, the
temperature of the gas leaving the
incinerator combustion zone must be
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determined using the monitoring
device. If the volumetric ratio of sulfur
dioxide to sulfur dioxide plus total
reduced sulfur (expressed as SO2) in the
gas leaving the incinerator is equal to or
less than 0.98, then temperature
monitoring may be used to demonstrate
that sulfur dioxide emission monitoring
is sufficient to determine total sulfur
emissions. At all times during the
operation of the facility, you must
maintain the average temperature of the
gas leaving the combustion zone of the
incinerator at or above the appropriate
level determined during the most recent
performance test to ensure the sulfur
compound oxidation criteria are met.
Operation at lower average temperatures
may be considered by the Administrator
to be unacceptable operation and
maintenance of the affected facility. You
may request that the minimum
incinerator temperature be reestablished
by conducting new performance tests
under § 60.8.
(4) Upon promulgation of a
performance specification of continuous
monitoring systems for total reduced
sulfur compounds at sulfur recovery
plants, you may, as an alternative to
paragraph (b)(2) of this section, install,
calibrate, maintain, and operate a
continuous emission monitoring system
for total reduced sulfur compounds as
required in paragraph (d) of this section
in addition to a sulfur dioxide emission
monitoring system. The sum of the
equivalent sulfur mass emission rates
from the two monitoring systems must
be used to compute the total sulfur
emission rate (E).
(c) Where compliance is achieved
through the use of a reduction control
system not followed by a continually
operated incineration device, you must
install, calibrate, maintain, and operate
a continuous monitoring system to
measure the emission rate of reduced
sulfur compounds as SO2 equivalent in
the gases discharged to the atmosphere.
The SO2 equivalent compound emission
rate must be expressed in terms of
equivalent sulfur mass flow rates (kg/hr
(lb/hr)). The span of this monitoring
system must be set so that the
equivalent emission limit of
§ 60.5405(b) will be between 30 and 70
percent of the measurement range of the
system. This requirement becomes
effective upon promulgation of a
performance specification for
continuous monitoring systems for total
reduced sulfur compounds at sulfur
recovery plants.
(d) For those sources required to
comply with paragraph (b) or (c) of this
section, you must calculate the average
sulfur emission reduction efficiency
achieved (R) for each 24-hour clock
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internal. The 24-hour interval may begin
and end at any selected clock time, but
must be consistent. You must compute
the 24-hour average reduction efficiency
(R) based on the 24-hour average sulfur
production rate (S) and sulfur emission
rate (E), using the equation in
§ 60.5406(c)(1).
(1) You must use data obtained from
the sulfur production rate monitoring
device specified in paragraph (a) of this
section to determine S.
(2) You must use data obtained from
the sulfur emission rate monitoring
systems specified in paragraphs (b) or
(c) of this section to calculate a 24-hour
average for the sulfur emission rate (E).
The monitoring system must provide at
least one data point in each successive
15-minute interval. You must use at
least two data points to calculate each
1-hour average. You must use a
minimum of 18 1-hour averages to
compute each 24-hour average.
(e) In lieu of complying with
paragraphs (b) or (c) of this section,
those sources with a design capacity of
less than 152 Mg/D (150 LT/D) of H2S
expressed as sulfur may calculate the
sulfur emission reduction efficiency
achieved for each 24-hour period by:
Where:
R = The sulfur dioxide removal efficiency
achieved during the 24-hour period,
percent.
K2 = Conversion factor, 0.02400 Mg/D per kg/
hr (0.01071 LT/D per lb/hr).
S = The sulfur production rate during the 24hour period, kg/hr (lb/hr).
X = The sulfur feed rate in the acid gas, Mg/
D (LT/D).
(f) The monitoring devices required in
paragraphs (b)(1), (b)(3) and (c) of this
section must be calibrated at least
annually according to the
manufacturer’s specifications, as
required by § 60.13(b).
(g) The continuous emission
monitoring systems required in
paragraphs (b)(1), (b)(3), and (c) of this
section must be subject to the emission
monitoring requirements of § 60.13 of
the General Provisions. For conducting
the continuous emission monitoring
system performance evaluation required
by § 60.13(c), Performance Specification
2 of appendix B to part 60 of this
chapter must apply, and Method 6 must
be used for systems required by
paragraph (b) of this section.
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§ 60.5408 What is an optional procedure
for measuring hydrogen sulfide in acid
gas—Tutwiler Procedure? 1
(a) When an instantaneous sample is
desired and H2S concentration is ten
grains per 1000 cubic foot or more, a
100 ml Tutwiler burette is used. For
concentrations less than ten grains, a
500 ml Tutwiler burette and more dilute
solutions are used. In principle, this
method consists of titrating hydrogen
sulfide in a gas sample directly with a
standard solution of iodine.
(b) Apparatus. (See Figure 1 of this
subpart) A 100 or 500 ml capacity
Tutwiler burette, with two-way glass
stopcock at bottom and three-way
stopcock at top which connect either
with inlet tubulature or glass-stoppered
cylinder, 10 ml capacity, graduated in
0.1 ml subdivision; rubber tubing
connecting burette with leveling bottle.
(c) Reagents. (1) Iodine stock solution,
0.1N. Weight 12.7 g iodine, and 20 to 25
g cp potassium iodide for each liter of
solution. Dissolve KI in as little water as
necessary; dissolve iodine in
concentrated KI solution, make up to
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1 Gas Engineers Handbook, Fuel Gas Engineering
practices, The Industrial Press, 93 Worth Street,
New York, NY, 1966, First Edition, Second Printing,
page 6/25 (Docket A–80–20–A, Entry II–I–67).
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proper volume, and store in glassstoppered brown glass bottle.
(2) Standard iodine solution, 1 ml =
0.001771 g I. Transfer 33.7 ml of above
0.1N stock solution into a 250 ml
volumetric flask; add water to mark and
mix well. Then, for 100 ml sample of
gas, 1 ml of standard iodine solution is
equivalent to 100 grains H2S per cubic
feet of gas.
(3) Starch solution. Rub into a thin
paste about one teaspoonful of wheat
starch with a little water; pour into
about a pint of boiling water; stir; let
cool and decant off clear solution. Make
fresh solution every few days.
(d) Procedure. Fill leveling bulb with
starch solution. Raise (L), open cock (G),
open (F) to (A), and close (F) when
solutions starts to run out of gas inlet.
Close (G). Purge gas sampling line and
connect with (A). Lower (L) and open
(F) and (G). When liquid level is several
ml past the 100 ml mark, close (G) and
(F), and disconnect sampling tube. Open
(G) and bring starch solution to 100 ml
mark by raising (L); then close (G). Open
(F) momentarily, to bring gas in burette
to atmospheric pressure, and close (F).
Open (G), bring liquid level down to 10
ml mark by lowering (L). Close (G),
clamp rubber tubing near (E) and
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disconnect it from burette. Rinse
graduated cylinder with a standard
iodine solution (0.00171 g I per ml); fill
cylinder and record reading. Introduce
successive small amounts of iodine thru
(F); shake well after each addition;
continue until a faint permanent blue
color is obtained. Record reading;
subtract from previous reading, and call
difference D.
(e) With every fresh stock of starch
solution perform a blank test as follows:
Introduce fresh starch solution into
burette up to 100 ml mark. Close (F) and
(G). Lower (L) and open (G). When
liquid level reaches the 10 ml mark,
close (G). With air in burette, titrate as
during a test and up to same end point.
Call ml of iodine used C. Then,
Grains H2S per 100 cubic foot of gas =
100 (D¥C)
(f) Greater sensitivity can be attained
if a 500 ml capacity Tutwiler burette is
used with a more dilute (0.001N) iodine
solution. Concentrations less than 1.0
grains per 100 cubic foot can be
determined in this way. Usually, the
starch-iodine end point is much less
distinct, and a blank determination of
end point, with H2S-free gas or air, is
required.
BILLING CODE 6560–50–P
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BILLING CODE 6560–50–C
§ 60.5410 How do I demonstrate initial
compliance with the standards for my gas
wellhead affected facility, my centrifugal
compressor affected facility, my
reciprocating compressor affected facility,
my pneumatic controller affected facility,
my storage vessel affected facility, and my
affected facilities at onshore natural gas
processing plants?
You must determine initial
compliance with the standards for each
affected facility using the requirements
in paragraphs (a) through (g) of this
section. The initial compliance period
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begins on the date of publication of the
final rule in the Federal Register or
upon initial startup, whichever is later,
and ends on the date the first annual
report is due as specified in
§ 60.5420(b).
(a) You have achieved initial
compliance with standards for each well
completion operation conducted at your
gas wellhead affected facility if you
have complied with paragraphs (a)(1)
and (a)(2) of this section.
(1) You have notified the
Administrator within 30 days of the
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commencement of the well completion
operation, the date of the
commencement of the well completion
operation, the latitude and longitude
coordinates of the well in decimal
degrees to an accuracy and precision of
five (5) decimals of a degree using the
North American Datum (NAD) of 1983.
(2) You have maintained a log of
records as specified in § 60.5375(b) or (f)
for each well completion operation
conducted during the initial compliance
period.
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(3) You have submitted the initial
annual report for your wellhead affected
facility as required in § 60.5420(b).
(b) You have achieved initial
compliance with standards for your
centrifugal compressor affected facility
if the centrifugal compressor is fitted
with a dry seal system upon initial
startup as required by § 60.5380.
(c) You have achieved initial
compliance with standards for each
reciprocating compressor affected
facility if you have complied with
paragraphs (c)(1) and (c)(2) of this
section.
(1) During the initial compliance
period, you have continuously
monitored the number of hours of
operation.
(2) You have included the cumulative
number of hours of operation for your
reciprocating compressor affected
facility during the initial compliance
period in your initial annual report
required in § 60.5420(b).
(d) You have achieved initial
compliance with emission standards for
your pneumatic controller affected
facility if you comply with the
requirements specified in paragraphs
(d)(1) through (d)(4) of this section.
(1) You have demonstrated, to the
Administrator’s satisfaction, the use of a
high bleed device is predicated as
specified in § 60.5490(a).
(2) You own or operate a pneumatic
controller affected facility located at a
natural gas processing plant and your
pneumatic controller is driven other
than by use of natural gas and therefore
emits zero natural gas.
(3) You own or operate a pneumatic
controller affected facility not located at
a natural gas processing plant and the
manufacturer’s design specifications
guarantee the controller emits less than
or equal to 6.0 standard cubic feet of gas
per hour.
(4) You have included the information
in paragraphs (d)(1) through (d)(3) of
this section in the initial annual report
submitted for your pneumatic controller
affected facilities according to the
requirements of § 60.5420(b).
(e) You have demonstrated initial
compliance with emission standards for
your storage vessel affected facility if
you are complying with paragraphs
(e)(1) through (e)(7) of this section.
(1) You have equipped the storage
vessel with a closed vent system that
meets the requirements of § 63.771(c) of
this chapter connected to a control
device that meets the conditions
specified in § 63.771(d).
(2) You have conducted an initial
performance test as required in
§ 63.772(e) of this chapter within 180
days after initial startup or the date of
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publication of the final rule in the
Federal Register and have conducted
the compliance demonstration in
§ 63.772(f).
(3) You have conducted the initial
inspections required in § 63.773(c) of
this chapter.
(4) You have installed and operated
continuous parameter monitoring
systems in accordance with § 63.773(d)
of this chapter.
(5) If you are exempt from the
standards of § 60.5395 according to
§ 60.5395(a)(1) or (a)(2), you have
determined the condensate or crude oil
throughput, as applicable, according to
paragraphs (e)(5)(i) or (e)(5)(ii) of this
section and demonstrated to the
Administrator’s satisfaction that your
annual average condensate throughput
is less than 1 barrel per day per tank and
your annual average crude oil
throughput is less than 20 barrels per
day per tank.
(i) You have installed and operated a
flow meter to measure condensate or
crude oil throughput in accordance with
the manufacturer’s procedures or
specifications.
(ii) You have used any other method
approved by the Administrator to
determine annual average condensate or
crude oil throughput.
(6) You have submitted the
information in paragraphs (e)(1) through
(e)(5) of this section in the initial annual
report for your storage vessel affected
facility as required in § 60.5420(b).
(f) For affected facilities at onshore
natural gas processing plants, initial
compliance with the VOC requirements
is demonstrated if you are in
compliance with the requirements of
§ 60.5400.
(g) For sweetening unit affected
facilities at onshore natural gas
processing plants, initial compliance is
demonstrated according to paragraphs
(g)(1) through (g)(3) of this section.
(1) To determine compliance with the
standards for SO2 specified in
§ 60.5405(a), during the initial
performance test as required by § 60.8,
the minimum required sulfur dioxide
emission reduction efficiency (Zi) is
compared to the emission reduction
efficiency (R) achieved by the sulfur
recovery technology as specified in
paragraphs (g)(1)(i) and (g)(1)(ii) of this
section.
(i) If R ≥ Zi, your affected facility is
in compliance.
(ii) If R < Zi, your affected facility is
not in compliance.
(2) The emission reduction efficiency
(R) achieved by the sulfur reduction
technology must be determined using
the procedures in § 60.5406(c)(1).
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(3) You have submitted the results of
paragraphs (g)(1) and (g)(2) of this
section in the initial annual report
submitted for your sweetening unit
affected facilities at onshore natural gas
processing plants.
§ 60.5415 How do I demonstrate
continuous compliance with the standards
for my gas wellhead affected facility, my
centrifugal compressor affected facility, my
stationary reciprocating compressor
affected facility, my pneumatic controller
affected facility, my storage vessel affected
facility, and my affected facilities at onshore
natural gas processing plants?
(a) For each gas wellhead affected
facility, you must demonstrate
continuous compliance by maintaining
the records for each completion
operation (as defined in § 60.5430)
specified in § 60.5420.
(b) For each centrifugal compressor
affected facility, continuous compliance
is demonstrated if the rotating
compressor shaft is equipped with a dry
seal.
(c) For each reciprocating compressor
affected facility, you have demonstrated
continuous compliance according to
paragraphs (c)(1) and (2) of this section
(1) You have continuously monitored
the number of hours of operation for
each reciprocating compressor affected
facility since initial startup, or the date
of publication of the final rule in the
Federal Register, or the date of the
previous reciprocating compressor rod
packing replacement, whichever is later.
The cumulative number of hours of
operation must be included in the
annual report as required in
§ 60.5420(b)(4).
(2) You have replaced the
reciprocating compressor rod packing
before the total number of hours of
operation reaches 26,000 hours.
(d) For each pneumatic controller
affected facility, continuous compliance
is demonstrated by maintaining the
records demonstrating that you have
installed and operated the pneumatic
controllers as required in § 60.5390(a),
(b) or (c).
(e) For each storage vessel affected
facility, continuous compliance is
demonstrated according to § 63.772(f) of
this chapter.
(f) For affected facilities at onshore
natural gas processing plants,
continuous compliance with VOC
requirements is demonstrated if you are
in compliance with the requirements of
§ 60.5400.
(g) For each sweetening unit affected
facility at onshore natural gas
processing plants, you must
demonstrate continuous compliance
with the standards for SO2 specified in
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§ 60.5405(b) according to paragraphs
(g)(1) and (g)(2) of this section.
(1) The minimum required SO2
emission reduction efficiency (Zc) is
compared to the emission reduction
efficiency (R) achieved by the sulfur
recovery technology.
(i) If R ≥ Zc, your affected facility is
in compliance.
(ii) If R < Zc, your affected facility is
not in compliance.
(2) The emission reduction efficiency
(R) achieved by the sulfur reduction
technology must be determined using
the procedures in § 60.5406(c)(1).
(h) Affirmative defense for
exceedance of emission limit during
malfunction. In response to an action to
enforce the standards set forth in
§§ 60.5375, 60.5380, 60.5385, 60.5390,
60.5395, 60.5400, and 60.5405, you may
assert an affirmative defense to a claim
for civil penalties for exceedances of
such standards that are caused by
malfunction, as defined at § 60.2.
Appropriate penalties may be assessed,
however, if you fail to meet your burden
of proving all of the requirements in the
affirmative defense. The affirmative
defense shall not be available for claims
for injunctive relief.
(1) To establish the affirmative
defense in any action to enforce such a
limit, you must timely meet the
notification requirements in
§ 60.5420(a), and must prove by a
preponderance of evidence that:
(i) The excess emissions:
(A) Were caused by a sudden,
infrequent, and unavoidable failure of
air pollution control and monitoring
equipment, process equipment, or a
process to operate in a normal or usual
manner, and
(B) Could not have been prevented
through careful planning, proper design
or better operation and maintenance
practices; and
(C) Did not stem from any activity or
event that could have been foreseen and
avoided, or planned for; and
(D) Were not part of a recurring
pattern indicative of inadequate design,
operation, or maintenance; and
(ii) 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 to make these repairs; and
(iii) The frequency, amount and
duration of the excess emissions
(including any bypass) were minimized
to the maximum extent practicable
during periods of such emissions; and
(iv) If the excess emissions resulted
from a bypass of control equipment or
a process, then the bypass was
unavoidable to prevent loss of life,
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personal injury, or severe property
damage; and
(v) All possible steps were taken to
minimize the impact of the excess
emissions on ambient air quality, the
environment and human health; and
(vi) All emissions monitoring and
control systems were kept in operation
if at all possible, consistent with safety
and good air pollution control practices;
and
(vii) All of the actions in response to
the excess emissions were documented
by properly signed, contemporaneous
operating logs; and
(viii) At all times, the facility was
operated in a manner consistent with
good practices for minimizing
emissions; and
(ix) A written root cause analysis has
been prepared, the purpose of which is
to determine, correct, and eliminate the
primary causes of the malfunction and
the excess emissions resulting from the
malfunction event at issue. The analysis
shall also specify, using best monitoring
methods and engineering judgment, the
amount of excess emissions that were
the result of the malfunction.
(2) The owner or operator of the
facility experiencing an exceedance of
its emission limit(s) during a
malfunction shall notify the
Administrator by telephone or facsimile
(FAX) transmission as soon as possible,
but no later than 2 business days after
the initial occurrence of the
malfunction, if it wishes to avail itself
of an affirmative defense to civil
penalties for that malfunction. The
owner or operator seeking to assert an
affirmative defense shall also submit a
written report to the Administrator
within 45 days of the initial occurrence
of the exceedance of the standards in
§§ 60.5375, 60.5380, 60.5385, 60.5390,
60.5395, and 60.5400 to demonstrate,
with all necessary supporting
documentation, that it has met the
requirements set forth in paragraph (a)
of this section. The owner or operator
may seek an extension of this deadline
for up to 30 additional days by
submitting a written request to the
Administrator before the expiration of
the 45-day period. Until a request for an
extension has been approved by the
Administrator, the owner or operator is
subject to the requirement to submit
such report within 45 days of the initial
occurrence of the exceedance.
§ 60.5420 What are my notification,
reporting, and recordkeeping
requirements?
(a) You must submit the notifications
required in § 60.7(a)(1), (a)(3) and (a)(4),
and according to paragraphs (a)(1) and
(a)(2) of this section, if you own or
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operate one or more of the affected
facilities specified in § 60.5365. For the
purposes of this subpart, a workover
that occurs after August 23, 2011 at each
affected facility for which construction,
reconstruction, or modification
commenced on or before August 23,
2011 is considered a modification for
which a notification must be submitted
under § 60.7(a)(4).
(1) If you own or operate a pneumatic
controller affected facility you are not
required to submit the notifications
required in § 60.7(a)(1), (a)(3) and (a)(4).
(2) If you own or operate a gas
wellhead affected facility, you must
submit a notification to the
Administrator within 30 days of the
commencement of the well completion
operation. The notification must include
the date of commencement of the well
completion operation, the latitude and
longitude coordinates of the well in
decimal degrees to an accuracy and
precision of five (5) decimals of a degree
using the North American Datum of
1983.
(b) Reporting requirements. You must
submit annual reports containing the
information specified in paragraphs
(b)(1) through (b)(6) of this section to the
Administrator. The initial annual report
is due 1 year after the initial startup date
for your affected facility or 1 year after
the date of publication of the final rule
in the Federal Register, whichever is
later. Subsequent annual reports are due
on the same date each year as the initial
annual report. If you own or operate
more than one affected facility, you may
submit one report for multiple affected
facilities provided the report contains
all of the information required as
specified in paragraphs (b)(1) through
(b)(6) of this section.
(1) The general information specified
in paragraphs (b)(1)(i) through (b)(1)(iii)
of this section.
(i) The company name and address of
the affected facility.
(ii) An identification of each affected
facility being included in the annual
report.
(iii) Beginning and ending dates of the
reporting period.
(2) For each gas wellhead affected
facility, the information in paragraphs
(b)(2)(i) through (b)(2)(iii) of this
section.
(i) An identification of each well
completion operation, as defined in
§ 60.5430, for each gas wellhead affected
facility conducted during the reporting
period;
(ii) A record of deviations in cases
where well completion operations with
hydraulic fracturing were not performed
in compliance with the requirements
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specified in § 60.5375 for each gas well
affected facility.
(iii) Records specified in § 60.5375(b)
for each well completion operation that
occurred during the reporting period.
(3) For each centrifugal compressor
affected facility installed during the
reporting period, documentation that
the centrifugal compressor is equipped
with dry seals.
(4) For each reciprocating compressor
affected facility, the information
specified in paragraphs (b)(4)(i) and
(b)(4)(ii) of this section.
(i) The cumulative number of hours or
operation since initial startup, the date
of publication of the final rule in the
Federal Register, or since the previous
reciprocating compressor rod packing
replacement, whichever is later.
(ii) Documentation that the
reciprocating compressor rod packing
was replaced before the cumulative
number of hours of operation reached
24,000 hours.
(5) For each pneumatic controller
affected facility, the information
specified in paragraphs (b)(5)(i) through
(b)(5)(iv) of this section.
(i) The date, location and
manufacturer specifications for each
pneumatic controller installed.
(ii) If applicable, documentation that
the use of high bleed pneumatic devices
is predicated and the reasons why.
(iii) For pneumatic controllers not
installed at a natural gas processing
plant, the manufacturer’s guarantee that
the device is designed such that natural
gas emissions are less than 6 standard
cubic feet per hour.
(iv) For pneumatic controllers
installed at a natural gas processing
plant, documentation that each
controllers has zero natural gas
emissions.
(6) For each storage vessel affected
facility, the information in paragraphs
(b)(6)(i) and (b)(6)(ii) of this section.
(i) If required to reduce emissions by
complying with § 60.5395(a)(1), the
records specified in § 63.774(b)(2)
through (b)(8) of this chapter.
(ii) Documentation that the annual
average condensate throughput is less
than 1 barrel per day per storage vessel
and crude oil throughput is less than 21
barrels per day per storage for meeting
the requirements in § 60.5395(a)(1) or
(a)(2).
(c) Recordkeeping requirements. You
must maintain the records identified as
specified in § 60.7(f) and in paragraphs
(c)(1) through (c)(5) of this section
(1) The records for each gas wellhead
affected facility as specified in
paragraphs (c)(1)(i) through (c)(1)(iii).
(i) Records identifying each well
completion operation for each gas
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wellhead affected facility conducted
during the reporting period;
(ii) Record of deviations in cases
where well completion operations with
hydraulic fracturing were not performed
in compliance with the requirements
specified in § 60.5375.
(iii) Records required in § 60.5375(b)
or (f) for each well completion operation
conducted for each gas wellhead
affected facility that occurred during the
reporting period. You must maintain the
records specified in paragraphs
(c)(1)(iii)(A) and (c)(1)(iii)(B) of this
section.
(A) For each gas wellheads affected
facility required to comply with the
requirements of § 60.5375(a), you must
record: The location of the well; the
duration of flowback; duration of
recovery to the sales line; duration of
combustion; duration of venting; and
specific reasons for venting in lieu of
capture or combustion. The duration
must be specified in hours of time.
(B) For each gas wellhead affected
facility required to comply with the
requirements of § 60.5375(f), you must
maintain the records specified in
paragraph (c)(1)(iii)(A) of this section
except that you do not have to record
the duration of recovery to the sales
line. In addition, you must record the
distance, in miles, of the nearest
gathering line.
(2) For each centrifugal compressor
affected facility, you must maintain
records on the type of seal system
installed.
(3) For each reciprocating
compressors affected facility, you must
maintain the records in paragraphs
(c)(3)(i) and (c)(3)(ii) of this section.
(i) Records of the cumulative number
of hours of operation since initial
startup or the date of publication of the
final rule in the Federal Register, or the
previous replacement of the
reciprocating compressor rod packing,
whichever is later.
(ii) Records of the date and time of
each reciprocating compressor rod
packing replacement.
(4) For each pneumatic controller
affected facility, you must maintain the
records identified in paragraphs (c)(4)(i)
through (c)(4)(iv) of this section.
(i) Records of the date, location and
manufacturer specifications for each
pneumatic controller installed.
(ii) Records of the determination that
the use of high bleed pneumatic devices
is predicated and the reasons why.
(iii) If the pneumatic controller
affected facility is not located at a
natural gas processing plant, records of
the manufacturer’s guarantee that the
device is designed such that natural gas
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emissions are less than 6 standard cubic
feet per hour.
(iv) If the pneumatic controller
affected facility is located at a natural
gas processing plant, records of the
documentation that only instrument air
controllers are used.
(5) For each storage vessel affected
facility, you must maintain the records
identified in paragraphs (c)(5)(i) and
(c)(5)(ii) of this section.
(i) If required to reduce emissions by
complying with § 63.766, the records
specified in § 63.774(b)(2) through (8) of
this chapter.
(ii) Records of the determination that
the annual average condensate
throughput is less than 1 barrel per day
per storage vessel and crude oil
throughput is less than 21 barrels per
day per storage vessel for the exemption
under § 60.5395(a)(1) and (a)(2).
§ 60.5421 What are my additional
recordkeeping requirements for my affected
facility subject to VOC requirements for
onshore natural gas processing plants?
(a) You must comply with the
requirements of paragraph (b) of this
section in addition to the requirements
of § 60.486a.
(b) The following recordkeeping
requirements apply to pressure relief
devices subject to the requirements of
§ 60.5401(b)(1) of this subpart.
(1) When each leak is detected as
specified in § 60.5401(b)(2), a
weatherproof and readily visible
identification, marked with the
equipment identification number, must
be attached to the leaking equipment.
The identification on the pressure relief
device may be removed after it has been
repaired.
(2) When each leak is detected as
specified in § 60.5401(b)(2), the
following information must be recorded
in a log and shall be kept for 2 years in
a readily accessible location:
(i) The instrument and operator
identification numbers and the
equipment identification number.
(ii) The date the leak was detected
and the dates of each attempt to repair
the leak.
(iii) Repair methods applied in each
attempt to repair the leak.
(iv) ‘‘Above 500 ppm’’ if the
maximum instrument reading measured
by the methods specified in paragraph
(a) of this section after each repair
attempt is 500 ppm or greater.
(v) ‘‘Repair delayed’’ and the reason
for the delay if a leak is not repaired
within 15 calendar days after discovery
of the leak.
(vi) The signature of the owner or
operator (or designate) whose decision it
was that repair could not be effected
without a process shutdown.
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(vii) The expected date of successful
repair of the leak if a leak is not repaired
within 15 days.
(viii) Dates of process unit shutdowns
that occur while the equipment is
unrepaired.
(ix) The date of successful repair of
the leak.
(x) A list of identification numbers for
equipment that are designated for no
detectable emissions under the
provisions of § 60.482–4a(a). The
designation of equipment subject to the
provisions of § 60.482–4a(a) must be
signed by the owner or operator.
§ 60.5422 What are my additional reporting
requirements for my affected facility subject
to VOC requirements for onshore natural
gas processing plants?
(a) You must comply with the
requirements of paragraphs (b) and (c) of
this section in addition to the
requirements of § 60.487a(a), (b), (c)(2)(i)
through (iv), and (c)(2)(vii) through
(viii).
(b) An owner or operator must
include the following information in the
initial semiannual report in addition to
the information required in
§ 60.487a(b)(1) through (4): Number of
pressure relief devices subject to the
requirements of § 60.5401(b) except for
those pressure relief devices designated
for no detectable emissions under the
provisions of § 60.482–4a(a) and those
pressure relief devices complying with
§ 60.482–4a(c).
(c) An owner or operator must include
the following information in all
semiannual reports in addition to the
information required in
§ 60.487a(c)(2)(i) through (vi):
(1) Number of pressure relief devices
for which leaks were detected as
required in § 60.5401(b)(2); and
(2) Number of pressure relief devices
for which leaks were not repaired as
required in § 60.5401(b)(3).
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
§ 60.5423 What additional recordkeeping
and reporting requirements apply to my
sweetening unit affected facilities at
onshore natural gas processing plants?
(a) You must retain records of the
calculations and measurements required
in § 60.5405(a) and (b) and § 60.5407(a)
through (g) for at least 2 years following
the date of the measurements. This
requirement is included under § 60.7(d)
of the General Provisions.
(b) You must submit a written report
of excess emissions to the Administrator
semiannually. For the purpose of these
reports, excess emissions are defined as:
(1) Any 24-hour period (at consistent
intervals) during which the average
sulfur emission reduction efficiency (R)
is less than the minimum required
efficiency (Z).
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(2) For any affected facility electing to
comply with the provisions of
§ 60.5407(b)(2), any 24-hour period
during which the average temperature of
the gases leaving the combustion zone
of an incinerator is less than the
appropriate operating temperature as
determined during the most recent
performance test in accordance with the
provisions of § 60.5407(b)(2). Each 24hour period must consist of at least 96
temperature measurements equally
spaced over the 24 hours.
(c) To certify that a facility is exempt
from the control requirements of these
standards, for each facility with a design
capacity less that 2 LT/D of H2S in the
acid gas (expressed as sulfur) you must
keep, for the life of the facility, an
analysis demonstrating that the facility’s
design capacity is less than 2 LT/D of
H2S expressed as sulfur.
(d) If you elect to comply with
§ 60.5407(e) you must keep, for the life
of the facility, a record demonstrating
that the facility’s design capacity is less
than 150 LT/D of H2S expressed as
sulfur.
(e) The requirements of paragraph (b)
of this section remain in force until and
unless the EPA, in delegating
enforcement authority to a state under
section 111(c) of the Act, approves
reporting requirements or an alternative
means of compliance surveillance
adopted by such state. In that event,
affected sources within the state will be
relieved of obligation to comply with
paragraph (b) of this section, provided
that they comply with the requirements
established by the state.
§ 60.5425 What part of the General
Provisions apply to me?
Table 3 to this subpart shows which
parts of the General Provisions in
§§ 60.1 through 60.19 apply to you.
§ 60.5430
subpart?
What definitions apply to this
As used in this subpart, all terms not
defined herein shall have the meaning
given them in the Act, in subpart A or
subpart VVa of part 60; and the
following terms shall have the specific
meanings given them.
Acid gas means a gas stream of
hydrogen sulfide (H2S) and carbon
dioxide (CO2) that has been separated
from sour natural gas by a sweetening
unit.
Alaskan North Slope means the
approximately 69,000 square-mile area
extending from the Brooks Range to the
Arctic Ocean.
API Gravity means the weight per unit
volume of hydrocarbon liquids as
measured by a system recommended by
the American Petroleum Institute (API)
and is expressed in degrees.
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52809
Centrifugal compressor means a piece
of equipment that compresses a process
gas by means of mechanical rotating
vanes or impellers.
City gate means the delivery point at
which natural gas is transferred from a
transmission pipeline to the local gas
utility.
Completion combustion device means
any ignition device, installed
horizontally or vertically, used in
exploration and production operations
to combust otherwise vented emissions
from completions or workovers.
Compressor means a piece of
equipment that compresses process gas
and is usually a centrifugal compressor
or a reciprocating compressor.
Compressor station means any
permanent combination of compressors
that move natural gas at increased
pressure from fields, in transmission
pipelines, or into storage.
Condensate means a hydrocarbon
liquid separated from natural gas that
condenses due to changes in the
temperature, pressure, or both, and
remains liquid at standard conditions,
as specified in § 60.2. For the purposes
of this subpart, a hydrocarbon liquid
with an API gravity equal to or greater
than 40 degrees is considered
condensate.
Crude oil means crude petroleum oil
or any other hydrocarbon liquid, which
are produced at the well in liquid form
by ordinary production methods, and
which are not the result of condensation
of gas before or after it leaves the
reservoir. For the purposes of this
subpart, a hydrocarbon liquid with an
API gravity less than 40 degrees is
considered crude oil.
Dehydrator means a device in which
an absorbent directly contacts a natural
gas stream and absorbs water in a
contact tower or absorption column
(absorber).
Delineation well means a well drilled
in order to determine the boundary of a
field or producing reservoir.
Equipment means each pump,
pressure relief device, open-ended valve
or line, valve, compressor, and flange or
other connector that is in VOC service
or in wet gas service, and any device or
system required by this subpart.
Field gas means feedstock gas
entering the natural gas processing
plant.
Field gas gathering means the system
used to transport field gas from a field
to the main pipeline in the area.
Flare means a thermal oxidation
system using an open (without
enclosure) flame.
Flowback means the process of
allowing fluids to flow from the well
following a treatment, either in
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preparation for a subsequent phase of
treatment or in preparation for cleanup
and returning the well to production.
Flow line means surface pipe through
which oil and/or natural gas travels
from the well.
Gas-driven pneumatic controller
means a pneumatic controller powered
by pressurized natural gas.
Gas processing plant process unit
means equipment assembled for the
extraction of natural gas liquids from
field gas, the fractionation of the liquids
into natural gas products, or other
operations associated with the
processing of natural gas products. A
process unit can operate independently
if supplied with sufficient feed or raw
materials and sufficient storage facilities
for the products.
Gas well means a well, the principal
production of which at the mouth of the
well is gas.
High-bleed pneumatic devices means
automated, continuous bleed flow
control devices powered by pressurized
natural gas and used for maintaining a
process condition such as liquid level,
pressure, delta-pressure and
temperature. Part of the gas power
stream which is regulated by the process
condition flows to a valve actuator
controller where it vents continuously
(bleeds) to the atmosphere at a rate in
excess of six standard cubic feet per
hour.
Hydraulic fracturing means the
process of directing pressurized liquids,
containing water, proppant, and any
added chemicals, to penetrate tight
sand, shale, or coal formations that
involve high rate, extended back flow to
expel fracture fluids and sand during
completions and well workovers.
In light liquid service means that the
piece of equipment contains a liquid
that meets the conditions specified in
§ 60.485a(e) or § 60.5401(h)(2) of this
part.
In wet gas service means that a
compressor or piece of equipment
contains or contacts the field gas before
the extraction step at a gas processing
plant process unit.
Liquefied natural gas unit means a
unit used to cool natural gas to the point
at which it is condensed into a liquid
which is colorless, odorless, noncorrosive and non-toxic.
Low-bleed pneumatic controller
means automated flow control devices
powered by pressurized natural gas and
used for maintaining a process
condition such as liquid level, pressure,
delta-pressure and temperature. Part of
the gas power stream which is regulated
by the process condition flows to a
valve actuator controller where it vents
continuously (bleeds) to the atmosphere
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at a rate equal to or less than six
standard cubic feet per hour.
Modification means any physical
change in, or change in the method of
operation of, an affected facility which
increases the amount of VOC or natural
gas emitted into the atmosphere by that
facility or which results in the emission
of VOC or natural gas into the
atmosphere not previously emitted. For
the purposes of this subpart, each
recompletion of a fractured or
refractured existing gas well is
considered to be a modification.
Natural gas liquids means the
hydrocarbons, such as ethane, propane,
butane, and pentane that are extracted
from field gas.
Natural gas processing plant (gas
plant) means any processing site
engaged in the extraction of natural gas
liquids from field gas, fractionation of
mixed natural gas liquids to natural gas
products, or both.
Nonfractionating plant means any gas
plant that does not fractionate mixed
natural gas liquids into natural gas
products.
Non gas-driven pneumatic device
means an instrument that is actuated
using other sources of power than
pressurized natural gas; examples
include solar, electric, and instrument
air.
Onshore means all facilities except
those that are located in the territorial
seas or on the outer continental shelf.
Plunger lift system means an
intermittent gas lift that uses gas
pressure buildup in the casing-tubing
annulus to push a steel plunger, and the
column of fluid ahead of it, up the well
tubing to the surface.
Pneumatic controller means an
automated instrument used for
maintaining a process condition such as
liquid level, pressure, delta-pressure
and temperature.
Pneumatic pump means a pump that
uses pressurized natural gas to move a
piston or diaphragm, which pumps
liquids on the opposite side of the
piston or diaphragm.
Process unit means components
assembled for the extraction of natural
gas liquids from field gas, the
fractionation of the liquids into natural
gas products, or other operations
associated with the processing of
natural gas products. A process unit can
operate independently if supplied with
sufficient feed or raw materials and
sufficient storage facilities for the
products.
Reciprocating compressor means a
piece of equipment that increases the
pressure of a process gas by positive
displacement, employing linear
movement of the driveshaft.
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Reciprocating compressor rod packing
means a series of flexible rings in
machined metal cups that fit around the
reciprocating compressor piston rod to
create a seal limiting the amount of
compressed natural gas that escapes to
the atmosphere.
Reduced emissions completion means
a well completion where gas flowback
that is otherwise vented is captured,
cleaned, and routed to the sales line.
Reduced emissions recompletion
means a well completion following
refracturing of a gas well where gas
flowback that is otherwise vented is
captured, cleaned, and routed to the
sales line.
Reduced sulfur compounds means
H2S, carbonyl sulfide (COS), and carbon
disulfide (CS2).
Routed to a process or route to a
process means the emissions are
conveyed to any enclosed portion of a
process unit where the emissions are
predominantly recycled and/or
consumed in the same manner as a
material that fulfills the same function
in the process and/or transformed by
chemical reaction into materials that are
not regulated materials and/or
incorporated into a product; and/or
recovered.
Salable quality gas means natural gas
that meets the composition, moisture, or
other limits set by the purchaser of the
natural gas.
Sales line means pipeline, generally
small in diameter, used to transport oil
or gas from the well to a processing
facility or a mainline pipeline.
Storage vessel means a stationary
vessel or series of stationary vessels that
are either manifolded together or are
located at a single well site and that
have potential for VOC emissions equal
to or greater than 10 tpy.
Sulfur production rate means the rate
of liquid sulfur accumulation from the
sulfur recovery unit.
Sulfur recovery unit means a process
device that recovers element sulfur from
acid gas.
Surface site means any combination
of one or more graded pad sites, gravel
pad sites, foundations, platforms, or the
immediate physical location upon
which equipment is physically affixed.
Sweetening unit means a process
device that removes hydrogen sulfide
and/or carbon dioxide from the natural
gas stream.
Total Reduced Sulfur (TRS) means the
sum of the sulfur compounds hydrogen
sulfide, methyl mercaptan, dimethyl
sulfide, and dimethyl disulfide as
measured by Method 16 of appendix A
to part 60 of this chapter.
Total SO2 equivalents means the sum
of volumetric or mass concentrations of
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the sulfur compounds obtained by
adding the quantity existing as SO2 to
the quantity of SO2 that would be
obtained if all reduced sulfur
compounds were converted to SO2
(ppmv or kg/dscm (lb/dscf)).
Underground storage tank means a
storage tank stored below ground.
Well means an oil or gas well, a hole
drilled for the purpose of producing oil
or gas, or a well into which fluids are
injected.
Well completion means the process
that allows for the flow of petroleum or
natural gas from newly drilled wells to
expel drilling and reservoir fluids and
tests the reservoir flow characteristics,
steps which may vent produced gas to
the atmosphere via an open pit or tank.
Well completion also involves
connecting the well bore to the
reservoir, which may include treating
the formation or installing tubing,
packer(s), or lifting equipment.
Well completion operation means any
well completion or well workover
occurring at a gas wellhead affected
facility.
Well site means the areas that are
directly disturbed during the drilling
and subsequent operation of, or affected
by, production facilities directly
associated with any oil well, gas well,
or injection well and its associated well
pad.
Wellhead means the piping, casing,
tubing and connected valves protruding
above the earth’s surface for an oil and/
or natural gas well. The wellhead ends
where the flow line connects to a
wellhead valve. The wellhead does not
include other equipment at the well site
except for any conveyance through
which gas is vented to the atmosphere.
Wildcat well means a well outside
known fields or the first well drilled in
an oil or gas field where no other oil and
gas production exists.
TABLE 1 TO SUBPART OOOO OF PART 60—REQUIRED MINIMUM INITIAL SO2 EMISSION REDUCTION EFFICIENCY (Zi)
Sulfur feed rate (X), LT/D
H2S content of acid gas (Y), %
2.0 ≤ X ≤ 5.0
Y ≥ 50 .......................................
79.0
20 ≤ Y < 50 ...............................
5.0 < X ≤ 15.0
79.0
15.0 < X ≤ 300.0
X > 300.0
88.51X0.0101Y0.0125 or 99.9, whichever is smaller
88.5X0.0101Y0.0125 or 97.9, whichever is smaller
97.9
10 ≤ Y < 20 ...............................
79.0
......................
or 97.9, whichever is smaller ...
93.5
93.5
Y < 10 .......................................
79.0
79.0
79.0
79.0
88.5X0.0101Y0.0125
TABLE 2 TO SUBPART OOOO OF PART 60—REQUIRED MINIMUM SO2 EMISSION REDUCTION EFFICIENCY (Zc)
Sulfur feed rate (X), LT/D
H2S content of acid gas (Y), %
2.0 ≤ X ≤ 5.0
5.0 < X ≤ 15.0
15.0 < X ≤ 300.0
X > 300.0
Y ≥ 50 .......................................
74.0
20 ≤ Y < 50 ...............................
74.0
10 ≤ Y < 20 ...............................
74.0
85.35X0.0144Y0.0128 ....................
or 90.8, whichever is smaller ...
90.8
90.8
Y < 10 .......................................
74.0
74.0
74.0
74.0
E = The sulfur emission rate expressed as
elemental sulfur, kilograms per hour (kg/
hr) [pounds per hour (lb/hr)], rounded to
one decimal place.
R = The sulfur emission reduction efficiency
achieved in percent, carried to one
decimal place.
S = The sulfur production rate, kilograms per
hour (kg/hr) [pounds per hour (lb/hr)],
rounded to one decimal place.
85.35X0.0144Y0.0128
or 99.9, whichever is smaller
85.35X0.0144Y0.0128 or 97.9, whichever is smaller
X = The sulfur feed rate from the sweetening
unit (i.e., the H2S in the acid gas),
expressed as sulfur, Mg/D(LT/D),
rounded to one decimal place.
Y = The sulfur content of the acid gas from
the sweetening unit, expressed as mole
percent H2S (dry basis) rounded to one
decimal place.
Z = The minimum required sulfur dioxide
(SO2) emission reduction efficiency,
97.5
expressed as percent carried to one
decimal place. Zi refers to the reduction
efficiency required at the initial
performance test. Zc refers to the
reduction efficiency required on a
continuous basis after compliance with
Zi has been demonstrated.
TABLE 3 TO SUBPART OOOO OF PART 60—APPLICABILITY OF GENERAL PROVISIONS TO SUBPART OOOO
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
[As stated in § 60.5425, you must comply with the following applicable General Provisions]
General provisions
citation
§ 60.1
§ 60.2
§ 60.3
§ 60.4
§ 60.5
§ 60.6
§ 60.7
.............................
.............................
.............................
.............................
.............................
.............................
.............................
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Subject of citation
Applies to
subpart?
General applicability of the General Provisions ...
Definitions .............................................................
Units and abbreviations ........................................
Address ................................................................
Determination of construction or modification ......
Review of plans ....................................................
Notification and record keeping ...........................
Yes.
Yes. ...............
Yes.
Yes.
Yes.
Yes.
Yes ................
18:53 Aug 22, 2011
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Explanation
Additional terms defined in § 60.5430.
Except that § 60.7 only applies as specified in
§ 60.5420(a).
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TABLE 3 TO SUBPART OOOO OF PART 60—APPLICABILITY OF GENERAL PROVISIONS TO SUBPART OOOO—Continued
[As stated in § 60.5425, you must comply with the following applicable General Provisions]
General provisions
citation
Subject of citation
Applies to
subpart?
Explanation
§ 60.8 .............................
Performance tests ................................................
No ..................
Performance testing is required for storage vessels as specified in 40 CFR part 63, subpart
HH.
§ 60.9 .............................
§ 60.10 ...........................
§ 60.11 ...........................
Yes.
Yes.
No ..................
§ 60.12 ...........................
§ 60.13 ...........................
Availability of information .....................................
State authority ......................................................
Compliance with standards and maintenance requirements.
Circumvention .......................................................
Monitoring requirements .......................................
§ 60.14
§ 60.15
§ 60.16
§ 60.17
§ 60.18
§ 60.19
Modification ..........................................................
Reconstruction ......................................................
Priority list .............................................................
Incorporations by reference .................................
General control device requirements ...................
General notification and reporting requirement ...
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
...........................
...........................
...........................
...........................
...........................
...........................
Yes.
Yes ................
9. Section 63.14 is amended by:
a. Adding paragraphs (b)(69), (b)(70),
(b)(71) and (b)(72); and
b. Revising paragraph (i)(1) to read as
follows:
63.4965(a)(3), 63.5160(d)(1)(iii),
63.9307(c)(2), 63.9323(a)(3),
63.11148(e)(3)(iii), 63.11155(e)(3),
63.11162(f)(3)(iii) and (f)(4),
63.11163(g)(1)(iii) and (g)(2),
63.11410(j)(1)(iii), 63.11551(a)(2)(i)(C),
63.11646(a)(1)(iii), table 5 to subpart
DDDDD of this part, and table 1 to
subpart ZZZZZ of this part.
*
*
*
*
*
§ 63.14
Subpart HH—[Amended]
PART 63—[AMENDED]
8. The authority citation for part 63
continues to read as follows:
Authority: 42 U.S.C. 7401, et seq.
Incorporations by reference.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
*
*
*
*
*
(b) * * *
*
*
*
*
*
(69) ASTM D1945–03(2010) Standard
Test Method for Analysis of Natural Gas
by Gas Chromatography, IBR approved
for §§ 63.772 and 63.1282.
(70) ASTM D5504–08 Standard Test
Method for Determination of Sulfur
Compounds in Natural Gas and Gaseous
Fuels by Gas Chromatography and
Chemiluminescence, IBR approved for
§§ 63.772 and 63.1282.
(71) ASTM D3588–98(2003) Standard
Practice for Calculating Heat Value,
Compressibility Factor, and Relative
Density of Gaseous Fuels, IBR approved
for §§ 63.772 and 63.1282.
(72) ASTM D4891–89(2006) Standard
Test Method for Heating Value of Gases
in Natural Gas Range by Stoichiometric
Combustion, IBR approved for §§ 63.772
and 63.1282.
*
*
*
*
*
(i) * * *
(1) ANSI/ASME PTC 19.10–1981,
Flue and Exhaust Gas Analyses [Part 10,
Instruments and Apparatus], issued
August 31, 1981 IBR approved for
§§ 63.309(k)(1)(iii), 63.771(e), 63.865(b),
63.1281(d), 63.3166(a)(3),
63.3360(e)(1)(iii), 63.3545(a)(3),
63.3555(a)(3), 63.4166(a)(3),
63.4362(a)(3), 63.4766(a)(3),
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10. Section 63.760 is amended by:
a. Revising paragraph (a)(1)
introductory text;
b. Revising paragraph (a)(1)(iii);
c. Revising paragraph (a)(2);
d. Revising paragraph (b)(1)(ii);
e. Revising paragraph (f) introductory
text;
f. Revising paragraph (f)(1);
g. Revising paragraph (f)(2); and
h. Adding paragraphs (f)(7), (f)(8),
(f)(9) and (f)(10) to read as follows:
§ 63.760 Applicability and designation of
affected source.
(a) * * *
(1) Facilities that are major or area
sources of hazardous air pollutants
(HAP) as defined in § 63.761. Emissions
for major source determination purposes
can be estimated using the maximum
natural gas or hydrocarbon liquid
throughput, as appropriate, calculated
in paragraphs (a)(1)(i) through (iii) of
this section. As an alternative to
calculating the maximum natural gas or
hydrocarbon liquid throughput, the
owner or operator of a new or existing
source may use the facility’s design
maximum natural gas or hydrocarbon
liquid throughput to estimate the
maximum potential emissions. Other
means to determine the facility’s major
source status are allowed, provided the
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Requirements are specified in subpart OOOO.
Continuous monitors are required for storage
vessels.
information is documented and
recorded to the Administrator’s
satisfaction in accordance with
§ 63.10(b)(3). A facility that is
determined to be an area source, but
subsequently increases its emissions or
its potential to emit above the major
source levels, and becomes a major
source, must comply thereafter with all
provisions of this subpart applicable to
a major source starting on the applicable
compliance date specified in paragraph
(f) of this section. Nothing in this
paragraph is intended to preclude a
source from limiting its potential to emit
through other appropriate mechanisms
that may be available through the
permitting authority.
*
*
*
*
*
(iii) The owner or operator shall
determine the maximum values for
other parameters used to calculate
emissions as the maximum for the
period over which the maximum natural
gas or hydrocarbon liquid throughput is
determined in accordance with
paragraph (a)(1)(i)(A) or (B) of this
section. Parameters, other than glycol
circulation rate, shall be based on either
highest measured values or annual
average. For estimating maximum
potential emissions from glycol
dehydration units, the glycol circulation
rate used in the calculation shall be the
unit’s maximum rate under its physical
and operational design consistent with
the definition of potential to emit in
§ 63.2.
(2) Facilities that process, upgrade, or
store hydrocarbon liquids prior to the
point where hydrocarbon liquids enter
either the Organic Liquids Distribution
(Non-gasoline) or Petroleum Refineries
source categories.
*
*
*
*
*
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(b) * * *
(1) * * *
(ii) Each storage vessel;
*
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*
*
*
(f) The owner or operator of an
affected major source shall achieve
compliance with the provisions of this
subpart by the dates specified in
paragraphs (f)(1), (f)(2), and (f)(7)
through (f)(10) of this section. The
owner or operator of an affected area
source shall achieve compliance with
the provisions of this subpart by the
dates specified in paragraphs (f)(3)
through (f)(6) of this section.
(1) Except as specified in paragraphs
(f)(7) through (10) of this section, the
owner or operator of an affected major
source, the construction or
reconstruction of which commenced
before February 6, 1998, shall achieve
compliance with the applicable
provisions of this subpart no later than
June 17, 2002, except as provided for in
§ 63.6(i). The owner or operator of an
area source, the construction or
reconstruction of which commenced
before February 6, 1998, that increases
its emissions of (or its potential to emit)
HAP such that the source becomes a
major source that is subject to this
subpart shall comply with this subpart
3 years after becoming a major source.
(2) Except as specified in paragraphs
(f)(7) through (10) of this section, the
owner or operator of an affected major
source, the construction or
reconstruction of which commences on
or after February 6, 1998, shall achieve
compliance with the applicable
provisions of this subpart immediately
upon initial startup or June 17, 1999,
whichever date is later. Area sources,
other than production field facilities
identified in (f)(9) of this section, the
construction or reconstruction of which
commences on or after February 6, 1998,
that become major sources shall comply
with the provisions of this standard
immediately upon becoming a major
source.
*
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*
*
(7) Each affected small glycol
dehydration unit and each storage
vessel that is not a storage vessel with
the potential for flash emissions located
at a major source, that commenced
construction before August 23, 2011
must achieve compliance no later than
3 years after the date of publication of
the final rule in the Federal Register,
except as provided in § 63.6(i).
(8) Each affected small glycol
dehydration unit and each storage
vessel that is not a storage vessel with
the potential for flash emissions, both as
defined in § 63.761, located at a major
source, that commenced construction on
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or after August 23, 2011 must achieve
compliance immediately upon initial
startup or the date of publication of the
final rule in the Federal Register,
whichever is later.
(9) A production field facility, as
defined in § 63.761, constructed before
August 23, 2011 that was previously
determined to be an area source but
becomes a major source (as defined in
paragraph 3 of the major source
definition in § 63.761) on the date of
publication of the final rule in the
Federal Register must achieve
compliance no later than 3 years after
the date of publication of the final rule
in the Federal Register, except as
provided in § 63.6(i).
(10) Each large glycol dehydration
unit, as defined in § 63.761, that has
complied with the provisions of this
subpart prior to August 23, 2011 by
reducing its benzene emissions to less
than 0.9 megagrams per year must
achieve compliance no later than 90
days after the date of publication of the
final rule in the Federal Register, except
as provided in § 63.6(i).
*
*
*
*
*
11. Section 63.761 is amended by:
a. Adding, in alphabetical order, new
definitions for the terms ‘‘affirmative
defense,’’ ‘‘BTEX,’’ ‘‘flare,’’ ‘‘large glycol
dehydration units’’ and ‘‘small glycol
dehydration units’’;
b. Revising the definitions for
‘‘associated equipment,’’ ‘‘facility,’’
‘‘glycol dehydration unit baseline
operations,’’ and ‘‘temperature
monitoring device’’; and
c. Revising paragraph (3) of the
definition for ‘‘major source’’ to read as
follows:
§ 63.761
Definitions.
*
*
*
*
*
Affirmative defense means, in the
context of an enforcement proceeding, a
response or defense put forward by a
defendant, regarding which the
defendant has the burden of proof, and
the merits of which are independently
and objectively evaluated in a judicial
or administrative proceeding.
*
*
*
*
*
Associated equipment, as used in this
subpart and as referred to in section
112(n)(4) of the Act, means equipment
associated with an oil or natural gas
exploration or production well, and
includes all equipment from the
wellbore to the point of custody
transfer, except glycol dehydration units
and storage vessels.
*
*
*
*
*
BTEX means benzene, toluene, ethyl
benzene and xylene.
*
*
*
*
*
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52813
Facility means any grouping of
equipment where hydrocarbon liquids
are processed, upgraded (i.e., remove
impurities or other constituents to meet
contract specifications), or stored; or
where natural gas is processed,
upgraded, or stored. For the purpose of
a major source determination, facility
(including a building, structure, or
installation) means oil and natural gas
production and processing equipment
that is located within the boundaries of
an individual surface site as defined in
this section. Equipment that is part of a
facility will typically be located within
close proximity to other equipment
located at the same facility. Pieces of
production equipment or groupings of
equipment located on different oil and
gas leases, mineral fee tracts, lease
tracts, subsurface or surface unit areas,
surface fee tracts, surface lease tracts, or
separate surface sites, whether or not
connected by a road, waterway, power
line or pipeline, shall not be considered
part of the same facility. Examples of
facilities in the oil and natural gas
production source category include, but
are not limited to, well sites, satellite
tank batteries, central tank batteries, a
compressor station that transports
natural gas to a natural gas processing
plant, and natural gas processing plants.
*
*
*
*
*
Flare means a thermal oxidation
system using an open flame (i.e.,
without enclosure).
*
*
*
*
*
Glycol dehydration unit baseline
operations means operations
representative of the large glycol
dehydration unit operations as of June
17, 1999 and the small glycol
dehydrator unit operations as of August
23, 2011. For the purposes of this
subpart, for determining the percentage
of overall HAP emission reduction
attributable to process modifications,
baseline operations shall be parameter
values (including, but not limited to,
glycol circulation rate or glycol-HAP
absorbency) that represent actual longterm conditions (i.e., at least 1 year).
Glycol dehydration units in operation
for less than 1 year shall document that
the parameter values represent expected
long-term operating conditions had
process modifications not been made.
*
*
*
*
*
Large glycol dehydration unit means a
glycol dehydration unit with an actual
annual average natural gas flowrate
equal to or greater than 85 thousand
standard cubic meters per day and
actual annual average benzene
emissions equal to or greater than 0.90
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Mg/yr, determined according to
§ 63.772(b).
*
*
*
*
*
Major source * * *
(3) For facilities that are production
field facilities, only HAP emissions from
glycol dehydration units and storage
vessels shall be aggregated for a major
source determination. For facilities that
are not production field facilities, HAP
emissions from all HAP emission units
shall be aggregated for a major source
determination.
*
*
*
*
*
Small glycol dehydration unit means
a glycol dehydration unit, located at a
major source, with an actual annual
average natural gas flowrate less than 85
thousand standard cubic meters per day
or actual annual average benzene
emissions less than 0.90 Mg/yr,
determined according to § 63.772(b).
*
*
*
*
*
Temperature monitoring device
means an instrument used to monitor
temperature and having a minimum
accuracy of ± 1 percent of the
temperature being monitored expressed
in °C, or ± 2.5 °C, whichever is greater.
The temperature monitoring device may
measure temperature in degrees
Fahrenheit or degrees Celsius, or both.
*
*
*
*
*
12. Section 63.762 is revised to read
as follows:
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
§ 63.762
Startups and shutdowns.
(a) The provisions set forth in this
subpart shall apply at all times.
(b) The owner or operator shall not
shut down items of equipment that are
required or utilized for compliance with
the provisions of this subpart during
times when emissions are being routed
to such items of equipment, if the
shutdown would contravene
requirements of this subpart applicable
to such items of equipment. This
paragraph does not apply if the owner
or operator must shut down the
equipment to avoid damage due to a
contemporaneous startup or shutdown,
of the affected source or a portion
thereof.
(c) During startups and shutdowns,
the owner or operator shall implement
measures to prevent or minimize excess
emissions to the maximum extent
practical.
(d) In response to an action to enforce
the standards set forth in this subpart,
you may assert an affirmative defense to
a claim for civil penalties for
exceedances of such standards that are
caused by malfunction, as defined in 40
CFR 63.2. Appropriate penalties may be
assessed, however, if you fail to meet
your burden of proving all the
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requirements in the affirmative defense.
The affirmative defense shall not be
available for claims for injunctive relief.
(1) To establish the affirmative
defense in any action to enforce such a
limit, you must timely meet the
notification requirements in paragraph
(d)(2) of this section, and must prove by
a preponderance of evidence that:
(i) The excess emissions:
(A) Were caused by a sudden,
infrequent, and unavoidable failure of
air pollution control and monitoring
equipment, process equipment, or a
process to operate in a normal or usual
manner; and
(B) Could not have been prevented
through careful planning, proper design
or better operation and maintenance
practices; and
(C) Did not stem from any activity or
event that could have been foreseen and
avoided, or planned for; and
(D) Were not part of a recurring
pattern indicative of inadequate design,
operation, or maintenance; and
(ii) 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 to make these repairs; and
(iii) The frequency, amount and
duration of the excess emissions
(including any bypass) were minimized
to the maximum extent practicable
during periods of such emissions; and
(iv) 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; and
(v) All possible steps were taken to
minimize the impact of the excess
emissions on ambient air quality, the
environment, and human health; and
(vi) All emissions monitoring and
control systems were kept in operation
if at all possible, consistent with safety
and good air pollution control practices;
and
(vii) All of the actions in response to
the excess emissions were documented
by properly signed, contemporaneous
operating logs; and
(viii) At all times, the affected source
was operated in a manner consistent
with good practices for minimizing
emissions; and
(ix) A written root cause analysis has
been prepared to determine, correct, and
eliminate the primary causes of the
malfunction and the excess emissions
resulting from the malfunction event at
issue. The analysis shall also specify,
using best monitoring methods and
engineering judgment, the amount of
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excess emissions that were the result of
the malfunction.
(2) Notification. The owner or
operator of the affected source
experiencing exceedance of its emission
limit(s) during a malfunction shall
notify the Administrator by telephone or
facsimile transmission as soon as
possible, but no later than two business
days after the initial occurrence of the
malfunction, if it wishes to avail itself
of an affirmative defense to civil
penalties for that malfunction. The
owner or operator seeking to assert an
affirmative defense shall also submit a
written report to the Administrator
within 45 days of the initial occurrence
of the exceedance of the standard in this
subpart to demonstrate, with all
necessary supporting documentation,
that it has met the requirements set forth
in paragraph (d)(1) of this section. The
owner or operator may seek an
extension of this deadline for up to 30
additional days by submitting a written
request to the Administrator before the
expiration of the 45 day period. Until a
request for an extension has been
approved by the Administrator, the
owner or operator is subject to the
requirement to submit such report
within 45 days of the initial occurrence
of the exceedance.
13. Section 63.764 is amended by:
a. Revising paragraph (c)(2)
introductory text;
b. Revising paragraph (e)(1)
introductory text;
c. Revising paragraph (i); and
d. Adding paragraph (j) to read as
follows:
§ 63.764
General standards.
*
*
*
*
*
(c) * * *
(2) For each storage vessel subject to
this subpart, the owner or operator shall
comply with the requirements specified
in paragraphs (c)(2)(i) through (iii) of
this section.
*
*
*
*
*
(e) Exemptions. (1) The owner or
operator of an area source is exempt
from the requirements of paragraph (d)
of this section if the criteria listed in
paragraph (e)(1)(i) or (ii) of this section
are met, except that the records of the
determination of these criteria must be
maintained as required in § 63.774(d)(1).
*
*
*
*
*
(i) In all cases where the provisions of
this subpart require an owner or
operator to repair leaks by a specified
time after the leak is detected, it is a
violation of this standard to fail to take
action to repair the leak(s) within the
specified time. If action is taken to
repair the leak(s) within the specified
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emcdonald on DSK2BSOYB1PROD with PROPOSALS2
Where:
ELBTEX = Unit-specific BTEX emission limit,
megagrams per year;
1.10 × 10¥4 = BTEX emission limit, grams
BTEX/standard cubic meter = ppmv;
Throughput = Annual average daily natural
gas throughput, standard cubic meters
per day;
Ci,BTEX = BTEX concentration of the natural
gas at the inlet to the glycol dehydration
unit, ppmv.
(A) Connect the process vent to a
control device or combination of control
devices through a closed-vent system.
The closed vent system shall be
designed and operated in accordance
with the requirements of § 63.771(c).
The control device(s) shall be designed
and operated in accordance with the
requirements of § 63.771(f).
(B) Meet the emissions limit through
process modifications in accordance
with the requirements specified in
§ 63.771(e).
(C) Meet the emissions limit for each
small glycol dehydration unit using a
combination of process modifications
and one or more control devices through
the requirements specified in
paragraphs (b)(1)(iii)(A) and (B) of this
section.
(D) Demonstrate that the emissions
limit is met through actual uncontrolled
operation of the small glycol
dehydration unit. Document operational
parameters in accordance with the
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c. Revising paragraph (c)(2); and
d. Revising paragraph (c)(3) to read as
follows:
§ 63.765 Glycol dehydration unit process
vent standards.
(a) This section applies to each glycol
dehydration unit subject to this subpart
that must be controlled for air emissions
as specified in either paragraph (c)(1)(i)
or paragraph (d)(1)(i) of § 63.764.
(b) * * *
(1) For each glycol dehydration unit
process vent, the owner or operator
shall control air emissions by either
paragraph (b)(1)(i), (ii), or (iii) of this
section.
(i) The owner or operator of a large
glycol dehydration unit, as defined in
§ 63.761, shall connect the process vent
to a control device or a combination of
control devices through a closed-vent
system. The closed-vent system shall be
designed and operated in accordance
with the requirements of § 63.771(c).
The control device(s) shall be designed
and operated in accordance with the
requirements of § 63.771(d).
requirements specified in § 63.771(e)
and emissions in accordance with the
requirements specified in § 63.772(b)(2).
*
*
*
*
*
(c) * * *
(2) The owner or operator shall
demonstrate, to the Administrator’s
satisfaction, that the total HAP
emissions to the atmosphere from the
large glycol dehydration unit process
vent are reduced by 95.0 percent
through process modifications, or a
combination of process modifications
and one or more control devices, in
accordance with the requirements
specified in § 63.771(e).
(3) Control of HAP emissions from a
GCG separator (flash tank) vent is not
required if the owner or operator
demonstrates, to the Administrator’s
satisfaction, that total emissions to the
atmosphere from the glycol dehydration
unit process vent are reduced by one of
the levels specified in paragraph
(c)(3)(i), (ii), or (iii) of this section,
through the installation and operation of
controls as specified in paragraph (b)(1)
of this section.
(i) For any large glycol dehydration
unit, HAP emissions are reduced by
95.0 percent or more.
(ii) For area source dehydration units,
benzene emissions are reduced to a
level less than 0.90 megagrams per year.
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(ii) The owner or operator of a glycol
dehydration unit located at an area
source, that must be controlled as
specified in § 63.764(d)(1)(i), shall
connect the process vent to a control
device or combination of control
devices through a closed-vent system
and the outlet benzene emissions from
the control device(s) shall be reduced to
a level less than 0.90 megagrams per
year. The closed-vent system shall be
designed and operated in accordance
with the requirements of § 63.771(c).
The control device(s) shall be designed
and operated in accordance with the
requirements of § 63.771(d), except that
the performance levels specified in
§ 63.771(d)(1)(i) and (ii) do not apply.
(iii) You must limit BTEX emissions
from each small glycol dehydration unit
process vent, as defined in § 63.761, to
the limit determined in Equation 1 of
this section. The limit must be met in
accordance with one of the alternatives
specified in paragraphs (b)(1)(iii)(A)
through (D) of this section.
(iii) For each small glycol dehydration
unit, BTEX emissions are reduced to a
level less than the limit calculated by
paragraph (b)(1)(iii) of this section.
15. Section 63.766 is amended by:
a. Revising paragraph (a);
b. Revising paragraph (b) introductory
text;
c. Revising paragraph (b)(1); and
d. Revising paragraph (d) to read as
follows:
§ 63.766
Storage vessel standards.
(a) This section applies to each
storage vessel (as defined in § 63.761)
subject to this subpart.
(b) The owner or operator of a storage
vessel (as defined in § 63.761) shall
comply with one of the control
requirements specified in paragraphs
(b)(1) and (2) of this section.
(1) The owner or operator shall equip
the affected storage vessel with a cover
that is connected, through a closed-vent
system that meets the conditions
specified in § 63.771(c), to a control
device or a combination of control
devices that meets any of the conditions
specified in § 63.771(d). The cover shall
be designed and operated in accordance
with the requirements of § 63.771(b).
*
*
*
*
*
(d) This section does not apply to
storage vessels for which the owner or
operator is subject to and controlled
under the requirements specified in 40
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time, failure of that action to
successfully repair the leak(s) is not a
violation of this standard. However, if
the repairs are unsuccessful, and a leak
is detected, the owner or operator shall
take further action as required by the
applicable provisions of this subpart.
(j) At all times the owner or operator
must operate and maintain any affected
source, including associated air
pollution control equipment and
monitoring equipment, in a manner
consistent with safety and good air
pollution control practices for
minimizing emissions. Determination of
whether such operation and
maintenance procedures are being used
will be based on information available
to the Administrator which may
include, but is not limited to,
monitoring results, review of operation
and maintenance procedures, review of
operation and maintenance records, and
inspection of the source.
14. Section 63.765 is amended by:
a. Revising paragraph (a);
b. Revising paragraph (b)(1);
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CFR part 60, subpart Kb; or the
requirements specified under 40 CFR
part 63 subparts G or CC.
16. Section 63.769 is amended by:
a. Revising paragraph (b);
b. Revising paragraph (c) introductory
text; and
b. Revising paragraph (c)(8) to read as
follows:
§ 63.769
Equipment leak standards.
*
*
*
*
*
(b) This section does not apply to
ancillary equipment and compressors
for which the owner or operator is
subject to and controlled under the
requirements specified in subpart H of
this part; or the requirements specified
in 40 CFR part 60, subpart KKK.
(c) For each piece of ancillary
equipment and each compressor subject
to this section located at an existing or
new source, the owner or operator shall
meet the requirements specified in 40
CFR part 61, subpart V, §§ 61.241
through 61.247, except as specified in
paragraphs (c)(1) through (8) of this
section, except for valves subject to
§ 61.247–2(b) a leak is detected if an
instrument reading of 500 ppm or
greater is measured.
*
*
*
*
*
(8) Flares, as defined in § 63.761, used
to comply with this subpart shall
comply with the requirements of
§ 63.11(b).
17. Section 63.771 is amended by:
a. Revising paragraph (c)(1)
introductory text;
b. Revising the heading of paragraph
(d);
c. Adding paragraph (d) introductory
text;
d. Revising paragraph (d)(1)(i)
introductory text;
e. Revising paragraph (d)(1)(i)(C);
f. Revising paragraph (d)(1)(ii);
g. Revising paragraph (d)(1)(iii);
h. Revising paragraph (d)(4)(i);
i. Revising paragraph (d)(5)(i);
j. Revising paragraph (e)(2);
k. Revising paragraph (e)(3)
introductory text;
l. Revising paragraph (e)(3)(ii); and
m. Adding paragraph (f) to read as
follows:
§ 63.771
Control equipment requirements.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
*
*
*
*
*
(c) Closed-vent system requirements.
(1) The closed-vent system shall route
all gases, vapors, and fumes emitted
from the material in an emissions unit
to a control device that meets the
requirements specified in paragraph (d)
of this section.
*
*
*
*
*
(d) Control device requirements for
sources except small glycol dehydration
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units. Owners and operators of small
glycol dehydration units, shall comply
with the control device requirements in
paragraph (f) of this section.
(1) * * *
(i) An enclosed combustion device
(e.g., thermal vapor incinerator, catalytic
vapor incinerator, boiler, or process
heater) that is designed and operated in
accordance with one of the following
performance requirements:
*
*
*
*
*
(C) For a control device that can
demonstrate a uniform combustion zone
temperature during the performance test
conducted under § 63.772(e), operates at
a minimum temperature of 760 degrees
C.
*
*
*
*
*
(ii) A vapor recovery device (e.g.,
carbon adsorption system or condenser)
or other non-destructive control device
that is designed and operated to reduce
the mass content of either TOC or total
HAP in the gases vented to the device
by 95.0 percent by weight or greater as
determined in accordance with the
requirements of § 63.772(e).
(iii) A flare, as defined in § 63.761,
that is designed and operated in
accordance with the requirements of
§ 63.11(b).
*
*
*
*
*
(4) * * *
(i) Each control device used to comply
with this subpart shall be operating at
all times when gases, vapors, and fumes
are vented from the HAP emissions unit
or units through the closed-vent system
to the control device, as required under
§ 63.765, § 63.766, and § 63.769. An
owner or operator may vent more than
one unit to a control device used to
comply with this subpart.
*
*
*
*
*
(5) * * *
(i) Following the initial startup of the
control device, all carbon in the control
device shall be replaced with fresh
carbon on a regular, predetermined time
interval that is no longer than the
carbon service life established for the
carbon adsorption system. Records
identifying the schedule for replacement
and records of each carbon replacement
shall be maintained as required in
§ 63.774(b)(7)(ix). The schedule for
replacement shall be submitted with the
Notification of Compliance Status
Report as specified in § 63.775(d)(5)(iv).
Each carbon replacement must be
reported in the Periodic Reports as
specified in § 63.772(e)(2)(xii).
*
*
*
*
*
(e) * * *
(2) The owner or operator shall
document, to the Administrator’s
satisfaction, the conditions for which
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glycol dehydration unit baseline
operations shall be modified to achieve
the 95.0 percent overall HAP emission
reduction, or BTEX limit determined in
§ 63.765(b)(1)(iii), as applicable, either
through process modifications or
through a combination of process
modifications and one or more control
devices. If a combination of process
modifications and one or more control
devices are used, the owner or operator
shall also establish the emission
reduction to be achieved by the control
device to achieve an overall HAP
emission reduction of 95.0 percent for
the glycol dehydration unit process vent
or, if applicable, the BTEX limit
determined in § 63.765(b)(1)(iii) for the
small glycol dehydration unit process
vent. Only modifications in glycol
dehydration unit operations directly
related to process changes, including
but not limited to changes in glycol
circulation rate or glycol-HAP
absorbency, shall be allowed. Changes
in the inlet gas characteristics or natural
gas throughput rate shall not be
considered in determining the overall
emission reduction due to process
modifications.
(3) The owner or operator that
achieves a 95.0 percent HAP emission
reduction or meets the BTEX limit
determined in § 63.765(b)(1)(iii), as
applicable, using process modifications
alone shall comply with paragraph
(e)(3)(i) of this section. The owner or
operator that achieves a 95.0 percent
HAP emission reduction or meets the
BTEX limit determined in
§ 63.765(b)(1)(iii), as applicable, using a
combination of process modifications
and one or more control devices shall
comply with paragraphs (e)(3)(i) and
(e)(3)(ii) of this section.
*
*
*
*
*
(ii) The owner or operator shall
comply with the control device
requirements specified in paragraph (d)
or (f) of this section, as applicable,
except that the emission reduction or
limit achieved shall be the emission
reduction or limit specified for the
control device(s) in paragraph (e)(2) of
this section.
(f) Control device requirements for
small glycol dehydration units. (1) The
control device used to meet BTEX the
emission limit calculated in
§ 63.765(b)(1)(iii) shall be one of the
control devices specified in paragraphs
(f)(1)(i) through (iii) of this section.
(i) An enclosed combustion device
(e.g., thermal vapor incinerator, catalytic
vapor incinerator, boiler, or process
heater) that is designed and operated to
reduce the mass content of BTEX in the
gases vented to the device as
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determined in accordance with the
requirements of § 63.772(e). If a boiler or
process heater is used as the control
device, then the vent stream shall be
introduced into the flame zone of the
boiler or process heater; or
(ii) A vapor recovery device (e.g.,
carbon adsorption system or condenser)
or other non-destructive control device
that is designed and operated to reduce
the mass content of BTEX in the gases
vented to the device as determined in
accordance with the requirements of
§ 63.772(e); or
(iii) A flare, as defined in § 63.761,
that is designed and operated in
accordance with the requirements of
§ 63.11(b).
(2) The owner or operator shall
operate each control device in
accordance with the requirements
specified in paragraphs (f)(2)(i) and (ii)
of this section.
(i) Each control device used to comply
with this subpart shall be operating at
all times. An owner or operator may
vent more than one unit to a control
device used to comply with this
subpart.
(ii) For each control device monitored
in accordance with the requirements of
§ 63.773(d), the owner or operator shall
demonstrate compliance according to
the requirements of either § 63.772(f) or
(h).
(3) For each carbon adsorption system
used as a control device to meet the
requirements of paragraph (f)(1)(ii) of
this section, the owner or operator shall
manage the carbon as required under
(d)(5)(i) and (ii) of this section.
18. Section 63.772 is amended by:
a. Revising paragraph (b) introductory
text;
b. Revising paragraph (b)(1)(ii);
c. Revising paragraph (b)(2);
d. Adding paragraph (d);
e. Revising paragraph (e) introductory
text;
f. Revising paragraphs (e)(1)(i)
through (v);
g. Revising paragraph (e)(2);
h. Revising paragraph (e)(3)
introductory text;
i. Revising paragraph (e)(3)(i)(B);
j. Revising paragraph (e)(3)(iv)(C)(1);
k. Adding paragraphs (e)(3)(v) and
(vi);
l. Revising paragraph (e)(4)
introductory text;
m. Revising paragraph (e)(4)(i);
n. Revising paragraph (e)(5);
o. Revising paragraph (f) introductory
text;
p. Adding paragraphs (f)(2) through
(f)(6);
q. Revising paragraph (g) introductory
text;
r. Revising paragraph (g)(1) and
paragraph (g)(2) introductory text;
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s. Revising paragraph (g)(2)(iii);
t. Revising paragraph (g)(3);
u. Adding paragraph (h); and
v. Adding paragraph (i) to read as
follows:
§ 63.772 Test methods, compliance
procedures, and compliance
demonstrations.
*
*
*
*
*
(b) Determination of glycol
dehydration unit flowrate, benzene
emissions, or BTEX emissions. The
procedures of this paragraph shall be
used by an owner or operator to
determine glycol dehydration unit
natural gas flowrate, benzene emissions,
or BTEX emissions.
(1) * * *
(ii) The owner or operator shall
document, to the Administrator’s
satisfaction, the actual annual average
natural gas flowrate to the glycol
dehydration unit.
(2) The determination of actual
average benzene or BTEX emissions
from a glycol dehydration unit shall be
made using the procedures of either
paragraph (b)(2)(i) or (b)(2)(ii) of this
section. Emissions shall be determined
either uncontrolled, or with federally
enforceable controls in place.
(i) The owner or operator shall
determine actual average benzene or
BTEX emissions using the model GRI–
GLYCalcTM, Version 3.0 or higher, and
the procedures presented in the
associated GRI–GLYCalcTM Technical
Reference Manual. Inputs to the model
shall be representative of actual
operating conditions of the glycol
dehydration unit and may be
determined using the procedures
documented in the Gas Research
Institute (GRI) report entitled
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1); or
(ii) The owner or operator shall
determine an average mass rate of
benzene or BTEX emissions in
kilograms per hour through direct
measurement using the methods in
§ 63.772(a)(1)(i) or (ii), or an alternative
method according to § 63.7(f). Annual
emissions in kilograms per year shall be
determined by multiplying the mass rate
by the number of hours the unit is
operated per year. This result shall be
converted to megagrams per year.
*
*
*
*
*
(d) Test procedures and compliance
demonstrations for small glycol
dehydration units. This paragraph
applies to the test procedures for small
dehydration units.
(1) If the owner or operator is using
a control device to comply with the
emission limit in § 63.765(b)(1)(iii), the
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requirements of paragraph (e) of this
section apply. Compliance is
demonstrated using the methods
specified in paragraph (f) of this section.
(2) If no control device is used to
comply with the emission limit in
§ 63.765(b)(1)(iii), the owner or operator
must determine the glycol dehydration
unit BTEX emissions as specified in
paragraphs (d)(2)(i) through (iii) of this
section. Compliance is demonstrated if
the BTEX emissions determined as
specified in paragraphs (d)(2)(i) through
(iii) are less than the emission limit
calculated using the equation in
§ 63.765(b)(1)(iii).
(i) Method 1 or 1A, 40 CFR part 60,
appendix A, as appropriate, shall be
used for selection of the sampling sites
at the outlet of the glycol dehydration
unit process vent. Any references to
particulate mentioned in Methods 1 and
1A do not apply to this section.
(ii) The gas volumetric flowrate shall
be determined using Method 2, 2A, 2C,
or 2D, 40 CFR part 60, appendix A, as
appropriate.
(iii) The BTEX emissions from the
outlet of the glycol dehydration unit
process vent shall be determined using
the procedures specified in paragraph
(e)(3)(v) of this section. As an
alternative, the mass rate of BTEX at the
outlet of the glycol dehydration unit
process vent may be calculated using
the model GRI–GLYCalcTM, Version 3.0
or higher, and the procedures presented
in the associated GRI–GLYCalcTM
Technical Reference Manual. Inputs to
the model shall be representative of
actual operating conditions of the glycol
dehydration unit and shall be
determined using the procedures
documented in the Gas Research
Institute (GRI) report entitled
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1). When the
BTEX mass rate is calculated for glycol
dehydration units using the model GRI–
GLYCalcTM, all BTEX measured by
Method 18, 40 CFR part 60, appendix A,
shall be summed.
(e) Control device performance test
procedures. This paragraph applies to
the performance testing of control
devices. The owners or operators shall
demonstrate that a control device
achieves the performance requirements
of § 63.771(d)(1), (e)(3)(ii) or (f)(1) using
a performance test as specified in
paragraph (e)(3) of this section. Owners
or operators using a condenser have the
option to use a design analysis as
specified in paragraph (e)(4) of this
section. The owner or operator may
elect to use the alternative procedures in
paragraph (e)(5) of this section for
performance testing of a condenser used
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to control emissions from a glycol
dehydration unit process vent. As an
alternative to conducting a performance
test under this section for combustion
control devices, a control device that
can be demonstrated to meet the
performance requirements of
§ 63.771(d)(1), (e)(3)(ii) or (f)(1) through
a performance test conducted by the
manufacturer, as specified in paragraph
(h) of this section can be used.
(1) * * *
(i) Except as specified in paragraph
(e)(2) of this section, a flare, as defined
in § 63.761, that is designed and
operated in accordance with § 63.11(b);
(ii) Except for control devices used for
small glycol dehydration units, a boiler
or process heater with a design heat
input capacity of 44 megawatts or
greater;
(iii) Except for control devices used
for small glycol dehydration units, a
boiler or process heater into which the
vent stream is introduced with the
primary fuel or is used as the primary
fuel;
(iv) Except for control devices used
for small glycol dehydration units, a
boiler or process heater burning
hazardous waste for which the owner or
operator has either been issued a final
permit under 40 CFR part 270 and
complies with the requirements of 40
CFR part 266, subpart H; or has certified
compliance with the interim status
requirements of 40 CFR part 266,
subpart H;
(v) Except for control devices used for
small glycol dehydration units, a
hazardous waste incinerator for which
the owner or operator has been issued
a final permit under 40 CFR part 270
and complies with the requirements of
40 CFR part 264, subpart O; or has
certified compliance with the interim
status requirements of 40 CFR part 265,
subpart O.
*
*
*
*
*
(2) An owner or operator shall design
and operate each flare, as defined in
§ 63.761, in accordance with the
requirements specified in § 63.11(b) and
the compliance determination shall be
conducted using Method 22 of 40 CFR
part 60, appendix A, to determine
visible emissions.
(3) For a performance test conducted
to demonstrate that a control device
meets the requirements of
§ 63.771(d)(1), (e)(3)(ii) or (f)(1), the
owner or operator shall use the test
methods and procedures specified in
paragraphs (e)(3)(i) through (v) of this
section. The initial and periodic
performance tests shall be conducted
according to the schedule specified in
paragraph (e)(3)(vi) of this section.
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(i) * * *
(B) To determine compliance with the
enclosed combustion device total HAP
concentration limit specified in
§ 63.765(b)(1)(iii), or the BTEX emission
limit specified in § 63.771(f)(1) the
sampling site shall be located at the
outlet of the combustion device.
*
*
*
*
*
(iv) * * *
(C) * * *
(1) The emission rate correction factor
for excess air, integrated sampling and
analysis procedures of Method 3A or
3B, 40 CFR part 60, appendix A, shall
be used to determine the oxygen
concentration. The samples shall be
taken during the same time that the
samples are taken for determining TOC
concentration or total HAP
concentration.
*
*
*
*
*
(v) To determine compliance with the
BTEX emission limit specified in
§ 63.771(f)(1) the owner or operator
shall use one of the following methods:
Method 18, 40 CFR part 60, appendix A;
ASTM D6420–99 (2004), as specified in
§ 63.772(a)(1)(ii); or any other method or
data that have been validated according
to the applicable procedures in Method
301, 40 CFR part 63, appendix A. The
following procedures shall be used to
calculate BTEX emissions:
(A) The minimum sampling time for
each run shall be 1 hour in which either
an integrated sample or a minimum of
four grab samples shall be taken. If grab
sampling is used, then the samples shall
be taken at approximately equal
intervals in time, such as 15-minute
intervals during the run.
(B) The mass rate of BTEX (Eo) shall
be computed using the equations and
procedures specified in paragraphs
(e)(3)(v)(B)(1) and (2) of this section.
(1) The following equation shall be
used:
Where:
Eo= Mass rate of BTEX at the outlet of the
control device, dry basis, kilogram per
hour.
Coj= Concentration of sample component j of
the gas stream at the outlet of the control
device, dry basis, parts per million by
volume.
Moj= Molecular weight of sample component
j of the gas stream at the outlet of the
control device, gram/gram-mole.
Qo= Flowrate of gas stream at the outlet of
the control device, dry standard cubic
meter per minute.
K2= Constant, 2.494 × 10¥6 (parts per
million) (gram-mole per standard cubic
meter) (kilogram/gram) (minute/hour),
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where standard temperature (gram-mole
per standard cubic meter) is 20 degrees
C.
n = Number of components in sample.
(2) When the BTEX mass rate is
calculated, only BTEX compounds
measured by Method 18, 40 CFR part
60, appendix A, or ASTM D6420–99
(2004) as specified in § 63.772(a)(1)(ii),
shall be summed using the equations in
paragraph (e)(3)(v)(B)(1) of this section.
(vi) The owner or operator shall
conduct performance tests according to
the schedule specified in paragraphs
(e)(3)(vi)(A) and (B) of this section.
(A) An initial performance test shall
be conducted within 180 days after the
compliance date that is specified for
each affected source in § 63.760(f)(7)
through (8), except that the initial
performance test for existing
combustion control devices at existing
major sources shall be conducted no
later than 3 years after the date of
publication of the final rule in the
Federal Register. If the owner or
operator of an existing combustion
control device at an existing major
source chooses to replace such device
with a control device whose model is
tested under § 63.772(h), then the newly
installed device shall comply with all
provisions of this subpart no later than
3 years after the date of publication of
the final rule in the Federal Register.
The performance test results shall be
submitted in the Notification of
Compliance Status Report as required in
§ 63.775(d)(1)(ii).
(B) Periodic performance tests shall be
conducted for all control devices
required to conduct initial performance
tests except as specified in paragraphs
(e)(3)(vi)(B)(1) and (2) of this section.
The first periodic performance test shall
be conducted no later than 60 months
after the initial performance test
required in paragraph (e)(3)(vi)(A) of
this section. Subsequent periodic
performance tests shall be conducted at
intervals no longer than 60 months
following the previous periodic
performance test or whenever a source
desires to establish a new operating
limit. The periodic performance test
results must be submitted in the next
Periodic Report as specified in
§ 63.775(e)(2)(xi). Combustion control
devices meeting the criteria in either
paragraph (e)(3)(vi)(B)(1) or (2) of this
section are not required to conduct
periodic performance tests.
(1) A control device whose model is
tested under, and meets the criteria of,
§ 63.772(h), or
(2) A combustion control device
tested under § 63.772(e) that meets the
outlet TOC or HAP performance level
specified in § 63.771(d)(1)(i)(B) and that
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establishes a correlation between firebox
or combustion chamber temperature and
the TOC or HAP performance level.
(4) For a condenser design analysis
conducted to meet the requirements of
§ 63.771(d)(1), (e)(3)(ii), or (f)(1), the
owner or operator shall meet the
requirements specified in paragraphs
(e)(4)(i) and (e)(4)(ii) of this section.
Documentation of the design analysis
shall be submitted as a part of the
Notification of Compliance Status
Report as required in § 63.775(d)(1)(i).
(i) The condenser design analysis
shall include an analysis of the vent
stream composition, constituent
concentrations, flowrate, relative
humidity, and temperature, and shall
establish the design outlet organic
compound concentration level, design
average temperature of the condenser
exhaust vent stream, and the design
average temperatures of the coolant
fluid at the condenser inlet and outlet.
As an alternative to the condenser
design analysis, an owner or operator
may elect to use the procedures
specified in paragraph (e)(5) of this
section.
*
*
*
*
*
(5) As an alternative to the procedures
in paragraph (e)(4)(i) of this section, an
owner or operator may elect to use the
procedures documented in the GRI
report entitled, ‘‘Atmospheric Rich/Lean
Method for Determining Glycol
Dehydrator Emissions’’ (GRI–95/0368.1)
as inputs for the model GRI–
GLYCalcTM, Version 3.0 or higher, to
generate a condenser performance
curve.
(f) Compliance demonstration for
control device performance
requirements. This paragraph applies to
the demonstration of compliance with
the control device performance
requirements specified in
§ 63.771(d)(1)(i), (e)(3) and (f)(1).
Compliance shall be demonstrated using
the requirements in paragraphs (f)(1)
through (3) of this section. As an
alternative, an owner or operator that
installs a condenser as the control
device to achieve the requirements
specified in § 63.771(d)(1)(ii), (e)(3) or
(f)(1) may demonstrate compliance
according to paragraph (g) of this
section. An owner or operator may
switch between compliance with
paragraph (f) of this section and
compliance with paragraph (g) of this
section only after at least 1 year of
operation in compliance with the
selected approach. Notification of such
a change in the compliance method
shall be reported in the next Periodic
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Report, as required in § 63.775(e),
following the change.
*
*
*
*
*
(2) The owner or operator shall
calculate the daily average of the
applicable monitored parameter in
accordance with § 63.773(d)(4) except
that the inlet gas flow rate to the control
device shall not be averaged.
(3) Compliance with the operating
parameter limit is achieved when the
daily average of the monitoring
parameter value calculated under
paragraph (f)(2) of this section is either
equal to or greater than the minimum or
equal to or less than the maximum
monitoring value established under
paragraph (f)(1) of this section. For inlet
gas flow rate, compliance with the
operating parameter limit is achieved
when the value is equal to or less than
the value established under § 63.772(h).
(4) Except for periods of monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
and required monitoring system quality
assurance or quality control activities
(including, as applicable, system
accuracy audits and required zero and
span adjustments), the CMS required in
§ 63.773(d) must be operated at all times
the affected source is operating. A
monitoring system malfunction is any
sudden, infrequent, not reasonably
preventable failure of the monitoring
system to provide valid data.
Monitoring system failures that are
caused in part by poor maintenance or
careless operation are not malfunctions.
Monitoring system repairs are required
to be completed in response to
monitoring system malfunctions and to
return the monitoring system to
operation as expeditiously as
practicable.
(5) Data recorded during monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
or required monitoring system quality
assurance or control activities may not
be used in calculations used to report
emissions or operating levels. All the
data collected during all other required
data collection periods must be used in
assessing the operation of the control
device and associated control system.
(6) Except for periods of monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
and required quality monitoring system
quality assurance or quality control
activities (including, as applicable,
system accuracy audits and required
zero and span adjustments), failure to
collect required data is a deviation of
the monitoring requirements.
(g) Compliance demonstration with
percent reduction or emission limit
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performance requirements—condensers.
This paragraph applies to the
demonstration of compliance with the
performance requirements specified in
§ 63.771(d)(1)(ii),(e)(3) or (f)(1) for
condensers. Compliance shall be
demonstrated using the procedures in
paragraphs (g)(1) through (3) of this
section.
(1) The owner or operator shall
establish a site-specific condenser
performance curve according to
§ 63.773(d)(5)(ii). For sources required
to meet the BTEX limit in accordance
with § 63.771(e) or (f)(1) the owner or
operator shall identify the minimum
percent reduction necessary to meet the
BTEX limit.
(2) Compliance with the requirements
in § 63.771(d)(1)(ii),(e)(3) or (f)(1) shall
be demonstrated by the procedures in
paragraphs (g)(2)(i) through (iii) of this
section.
*
*
*
*
*
(iii) Except as provided in paragraphs
(g)(2)(iii)(A) and (B) of this section, at
the end of each operating day, the
owner or operator shall calculate the
365-day average HAP, or BTEX,
emission reduction, as appropriate, from
the condenser efficiencies as
determined in paragraph (g)(2)(ii) of this
section for the preceding 365 operating
days. If the owner or operator uses a
combination of process modifications
and a condenser in accordance with the
requirements of § 63.771(e), the 365-day
average HAP, or BTEX, emission
reduction shall be calculated using the
emission reduction achieved through
process modifications and the
condenser efficiency as determined in
paragraph (g)(2)(ii) of this section, both
for the previous 365 operating days.
(A) After the compliance dates
specified in § 63.760(f), an owner or
operator with less than 120 days of data
for determining average HAP, or BTEX,
emission reduction, as appropriate,
shall calculate the average HAP, or
BTEX emission reduction, as
appropriate, for the first 120 days of
operation after the compliance dates.
For sources required to meet the overall
95.0 percent reduction requirement,
compliance is achieved if the 120-day
average HAP emission reduction is
equal to or greater than 90.0 percent. For
sources required to meet the BTEX limit
under § 63.765(b)(1)(iii), compliance is
achieved if the average BTEX emission
reduction is at least 95.0 percent of the
required 365-day value identified under
paragraph (g)(1) of this section (i.e., at
least 76.0 percent if the 365-day design
value is 80.0 percent).
(B) After 120 days and no more than
364 days of operation after the
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compliance dates specified in
§ 63.760(f), the owner or operator shall
calculate the average HAP emission
reduction as the HAP emission
reduction averaged over the number of
days between the current day and the
applicable compliance date. For sources
required to meet the overall 95.0percent reduction requirement,
compliance with the performance
requirements is achieved if the average
HAP emission reduction is equal to or
greater than 90.0 percent. For sources
required to meet the BTEX limit under
§ 63.765(b)(1)(iii), compliance is
achieved if the average BTEX emission
reduction is at least 95.0 percent of the
required 365-day value identified under
paragraph (g)(1) of this section (i.e., at
least 76.0 percent if the 365-day design
value is 80.0 percent).
(3) If the owner or operator has data
for 365 days or more of operation,
compliance is achieved based on the
applicable criteria in paragraphs (g)(3)(i)
or (ii) of this section.
(i) For sources meeting the HAP
emission reduction specified in
§ 63.771(d)(1)(ii) or (e)(3) the average
HAP emission reduction calculated in
paragraph (g)(2)(iii) of this section is
equal to or greater than 95.0 percent.
(ii) For sources required to meet the
BTEX limit under § 63.771(e)(3) or (f)(1),
compliance is achieved if the average
BTEX emission reduction calculated in
paragraph (g)(2)(iii) of this section is
equal to or greater than the minimum
percent reduction identified in
paragraph (g)(1) of this section.
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(h) Performance testing for
combustion control devices—
manufacturers’ performance test. (1)
This paragraph applies to the
performance testing of a combustion
control device conducted by the device
manufacturer. The manufacturer shall
demonstrate that a specific model of
control device achieves the performance
requirements in (h)(7) of this section by
conducting a performance test as
specified in paragraphs (h)(2) through
(6) of this section.
(2) Performance testing shall consist
of three one-hour (or longer) test runs
for each of the four following firing rate
settings making a total of 12 test runs
per test. Propene (propylene) gas shall
be used for the testing fuel. All fuel
analyses shall be performed by an
independent third-party laboratory (not
affiliated with the control device
manufacturer or fuel supplier).
(i) 90–100 percent of maximum
design rate (fixed rate).
(ii) 70–100–70 percent (ramp up,
ramp down). Begin the test at 70 percent
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of the maximum design rate. Within the
first 5 minutes, ramp the firing rate to
100 percent of the maximum design
rate. Hold at 100 percent for 5 minutes.
In the 10–15 minute time range, ramp
back down to 70 percent of the
maximum design rate. Repeat three
more times for a total of 60 minutes of
sampling.
(iii) 30–70–30 percent (ramp up, ramp
down). Begin the test at 30 percent of
the maximum design rate. Within the
first 5 minutes, ramp the firing rate to
70 percent of the maximum design rate.
Hold at 70 percent for 5 minutes. In the
10–15 minute time range, ramp back
down to 30 percent of the maximum
design rate. Repeat three more times for
a total of 60 minutes of sampling.
(iv) 0–30–0 percent (ramp up, ramp
down). Begin the test at 0 percent of the
maximum design rate. Within the first 5
minutes, ramp the firing rate to 100
percent of the maximum design rate.
Hold at 30 percent for 5 minutes. In the
10–15 minute time range, ramp back
down to 0 percent of the maximum
design rate. Repeat three more times for
a total of 60 minutes of sampling.
(3) All models employing multiple
enclosures shall be tested
simultaneously and with all burners
operational. Results shall be reported for
the each enclosure individually and for
the average of the emissions from all
interconnected combustion enclosures/
chambers. Control device operating data
shall be collected continuously
throughout the performance test using
an electronic Data Acquisition System
and strip chart. Data shall be submitted
with the test report in accordance with
paragraph (8)(iii) of this section.
(4) Inlet testing shall be conducted as
specified in paragraphs (h)(4)(i) through
(iii) of this section.
(i) The fuel flow metering system
shall be located in accordance with
Method 2A, 40 CFR part 60, appendix
A–1, (or other approved procedure) to
measure fuel flow rate at the control
device inlet location. The fitting for
filling fuel sample containers shall be
located a minimum of 8 pipe diameters
upstream of any inlet fuel flow
monitoring meter.
(ii) Inlet flow rate shall be determined
using Method 2A, 40 CFR part 60,
appendix A–1. Record the start and stop
reading for each 60-minute THC test.
Record the gas pressure and temperature
at 5-minute intervals throughout each
60-minute THC test.
(iii) Inlet fuel sampling shall be
conducted in accordance with the
criteria in paragraphs (h)(4)(iii)(A) and
(B) of this section.
(A) At the inlet fuel sampling
location, securely connect a Silonite-
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coated stainless steel evacuated canister
fitted with a flow controller sufficient to
fill the canister over a 1 hour period.
Filling shall be conducted as specified
in the following:
(1) Open the canister sampling valve
at the beginning of the total
hydrocarbon (THC) test, and close the
canister at the end of the THC test.
(2) Fill one canister for each THC test
run.
(3) Label the canisters individually
and record on a chain of custody form.
(B) Each fuel sample shall be analyzed
using the following methods. The
results shall be included in the test
report.
(1) Hydrocarbon compounds
containing between one and five atoms
of carbon plus benzene using ASTM
D1945–03.
(2) Hydrogen (H2), carbon monoxide
(CO), carbon dioxide (CO2), nitrogen
(N2), oxygen (O2) using ASTM D1945–
03.
(3) Carbonyl sulfide, carbon disulfide
plus mercaptans using ASTM D5504.
(4) Higher heating value using ASTM
D3588–98 or ASTM D4891–89.
(5) Outlet testing shall be conducted
in accordance with the criteria in
paragraphs (h)(5)(i) through (v) of this
section.
(i) Sampling and flowrate measured in
accordance with the following:
(A) The outlet sampling location shall
be a minimum of 4 equivalent stack
diameters downstream from the highest
peak flame or any other flow
disturbance, and a minimum of one
equivalent stack diameter upstream of
the exit or any other flow disturbance.
A minimum of two sample ports shall
be used.
(B) Flow rate shall be measured using
Method 1, 40 CFR part 60, Appendix 1,
for determining flow measurement
traverse point location; and Method 2,
40 CFR part 60, Appendix 1, shall be
used to measure duct velocity. If low
flow conditions are encountered (i.e.,
velocity pressure differentials less than
0.05 inches of water) during the
performance test, a more sensitive
manometer shall be used to obtain an
accurate flow profile.
(ii) Molecular weight shall be
determined as specified in paragraphs
(h)(4)(iii)(B), (h)(5)(ii)(A), and
(h)(5)(ii)(B) of this section.
(A) An integrated bag sample shall be
collected during the Method 4, 40 CFR
part 60, Appendix A, moisture test.
Analyze the bag sample using a gas
chromatograph-thermal conductivity
detector (GC–TCD) analysis meeting the
following criteria:
(1) Collect the integrated sample
throughout the entire test, and collect
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representative volumes from each
traverse location.
(2) The sampling line shall be purged
with stack gas before opening the valve
and beginning to fill the bag.
(3) The bag contents shall be kneaded
or otherwise vigorously mixed prior to
the GC analysis.
(4) The GC–TCD calibration
procedure in Method 3C, 40 CFR part
60, Appendix A, shall be modified by
using EPAAlt–045 as follows: For the
initial calibration, triplicate injections of
any single concentration must agree
within 5 percent of their mean to be
valid. The calibration response factor for
a single concentration re-check must be
within 10 percent of the original
calibration response factor for that
concentration. If this criterion is not
met, the initial calibration using at least
three concentration levels shall be
repeated.
(B) Report the molecular weight of:
O2, CO2, methane (CH4), and N2 and
include in the test report submitted
under § 63.775(d)(iii). Moisture shall be
determined using Method 4, 40 CFR
part 60, Appendix A. Traverse both
ports with the Method 4, 40 CFR part
60, Appendix A, sampling train during
each test run. Ambient air shall not be
introduced into the Method 3C, 40 CFR
part 60, Appendix A, integrated bag
sample during the port change.
(iii) Carbon monoxide shall be
determined using Method 10, 40 CFR
part 60, Appendix A. The test shall be
run at the same time and with the
sample points used for the EPA Method
25A, 40 CFR part 60, Appendix A,
testing. An instrument range of 0–10 per
million by volume-dry (ppmvd) shall be
used.
(iv) Visible emissions shall be
determined using Method 22, 40 CFR
part 60, Appendix A. The test shall be
performed continuously during each
test run. A digital color photograph of
the exhaust point, taken from the
position of the observer and annotated
with date and time, will be taken once
per test run and the four photos
included in the test report.
(6) Total hydrocarbons (THC) shall be
determined as specified by the
following criteria:
(i) Conduct THC sampling using
Method 25A, 40 CFR part 60, Appendix
A, except the option for locating the
probe in the center 10 percent of the
stack shall not be allowed. The THC
probe must be traversed to 16.7 percent,
50 percent, and 83.3 percent of the stack
diameter during the testing.
(ii) A valid test shall consist of three
Method 25A, 40 CFR part 60, Appendix
A, tests, each no less than 60 minutes
in duration.
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(iii) A 0–10 parts per million by
volume-wet (ppmvw) (as propane)
measurement range is preferred; as an
alternative a 0–30 ppmvw (as carbon)
measurement range may be used.
(iv) Calibration gases will be propane
in air and be certified through EPA
Protocol 1—‘‘EPA Traceability Protocol
for Assay and Certification of Gaseous
Calibration Standards,’’ September
1997, as amended August 25, 1999,
EPA–600/R–97/121 (or more recent if
updated since 1999).
(v) THC measurements shall be
reported in terms of ppmvw as propane.
(vi) THC results shall be corrected to
3 percent CO2, as measured by Method
3C, 40 CFR part 60, Appendix A.
(vii) Subtraction of methane/ethane
from the THC data is not allowed in
determining results.
(7) Performance test criteria:
(i) The control device model tested
must meet the criteria in paragraphs
(h)(7)(i)(A) through (C) of this section:
(A) Method 22, 40 CFR part 60,
Appendix A, results under paragraph
(h)(5)(v) of this section with no
indication of visible emissions, and
(B) Average Method 25A, 40 CFR part
60, Appendix A, results under
paragraph (h)(6) of this section equal to
or less than 10.0 ppmvw THC as
propane corrected to 3.0 percent CO2,
and
(C) Average CO emissions determined
under paragraph (h)(5)(iv) of this section
equal to or less than 10 parts ppmvd,
corrected to 3.0 percent CO2.
(ii) The manufacturer shall determine
a maximum inlet gas flow rate which
shall not be exceeded for each control
device model to achieve the criteria in
paragraph (h)(7)(i) of this section.
(iii) A control device meeting the
criteria in paragraphs (h)(7)(i)(A)
through (C) of this section will have
demonstrated a destruction efficiency of
98.0 percent for HAP regulated under
this subpart.
(8) The owner or operator of a
combustion control device model tested
under this section shall submit the
information listed in paragraphs (h)(8)(i)
through (iii) of this section in the test
report required under § 63.775(d)(1)(iii).
(i) Full schematic of the control
device and dimensions of the device
components.
(ii) Design net heating value
(minimum and maximum) of the device.
(iii) Test fuel gas flow range (in both
mass and volume). Include the
minimum and maximum allowable inlet
gas flow rate.
(iv) Air/stream injection/assist ranges,
if used.
(v) The test parameter ranges listed in
paragraphs (h)(8)(v)(A) through (O) of
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this section, as applicable for the tested
model.
(A) Fuel gas delivery pressure and
temperature.
(B) Fuel gas moisture range.
(C) Purge gas usage range.
(D) Condensate (liquid fuel)
separation range.
(E) Combustion zone temperature
range. This is required for all devices
that measure this parameter.
(F) Excess combustion air range.
(G) Flame arrestor(s).
(H) Burner manifold pressure.
(I) Pilot flame sensor.
(J) Pilot flame design fuel and fuel
usage.
(K) Tip velocity range.
(L) Momentum flux ratio.
(M) Exit temperature range.
(N) Exit flow rate.
(O) Wind velocity and direction.
(vi) The test report shall include all
calibration quality assurance/quality
control data, calibration gas values, gas
cylinder certification, and strip charts
annotated with test times and
calibration values.
(i) Compliance demonstration for
combustion control devices—
manufacturers’ performance test. This
paragraph applies to the demonstration
of compliance for a combustion control
device tested under the provisions in
paragraph (h) of this section. Owners or
operators shall demonstrate that a
control device achieves the performance
requirements of § 63.771(d)(1), (e)(3)(ii)
or (f)(1), by installing a device tested
under paragraph (h) of this section and
complying with the following criteria:
(1) The inlet gas flow rate shall meet
the range specified by the manufacturer.
Flow rate shall be measured as specified
in § 63.773(d)(3)(i)(H)(1).
(2) A pilot flame shall be present at all
times of operation. The pilot flame shall
be monitored in accordance with
§ 63.773(d)(3)(i)(H)(2).
(3) Devices shall be operated with no
visible emissions, except for periods not
to exceed a total of 5 minutes during
any 2 consecutive hours. A visible
emissions test using Method 22, 40 CFR
part 60, Appendix A, shall be performed
monthly. The observation period shall
be 2 hours and shall be used according
to Method 22.
(4) Compliance with the operating
parameter limit is achieved when the
following criteria are met:
(i) The inlet gas flow rate monitored
under paragraph (i)(1) of this section is
equal to or below the maximum
established by the manufacturer; and
(ii) The pilot flame is present at all
times; and
(iii) During the visible emissions test
performed under paragraph (i)(3) of this
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section the duration of visible emissions
does not exceed a total of 5 minutes
during the observation period. Devices
failing the visible emissions test shall
follow the requirements in paragraphs
(i)(4)(iii)(A) and (B) of this section.
(A) Following the first failure, the fuel
nozzle(s) and burner tubes shall be
replaced.
(B) If, following replacement of the
fuel nozzle(s) and burner tubes as
specified in paragraph (i)(4)(iii)(A), the
visible emissions test is not passed in
the next scheduled test, either a
performance test shall be performed
under paragraph (e) of this section, or
the device shall be replaced with
another control device whose model
was tested, and meets, the requirements
in paragraph (h) of this section.
19. Section 63.773 is amended by:
a. Adding paragraph (b);
b. Revising paragraph (d)(1)
introductory text;
c. Revising paragraph (d)(1)(ii) and
adding paragraphs (d)(1)(iii) and (iv);
d. Revising paragraphs (d)(2)(i) and
(d)(2)(ii);
e. Revising paragraphs (d)(3)(i)(A) and
(B);
f. Revising paragraphs (d)(3)(i)(D) and
(E);
g. Revising paragraphs (d)(3)(i)(F)(1)
and (2);
h. Revising paragraph (d)(3)(i)(G);
i. Adding paragraph (d)(3)(i)(H);
j. Revising paragraph (d)(4);
k. Revising paragraph (d)(5)(i);
l. Revising paragraphs (d)(5)(ii)(A)
through (C);
m. Revising paragraphs (d)(6)(ii) and
(iii);
n. Adding paragraph (d)(6)(vi);
o. Revising paragraph (d)(8)(i)(A); and
p. Revising paragraph (d)(8)(ii) to read
as follows:
§ 63.773 Inspection and monitoring
requirements.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
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(b) The owner or operator of a control
device whose model was tested under
§ 63.772(h) shall develop an inspection
and maintenance plan for each control
device. At a minimum, the plan shall
contain the control device
manufacturer’s recommendations for
ensuring proper operation of the device.
Semi-annual inspections shall be
conducted for each control device with
maintenance and replacement of control
device components made in accordance
with the plan.
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(d) Control device monitoring
requirements. (1) For each control
device, except as provided for in
paragraph (d)(2) of this section, the
owner or operator shall install and
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operate a continuous parameter
monitoring system in accordance with
the requirements of paragraphs (d)(3)
through (9) of this section. Owners or
operators that install and operate a flare
in accordance with § 63.771(d)(1)(iii) or
(f)(1)(iii) are exempt from the
requirements of paragraphs (d)(4) and
(5) of this section. The continuous
monitoring system shall be designed
and operated so that a determination
can be made on whether the control
device is achieving the applicable
performance requirements of
§ 63.771(d), (e)(3) or (f)(1). Each
continuous parameter monitoring
system shall meet the following
specifications and requirements:
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(ii) A site-specific monitoring plan
must be prepared that addresses the
monitoring system design, data
collection, and the quality assurance
and quality control elements outlined in
paragraph (d) of this section and in
§ 63.8(d). Each CPMS must be installed,
calibrated, operated, and maintained in
accordance with the procedures in your
approved site-specific monitoring plan.
Using the process described in
§ 63.8(f)(4), you may request approval of
monitoring system quality assurance
and quality control procedures
alternative to those specified in
paragraphs (d)(1)(ii)(A) through (E) of
this section in your site-specific
monitoring plan.
(A) The performance criteria and
design specifications for the monitoring
system equipment, including the sample
interface, detector signal analyzer, and
data acquisition and calculations;
(B) Sampling interface (e.g.,
thermocouple) location such that the
monitoring system will provide
representative measurements;
(C) Equipment performance checks,
system accuracy audits, or other audit
procedures;
(D) Ongoing operation and
maintenance procedures in accordance
with provisions in § 63.8(c)(1) and
(c)(3); and
(E) Ongoing reporting and
recordkeeping procedures in accordance
with provisions in § 63.10(c), (e)(1), and
(e)(2)(i).
(iii) The owner or operator must
conduct the CPMS equipment
performance checks, system accuracy
audits, or other audit procedures
specified in the site-specific monitoring
plan at least once every 12 months.
(iv) The owner or operator must
conduct a performance evaluation of
each CPMS in accordance with the sitespecific monitoring plan.
(2) * * *
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(i) Except for control devices for small
glycol dehydration units, a boiler or
process heater in which all vent streams
are introduced with the primary fuel or
is used as the primary fuel; or
(ii) Except for control devices for
small glycol dehydration units, a boiler
or process heater with a design heat
input capacity equal to or greater than
44 megawatts.
(3) * * *
(i) * * *
(A) For a thermal vapor incinerator
that demonstrates during the
performance test conducted under
§ 63.772(e) that the combustion zone
temperature is an accurate indicator of
performance, a temperature monitoring
device equipped with a continuous
recorder. The monitoring device shall
have a minimum accuracy of ± 1 percent
of the temperature being monitored in
degrees C, or ± 2.5 degrees C, whichever
value is greater. The temperature sensor
shall be installed at a location
representative of the combustion zone
temperature.
(B) For a catalytic vapor incinerator,
a temperature monitoring device
equipped with a continuous recorder.
The device shall be capable of
monitoring temperature at two locations
and have a minimum accuracy of ± 1
percent of the temperature being
monitored in degrees C, or ± 2.5 degrees
C, whichever value is greater. One
temperature sensor shall be installed in
the vent stream at the nearest feasible
point to the catalyst bed inlet and a
second temperature sensor shall be
installed in the vent stream at the
nearest feasible point to the catalyst bed
outlet.
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(D) For a boiler or process heater a
temperature monitoring device
equipped with a continuous recorder.
The temperature monitoring device
shall have a minimum accuracy of ± 1
percent of the temperature being
monitored in degrees C, or ± 2.5 degrees
C, whichever value is greater. The
temperature sensor shall be installed at
a location representative of the
combustion zone temperature.
(E) For a condenser, a temperature
monitoring device equipped with a
continuous recorder. The temperature
monitoring device shall have a
minimum accuracy of ± 1 percent of the
temperature being monitored in degrees
C, or ± 2.8 degrees C, whichever value
is greater. The temperature sensor shall
be installed at a location in the exhaust
vent stream from the condenser.
(F) * * *
(1) A continuous parameter
monitoring system to measure and
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record the average total regeneration
stream mass flow or volumetric flow
during each carbon bed regeneration
cycle. The flow sensor must have a
measurement sensitivity of 5 percent of
the flow rate or 10 cubic feet per
minute, whichever is greater. The
mechanical connections for leakage
must be checked at least every month,
and a visual inspection must be
performed at least every 3 months of all
components of the flow CPMS for
physical and operational integrity and
all electrical connections for oxidation
and galvanic corrosion if your flow
CPMS is not equipped with a redundant
flow sensor; and
(2) A continuous parameter
monitoring system to measure and
record the average carbon bed
temperature for the duration of the
carbon bed steaming cycle and to
measure the actual carbon bed
temperature after regeneration and
within 15 minutes of completing the
cooling cycle. The temperature
monitoring device shall have a
minimum accuracy of ± 1 percent of the
temperature being monitored in degrees
C, or ± 2.5 degrees C, whichever value
is greater.
(G) For a nonregenerative-type carbon
adsorption system, the owner or
operator shall monitor the design carbon
replacement interval established using a
performance test performed in
accordance with § 63.772(e)(3) shall be
based on the total carbon working
capacity of the control device and
source operating schedule.
(H) For a control device model whose
model is tested under § 63.772(h):
(1) A continuous monitoring system
that measures gas flow rate at the inlet
to the control device. The monitoring
instrument shall have an accuracy of
plus or minus 2 percent or better.
(2) A heat sensing monitoring device
equipped with a continuous recorder
that indicates the continuous ignition of
the pilot flame.
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(4) Using the data recorded by the
monitoring system, except for inlet gas
flow rate, the owner or operator must
calculate the daily average value for
each monitored operating parameter for
each operating day. If the emissions unit
operation is continuous, the operating
day is a 24-hour period. If the emissions
unit operation is not continuous, the
operating day is the total number of
hours of control device operation per
24-hour period. Valid data points must
be available for 75 percent of the
operating hours in an operating day to
compute the daily average.
(5) * * *
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(i) The owner or operator shall
establish a minimum operating
parameter value or a maximum
operating parameter value, as
appropriate for the control device, to
define the conditions at which the
control device must be operated to
continuously achieve the applicable
performance requirements of
§ 63.771(d)(1), (e)(3)(ii) or (f)(1). Each
minimum or maximum operating
parameter value shall be established as
follows:
(A) If the owner or operator conducts
performance tests in accordance with
the requirements of § 63.772(e)(3) to
demonstrate that the control device
achieves the applicable performance
requirements specified in § 63.771(d)(1),
(e)(3)(ii) or (f)(1), then the minimum
operating parameter value or the
maximum operating parameter value
shall be established based on values
measured during the performance test
and supplemented, as necessary, by a
condenser design analysis or control
device manufacturer recommendations
or a combination of both.
(B) If the owner or operator uses a
condenser design analysis in accordance
with the requirements of § 63.772(e)(4)
to demonstrate that the control device
achieves the applicable performance
requirements specified in § 63.771(d)(1),
(e)(3)(ii) or (f)(1), then the minimum
operating parameter value or the
maximum operating parameter value
shall be established based on the
condenser design analysis and may be
supplemented by the condenser
manufacturer’s recommendations.
(C) If the owner or operator operates
a control device where the performance
test requirement was met under
§ 63.772(h) to demonstrate that the
control device achieves the applicable
performance requirements specified in
§ 63.771(d)(1), (e)(3)(ii) or (f)(1), then the
maximum inlet gas flow rate shall be
established based on the performance
test and supplemented, as necessary, by
the manufacturer recommendations.
(ii) * * *
(A) If the owner or operator conducts
a performance test in accordance with
the requirements of § 63.772(e)(3) to
demonstrate that the condenser achieves
the applicable performance
requirements in § 63.771(d)(1), (e)(3)(ii)
or (f)(1), then the condenser
performance curve shall be based on
values measured during the
performance test and supplemented as
necessary by control device design
analysis, or control device
manufacturer’s recommendations, or a
combination or both.
(B) If the owner or operator uses a
control device design analysis in
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52823
accordance with the requirements of
§ 63.772(e)(4)(i) to demonstrate that the
condenser achieves the applicable
performance requirements specified in
§ 63.771(d)(1), (e)(3)(ii) or (f)(1), then the
condenser performance curve shall be
based on the condenser design analysis
and may be supplemented by the
control device manufacturer’s
recommendations.
(C) As an alternative to paragraph
(d)(5)(ii)(B) of this section, the owner or
operator may elect to use the procedures
documented in the GRI report entitled,
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1) as inputs
for the model GRI–GLYCalcTM, Version
3.0 or higher, to generate a condenser
performance curve.
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(6) * * *
(ii) For sources meeting
§ 63.771(d)(1)(ii), an excursion occurs
when the 365-day average condenser
efficiency calculated according to the
requirements specified in
§ 63.772(g)(2)(iii) is less than 95.0
percent. For sources meeting
§ 63.771(f)(1), an excursion occurs when
the 365-day average condenser
efficiency calculated according to the
requirements specified in
§ 63.772(g)(2)(iii) is less than 95.0
percent of the identified 365-day
required percent reduction.
(iii) For sources meeting
§ 63.771(d)(1)(ii), if an owner or
operator has less than 365 days of data,
an excursion occurs when the average
condenser efficiency calculated
according to the procedures specified in
§ 63.772(g)(2)(iii)(A) or (B) is less than
90.0 percent. For sources meeting
§ 63.771(d)(1)(ii), an excursion occurs
when the 365-day average condenser
efficiency calculated according to the
requirements specified in
§ 63.772(g)(2)(iii) is less than the
identified 365-day required percent
reduction.
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(vi) For control device whose model
is tested under § 63.772(h) an excursion
occurs when:
(A) The inlet gas flow rate exceeds the
maximum established during the test
conducted under § 63.772(h).
(B) Failure of the monthly visible
emissions test conducted under
§ 63.772(i)(3) occurs.
*
*
*
*
*
(8) * * *
(i) * * *
(A) During a malfunction when the
affected facility is operated during such
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
period in accordance with § 63.6(e)(1);
or
*
*
*
*
*
(ii) For each control device, or
combinations of control devices
installed on the same emissions unit,
one excused excursion is allowed per
semiannual period for any reason. The
initial semiannual period is the 6-month
reporting period addressed by the first
Periodic Report submitted by the owner
or operator in accordance with
§ 63.775(e) of this subpart.
*
*
*
*
*
20. Section 63.774 is amended by:
a. Revising paragraph (b)(3)
introductory text;
b. Removing and reserving paragraph
(b)(3)(ii);
c. Revising paragraph (b)(4)(ii)
introductory text;
d. Adding paragraph (b)(4)(ii)(C);
e. Adding paragraph (b)(7)(ix); and
f. Adding paragraphs (g) through (i) to
read as follows:
§ 63.774
Recordkeeping requirements.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
*
*
*
*
*
(b) * * *
(3) Records specified in § 63.10(c) for
each monitoring system operated by the
owner or operator in accordance with
the requirements of § 63.773(d).
Notwithstanding the requirements of
§ 63.10(c), monitoring data recorded
during periods identified in paragraphs
(b)(3)(i) through (b)(3)(iv) of this section
shall not be included in any average or
percent leak rate computed under this
subpart. Records shall be kept of the
times and durations of all such periods
and any other periods during process or
control device operation when monitors
are not operating or failed to collect
required data.
*
*
*
*
*
(ii) [Reserved]
*
*
*
*
*
(4) * * *
(ii) Records of the daily average value
of each continuously monitored
parameter for each operating day
determined according to the procedures
specified in § 63.773(d)(4) of this
subpart, except as specified in
paragraphs (b)(4)(ii)(A) through (C) of
this section.
*
*
*
*
*
(C) For control device whose model is
tested under § 63.772(h), the records
required in paragraph (h) of this section.
*
*
*
*
*
(7) * * *
(ix) Records identifying the carbon
replacement schedule under
§ 63.771(d)(5) and records of each
carbon replacement.
*
*
*
*
*
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(g) The owner or operator of an
affected source subject to this subpart
shall maintain records of the occurrence
and duration of each malfunction of
operation (i.e., process equipment) or
the air pollution control equipment and
monitoring equipment. The owner or
operator shall maintain records of
actions taken during periods of
malfunction to minimize emissions in
accordance with § 63.764(a), including
corrective actions to restore
malfunctioning process and air
pollution control and monitoring
equipment to its normal or usual
manner of operation.
(h) Record the following when using
a control device whose model is tested
under § 63.772(h) to comply with
§ 63.771(d), (e)(3)(ii) and (f)(1):
(1) All visible emission readings and
flowrate measurements made during the
compliance determination required by
§ 63.772(i); and
(2) All hourly records and other
recorded periods when the pilot flame
is absent.
(i) The date the semi-annual
maintenance inspection required under
§ 63.773(b) is performed. Include a list
of any modifications or repairs made to
the control device during the inspection
and other maintenance performed such
as cleaning of the fuel nozzles.
21. Section 63.775 is amended by:
a. Revising paragraph (b)(1);
b. Revising paragraph (b)(6);
c. Removing and reserving paragraph
(b)(7);
d. Revising paragraph (c)(1);
e. Revising paragraph (c)(6);
f. Revising paragraph (c)(7)(i);
g. Revising paragraph (d)(1)(i);
h. Revising paragraph (d)(1)(ii)
introductory text;
i. Revising paragraph (d)(5)(ii);
j. Adding paragraph (d)(5)(iv);
k. Revising paragraph (d)(11);
l. Adding paragraphs (d)(13) and
(d)(14);
m. Revising paragraphs (e)(2)
introductory text, (e)(2)(ii)(B) and (C);
n. Adding paragraphs (e)(2)(ii)(E) and
(F);
o. Adding paragraphs (e)(2)(xi)
through (xiii); and
p. Adding paragraph (g) to read as
follows:
§ 63.775
Reporting requirements.
*
*
*
*
*
(b) * * *
(1) The initial notifications required
for existing affected sources under
§ 63.9(b)(2) shall be submitted as
provided in paragraphs (b)(1)(i) and (ii)
of this section.
(i) Except as otherwise provided in
paragraph (ii), the initial notifications
PO 00000
Frm 00088
Fmt 4701
Sfmt 4702
shall be submitted by 1 year after an
affected source becomes subject to the
provisions of this subpart or by June 17,
2000, whichever is later. Affected
sources that are major sources on or
before June 17, 2000 and plan to be area
sources by June 17, 2002 shall include
in this notification a brief, nonbinding
description of a schedule for the
action(s) that are planned to achieve
area source status.
(ii) An affected source identified
under § 63.760(f)(7) or (9) shall submit
an initial notification required for
existing affected sources under
§ 63.9(b)(2) within 1 year after the
affected source becomes subject to the
provisions of this subpart or by one year
after publication of the final rule in the
Federal Register, whichever is later. An
affected source identified under
§ 63.760(f)(7) or (9) that plans to be an
area source by three years after
publication of the final rule in the
Federal Register, shall include in this
notification a brief, nonbinding
description of a schedule for the
action(s) that are planned to achieve
area source status.
*
*
*
*
*
(6) If there was a malfunction during
the reporting period, the Periodic Report
specified in paragraph (e) of this section
shall include the number, duration, and
a brief description for each type of
malfunction which occurred during the
reporting period and which caused or
may have caused any applicable
emission limitation to be exceeded. The
report must also include a description of
actions taken by an owner or operator
during a malfunction of an affected
source to minimize emissions in
accordance with § 63.764(j), including
actions taken to correct a malfunction.
(7) [Reserved]
*
*
*
*
*
(c) * * *
(1) The initial notifications required
under § 63.9(b)(2) not later than January
3, 2008. In addition to submitting your
initial notification to the addressees
specified under § 63.9(a), you must also
submit a copy of the initial notification
to the EPA’s Office of Air Quality
Planning and Standards. Send your
notification via e-mail to Oil and Gas
Sector@epa.gov or via U.S. mail or other
mail delivery service to U.S. EPA,
Sector Policies and Programs Division/
Fuels and Incineration Group (E143–
01), Attn: Oil and Gas Project Leader,
Research Triangle Park, NC 27711.
*
*
*
*
*
(6) If there was a malfunction during
the reporting period, the Periodic Report
specified in paragraph (e) of this section
shall include the number, duration, and
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
a brief description for each type of
malfunction which occurred during the
reporting period and which caused or
may have caused any applicable
emission limitation to be exceeded. The
report must also include a description of
actions taken by an owner or operator
during a malfunction of an affected
source to minimize emissions in
accordance with § 63.764(j), including
actions taken to correct a malfunction.
(7) * * *
(i) Documentation of the source’s
location relative to the nearest UA plus
offset and UC boundaries. This
information shall include the latitude
and longitude of the affected source;
whether the source is located in an
urban cluster with 10,000 people or
more; the distance in miles to the
nearest urbanized area boundary if the
source is not located in an urban cluster
with 10,000 people or more; and the
name of the nearest urban cluster with
10,000 people or more and nearest
urbanized area.
*
*
*
*
*
(d) * * *
(1) * * *
(i) The condenser design analysis
documentation specified in
§ 63.772(e)(4) of this subpart, if the
owner or operator elects to prepare a
design analysis.
(ii) If the owner or operator is
required to conduct a performance test,
the performance test results including
the information specified in paragraphs
(d)(1)(ii)(A) and (B) of this section.
Results of a performance test conducted
prior to the compliance date of this
subpart can be used provided that the
test was conducted using the methods
specified in § 63.772(e)(3) and that the
test conditions are representative of
current operating conditions. If the
owner or operator operates a
combustion control device model tested
under § 63.772(h), an electronic copy of
the performance test results shall be
submitted via e-mail to Oil and Gas
PT@EPA.GOV.
*
*
*
*
*
(5) * * *
(ii) An explanation of the rationale for
why the owner or operator selected each
of the operating parameter values
established in § 63.773(d)(5). This
explanation shall include any data and
calculations used to develop the value
and a description of why the chosen
value indicates that the control device is
operating in accordance with the
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applicable requirements of
§ 63.771(d)(1), (e)(3)(ii) or (f)(1).
*
*
*
*
*
(iv) For each carbon adsorber, the
predetermined carbon replacement
schedule as required in § 63.771(d)(5)(i).
*
*
*
*
*
(11) The owner or operator shall
submit the analysis prepared under
§ 63.771(e)(2) to demonstrate the
conditions by which the facility will be
operated to achieve the HAP emission
reduction of 95.0 percent, or the BTEX
limit in § 63.765(b)(1)(iii), through
process modifications or a combination
of process modifications and one or
more control devices.
*
*
*
*
*
(13) If the owner or operator installs
a combustion control device model
tested under the procedures in
§ 63.772(h), the data listed under
§ 63.772(h)(8).
(14) For each combustion control
device model tested under § 63.772(h),
the information listed in paragraphs
(d)(14)(i) through (vi) of this section.
(i) Name, address and telephone
number of the control device
manufacturer.
(ii) Control device model number.
(iii) Control device serial number.
(iv) Date of control device
certification test.
(v) Manufacturer’s HAP destruction
efficiency rating.
(vi) Control device operating
parameters, maximum allowable inlet
gas flowrate.
(e) * * *
(2) The owner or operator shall
include the information specified in
paragraphs (e)(2)(i) through (xiii) of this
section, as applicable.
*
*
*
*
*
(ii) * * *
(B) For each excursion caused when
the 365-day average condenser control
efficiency is less than the value
specified in § 63.773(d)(6)(ii), the report
must include the 365-day average values
of the condenser control efficiency, and
the date and duration of the period that
the excursion occurred.
(C) For each excursion caused when
condenser control efficiency is less than
the value specified in § 63.773(d)(6)(iii),
the report must include the average
values of the condenser control
efficiency, and the date and duration of
the period that the excursion occurred.
*
*
*
*
*
PO 00000
Frm 00089
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52825
(E) For each excursion caused when
the maximum inlet gas flow rate
identified under § 63.772(h) is
exceeded, the report must include the
values of the inlet gas identified and the
date and duration of the period that the
excursion occurred.
(F) For each excursion caused when
visible emissions determined under
§ 63.772(i) exceed the maximum
allowable duration, the report must
include the date and duration of the
period that the excursion occurred.
*
*
*
*
*
(xi) The results of any periodic test as
required in § 63.772(e)(3) conducted
during the reporting period.
(xii) For each carbon adsorber used to
meet the control device requirements of
§ 63.771(d)(1), records of each carbon
replacement that occurred during the
reporting period.
(xiii) For combustion control device
inspections conducted in accordance
with § 63.773(b) the records specified in
§ 63.774(i).
*
*
*
*
*
(g) Electronic reporting. (1) As of
January 1, 2012 and within 60 days after
the date of completing each
performance test, as defined in § 63.2
and as required in this subpart, you
must submit performance test data,
except opacity data, electronically to the
EPA’s Central Data Exchange (CDX) by
using the Electronic Reporting Tool
(ERT) (see https://www.epa.gov/ttn/chief/
ert/ert tool.html/). Only data collected
using test methods compatible with ERT
are subject to this requirement to be
submitted electronically into the EPA’s
WebFIRE database.
(2) All reports required by this
subpart not subject to the requirements
in paragraphs (g)(1) of this section must
be sent to the Administrator at the
appropriate address listed in § 63.13. If
acceptable to both the Administrator
and the owner or operator of a source,
these reports may be submitted on
electronic media. The Administrator
retains the right to require submittal of
reports subject to paragraph (g)(1) of this
section in paper format.
22. Appendix to subpart HH of part 63
is amended by revising Table 2 to read
as follows:
Appendix to Subpart HH of Part 63—
Tables
*
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*
23AUP2
*
*
52826
Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
TABLE 2 TO SUBPART HH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART HH
Applicable to
subpart HH
§ 63.1(a)(1) ................................................
§ 63.1(a)(2) ................................................
§ 63.1(a)(3) ................................................
§ 63.1(a)(4) ................................................
§ 63.1(a)(5) ................................................
§ 63.1(a)(6) ................................................
§ 63.1(a)(7) through (a)(9) .........................
§ 63.1(a)(10) ..............................................
§ 63.1(a)(11) ..............................................
§ 63.1(a)(12) ..............................................
§ 63.1(b)(1) ................................................
§ 63.1(b)(2) ................................................
§ 63.1(b)(3) ................................................
§ 63.1(c)(1) ................................................
§ 63.1(c)(2) ................................................
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes.
Yes.
No .................
No .................
Yes.
No .................
Yes ................
§ 63.1(c)(3) and (c)(4) ...............................
§ 63.1(c)(5) ................................................
§ 63.1(d) .....................................................
§ 63.1(e) .....................................................
§ 63.2 .........................................................
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
General provisions reference
No .................
Yes.
No .................
Yes.
Yes ................
§ 63.3(a) through (c) ..................................
§ 63.4(a)(1) through (a)(2) .........................
§ 63.4(a)(3) through (a)(5) .........................
§ 63.4(b) .....................................................
§ 63.4(c) .....................................................
§ 63.5(a)(1) ................................................
§ 63.5(a)(2) ................................................
§ 63.5(b)(1) ................................................
§ 63.5(b)(2) ................................................
§ 63.5(b)(3) ................................................
§ 63.5(b)(4) ................................................
§ 63.5(b)(5) ................................................
§ 63.5(b)(6) ................................................
§ 63.5(c) .....................................................
§ 63.5(d)(1) ................................................
§ 63.5(d)(2) ................................................
§ 63.5(d)(3) ................................................
§ 63.5(d)(4) ................................................
§ 63.5(e) .....................................................
§ 63.5(f)(1) .................................................
§ 63.5(f)(2) .................................................
§ 63.6(a) .....................................................
§ 63.6(b)(1) ................................................
§ 63.6(b)(2) ................................................
§ 63.6(b)(3) ................................................
§ 63.6(b)(4) ................................................
§ 63.6(b)(5) ................................................
§ 63.6(b)(6) ................................................
§ 63.6(b)(7) ................................................
§ 63.6(c)(1) ................................................
§ 63.6(c)(2) ................................................
§ 63.6(c)(3) through (c)(4) .........................
§ 63.6(c)(5) ................................................
§ 63.6(d) .....................................................
§ 63.6(e) .....................................................
§ 63.6(e)(1)(i) .............................................
§ 63.6(e)(1)(ii) ............................................
§ 63.6(e)(1)(iii) ...........................................
§ 63.6(e)(2) ................................................
§ 63.6(e)(3) ................................................
§ 63.6(f)(1) .................................................
§ 63.6(f)(2) .................................................
§ 63.6(f)(3) .................................................
§ 63.6(g) .....................................................
§ 63.6(h) .....................................................
§ 63.6(i)(1) through (i)(14) .........................
§ 63.6(i)(15) ...............................................
§ 63.6(i)(16) ...............................................
§ 63.6(j) ......................................................
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
No .................
No.
Yes.
No .................
No.
No.
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes.
VerDate Mar<15>2010
18:55 Aug 22, 2011
Jkt 223001
PO 00000
Explanation
Section reserved.
Section reserved.
Subpart HH specifies applicability.
Section reserved.
Subpart HH specifies applicability.
Subpart HH exempts area sources from the requirement to obtain a Title V permit
unless otherwise required by law as specified in § 63.760(h).
Section reserved.
Section reserved.
Except definition of major source is unique for this source category and there are
additional definitions in subpart HH.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
See § 63.764(j) for general duty requirement.
Section reserved.
Subpart HH does not contain opacity or visible emission standards.
Section reserved.
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
52827
TABLE 2 TO SUBPART HH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART HH—
Continued
Applicable to
subpart HH
§ 63.7(a)(1) ................................................
§ 63.7(a)(2) ................................................
Yes.
Yes ................
§ 63.7(a)(3) ................................................
§ 63.7(b) .....................................................
§ 63.7(c) .....................................................
§ 63.7(d) .....................................................
§ 63.7(e)(1) ................................................
§ 63.7(e)(2) ................................................
§ 63.7(e)(3) ................................................
§ 63.7(e)(4) ................................................
§ 63.7(f) ......................................................
§ 63.7(g) .....................................................
§ 63.7(h) .....................................................
§ 63.8(a)(1) ................................................
§ 63.8(a)(2) ................................................
§ 63.8(a)(3) ................................................
§ 63.8(a)(4) ................................................
§ 63.8(b)(1) ................................................
§ 63.8(b)(2) ................................................
§ 63.8(b)(3) ................................................
§ 63.8(c)(1) ................................................
§ 63.8(c)(1)(i) .............................................
§ 63.8(c)(1)(ii) ............................................
§ 63.8(c)(1)(iii) ............................................
§ 63.8(c)(2) ................................................
§ 63.8(c)(3) ................................................
§ 63.8(c)(4) ................................................
§ 63.8(c)(4)(i) .............................................
§ 63.8(c)(4)(ii) ............................................
§ 63.8(c)(5) through (c)(8) .........................
§ 63.8(d) .....................................................
§ 63.8(d)(3) ................................................
§ 63.8(e) .....................................................
Yes.
Yes.
Yes.
Yes.
No.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
No.
No.
Yes.
Pending.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes ................
Yes ................
§ 63.8(f)(1) through (f)(5) ...........................
§ 63.8(f)(6) .................................................
§ 63.8(g) .....................................................
§ 63.9(a) .....................................................
§ 63.9(b)(1) ................................................
§ 63.9(b)(2) ................................................
Yes.
Yes.
No .................
Yes.
Yes.
Yes ................
§ 63.9(b)(3) ................................................
§ 63.9(b)(4) ................................................
§ 63.9(b)(5) ................................................
§ 63.9(c) .....................................................
§ 63.9(d) .....................................................
§ 63.9(e) .....................................................
§ 63.9(f) ......................................................
§ 63.9(g)(1) ................................................
§ 63.9(g)(2) ................................................
§ 63.9(g)(3) ................................................
§ 63.9(h)(1) through (h)(3) .........................
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
General provisions reference
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes ................
§ 63.9(h)(4) ................................................
§ 63.9(h)(5) through (h)(6) .........................
§ 63.9(i) ......................................................
§ 63.9(j) ......................................................
§ 63.10(a) ...................................................
§ 63.10(b)(1) ..............................................
No .................
Yes.
Yes.
Yes.
Yes.
Yes ................
§ 63.10(b)(2) ..............................................
§ 63.10(b)(2)(i) ...........................................
§ 63.10(b)(2)(ii) ..........................................
Yes.
No .................
No .................
§ 63.10(b)(2)(iii) .........................................
§ 63.10(b)(2)(iv) through (b)(2)(v) ..............
§ 63.10(b)(2)(vi) through (b)(2)(xiv) ...........
Yes.
No.
Yes.
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PO 00000
Explanation
But the performance test results must be submitted within 180 days after the compliance date.
Section reserved.
Subpart HH does not require continuous opacity monitors.
Except for last sentence, which refers to an SSM plan. SSM plans are not required.
Subpart HH does not specifically require continuous emissions monitor performance evaluation, however, the Administrator can request that one be conducted.
Subpart HH specifies continuous monitoring system data reduction requirements.
Existing sources are given 1 year (rather than 120 days) to submit this notification.
Major and area sources that meet § 63.764(e) do not have to submit initial notifications.
Section reserved.
Subpart HH does not have opacity or visible emission standards.
Subpart HH does not have opacity or visible emission standards.
Area sources located outside UA plus offset and UC boundaries are not required to
submit notifications of compliance status.
Section reserved.
§ 63.774(b)(1) requires sources to maintain the most recent 12 months of data onsite and allows offsite storage for the remaining 4 years of data.
See § 63.774(g) for recordkeeping of occurrence, duration, and actions taken during malfunctions.
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Federal Register / Vol. 76, No. 163 / Tuesday, August 23, 2011 / Proposed Rules
TABLE 2 TO SUBPART HH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART HH—
Continued
General provisions reference
Applicable to
subpart HH
Explanation
§ 63.10(b)(3) ..............................................
Yes ................
§ 63.774(b)(1) requires sources to maintain the most recent 12 months of data onsite and allows offsite storage for the remaining 4 years of data.
§ 63.10(c)(1) ..............................................
§ 63.10(c)(2) through (c)(4) .......................
§ 63.10(c)(5) through (8)(c)(8) ...................
§ 63.10(c)(9) ..............................................
§ 63.10(c)(10) through (11) .......................
§ 63.10(c)(12) through (14) .......................
§ 63.10(c)(15) ............................................
§ 63.10(d)(1) ..............................................
§ 63.10(d)(2) ..............................................
Yes.
No .................
Yes.
No .................
No .................
Yes.
No.
Yes.
Yes ................
§ 63.10(d)(3)
§ 63.10(d)(4)
§ 63.10(d)(5)
§ 63.10(e)(1)
..............................................
..............................................
..............................................
..............................................
Yes.
Yes.
No .................
Yes ................
§ 63.10(e)(2) ..............................................
Yes ................
§ 63.10(e)(3)(i) ...........................................
Yes ................
§ 63.10(e)(3)(i)(A) ......................................
§ 63.10(e)(3)(i)(B) ......................................
§ 63.10(e)(3)(i)(C) ......................................
§ 63.10(e)(3)(ii) through (viii) .....................
§ 63.10(f) ....................................................
§ 63.11(a) and (b) ......................................
§ 63.11(c), (d), and (e) ...............................
§ 63.12(a) through (c) ................................
§ 63.13(a) through (c) ................................
§ 63.14(a) and (b) ......................................
§ 63.15(a) and (b) ......................................
§ 63.16 .......................................................
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Subpart HHH—[Amended]
23. Section 63.1270 is amended by:
a. Revising paragraph (a) introductory
text;
b. Revising paragraph (a)(4);
c. Revising paragraphs (d)(1) and
(d)(2); and
d. Adding paragraphs (d)(3), (4) and
(5) to read as follows:
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
§ 63.1270 Applicability and designation of
affected source.
(a) This subpart applies to owners and
operators of natural gas transmission
and storage facilities that transport or
store natural gas prior to entering the
pipeline to a local distribution company
or to a final end user (if there is no local
distribution company), and that are
major sources of hazardous air
pollutants (HAP) emissions as defined
in § 63.1271. Emissions for major source
determination purposes can be
estimated using the maximum natural
gas throughput calculated in either
paragraph (a)(1) or (2) of this section
and paragraphs (a)(3) and (4) of this
section. As an alternative to calculating
the maximum natural gas throughput,
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Sections reserved.
Section reserved.
See § 63.774(g) for recordkeeping of malfunctions.
Area sources located outside UA plus offset and UC boundaries do not have to
submit performance test reports.
See § 63.775(b)(6) or (c)(6) for reporting of malfunctions.
Area sources located outside UA plus offset and UC boundaries are not required to
submit reports.
Area sources located outside UA plus offset and UC boundaries are not required to
submit reports.
Subpart HH requires major sources to submit Periodic Reports semi-annually. Area
sources are required to submit Periodic Reports annually. Area sources located
outside UA plus offset and UC boundaries are not required to submit reports.
Section reserved.
the owner or operator of a new or
existing source may use the facility
design maximum natural gas throughput
to estimate the maximum potential
emissions. Other means to determine
the facility’s major source status are
allowed, provided the information is
documented and recorded to the
Administrator’s satisfaction in
accordance with § 63.10(b)(3). A
compressor station that transports
natural gas prior to the point of custody
transfer or to a natural gas processing
plant (if present) is not considered a
part of the natural gas transmission and
storage source category. A facility that is
determined to be an area source, but
subsequently increases its emissions or
its potential to emit above the major
source levels (without obtaining and
complying with other limitations that
keep its potential to emit HAP below
major source levels), and becomes a
major source, must comply thereafter
with all applicable provisions of this
subpart starting on the applicable
compliance date specified in paragraph
(d) of this section. Nothing in this
paragraph is intended to preclude a
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source from limiting its potential to emit
through other appropriate mechanisms
that may be available through the
permitting authority.
*
*
*
*
*
(4) The owner or operator shall
determine the maximum values for
other parameters used to calculate
potential emissions as the maximum
over the same period for which
maximum throughput is determined as
specified in paragraph (a)(1) or (a)(2) of
this section. These parameters shall be
based on an annual average or the
highest single measured value. For
estimating maximum potential
emissions from glycol dehydration
units, the glycol circulation rate used in
the calculation shall be the unit’s
maximum rate under its physical and
operational design consistent with the
definition of potential to emit in § 63.2.
*
*
*
*
*
(d) * * *
(1) Except as specified in paragraphs
(d)(3) through (5) of this section, the
owner or operator of an affected source,
the construction or reconstruction of
which commenced before February 6,
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1998, shall achieve compliance with the
provisions of this subpart no later than
June 17, 2002 except as provided for in
§ 63.6(i). The owner or operator of an
area source, the construction or
reconstruction of which commenced
before February 6, 1998, that increases
its emissions of (or its potential to emit)
HAP such that the source becomes a
major source that is subject to this
subpart shall comply with this subpart
3 years after becoming a major source.
(2) Except as specified in paragraphs
(d)(3) through (5) of this section, the
owner or operator of an affected source,
the construction or reconstruction of
which commences on or after February
6, 1998, shall achieve compliance with
the provisions of this subpart
immediately upon initial startup or June
17, 1999, whichever date is later. Area
sources, the construction or
reconstruction of which commences on
or after February 6, 1998, that become
major sources shall comply with the
provisions of this standard immediately
upon becoming a major source.
(3) Each affected small glycol
dehydration unit, as defined in
§ 63.1271, located at a major source, that
commenced construction before August
23, 2011 must achieve compliance no
later than 3 years after the date of
publication of the final rule in the
Federal Register, except as provided in
§ 63.6(i).
(4) Each affected small glycol
dehydration unit, as defined in
§ 63.1271, located at a major source, that
commenced construction on or after
August 23, 2011 must achieve
compliance immediately upon initial
startup or the date of publication of the
final rule in the Federal Register,
whichever is later.
(5) Each large glycol dehydration unit,
as defined in § 63.1271, that has
complied with the provisions of this
subpart prior to August 23, 2011 by
reducing its benzene emissions to less
than 0.9 megagrams per year must
achieve compliance no later than
90 days after the date of publication of
the final rule in the Federal Register,
except as provided in § 63.6(i).
*
*
*
*
*
24. Section 63.1271 is amended by:
a. Adding, in alphabetical order, new
definitions for the terms ‘‘affirmative
defense,’’ ‘‘BTEX,’’ ‘‘flare,’’ ‘‘large glycol
dehydration units,’’ ‘‘small glycol
dehydration units’’; and
b. Revising the definitions for ‘‘glycol
dehydration unit baseline operations’’
and ‘‘temperature monitoring device’’ to
read as follows:
§ 63.1271
Definitions.
*
*
*
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*
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Affirmative defense means, in the
context of an enforcement proceeding, a
response or defense put forward by a
defendant, regarding which the
defendant has the burden of proof, and
the merits of which are independently
and objectively evaluated in a judicial
or administrative proceeding.
*
*
*
*
*
BTEX means benzene, toluene, ethyl
benzene and xylene.
*
*
*
*
*
Flare means a thermal oxidation
system using an open flame (i.e.,
without enclosure).
*
*
*
*
*
Glycol dehydration unit baseline
operations means operations
representative of the large glycol
dehydration unit operations as of June
17, 1999 and the small glycol
dehydration unit operations as of
August 23, 2011. For the purposes of
this subpart, for determining the
percentage of overall HAP emission
reduction attributable to process
modifications, glycol dehydration unit
baseline operations shall be parameter
values (including, but not limited to,
glycol circulation rate or glycol-HAP
absorbency) that represent actual longterm conditions (i.e., at least 1 year).
Glycol dehydration units in operation
for less than 1 year shall document that
the parameter values represent expected
long-term operating conditions had
process modifications not been made.
*
*
*
*
*
Large glycol dehydration unit means a
glycol dehydration unit with an actual
annual average natural gas flowrate
equal to or greater than 283.0 thousand
standard cubic meters per day and
actual annual average benzene
emissions equal to or greater than 0.90
Mg/yr, determined according to
§ 63.1282(a).
*
*
*
*
*
Small glycol dehydration unit means
a glycol dehydration unit, located at a
major source, with an actual annual
average natural gas flowrate less than
283.0 thousand standard cubic meters
per day or actual annual average
benzene emissions less than 0.90 Mg/yr,
determined according to § 63.1282(a).
Temperature monitoring device
means an instrument used to monitor
temperature and having a minimum
accuracy of ± 1 percent of the
temperature being monitored expressed
in °C, or ± 2.5 °C, whichever is greater.
The temperature monitoring device may
measure temperature in degrees
Fahrenheit or degrees Celsius, or both.
*
*
*
*
*
25. Section 63.1272 is revised to read
as follows:
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§ 63.1272
52829
Startups and shutdowns.
(a) The provisions set forth in this
subpart shall apply at all times.
(b) The owner or operator shall not
shut down items of equipment that are
required or utilized for compliance with
the provisions of this subpart during
times when emissions are being routed
to such items of equipment, if the
shutdown would contravene
requirements of this subpart applicable
to such items of equipment. This
paragraph does not apply if the owner
or operator must shut down the
equipment to avoid damage due to a
contemporaneous startup or shutdown
of the affected source or a portion
thereof.
(c) During startups and shutdowns,
the owner or operator shall implement
measures to prevent or minimize excess
emissions to the maximum extent
practical.
(d) In response to an action to enforce
the standards set forth in this subpart,
you may assert an affirmative defense to
a claim for civil penalties for
exceedances of such standards that are
caused by malfunction, as defined in
§ 63.2. Appropriate penalties may be
assessed, however, if you fail to meet
your burden of proving all the
requirements in the affirmative defense.
The affirmative defense shall not be
available for claims for injunctive relief.
(1) To establish the affirmative
defense in any action to enforce such a
limit, the owner or operator must timely
meet the notification requirements in
paragraph (d)(2) of this section, and
must prove by a preponderance of
evidence that:
(i) The excess emissions:
(A) Were caused by a sudden,
infrequent, and unavoidable failure of
air pollution control and monitoring
equipment, process equipment, or a
process to operate in a normal or usual
manner; and
(B) Could not have been prevented
through careful planning, proper design
or better operation and maintenance
practices; and
(C) Did not stem from any activity or
event that could have been foreseen and
avoided, or planned for; and
(D) Were not part of a recurring
pattern indicative of inadequate design,
operation, or maintenance; and
(ii) 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 to make these repairs; and
(iii) The frequency, amount and
duration of the excess emissions
(including any bypass) were minimized
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to the maximum extent practicable
during periods of such emissions; and
(iv) 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; and
(v) All possible steps were taken to
minimize the impact of the excess
emissions on ambient air quality, the
environment, and human health; and
(vi) All emissions monitoring and
control systems were kept in operation
if at all possible, consistent with safety
and good air pollution control practices;
and
(vii) All of the actions in response to
the excess emissions were documented
by properly signed, contemporaneous
operating logs; and
(viii) At all times, the affected source
was operated in a manner consistent
with good practices for minimizing
emissions; and
(ix) A written root cause analysis has
been prepared to determine, correct, and
eliminate the primary causes of the
malfunction and the excess emissions
resulting from the malfunction event at
issue. The analysis shall also specify,
using best monitoring methods and
engineering judgment, the amount of
excess emissions that were the result of
the malfunction.
(2) Notification. The owner or
operator of the affected source
experiencing an exceedance of its
emission limit(s) during a malfunction
shall notify the Administrator by
telephone or facsimile transmission as
soon as possible, but no later than two
business days after the initial
occurrence of the malfunction, if it
wishes to avail itself of an affirmative
defense to civil penalties for that
malfunction. The owner or operator
seeking to assert an affirmative defense
shall also submit a written report to the
Administrator within 45 days of the
initial occurrence of the exceedance of
the standard in this subpart to
demonstrate, with all necessary
supporting documentation, that it has
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met the requirements set forth in
paragraph (d)(1) of this section. The
owner or operator may seek an
extension of this deadline for up to 30
additional days by submitting a written
request to the Administrator before the
expiration of the 45 day period. Until a
request for an extension has been
approved by the Administrator, the
owner or operator is subject to the
requirement to submit such report
within 45 days of the initial occurrence
of the exceedance.
26. Section 63.1274 is amended by:
a. Revising paragraph (c) introductory
text;
b. Removing and reserving paragraph
(d);
c. Revising paragraph (g); and
d. Adding paragraph (h) to read as
follows:
§ 63.1274
General standards.
*
*
*
*
*
(c) The owner or operator of an
affected source (i.e., glycol dehydration
unit) located at an existing or new major
source of HAP emissions shall comply
with the requirements in this subpart as
follows:
*
*
*
*
*
(d) [Reserved]
*
*
*
*
*
(g) In all cases where the provisions
of this subpart require an owner or
operator to repair leaks by a specified
time after the leak is detected, it is a
violation of this standard to fail to take
action to repair the leak(s) within the
specified time. If action is taken to
repair the leak(s) within the specified
time, failure of that action to
successfully repair the leak(s) is not a
violation of this standard. However, if
the repairs are unsuccessful, and a leak
is detected, the owner or operator shall
take further action as required by the
applicable provisions of this subpart.
(h) At all times the owner or operator
must operate and maintain any affected
source, including associated air
pollution control equipment and
monitoring equipment, in a manner
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consistent with safety and good air
pollution control practices for
minimizing emissions. Determination of
whether such operation and
maintenance procedures are being used
will be based on information available
to the Administrator which may
include, but is not limited to,
monitoring results, review of operation
and maintenance procedures, review of
operation and maintenance records, and
inspection of the source.
27. Section 63.1275 is amended by:
a. Revising paragraph (a);
b. Revising paragraph (b)(1);
c. Revising paragraph (c)(2); and
d. Revising paragraph (c)(3) to read as
follows:
§ 63.1275 Glycol dehydration unit process
vent standards.
(a) This section applies to each glycol
dehydration unit subject to this subpart
that must be controlled for air emissions
as specified in paragraph (c)(1) of
§ 63.1274.
(b) * * *
(1) For each glycol dehydration unit
process vent, the owner or operator
shall control air emissions by either
paragraph (b)(1)(i) or (b)(1)(iii) of this
section.
(i) The owner or operator of a large
glycol dehydration unit, as defined in
§ 63.1271, shall connect the process
vent to a control device or a
combination of control devices through
a closed-vent system. The closed-vent
system shall be designed and operated
in accordance with the requirements of
§ 63.1281(c). The control device(s) shall
be designed and operated in accordance
with the requirements of § 63.1281(d).
(ii) [Reserved]
(iii) You must limit BTEX emissions
from each small glycol dehydration
unit, as defined in § 63.1271, to the limit
determined in Equation 1 of this
section. The limit must be met in
accordance with one of the alternatives
specified in paragraphs (b)(i)(iii)(A)
through (D) of this section.
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Where:
ELBTEX = Unit-specific BTEX emission limit,
megagrams per year;
6.42 × 10¥5 = BTEX emission limit, grams
BTEX/standard cubic meter -ppmv;
Throughput = Annual average daily natural
gas throughput, standard cubic meters
per day
Ci,BTEX = BTEX concentration of the natural
gas at the inlet to the glycol dehydration
unit, ppmv.
(A) Connect the process vent to a
control device or combination of control
devices through a closed-vent system.
The closed vent system shall be
designed and operated in accordance
with the requirements of § 63.1281(c).
The control device(s) shall be designed
and operated in accordance with the
requirements of § 63.1281(f).
(B) Meet the emissions limit through
process modifications in accordance
with the requirements specified in
§ 63.1281(e).
(C) Meet the emission limit for each
small glycol dehydration unit using a
combination of process modifications
and one or more control devices through
the requirements specified in
paragraphs (b)(1)(iii)(A) and (B) of this
section.
(D) Demonstrate that the emissions
limit is met through actual uncontrolled
operation of the small glycol
dehydration unit. Document operational
parameters in accordance with the
requirements specified in § 63.1281(e)
and emissions in accordance with the
requirements specified in
§ 63.1282(a)(3).
*
*
*
*
*
(c) * * *
(2) The owner or operator shall
demonstrate, to the Administrator’s
satisfaction, that the total HAP
emissions to the atmosphere from the
large glycol dehydration unit process
vent are reduced by 95.0 percent
through process modifications or a
combination of process modifications
and one or more control devices, in
accordance with the requirements
specified in § 63.1281(e).
(3) Control of HAP emissions from a
GCG separator (flash tank) vent is not
required if the owner or operator
demonstrates, to the Administrator’s
satisfaction, that total emissions to the
atmosphere from the glycol dehydration
unit process vent are reduced by one of
the levels specified in paragraph (c)(3)(i)
or (iii) through the installation and
operation of controls as specified in
paragraph (b)(1) of this section.
(i) For any large glycol dehydration
unit, HAP emissions are reduced by
95.0 percent or more.
(ii) [Reserved]
(iii) For each small glycol dehydration
unit, BTEX emissions are reduced to a
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level less than the limit calculated in
paragraph (b)(1)(iii) of this section.
28. Section 63.1281 is amended by:
a. Revising paragraph (c)(1);
b. Revising the heading of paragraph
(d).
c. Adding paragraph (d) introductory
text;
d. Revising paragraph (d)(1)(i)
introductory text;
e. Revising paragraph (d)(1)(i)(C);
f. Revising paragraphs (d)(1)(ii) and
(iii);
g. Revising paragraph (d)(4)(i);
h. Revising paragraph (d)(5)(i);
i. Revising paragraph (e)(2);
j. Revising paragraph (e)(3)
introductory text;
k. Revising paragraph (e)(3)(ii); and
l. Adding paragraph (f) to read as
follows:
§ 63.1281 Control equipment
requirements.
*
*
*
*
*
(c) * * *
(1) The closed-vent system shall route
all gases, vapors, and fumes emitted
from the material in an emissions unit
to a control device that meets the
requirements specified in paragraph (d)
of this section.
*
*
*
*
*
(d) Control device requirements for
sources except small glycol dehydration
units. Owners and operators of small
glycol dehydration units shall comply
with the control requirements in
paragraph (f) of this section.
(1) * * *
(i) An enclosed combustion device
(e.g., thermal vapor incinerator, catalytic
vapor incinerator, boiler, or process
heater) that is designed and operated in
accordance with one of the following
performance requirements:
*
*
*
*
*
(C) For a control device that can
demonstrate a uniform combustion zone
temperature during the performance test
conducted under § 63.1282(d), operates
at a minimum temperature of 760 °C.
*
*
*
*
*
(ii) A vapor recovery device (e.g.,
carbon adsorption system or condenser)
or other non-destructive control device
that is designed and operated to reduce
the mass content of either TOC or total
HAP in the gases vented to the device
by 95.0 percent by weight or greater as
determined in accordance with the
requirements of § 63.1282(d).
(iii) A flare, as defined in § 63.1271,
that is designed and operated in
accordance with the requirements of
§ 63.11(b).
*
*
*
*
*
(4) * * *
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52831
(i) Each control device used to comply
with this subpart shall be operating at
all times when gases, vapors, and fumes
are vented from the emissions unit or
units through the closed vent system to
the control device as required under
§ 63.1275. An owner or operator may
vent more than one unit to a control
device used to comply with this
subpart.
*
*
*
*
*
(5) * * *
(i) Following the initial startup of the
control device, all carbon in the control
device shall be replaced with fresh
carbon on a regular, predetermined time
interval that is no longer than the
carbon service life established for the
carbon adsorption system. Records
identifying the schedule for replacement
and records of each carbon replacement
shall be maintained as required in
§ 63.1284(b)(7)(ix). The schedule for
replacement shall be submitted with the
Notification of Compliance Status
Report as specified in
§ 63.1285(d)(4)(iv). Each carbon
replacement must be reported in the
Periodic Reports as specified in
§ 63.1285(e)(2)(xi).
*
*
*
*
*
(e) * * *
(2) The owner or operator shall
document, to the Administrator’s
satisfaction, the conditions for which
glycol dehydration unit baseline
operations shall be modified to achieve
the 95.0 percent overall HAP emission
reduction, or BTEX limit determined in
§ 63.1275(b)(1)(iii), as applicable, either
through process modifications or
through a combination of process
modifications and one or more control
devices. If a combination of process
modifications and one or more control
devices are used, the owner or operator
shall also establish the emission
reduction to be achieved by the control
device to achieve an overall HAP
emission reduction of 95.0 percent for
the glycol dehydration unit process vent
or, if applicable, the BTEX limit
determined in § 63.1275(b)(1)(iii) for the
small glycol dehydration unit process
vent. Only modifications in glycol
dehydration unit operations directly
related to process changes, including
but not limited to changes in glycol
circulation rate or glycol-HAP
absorbency, shall be allowed. Changes
in the inlet gas characteristics or natural
gas throughput rate shall not be
considered in determining the overall
emission reduction due to process
modifications.
(3) The owner or operator that
achieves a 95.0 percent HAP emission
reduction or meets the BTEX limit
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determined in § 63.1275(b)(1)(iii), as
applicable, using process modifications
alone shall comply with paragraph
(e)(3)(i) of this section. The owner or
operator that achieves a 95.0 percent
HAP emission reduction or meets the
BTEX limit determined in
§ 63.1275(b)(1)(iii), as applicable, using
a combination of process modifications
and one or more control devices shall
comply with paragraphs (e)(3)(i) and
(e)(3)(ii) of this section.
*
*
*
*
*
(ii) The owner or operator shall
comply with the control device
requirements specified in paragraph (d)
or (f) of this section, as applicable,
except that the emission reduction or
limit achieved shall be the emission
reduction or limit specified for the
control device(s) in paragraph (e)(2) of
this section.
(f) Control device requirements for
small glycol dehydration units. (1) The
control device used to meet BTEX the
emission limit calculated in
§ 63.1275(b)(1)(iii) shall be one of the
control devices specified in paragraphs
(f)(1)(i) through (iii) of this section.
(i) An enclosed combustion device
(e.g., thermal vapor incinerator, catalytic
vapor incinerator, boiler, or process
heater) that is designed and operated to
reduce the mass content of BTEX in the
gases vented to the device as
determined in accordance with the
requirements of § 63.1282(d). If a boiler
or process heater is used as the control
device, then the vent stream shall be
introduced into the flame zone of the
boiler or process heater; or
(ii) A vapor recovery device (e.g.,
carbon adsorption system or condenser)
or other non-destructive control device
that is designed and operated to reduce
the mass content of BTEX in the gases
vented to the device as determined in
accordance with the requirements of
§ 63.1282(d); or
(iii) A flare, as defined in § 63.1271,
that is designed and operated in
accordance with the requirements of
§ 63.11(b).
(2) The owner or operator shall
operate each control device in
accordance with the requirements
specified in paragraphs (f)(2)(i) and (ii)
of this section.
(i) Each control device used to comply
with this subpart shall be operating at
all times. An owner or operator may
vent more than one unit to a control
device used to comply with this
subpart.
(ii) For each control device monitored
in accordance with the requirements of
§ 63.1283(d), the owner or operator shall
demonstrate compliance according to
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the requirements of either § 63.1282(e)
or (h).
(3) For each carbon adsorption system
used as a control device to meet the
requirements of paragraph (f)(1) of this
section, the owner or operator shall
manage the carbon as required under
(d)(5)(i) and (ii) of this section.
29. Section 63.1282 is amended by:
a. Revising paragraph (a) introductory
text;
b. Revising paragraph (a)(1)(ii);
c. Revising paragraph (a)(2);
d. Adding paragraph (c);
e. Revising paragraph (d) introductory
text;
f. Revising paragraphs (d)(1)(i)
through (v);
g. Revising paragraph (d)(2);
h. Revising paragraph (d)(3)
introductory text;
i. Revising paragraph (d)(3)(i)(B);
j. Revising paragraph (d)(3)(iv)(C)(1);
k. Adding paragraphs (d)(3)(v) and
(vi);
l. Revising paragraph (d)(4)
introductory text;
m. Revising paragraph (d)(4)(i);
n. Revising paragraph (d)(5);
o. Revising paragraph (e) introductory
text;
p. Revising paragraphs (e)(2) and
(e)(3);
q. Adding paragraphs (e)(4) through
(e)(6);
r. Revising paragraph (f) introductory
text;
s. Revising paragraph (f)(1);
t. Revising paragraph (f)(2)
introductory text;
u. Revising paragraph (f)(2)(iii);
v. Revising paragraph (f)(3); and
w. Adding paragraphs (g) and (h) to
read as follows:
§ 63.1282 Test methods, compliance
procedures, and compliance
demonstrations.
(a) Determination of glycol
dehydration unit flowrate, benzene
emissions, or BTEX emissions. The
procedures of this paragraph shall be
used by an owner or operator to
determine glycol dehydration unit
natural gas flowrate, benzene emissions,
or BTEX emissions.
(1) * * *
(ii) The owner or operator shall
document, to the Administrator’s
satisfaction, the actual annual average
natural gas flowrate to the glycol
dehydration unit.
(2) The determination of actual
average benzene or BTEX emissions
from a glycol dehydration unit shall be
made using the procedures of either
paragraph (a)(2)(i) or (a)(2)(ii) of this
section. Emissions shall be determined
either uncontrolled or with federally
enforceable controls in place.
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(i) The owner or operator shall
determine actual average benzene or
BTEX emissions using the model GRI–
GLYCalcTM, Version 3.0 or higher, and
the procedures presented in the
associated GRI–GLYCalcTM Technical
Reference Manual. Inputs to the model
shall be representative of actual
operating conditions of the glycol
dehydration unit and may be
determined using the procedures
documented in the Gas Research
Institute (GRI) report entitled
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1); or
(ii) The owner or operator shall
determine an average mass rate of
benzene or BTEX emissions in
kilograms per hour through direct
measurement by performing three runs
of Method 18 in 40 CFR part 60,
appendix A (or an equivalent method),
and averaging the results of the three
runs. Annual emissions in kilograms per
year shall be determined by multiplying
the mass rate by the number of hours
the unit is operated per year. This result
shall be converted to megagrams per
year.
*
*
*
*
*
(c) Test procedures and compliance
demonstrations for small glycol
dehydration units. This paragraph
applies to the test procedures for small
dehydration units.
(1) If the owner or operator is using
a control device to comply with the
emission limit in § 63.1275(b)(1)(iii), the
requirements of paragraph (d) of this
section apply. Compliance is
demonstrated using the methods
specified in paragraph (e) of this
section.
(2) If no control device is used to
comply with the emission limit in
§ 63.1275(b)(1)(iii), the owner or
operator must determine the glycol
dehydration unit BTEX emissions as
specified in paragraphs (c)(2)(i) through
(iii) of this section. Compliance is
demonstrated if the BTEX emissions
determined as specified in paragraphs
(c)(2)(i) through (iii) are less than the
emission limit calculated using the
equation in § 63.1275(b)(1)(iii).
(i) Method 1 or 1A, 40 CFR part 60,
appendix A, as appropriate, shall be
used for selection of the sampling sites
at the outlet of the glycol dehydration
unit process vent. Any references to
particulate mentioned in Methods 1 and
1A do not apply to this section.
(ii) The gas volumetric flowrate shall
be determined using Method 2, 2A, 2C,
or 2D, 40 CFR part 60, appendix A, as
appropriate.
(iii) The BTEX emissions from the
outlet of the glycol dehydration unit
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process vent shall be determined using
the procedures specified in paragraph
(d)(3)(v) of this section. As an
alternative, the mass rate of BTEX at the
outlet of the glycol dehydration unit
process vent may be calculated using
the model GRI–GLYCalcTM, Version 3.0
or higher, and the procedures presented
in the associated GRI–GLYCalcTM
Technical Reference Manual. Inputs to
the model shall be representative of
actual operating conditions of the glycol
dehydration unit and shall be
determined using the procedures
documented in the Gas Research
Institute (GRI) report entitled
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1). When the
BTEX mass rate is calculated for glycol
dehydration units using the model GRI–
GLYCalcTM, all BTEX measured by
Method 18, 40 CFR part 60, appendix A,
shall be summed.
(d) Control device performance test
procedures. This paragraph applies to
the performance testing of control
devices. The owners or operators shall
demonstrate that a control device
achieves the performance requirements
of § 63.1281(d)(1), (e)(3)(ii), or (f)(1)
using a performance test as specified in
paragraph (d)(3) of this section. Owners
or operators using a condenser have the
option to use a design analysis as
specified in paragraph (d)(4) of this
section. The owner or operator may
elect to use the alternative procedures in
paragraph (d)(5) of this section for
performance testing of a condenser used
to control emissions from a glycol
dehydration unit process vent. As an
alternative to conducting a performance
test under this section for combustion
control devices, a control device that
can be demonstrated to meet the
performance requirements of
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1)
through a performance test conducted
by the manufacturer, as specified in
paragraph (g) of this section, can be
used.
(1) * * *
(i) Except as specified in paragraph
(d)(2) of this section, a flare, as defined
in § 63.1271, that is designed and
operated in accordance with § 63.11(b);
(ii) Except for control devices used for
small glycol dehydration units, a boiler
or process heater with a design heat
input capacity of 44 megawatts or
greater;
(iii) Except for control devices used
for small glycol dehydration units, a
boiler or process heater into which the
vent stream is introduced with the
primary fuel or is used as the primary
fuel;
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(iv) Except for control devices used
for small glycol dehydration units, a
boiler or process heater burning
hazardous waste for which the owner or
operator has either been issued a final
permit under 40 CFR part 270 and
complies with the requirements of 40
CFR part 266, subpart H, or has certified
compliance with the interim status
requirements of 40 CFR part 266,
subpart H;
(v) Except for control devices used for
small glycol dehydration units, a
hazardous waste incinerator for which
the owner or operator has been issued
a final permit under 40 CFR part 270
and complies with the requirements of
40 CFR part 264, subpart O, or has
certified compliance with the interim
status requirements of 40 CFR part 265,
subpart O.
*
*
*
*
*
(2) An owner or operator shall design
and operate each flare, as defined in
§ 63.1271, in accordance with the
requirements specified in § 63.11(b) and
the compliance determination shall be
conducted using Method 22 of 40 CFR
part 60, appendix A, to determine
visible emissions.
(3) For a performance test conducted
to demonstrate that a control device
meets the requirements of
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1) the
owner or operator shall use the test
methods and procedures specified in
paragraphs (d)(3)(i) through (v) of this
section. The initial and periodic
performance tests shall be conducted
according to the schedule specified in
paragraph (d)(3)(vi) of this section.
(i) * * *
(B) To determine compliance with the
enclosed combustion device total HAP
concentration limit specified in
§ 63.1281(d)(1)(i)(B), or the BTEX
emission limit specified in
§ 63.1275(b)(1)(iii), the sampling site
shall be located at the outlet of the
combustion device.
*
*
*
*
*
(iv) * * *
(C) * * *
(1) The emission rate correction factor
for excess air, integrated sampling and
analysis procedures of Method 3A or
3B, 40 CFR part 60, appendix A, shall
be used to determine the oxygen
concentration (%O2d). The samples shall
be taken during the same time that the
samples are taken for determining TOC
concentration or total HAP
concentration.
*
*
*
*
*
(v) To determine compliance with the
BTEX emission limit specified in
§ 63.1281(f)(1) the owner or operator
shall use one of the following methods:
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Method 18, 40 CFR part 60, appendix A;
ASTM D6420–99 (2004), as specified in
§ 63.772(a)(1)(ii); or any other method or
data that have been validated according
to the applicable procedures in Method
301, 40 CFR part 63, appendix A. The
following procedures shall be used to
calculate BTEX emissions:
(A) The minimum sampling time for
each run shall be 1 hour in which either
an integrated sample or a minimum of
four grab samples shall be taken. If grab
sampling is used, then the samples shall
be taken at approximately equal
intervals in time, such as 15-minute
intervals during the run.
(B) The mass rate of BTEX (Eo) shall
be computed using the equations and
procedures specified in paragraphs
(d)(3)(v)(B)(1) and (2) of this section.
(1) The following equation shall be
used:
Where:
Eo = Mass rate of BTEX at the outlet of the
control device, dry basis, kilogram per
hour.
Coj = Concentration of sample component j of
the gas stream at the outlet of the control
device, dry basis, parts per million by
volume.
Moj = Molecular weight of sample component
j of the gas stream at the outlet of the
control device, gram/gram-mole.
Qo = Flowrate of gas stream at the outlet of
the control device, dry standard cubic
meter per minute.
K2 = Constant, 2.494 × 10¥6 (parts per
million) (gram-mole per standard cubic
meter) (kilogram/gram) (minute/hour),
where standard temperature (gram-mole
per standard cubic meter) is 20 degrees
C.
n = Number of components in sample.
(2) When the BTEX mass rate is
calculated, only BTEX compounds
measured by Method 18, 40 CFR part
60, appendix A, or ASTM D6420–99
(2004) as specified in § 63.772(a)(1)(ii),
shall be summed using the equations in
paragraph (d)(3)(v)(B)(1) of this section.
(vi) The owner or operator shall
conduct performance tests according to
the schedule specified in paragraphs
(d)(3)(vi)(A) and (B) of this section.
(A) An initial performance test shall
be conducted within 180 days after the
compliance date that is specified for
each affected source in § 63.1270(d)(3)
and (4) except that the initial
performance test for existing
combustion control devices at existing
major sources shall be conducted no
later than 3 years after the date of
publication of the final rule in the
Federal Register. If the owner or
operator of an existing combustion
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control device at an existing major
source chooses to replace such device
with a control device whose model is
tested under § 63.1282(g), then the
newly installed device shall comply
with all provisions of this subpart no
later than 3 years after the date of
publication of the final rule in the
Federal Register. The performance test
results shall be submitted in the
Notification of Compliance Status
Report as required in § 63.1285(d)(1)(ii).
(B) Periodic performance tests shall be
conducted for all control devices
required to conduct initial performance
tests except as specified in paragraphs
(e)(3)(vi)(B)(1) and (2) of this section.
The first periodic performance test shall
be conducted no later than 60 months
after the initial performance test
required in paragraph (d)(3)(vi)(A) of
this section. Subsequent periodic
performance tests shall be conducted at
intervals no longer than 60 months
following the previous periodic
performance test or whenever a source
desires to establish a new operating
limit. The periodic performance test
results must be submitted in the next
Periodic Report as specified in
§ 63.1285(e)(2)(x). Combustion control
devices meeting the criteria in either
paragraph (e)(3)(vi)(B)(1) or (2) of this
section are not required to conduct
periodic performance tests.
(1) A control device whose model is
tested under, and meets the criteria of,
§ 63.1282(g), or
(2) A combustion control device
tested under § 63.1282(d) that meets the
outlet TOC or HAP performance level
specified in § 63.1281(d)(1)(i)(B) and
that establishes a correlation between
firebox or combustion chamber
temperature and the TOC or HAP
performance level.
*
*
*
*
*
(4) For a condenser design analysis
conducted to meet the requirements of
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1), the
owner or operator shall meet the
requirements specified in paragraphs
(d)(4)(i) and (d)(4)(ii) of this section.
Documentation of the design analysis
shall be submitted as a part of the
Notification of Compliance Status
Report as required in § 63.1285(d)(1)(i).
(i) The condenser design analysis
shall include an analysis of the vent
stream composition, constituent
concentrations, flowrate, relative
humidity, and temperature, and shall
establish the design outlet organic
compound concentration level, design
average temperature of the condenser
exhaust vent stream, and the design
average temperatures of the coolant
fluid at the condenser inlet and outlet.
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As an alternative to the condenser
design analysis, an owner or operator
may elect to use the procedures
specified in paragraph (d)(5) of this
section.
*
*
*
*
*
(5) As an alternative to the procedures
in paragraph (d)(4)(i) of this section, an
owner or operator may elect to use the
procedures documented in the GRI
report entitled, ‘‘Atmospheric Rich/Lean
Method for Determining Glycol
Dehydrator Emissions,’’ (GRI–95/
0368.1) as inputs for the model GRI–
GLYCalcTM, Version 3.0 or higher, to
generate a condenser performance
curve.
(e) Compliance demonstration for
control devices performance
requirements. This paragraph applies to
the demonstration of compliance with
the control device performance
requirements specified in
§ 63.1281(d)(1), (e)(3)(ii), and (f)(1).
Compliance shall be demonstrated using
the requirements in paragraphs (e)(1)
through (3) of this section. As an
alternative, an owner or operator that
installs a condenser as the control
device to achieve the requirements
specified in § 63.1281(d)(1)(ii), (e)(3)(ii),
or (f)(1) may demonstrate compliance
according to paragraph (f) of this
section. An owner or operator may
switch between compliance with
paragraph (e) of this section and
compliance with paragraph (f) of this
section only after at least 1 year of
operation in compliance with the
selected approach. Notification of such
a change in the compliance method
shall be reported in the next Periodic
Report, as required in § 63.1285(e),
following the change.
*
*
*
*
*
(2) The owner or operator shall
calculate the daily average of the
applicable monitored parameter in
accordance with § 63.1283(d)(4) except
that the inlet gas flowrate to the control
device shall not be averaged.
(3) Compliance is achieved when the
daily average of the monitoring
parameter value calculated under
paragraph (e)(2) of this section is either
equal to or greater than the minimum or
equal to or less than the maximum
monitoring value established under
paragraph (e)(1) of this section. For inlet
gas flowrate, compliance with the
operating parameter limit is achieved
when the value is equal to or less than
the value established under
§ 63.1282(g).
(4) Except for periods of monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
and required monitoring system quality
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assurance or quality control activities
(including, as applicable, system
accuracy audits and required zero and
span adjustments), the CMS required in
§ 63.1283(d) must be operated at all
times the affected source is operating. A
monitoring system malfunction is any
sudden, infrequent, not reasonably
preventable failure of the monitoring
system to provide valid data.
Monitoring system failures that are
caused in part by poor maintenance or
careless operation are not malfunctions.
Monitoring system repairs are required
to be completed in response to
monitoring system malfunctions and to
return the monitoring system to
operation as expeditiously as
practicable.
(5) Data recorded during monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
or required monitoring system quality
assurance or control activities may not
be used in calculations used to report
emissions or operating levels. All the
data collected during all other required
data collection periods must be used in
assessing the operation of the control
device and associated control system.
(6) Except for periods of monitoring
system malfunctions, repairs associated
with monitoring system malfunctions,
and required quality monitoring system
quality assurance or quality control
activities (including, as applicable,
system accuracy audits and required
zero and span adjustments), failure to
collect required data is a deviation of
the monitoring requirements.
(f) Compliance demonstration with
percent reduction or emission limit
performance requirements—condensers.
This paragraph applies to the
demonstration of compliance with the
performance requirements specified in
§ 63.1281(d)(1)(ii), (e)(3) or (f)(1) for
condensers. Compliance shall be
demonstrated using the procedures in
paragraphs (f)(1) through (f)(3) of this
section.
(1) The owner or operator shall
establish a site-specific condenser
performance curve according to the
procedures specified in
§ 63.1283(d)(5)(ii). For sources required
to meet the BTEX limit in accordance
with § 63.1281(e) or (f)(1) the owner or
operator shall identify the minimum
percent reduction necessary to meet the
BTEX limit.
(2) Compliance with the percent
reduction requirement in
§ 63.1281(d)(1)(ii), (e)(3), or (f)(1) shall
be demonstrated by the procedures in
paragraphs (f)(2)(i) through (iii) of this
section.
*
*
*
*
*
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(iii) Except as provided in paragraphs
(f)(2)(iii)(A), (B), and (D) of this section,
at the end of each operating day the
owner or operator shall calculate the 30day average HAP, or BTEX, emission
reduction, as appropriate, from the
condenser efficiencies as determined in
paragraph (f)(2)(ii) of this section for the
preceding 30 operating days. If the
owner or operator uses a combination of
process modifications and a condenser
in accordance with the requirements of
§ 63.1281(e), the 30-day average HAP
emission, or BTEX, emission reduction,
shall be calculated using the emission
reduction achieved through process
modifications and the condenser
efficiency as determined in paragraph
(f)(2)(ii) of this section, both for the
preceding 30 operating days.
(A) After the compliance date
specified in § 63.1270(d), an owner or
operator of a facility that stores natural
gas that has less than 30 days of data for
determining the average HAP, or BTEX,
emission reduction, as appropriate,
shall calculate the cumulative average at
the end of the withdrawal season, each
season, until 30 days of condenser
operating data are accumulated. For a
facility that does not store natural gas,
the owner or operator that has less than
30 days of data for determining average
HAP, or BTEX, emission reduction, as
appropriate, shall calculate the
cumulative average at the end of the
calendar year, each year, until 30 days
of condenser operating data are
accumulated.
(B) After the compliance date
specified in § 63.1270(d), for an owner
or operator that has less than 30 days of
data for determining the average HAP,
or BTEX, emission reduction, as
appropriate, compliance is achieved if
the average HAP, or BTEX, emission
reduction, as appropriate, calculated in
paragraph (f)(2)(iii)(A) of this section is
equal to or greater than 95.0 percent.
*
*
*
*
*
(3) Compliance is achieved based on
the applicable criteria in paragraphs
(f)(3)(i) or (ii) of this section.
(i) For sources meeting the HAP
emission reduction specified in
§ 63.1281(d)(1)(ii) or (e)(3) if the average
HAP emission reduction calculated in
paragraph (f)(2)(iii) of this section is
equal to or greater than 95.0 percent.
(ii) For sources required to meet the
BTEX limit under § 63.1281(e)(3) or
(f)(1), compliance is achieved if the
average BTEX emission reduction
calculated in paragraph (f)(2)(iii) of this
section is equal to or greater than the
minimum percent reduction identified
in paragraph (f)(1) of this section.
*
*
*
*
*
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(g) Performance testing for
combustion control devices—
manufacturers’ performance test. (1)
This paragraph applies to the
performance testing of a combustion
control device conducted by the device
manufacturer. The manufacturer shall
demonstrate that a specific model of
control device achieves the performance
requirements in (g)(7) of this section by
conducting a performance test as
specified in paragraphs (g)(2) through
(6) of this section.
(2) Performance testing shall consist
of three one-hour (or longer) test runs
for each of the four following firing rate
settings making a total of 12 test runs
per test. Propene (propylene) gas shall
be used for the testing fuel. All fuel
analyses shall be performed by an
independent third-party laboratory (not
affiliated with the control device
manufacturer or fuel supplier).
(i) 90–100 percent of maximum
design rate (fixed rate).
(ii) 70–100–70 percent (ramp up,
ramp down). Begin the test at 70 percent
of the maximum design rate. Within the
first 5 minutes, ramp the firing rate to
100 percent of the maximum design
rate. Hold at 100 percent for 5 minutes.
In the 10–15 minute time range, ramp
back down to 70 percent of the
maximum design rate. Repeat three
more times for a total of 60 minutes of
sampling.
(iii) 30–70–30 percent (ramp up, ramp
down). Begin the test at 30 percent of
the maximum design rate. Within the
first 5 minutes, ramp the firing rate to
70 percent of the maximum design rate.
Hold at 70 percent for 5 minutes. In the
10–15 minute time range, ramp back
down to 30 percent of the maximum
design rate. Repeat three more times for
a total of 60 minutes of sampling.
(iv) 0–30–0 percent (ramp up, ramp
down). Begin the test at 0 percent of the
maximum design rate. Within the first 5
minutes, ramp the firing rate to 100
percent of the maximum design rate.
Hold at 30 percent for 5 minutes. In the
10–15 minute time range, ramp back
down to 0 percent of the maximum
design rate. Repeat three more times for
a total of 60 minutes of sampling.
(3) All models employing multiple
enclosures shall be tested
simultaneously and with all burners
operational. Results shall be reported for
the each enclosure individually and for
the average of the emissions from all
interconnected combustion enclosures/
chambers. Control device operating data
shall be collected continuously
throughout the performance test using
an electronic Data Acquisition System
and strip chart. Data shall be submitted
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with the test report in accordance with
paragraph (g)(8)(iii) of this section.
(4) Inlet testing shall be conducted as
specified in paragraphs (g)(4)(i) through
(iii) of this section.
(i) The fuel flow metering system
shall be located in accordance with
Method 2A, 40 CFR part 60, appendix
A–1, (or other approved procedure) to
measure fuel flow rate at the control
device inlet location. The fitting for
filling fuel sample containers shall be
located a minimum of 8 pipe diameters
upstream of any inlet fuel flow
monitoring meter.
(ii) Inlet flow rate shall be determined
using Method 2A, 40 CFR part 60,
appendix A–1. Record the start and stop
reading for each 60-minute THC test.
Record the gas pressure and temperature
at 5-minute intervals throughout each
60-minute THC test.
(iii) Inlet fuel sampling shall be
conducted in accordance with the
criteria in paragraphs (g)(4)(iii)(A) and
(B) of this section.
(A) At the inlet fuel sampling
location, securely connect a Silonitecoated stainless steel evacuated canister
fitted with a flow controller sufficient to
fill the canister over a 1 hour period.
Filling shall be conducted as specified
in the following:
(1) Open the canister sampling valve
at the beginning of the total
hydrocarbon (THC) test, and close the
canister at the end of the THC test.
(2) Fill one canister for each THC test
run.
(3) Label the canisters individually
and record on a chain of custody form.
(B) Each fuel sample shall be analyzed
using the following methods. The
results shall be included in the test
report.
(1) Hydrocarbon compounds
containing between one and five atoms
of carbon plus benzene using ASTM
D1945–03.
(2) Hydrogen (H2), carbon monoxide
(CO), carbon dioxide (CO2), nitrogen
(N2), oxygen (O2) using ASTM D1945–
03.
(3) Carbonyl sulfide, carbon disulfide
plus mercaptans using ASTM D5504.
(4) Higher heating value using ASTM
D3588–98 or ASTM D4891–89.
(5) Outlet testing shall be conducted
in accordance with the criteria in
paragraphs (g)(5)(i) through (v) of this
section.
(i) Sampling and flowrate measured in
accordance with the following:
(A) The outlet sampling location shall
be a minimum of 4 equivalent stack
diameters downstream from the highest
peak flame or any other flow
disturbance, and a minimum of one
equivalent stack diameter upstream of
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the exit or any other flow disturbance.
A minimum of two sample ports shall
be used.
(B) Flow rate shall be measured using
Method 1, 40 CFR part 60, Appendix 1,
for determining flow measurement
traverse point location; and Method 2,
40 CFR part 60, Appendix 1, shall be
used to measure duct velocity. If low
flow conditions are encountered (i.e.,
velocity pressure differentials less than
0.05 inches of water) during the
performance test, a more sensitive
manometer shall be used to obtain an
accurate flow profile.
(ii) Molecular weight shall be
determined as specified in paragraphs
(g)(4)(iii)(B), and (g)(5)(ii)(A) and (B) of
this section.
(A) An integrated bag sample shall be
collected during the Method 4, 40 CFR
part 60, Appendix A, moisture test.
Analyze the bag sample using a gas
chromatograph-thermal conductivity
detector (GC–TCD) analysis meeting the
following criteria:
(1) Collect the integrated sample
throughout the entire test, and collect
representative volumes from each
traverse location.
(2) The sampling line shall be purged
with stack gas before opening the valve
and beginning to fill the bag.
(3) The bag contents shall be kneaded
or otherwise vigorously mixed prior to
the GC analysis.
(4) The GC–TCD calibration
procedure in Method 3C, 40 CFR part
60, Appendix A, shall be modified by
using EPAAlt-045 as follows: For the
initial calibration, triplicate injections of
any single concentration must agree
within 5 percent of their mean to be
valid. The calibration response factor for
a single concentration re-check must be
within 10 percent of the original
calibration response factor for that
concentration. If this criterion is not
met, the initial calibration using at least
three concentration levels shall be
repeated.
(B) Report the molecular weight of:
O2, CO2, methane (CH4), and N2 and
include in the test report submitted
under § 63.775(d)(iii). Moisture shall be
determined using Method 4, 40 CFR
part 60, Appendix A. Traverse both
ports with the Method 4, 40 CFR part
60, Appendix A, sampling train during
each test run. Ambient air shall not be
introduced into the Method 3C, 40 CFR
part 60, Appendix A, integrated bag
sample during the port change.
(iv) Carbon monoxide shall be
determined using Method 10, 40 CFR
part 60, Appendix A. The test shall be
run at the same time and with the
sample points used for the EPA Method
25A, 40 CFR part 60, Appendix A,
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testing. An instrument range of 0–10 per
million by volume-dry (ppmvd) shall be
used.
(v) Visible emissions shall be
determined using Method 22, 40 CFR
part 60, Appendix A. The test shall be
performed continuously during each
test run. A digital color photograph of
the exhaust point, taken from the
position of the observer and annotated
with date and time, will be taken once
per test run and the four photos
included in the test report.
(6) Total hydrocarbons (THC) shall be
determined as specified by the
following criteria:
(i) Conduct THC sampling using
Method 25A, 40 CFR part 60, Appendix
A, except the option for locating the
probe in the center 10 percent of the
stack shall not be allowed. The THC
probe must be traversed to 16.7 percent,
50 percent, and 83.3 percent of the stack
diameter during the testing.
(ii) A valid test shall consist of three
Method 25A, 40 CFR part 60, Appendix
A, tests, each no less than 60 minutes
in duration.
(iii) A 0–10 parts per million by
volume-wet (ppmvw) (as propane)
measurement range is preferred; as an
alternative a 0–30 ppmvw (as carbon)
measurement range may be used.
(iv) Calibration gases will be propane
in air and be certified through EPA
Protocol 1—‘‘EPA Traceability Protocol
for Assay and Certification of Gaseous
Calibration Standards,’’ September
1997, as amended August 25, 1999,
EPA–600/R–97/121 (or more recent if
updated since 1999).
(v) THC measurements shall be
reported in terms of ppmvw as propane.
(vi) THC results shall be corrected to
3 percent CO2, as measured by Method
3C, 40 CFR part 60, Appendix A.
(vii) Subtraction of methane/ethane
from the THC data is not allowed in
determining results.
(7) Performance test criteria:
(i) The control device model tested
must meet the criteria in paragraphs
(g)(7)(i)(A) through (C) of this section:
(A) Method 22, 40 CFR part 60,
Appendix A, results under paragraph
(g)(5)(v) of this section with no
indication of visible emissions, and
(B) Average Method 25A, 40 CFR part
60, Appendix A, results under
paragraph (g)(6) of this section equal to
or less than 10.0 ppmvw THC as
propane corrected to 3.0 percent CO2,
and
(C) Average CO emissions determined
under paragraph (g)(5)(iv) of this section
equal to or less than 10 parts ppmvd,
corrected to 3.0 percent CO2.
(ii) The manufacturer shall determine
a maximum inlet gas flow rate which
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shall not be exceeded for each control
device model to achieve the criteria in
paragraph (g)(7)(i) of this section.
(iii) A control device meeting the
criteria in paragraph (g)(7)(i)(A) through
(C) of this section will have
demonstrated a destruction efficiency of
98.0 percent for HAP regulated under
this subpart.
(8) The owner or operator of a
combustion control device model tested
under this section shall submit the
information listed in paragraphs (g)(8)(i)
through (iii) in the test report required
under § 63.775(d)(1)(iii).
(i) Full schematic of the control
device and dimensions of the device
components.
(ii) Design net heating value
(minimum and maximum) of the device.
(iii) Test fuel gas flow range (in both
mass and volume). Include the
minimum and maximum allowable inlet
gas flow rate.
(iv) Air/stream injection/assist ranges,
if used.
(v) The test parameter ranges listed in
paragraphs (g)(8)(v)(A) through (O) of
this section, as applicable for the tested
model.
(A) Fuel gas delivery pressure and
temperature.
(B) Fuel gas moisture range.
(C) Purge gas usage range.
(D) Condensate (liquid fuel)
separation range.
(E) Combustion zone temperature
range. This is required for all devices
that measure this parameter.
(F) Excess combustion air range.
(G) Flame arrestor(s).
(H) Burner manifold pressure.
(I) Pilot flame sensor.
(J) Pilot flame design fuel and fuel
usage.
(K) Tip velocity range.
(L) Momentum flux ratio.
(M) Exit temperature range.
(N) Exit flow rate.
(O) Wind velocity and direction.
(vi) The test report shall include all
calibration quality assurance/quality
control data, calibration gas values, gas
cylinder certification, and strip charts
annotated with test times and
calibration values.
(h) Compliance demonstration for
combustion control devices—
manufacturers’ performance test. This
paragraph applies to the demonstration
of compliance for a combustion control
device tested under the provisions in
paragraph (g) of this section. Owners or
operators shall demonstrate that a
control device achieves the performance
requirements of § 63.1281(d)(1), (e)(3)(ii)
or (f)(1), by installing a device tested
under paragraph (g) of this section and
complying with the following criteria:
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(1) The inlet gas flow rate shall meet
the range specified by the manufacturer.
Flow rate shall be measured as specified
in § 63.1283(d)(3)(i)(H)(1).
(2) A pilot flame shall be present at all
times of operation. The pilot flame shall
be monitored in accordance with
§ 63.1283(d)(3)(i)(H)(2).
(3) Devices shall be operated with no
visible emissions, except for periods not
to exceed a total of 5 minutes during
any 2 consecutive hours. A visible
emissions test using Method 22, 40 CFR
part 60, Appendix A, shall be performed
monthly. The observation period shall
be 2 hours and shall be used according
to Method 22.
(4) Compliance with the operating
parameter limit is achieved when the
following criteria are met:
(i) The inlet gas flow rate monitored
under paragraph (h)(1) of this section is
equal to or below the maximum
established by the manufacturer; and
(ii) The pilot flame is present at all
times; and
(iii) During the visible emissions test
performed under paragraph (h)(3) of this
section the duration of visible emissions
does not exceed a total of 5 minutes
during the observation period. Devices
failing the visible emissions test shall
follow the requirements in paragraphs
(h)(4)(iii)(A) and (B) of this section.
(A) Following the first failure, the fuel
nozzle(s) and burner tubes shall be
replaced.
(B) If, following replacement of the
fuel nozzle(s) and burner tubes as
specified in paragraph (h)(4)(iii)(A), the
visible emissions test is not passed in
the next scheduled test, either a
performance test shall be performed
under paragraph (d) of this section, or
the device shall be replaced with
another control device whose model
was tested, and meets, the requirements
in paragraph (g) of this section.
30. Section 63.1283 is amended by:
a. Adding paragraph (b);
b. Revising paragraph (d)(1)
introductory text;
c. Revising paragraph (d)(1)(ii) and
adding paragraphs (d)(1)(iii) and (iv);
d. Revising paragraph (d)(2)(i) and
(d)(2)(ii);
e. Revising paragraphs (d)(3)(i)(A) and
(B);
f. Revising paragraphs (d)(3)(i)(D) and
(E);
g. Revising paragraphs (d)(3)(i)(F)(1)
and (2);
h. Revising paragraph (d)(3)(i)(G);
i. Adding paragraph (d)(3)(i)(H);
j. Revising paragraph (d)(4);
k. Revising paragraph (d)(5)(i);
l. Revising paragraphs (d)(5)(ii)(A)
through (C);
m. Revising paragraph (d)(6)
introductory text;
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n. Revising paragraph (d)(6)(ii);
o. Adding paragraph (d)(6)(v);
p. Revising paragraph (d)(8)(i)(A); and
q. Revising paragraph (d)(8)(ii) to read
as follows:
§ 63.1283 Inspection and monitoring
requirements.
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(b) The owner or operator of a control
device whose model was tested under
63.1282(g) shall develop an inspection
and maintenance plan for each control
device. At a minimum, the plan shall
contain the control device
manufacturer’s recommendations for
ensuring proper operation of the device.
Semi-annual inspections shall be
conducted for each control device with
maintenance and replacement of control
device components made in accordance
with the plan.
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(d) Control device monitoring
requirements. (1) For each control
device except as provided for in
paragraph (d)(2) of this section, the
owner or operator shall install and
operate a continuous parameter
monitoring system in accordance with
the requirements of paragraphs (d)(3)
through (9) of this section. Owners or
operators that install and operate a flare
in accordance with § 63.1281(d)(1)(iii)
or (f)(1)(iii) are exempt from the
requirements of paragraphs (d)(4) and
(5) of this section. The continuous
monitoring system shall be designed
and operated so that a determination
can be made on whether the control
device is achieving the applicable
performance requirements of
§ 63.1281(d), (e)(3), or (f)(1). Each
continuous parameter monitoring
system shall meet the following
specifications and requirements:
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*
(ii) A site-specific monitoring plan
must be prepared that addresses the
monitoring system design, data
collection, and the quality assurance
and quality control elements outlined in
paragraph (d) of this section and in
§ 63.8(d). Each CPMS must be installed,
calibrated, operated, and maintained in
accordance with the procedures in your
approved site-specific monitoring plan.
Using the process described in
§ 63.8(f)(4), you may request approval of
monitoring system quality assurance
and quality control procedures
alternative to those specified in
paragraphs (d)(1)(ii)(A) through (E) of
this section in your site-specific
monitoring plan.
(A) The performance criteria and
design specifications for the monitoring
system equipment, including the sample
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52837
interface, detector signal analyzer, and
data acquisition and calculations;
(B) Sampling interface (e.g.,
thermocouple) location such that the
monitoring system will provide
representative measurements;
(C) Equipment performance checks,
system accuracy audits, or other audit
procedures;
(D) Ongoing operation and
maintenance procedures in accordance
with provisions in § 63.8(c)(1) and
(c)(3); and
(E) Ongoing reporting and
recordkeeping procedures in accordance
with provisions in § 63.10(c), (e)(1), and
(e)(2)(i).
(iii) The owner or operator must
conduct the CPMS equipment
performance checks, system accuracy
audits, or other audit procedures
specified in the site-specific monitoring
plan at least once every 12 months.
(iv) The owner or operator must
conduct a performance evaluation of
each CPMS in accordance with the sitespecific monitoring plan.
(2) * * *
(i) Except for control devices for small
glycol dehydration units, a boiler or
process heater in which all vent streams
are introduced with the primary fuel or
are used as the primary fuel;
(ii) Except for control devices for
small glycol dehydration units, a boiler
or process heater with a design heat
input capacity equal to or greater than
44 megawatts.
(3) * * *
(i) * * *
(A) For a thermal vapor incinerator
that demonstrates during the
performance test conducted under
§ 63.1282(d) that combustion zone
temperature is an accurate indicator of
performance, a temperature monitoring
device equipped with a continuous
recorder. The monitoring device shall
have a minimum accuracy of ± 1 percent
of the temperature being monitored in
degrees C, or ± 2.5 degrees C, whichever
value is greater. The temperature sensor
shall be installed at a location
representative of the combustion zone
temperature.
(B) For a catalytic vapor incinerator,
a temperature monitoring device
equipped with a continuous recorder.
The device shall be capable of
monitoring temperatures at two
locations and have a minimum accuracy
of ± 1 percent of the temperatures being
monitored in degrees C, or ± 2.5 degrees
C, whichever value is greater. One
temperature sensor shall be installed in
the vent stream at the nearest feasible
point to the catalyst bed inlet and a
second temperature sensor shall be
installed in the vent stream at the
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nearest feasible point to the catalyst bed
outlet.
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(D) For a boiler or process heater, a
temperature monitoring device
equipped with a continuous recorder.
The temperature monitoring device
shall have a minimum accuracy of ± 1
percent of the temperature being
monitored in degrees C, or ± 2.5 degrees
C, whichever value is greater. The
temperature sensor shall be installed at
a location representative of the
combustion zone temperature.
(E) For a condenser, a temperature
monitoring device equipped with a
continuous recorder. The temperature
monitoring device shall have a
minimum accuracy of ± 1 percent of the
temperature being monitored in degrees
C, or ± 2.8 degrees C, whichever value
is greater. The temperature sensor shall
be installed at a location in the exhaust
vent stream from the condenser.
(F) * * *
(1) A continuous parameter
monitoring system to measure and
record the average total regeneration
stream mass flow or volumetric flow
during each carbon bed regeneration
cycle. The flow sensor must have a
measurement sensitivity of 5 percent of
the flow rate or 10 cubic feet per
minute, whichever is greater. The
mechanical connections for leakage
must be checked at least every month,
and a visual inspection must be
performed at least every 3 months of all
components of the flow CPMS for
physical and operational integrity and
all electrical connections for oxidation
and galvanic corrosion if your flow
CPMS is not equipped with a redundant
flow sensor; and
(2) A continuous parameter
monitoring system to measure and
record the average carbon bed
temperature for the duration of the
carbon bed steaming cycle and to
measure the actual carbon bed
temperature after regeneration and
within 15 minutes of completing the
cooling cycle. The temperature
monitoring device shall have a
minimum accuracy of ± 1 percent of the
temperature being monitored in degrees
C, or ± 2.5 degrees C, whichever value
is greater.
(G) For a nonregenerative-type carbon
adsorption system, the owner or
operator shall monitor the design carbon
replacement interval established using a
performance test performed in
accordance with § 63.1282(d)(3) and
shall be based on the total carbon
working capacity of the control device
and source operating schedule.
(H) For a control device whose model
is tested under § 63.1282(g):
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(1) A continuous monitoring system
that measures gas flow rate at the inlet
to the control device. The monitoring
instrument shall have an accuracy of
plus or minus 2 percent or better.
(2) A heat sensing monitoring device
equipped with a continuous recorder
that indicates the continuous ignition of
the pilot flame.
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(4) Using the data recorded by the
monitoring system, except for inlet gas
flowrate, the owner or operator must
calculate the daily average value for
each monitored operating parameter for
each operating day. If the emissions unit
operation is continuous, the operating
day is a 24-hour period. If the emissions
unit operation is not continuous, the
operating day is the total number of
hours of control device operation per
24-hour period. Valid data points must
be available for 75 percent of the
operating hours in an operating day to
compute the daily average.
(5) * * *
(i) The owner or operator shall
establish a minimum operating
parameter value or a maximum
operating parameter value, as
appropriate for the control device, to
define the conditions at which the
control device must be operated to
continuously achieve the applicable
performance requirements of
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1). Each
minimum or maximum operating
parameter value shall be established as
follows:
(A) If the owner or operator conducts
performance tests in accordance with
the requirements of § 63.1282(d)(3) to
demonstrate that the control device
achieves the applicable performance
requirements specified in
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1), then
the minimum operating parameter value
or the maximum operating parameter
value shall be established based on
values measured during the
performance test and supplemented, as
necessary, by a condenser design
analysis or control device
manufacturer’s recommendations or a
combination of both.
(B) If the owner or operator uses a
condenser design analysis in accordance
with the requirements of § 63.1282(d)(4)
to demonstrate that the control device
achieves the applicable performance
requirements specified in
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1), then
the minimum operating parameter value
or the maximum operating parameter
value shall be established based on the
condenser design analysis and may be
supplemented by the condenser
manufacturer’s recommendations.
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(C) If the owner or operator operates
a control device where the performance
test requirement was met under
§ 63.1282(g) to demonstrate that the
control device achieves the applicable
performance requirements specified in
§ 63.1281(d)(1), (e)(3)(ii) or (f)(1), then
the maximum inlet gas flow rate shall be
established based on the performance
test and supplemented, as necessary, by
the manufacturer recommendations.
(ii) * * *
(A) If the owner or operator conducts
a performance test in accordance with
the requirements of § 63.1282(d)(3) to
demonstrate that the condenser achieves
the applicable performance
requirements in § 63.1281(d)(1),
(e)(3)(ii), or (f)(1), then the condenser
performance curve shall be based on
values measured during the
performance test and supplemented as
necessary by control device design
analysis, or control device
manufacturer’s recommendations, or a
combination or both.
(B) If the owner or operator uses a
control device design analysis in
accordance with the requirements of
§ 63.1282(d)(4)(i) to demonstrate that
the condenser achieves the applicable
performance requirements specified in
§ 63.1281(d)(1), (e)(3)(ii), or (f)(1), then
the condenser performance curve shall
be based on the condenser design
analysis and may be supplemented by
the control device manufacturer’s
recommendations.
(C) As an alternative to paragraph
(d)(5)(ii)(B) of this section, the owner or
operator may elect to use the procedures
documented in the GRI report entitled,
‘‘Atmospheric Rich/Lean Method for
Determining Glycol Dehydrator
Emissions’’ (GRI–95/0368.1) as inputs
for the model GRI–GLYCalcTM, Version
3.0 or higher, to generate a condenser
performance curve.
(6) An excursion for a given control
device is determined to have occurred
when the monitoring data or lack of
monitoring data result in any one of the
criteria specified in paragraphs (d)(6)(i)
through (d)(6)(v) of this section being
met. When multiple operating
parameters are monitored for the same
control device and during the same
operating day, and more than one of
these operating parameters meets an
excursion criterion specified in
paragraphs (d)(6)(i) through (d)(6)(iv) of
this section, then a single excursion is
determined to have occurred for the
control device for that operating day.
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(ii) For sources meeting
§ 63.1281(d)(1)(ii), an excursion occurs
when average condenser efficiency
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calculated according to the
requirements specified in
§ 63.1282(f)(2)(iii) is less than 95.0
percent, as specified in § 63.1282(f)(3).
For sources meeting § 63.1281(f)(1), an
excursion occurs when the 30-day
average condenser efficiency calculated
according to the requirements of
§ 63.1282(f)(2)(iii) is less than the
identified 30-day required percent
reduction.
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(v) For control device whose model is
tested under § 63.1282(g) an excursion
occurs when:
(A) The inlet gas flow rate exceeds the
maximum established during the test
conducted under § 63.1282(g).
(B) Failure of the monthly visible
emissions test conducted under
§ 63.1282(h)(3) occurs.
(8) * * *
(i) * * *
(A) During a malfunction when the
affected facility is operated during such
period in accordance with § 63.6(e)(1);
or
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(ii) For each control device, or
combinations of control devices,
installed on the same emissions unit,
one excused excursion is allowed per
semiannual period for any reason. The
initial semiannual period is the 6-month
reporting period addressed by the first
Periodic Report submitted by the owner
or operator in accordance with
§ 63.1285(e) of this subpart.
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31. Section 63.1284 is amended by:
a. Revising paragraph (b)(3)
introductory text;
b. Removing and reserving paragraph
(b)(3)(ii);
c. Revising paragraph (b)(4)(ii);
d. Adding paragraph (b)(7)(ix); and
e. Adding paragraph (f), (g) and (h) to
read as follows:
§ 63.1284
Recordkeeping requirements.
emcdonald on DSK2BSOYB1PROD with PROPOSALS2
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(b) * * *
(3) Records specified in § 63.10(c) for
each monitoring system operated by the
owner or operator in accordance with
the requirements of § 63.1283(d).
Notwithstanding the previous sentence,
monitoring data recorded during
periods identified in paragraphs (b)(3)(i)
through (iv) of this section shall not be
included in any average or percent leak
rate computed under this subpart.
Records shall be kept of the times and
durations of all such periods and any
other periods during process or control
device operation when monitors are not
operating or failed to collect required
data.
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(ii) [Reserved]
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(4) * * *
(ii) Records of the daily average value
of each continuously monitored
parameter for each operating day
determined according to the procedures
specified in § 63.1283(d)(4) of this
subpart, except as specified in
paragraphs (b)(4)(ii)(A) through (C) of
this section.
(A) For flares, the records required in
paragraph (e) of this section.
(B) For condensers installed to
comply with § 63.1275, records of the
annual 30-day rolling average condenser
efficiency determined under § 63.1282(f)
shall be kept in addition to the daily
averages.
(C) For a control device whose model
is tested under § 63.1282(g), the records
required in paragraph (g) of this section.
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(7) * * *
(ix) Records identifying the carbon
replacement schedule under
§ 63.1281(d)(5) and records of each
carbon replacement.
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(f) The owner or operator of an
affected source subject to this subpart
shall maintain records of the occurrence
and duration of each malfunction of
operation (i.e., process equipment) or
the air pollution control equipment and
monitoring equipment. The owner or
operator shall maintain records of
actions taken during periods of
malfunction to minimize emissions in
accordance with § 63.1274(a), including
corrective actions to restore
malfunctioning process and air
pollution control and monitoring
equipment to its normal or usual
manner of operation.
(g) Record the following when using
a control device whose model is tested
under § 63.1282(g) to comply with
§ 63.1281(d), (e)(3)(ii) and (f)(1):
(1) All visible emission readings and
flowrate measurements made during the
compliance determination required by
§ 63.1282(h); and
(2) All hourly records and other
recorded periods when the pilot flame
is absent.
(h) The date the semi-annual
maintenance inspection required under
§ 63.1283(b) is performed. Include a list
of any modifications or repairs made to
the control device during the inspection
and other maintenance performed such
as cleaning of the fuel nozzles.
32. Section 63.1285 is amended by:
a. Revising paragraph (b)(1);
b. Revising paragraph (b)(6);
c. Removing paragraph (b)(7);
d. Revising paragraph (d)(1)
introductory text;
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e. Revising paragraph (d)(1)(i);
f. Revising paragraph (d)(1)(ii)
introductory text;
g. Revising paragraph (d)(2)
introductory text;
h. Revising paragraph (d)(4)(ii);
i. Adding paragraph (d)(4)(iv);
j. Revising paragraph (d)(10);
k. Adding paragraphs (d)(11) and
(d)(12);
l. Revising paragraph (e)(2)
introductory text;
m. Revising paragraph (e)(2)(ii)(B);
n. Adding paragraphs (e)(2)(ii)(D) and
(E);
o. Adding paragraphs (e)(2)(x), (xi)
and (xii); and
p. Adding paragraph (g) to read as
follows:
§ 63.1285
Reporting requirements.
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(b) * * *
(1) The initial notifications required
for existing affected sources under
§ 63.9(b)(2) shall be submitted as
provided in paragraphs (b)(1)(i) and (ii)
of this section.
(i) Except as otherwise provided in
paragraph (b)(1)(ii) of this section, the
initial notification shall be submitted by
1 year after an affected source becomes
subject to the provisions of this subpart
or by June 17, 2000, whichever is later.
Affected sources that are major sources
on or before June 17, 2000 and plan to
be area sources by June 17, 2002 shall
include in this notification a brief,
nonbinding description of a schedule
for the action(s) that are planned to
achieve area source status.
(ii) An affected source identified
under § 63.1270(d)(3) shall submit an
initial notification required for existing
affected sources under § 63.9(b)(2)
within 1 year after the affected source
becomes subject to the provisions of this
subpart or by one year after publication
of the final rule in the Federal Register,
whichever is later. An affected source
identified under § 63.1270(d)(3) that
plans to be an area source by three years
after publication of the final rule in the
Federal Register, shall include in this
notification a brief, nonbinding
description of a schedule for the
action(s) that are planned to achieve
area source status.
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*
*
*
*
(6) If there was a malfunction during
the reporting period, the Periodic Report
specified in paragraph (e) of this section
shall include the number, duration, and
a brief description for each type of
malfunction which occurred during the
reporting period and which caused or
may have caused any applicable
emission limitation to be exceeded. The
report must also include a description of
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actions taken by an owner or operator
during a malfunction of an affected
source to minimize emissions in
accordance with § 63.1274(h), including
actions taken to correct a malfunction.
*
*
*
*
*
(d) * * *
(1) If a closed-vent system and a
control device other than a flare are
used to comply with § 63.1274, the
owner or operator shall submit the
information in paragraph (d)(1)(iii) of
this section and the information in
either paragraph (d)(1)(i) or (ii) of this
section.
(i) The condenser design analysis
documentation specified in
§ 63.1282(d)(4) of this subpart if the
owner or operator elects to prepare a
design analysis; or
(ii) If the owner or operator is
required to conduct a performance test,
the performance test results including
the information specified in paragraphs
(d)(1)(ii)(A) and (B) of this section.
Results of a performance test conducted
prior to the compliance date of this
subpart can be used provided that the
test was conducted using the methods
specified in § 63.1282(d)(3), and that the
test conditions are representative of
current operating conditions. If the
owner or operator operates a
combustion control device model tested
under § 63.1282(g), an electronic copy of
the performance test results shall be
submitted via e-mail to
Oil_and_Gas_PT@EPA.GOV.
*
*
*
*
*
(2) If a closed-vent system and a flare
are used to comply with § 63.1274, the
owner or operator shall submit
performance test results including the
information in paragraphs (d)(2)(i) and
(ii) of this section. The owner or
operator shall also submit the
information in paragraph (d)(2)(iii) of
this section.
*
*
*
*
*
(4) * * *
(ii) An explanation of the rationale for
why the owner or operator selected each
of the operating parameter values
established in § 63.1283(d)(5) of this
subpart. This explanation shall include
any data and calculations used to
develop the value, and a description of
why the chosen value indicates that the
control device is operating in
accordance with the applicable
requirements of § 63.1281(d)(1),
(e)(3)(ii), or (f)(1).
*
*
*
*
*
(iv) For each carbon adsorber, the
predetermined carbon replacement
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schedule as required in
§ 63.1281(d)(5)(i).
*
*
*
*
*
(10) The owner or operator shall
submit the analysis prepared under
§ 63.1281(e)(2) to demonstrate that the
conditions by which the facility will be
operated to achieve the HAP emission
reduction of 95.0 percent, or the BTEX
limit in § 63.1275(b)(1)(iii) through
process modifications or a combination
of process modifications and one or
more control devices.
(11) If the owner or operator installs
a combustion control device model
tested under the procedures in
§ 63.1282(g), the data listed under
§ 63.1282(g)(8).
(12) For each combustion control
device model tested under § 63.1282(g),
the information listed in paragraphs
(d)(12)(i) through (vi) of this section.
(i) Name, address and telephone
number of the control device
manufacturer.
(ii) Control device model number.
(iii) Control device serial number.
(iv) Date of control device
certification test.
(v) Manufacturer’s HAP destruction
efficiency rating.
(vi) Control device operating
parameters, maximum allowable inlet
gas flowrate.
*
*
*
*
*
(e) * * *
(2) The owner or operator shall
include the information specified in
paragraphs (e)(2)(i) through (xii) of this
section, as applicable.
*
*
*
*
*
(ii) * * *
(B) For each excursion caused when
the 30-day average condenser control
efficiency is less than the value, as
specified in § 63.1283(d)(6)(ii), the
report must include the 30-day average
values of the condenser control
efficiency, and the date and duration of
the period that the excursion occurred.
*
*
*
*
*
(D) For each excursion caused when
the maximum inlet gas flow rate
identified under § 63.1282(g) is
exceeded, the report must include the
values of the inlet gas identified and the
date and duration of the period that the
excursion occurred.
(E) For each excursion caused when
visible emissions determined under
§ 63.1282(h) exceed the maximum
allowable duration, the report must
include the date and duration of the
period that the excursion occurred.
*
*
*
*
*
(x) The results of any periodic test as
required in § 63.1282(d)(3) conducted
during the reporting period.
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(xi) For each carbon adsorber used to
meet the control device requirements of
§ 63.1281(d)(1), records of each carbon
replacement that occurred during the
reporting period.
(xii) For combustion control device
inspections conducted in accordance
with § 63.1283(b) the records specified
in § 63.1284(h).
*
*
*
*
*
(g) Electronic reporting. (1) As of
January 1, 2012, and within 60 days
after the date of completing each
performance test, as defined in § 63.2
and as required in this subpart, you
must submit performance test data,
except opacity data, electronically to the
EPA’s Central Data Exchange (CDX) by
using the Electronic Reporting Tool
(ERT) (see https://www.epa.gov/ttn/chief/
ert/ert_tool.html/). Only data collected
using test methods compatible with ERT
are subject to this requirement to be
submitted electronically into the EPA’s
WebFIRE database.
(2) All reports required by this
subpart not subject to the requirements
in paragraphs (g)(1) of this section must
be sent to the Administrator at the
appropriate address listed in § 63.13. If
acceptable to both the Administrator
and the owner or operator of a source,
these reports may be submitted on
electronic media. The Administrator
retains the right to require submittal of
reports subject to paragraph (g)(1) of this
section in paper format.
33. Section 63.1287 is amended by
revising paragraph (a) to read as follows:
§ 63.1287 Alternative means of emission
limitation.
(a) If, in the judgment of the
Administrator, an alternative means of
emission limitation will achieve a
reduction in HAP emissions at least
equivalent to the reduction in HAP
emissions from that source achieved
under the applicable requirements in
§§ 63.1274 through 63.1281, the
Administrator will publish a notice in
the Federal Register permitting the use
of the alternative means for purposes of
compliance with that requirement. The
notice may condition the permission on
requirements related to the operation
and maintenance of the alternative
means.
*
*
*
*
*
34. Appendix to Subpart HHH of Part
63—Table is amended by revising Table
2 to read as follows:
Appendix to Subpart HHH of Part 63—
Tables
*
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*
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*
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52841
TABLE 2 TO SUBPART HHH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART HHH
Applicable to
subpart HHH
§ 63.1(a)(1) ................................................
§ 63.1(a)(2) ................................................
§ 63.1(a)(3) ................................................
§ 63.1(a)(4) ................................................
§ 63.1(a)(5) ................................................
§ 63.1(a)(6) through (a)(8) .........................
§ 63.1(a)(9) ................................................
§ 63.1(a)(10) ..............................................
§ 63.1(a)(11) ..............................................
§ 63.1(a)(12) through (a)(14) .....................
§ 63.1(b)(1) ................................................
§ 63.1(b)(2) ................................................
§ 63.1(b)(3) ................................................
§ 63.1(c)(1) ................................................
§ 63.1(c)(2) ................................................
§ 63.1(c)(3) ................................................
§ 63.1(c)(4) ................................................
§ 63.1(c)(5) ................................................
§ 63.1(d) .....................................................
§ 63.1(e) .....................................................
§ 63.2 .........................................................
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes.
Yes.
No .................
Yes.
No.
No .................
No.
No .................
Yes.
Yes.
No .................
Yes.
Yes ................
§ 63.3(a) through (c) ..................................
§ 63.4(a)(1) through (a)(3) .........................
§ 63.4(a)(4) ................................................
§ 63.4(a)(5) ................................................
§ 63.4(b) .....................................................
§ 63.4(c) .....................................................
§ 63.5(a)(1) ................................................
§ 63.5(a)(2) ................................................
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Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
No .................
§ 63.5(b)(1) ................................................
§ 63.5(b)(2) ................................................
§ 63.5(b)(3) ................................................
§ 63.5(b)(4) ................................................
§ 63.5(b)(5) ................................................
§ 63.5(b)(6) ................................................
§ 63.5(c) .....................................................
§ 63.5(d)(1) ................................................
§ 63.5(d)(2) ................................................
§ 63.5(d)(3) ................................................
§ 63.5(d)(4) ................................................
§ 63.5(e) .....................................................
§ 63.5(f)(1) .................................................
§ 63.5(f)(2) .................................................
§ 63.6(a) .....................................................
§ 63.6(b)(1) ................................................
§ 63.6(b)(2) ................................................
§ 63.6(b)(3) ................................................
§ 63.6(b)(4) ................................................
§ 63.6(b)(5) ................................................
§ 63.6(b)(6) ................................................
§ 63.6(b)(7) ................................................
§ 63.6(c)(1) ................................................
§ 63.6(c)(2) ................................................
§ 63.6(c)(3) and (c)(4) ...............................
§ 63.6(c)(5) ................................................
§ 63.6(d) .....................................................
§ 63.6(e) .....................................................
§ 63.6(e) .....................................................
§ 63.6(e)(1)(i) .............................................
§ 63.6(e)(1)(ii) ............................................
§ 63.6(e)(1)(iii) ...........................................
§ 63.6(e)(2) ................................................
§ 63.6(e)(3) ................................................
§ 63.6(f)(1) .................................................
§ 63.6(f)(2) .................................................
§ 63.6(f)(3) .................................................
§ 63.6(g) .....................................................
§ 63.6(h) .....................................................
§ 63.6(i)(1) through (i)(14) .........................
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
No .................
Yes.
No .................
Yes.
Yes ................
No .................
No.
Yes.
Yes.
No.
No.
Yes.
Yes.
Yes.
No .................
Yes.
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Explanation
Section reserved.
Section reserved.
Subpart HHH specifies applicability.
Subpart HHH specifies applicability.
Section reserved.
Section reserved.
Except definition of major source is unique for this source category and there are
additional definitions in subpart HHH.
Section reserved.
Preconstruction review required only for major sources that commence construction
after promulgation of the standard.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
Section reserved.
Except as otherwise specified.
See § 63.1274(h) for general duty requirement.
Subpart HHH does not contain opacity or visible emission standards.
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TABLE 2 TO SUBPART HHH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART
HHH—Continued
Applicable to
subpart HHH
§ 63.6(i)(15) ...............................................
§ 63.6(i)(16) ...............................................
§ 63.6(j) ......................................................
§ 63.7(a)(1) ................................................
§ 63.7(a)(2) ................................................
No .................
Yes.
Yes.
Yes.
Yes ................
§ 63.7(a)(3) ................................................
§ 63.7(b) .....................................................
§ 63.7(c) .....................................................
§ 63.7(d) .....................................................
§ 63.7(e)(1) ................................................
§ 63.7(e)(2) ................................................
§ 63.7(e)(3) ................................................
§ 63.7(e)(4) ................................................
§ 63.7(f) ......................................................
§ 63.7(g) .....................................................
§ 63.7(h) .....................................................
§ 63.8(a)(1) ................................................
§ 63.8(a)(2) ................................................
§ 63.8(a)(3) ................................................
§ 63.8(a)(4) ................................................
§ 63.8(b)(1) ................................................
§ 63.8(b)(2) ................................................
§ 63.8(b)(3) ................................................
§ 63.8(c)(1) ................................................
63.8(c)(1)(i) ................................................
§ 63.8(c)(1)(ii) ............................................
§ 63.8(c)(1)(iii) ............................................
§ 63.8(c)(2) ................................................
§ 63.8(c)(3) ................................................
§ 63.8(c)(4) ................................................
§ 63.8(c)(5) through (c)(8) .........................
§ 63.8(d) .....................................................
§ 63.8(d)(3) ................................................
§ 63.8(e) .....................................................
Yes.
Yes.
Yes.
Yes.
No.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
No.
Yes.
Pending.
Yes.
Yes.
No.
Yes.
Yes.
Yes ................
Yes ................
§ 63.8(f)(1) through (f)(5) ...........................
§ 63.8(f)(6) .................................................
§ 63.8(g) .....................................................
§ 63.9(a) .....................................................
§ 63.9(b)(1) ................................................
§ 63.9(b)(2) ................................................
§ 63.9(b)(3) ................................................
§ 63.9(b)(4) ................................................
§ 63.9(b)(5) ................................................
§ 63.9(c) .....................................................
§ 63.9(d) .....................................................
§ 63.9(e) .....................................................
§ 63.9(f) ......................................................
§ 63.9(g) .....................................................
§ 63.9(h)(1) through (h)(3) .........................
§ 63.9(h)(4) ................................................
§ 63.9(h)(5) and (h)(6) ...............................
§ 63.9(i) ......................................................
§ 63.9(j) ......................................................
§ 63.10(a) ...................................................
§ 63.10(b)(1) ..............................................
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Yes.
No .................
No .................
Yes.
Yes.
Yes ................
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No.
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes ................
§ 63.10(b)(2) ..............................................
§ 63.10(b)(2)(i) ...........................................
§ 63.10(b)(2)(ii) ..........................................
Yes.
No.
No .................
§ 63.10(b)(2)(iii) .........................................
§ 63.10(b)(2)(iv) through (b)(2)(v) ..............
§ 63.10(b)(2)(vi) through (b)(2)(xiv) ...........
§ 63.10(b)(3) ..............................................
§ 63.10(c)(1) ..............................................
§ 63.10(c)(2) through (c)(4) .......................
§ 63.10(c)(5) through (c)(8) .......................
§ 63.10(c)(9) ..............................................
Yes.
No.
Yes.
No.
Yes.
No .................
Yes.
No .................
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Explanation
Section reserved.
But the performance test results must be submitted within 180 days after the compliance date.
Section reserved.
Except for last sentence, which refers to an SSM plan. SSM plans are not required.
Subpart HHH does not specifically require continuous emissions monitor performance evaluations, however, the Administrator can request that one be conducted.
Subpart HHH does not require continuous emissions monitoring.
Subpart HHH specifies continuous monitoring system data reduction requirements.
Existing sources are given 1 year (rather than 120 days) to submit this notification.
Section reserved.
Section 63.1284(b)(1) requires sources to maintain the most recent 12 months of
data on-site and allows offsite storage for the remaining 4 years of data.
See § 63.1284(f) for recordkeeping of occurrence, duration, and actions taken during malfunction.
Sections reserved.
Section reserved.
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52843
TABLE 2 TO SUBPART HHH OF PART 63—APPLICABILITY OF 40 CFR PART 63 GENERAL PROVISIONS TO SUBPART
HHH—Continued
General provisions reference
Applicable to
subpart HHH
§ 63.10(c)(10) and (c)(11) ..........................
§ 63.10(c)(12) through (c)(14) ...................
§ 63.10(c)(15) ............................................
§ 63.10(d)(1) ..............................................
§ 63.10(d)(2) ..............................................
§ 63.10(d)(3) ..............................................
§ 63.10(d)(4) ..............................................
§ 63.10(d)(5) ..............................................
§ 63.10(e)(1) ..............................................
§ 63.10(e)(2) ..............................................
§ 63.10(e)(3)(i) ...........................................
§ 63.10(e)(3)(i)(A) ......................................
§ 63.10(e)(3)(i)(B) ......................................
§ 63.10(e)(3)(i)(C) ......................................
§ 63.10(e)(3)(ii) through (e)(3)(viii) ............
§ 63.10(f) ....................................................
§ 63.11(a) and (b) ......................................
§ 63.11(c), (d), and (e) ...............................
§ 63.12(a) through (c) ................................
§ 63.13(a) through (c) ................................
§ 63.14(a) and (b) ......................................
§ 63.15(a) and (b) ......................................
No .................
Yes.
No.
Yes.
Yes.
Yes.
Yes.
No .................
Yes.
Yes.
Yes ................
Yes.
Yes.
No .................
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Explanation
See § 63.1284(f)for recordkeeping of malfunctions
See § 63.1285(b)(6) for reporting of malfunctions.
Subpart HHH requires major sources to submit Periodic Reports semi-annually.
Subpart HHH does not require quarterly reporting for excess emissions.
[FR Doc. 2011–19899 Filed 8–22–11; 8:45 am]
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Agencies
[Federal Register Volume 76, Number 163 (Tuesday, August 23, 2011)]
[Proposed Rules]
[Pages 52738-52843]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: 2011-19899]
[[Page 52737]]
Vol. 76
Tuesday,
No. 163
August 23, 2011
Part II
Environmental Protection Agency
-----------------------------------------------------------------------
40 CFR Parts 60 and 63
Oil and Natural Gas Sector: New Source Performance Standards and
National Emission Standards for Hazardous Air Pollutants Reviews;
Proposed Rule
Federal Register / Vol. 76 , No. 163 / Tuesday, August 23, 2011 /
Proposed Rules
[[Page 52738]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Parts 60 and 63
[EPA-HQ-OAR-2010-0505; FRL-9448-6]
RIN 2060-AP76
Oil and Natural Gas Sector: New Source Performance Standards and
National Emission Standards for Hazardous Air Pollutants Reviews
AGENCY: Environmental Protection Agency (EPA).
ACTION: Proposed rule.
-----------------------------------------------------------------------
SUMMARY: This action announces how the EPA proposes to address the
reviews of the new source performance standards for volatile organic
compound and sulfur dioxide emissions from natural gas processing
plants. We are proposing to add to the source category list any oil and
gas operation not covered by the current listing. This action also
includes proposed amendments to the existing new source performance
standards for volatile organic compounds from natural gas processing
plants and proposed standards for operations that are not covered by
the existing new source performance standards. In addition, this action
proposes how the EPA will address the residual risk and technology
review conducted for the oil and natural gas production and natural gas
transmission and storage national emission standards for hazardous air
pollutants. This action further proposes standards for emission sources
within these two source categories that are not currently addressed, as
well as amendments to improve aspects of these national emission
standards for hazardous air pollutants related to applicability and
implementation. Finally, this action addresses provisions in these new
source performance standards and national emission standards for
hazardous air pollutants related to emissions during periods of
startup, shutdown and malfunction.
DATES: Comments must be received on or before October 24, 2011.
Public Hearing. Three public hearings will be held to provide the
public an opportunity to provide comments on this proposed rulemaking.
One will be held in the Dallas, Texas area, one in Pittsburgh,
Pennsylvania, and one in Denver, Colorado, on dates to be announced in
a separate document. Each hearing will convene at 10 a.m. local time.
For additional information on the public hearings and requesting to
speak, see the SUPPLEMENTARY INFORMATION section of this preamble.
ADDRESSES: Submit your comments, identified by Docket ID Number EPA-HQ-
OAR-2010-0505, by one of the following methods:
Federal eRulemaking Portal: https://www.regulations.gov:
Follow the instructions for submitting comments.
Agency Web site: https://www.epa.gov/oar/docket.html.
Follow the instructions for submitting comments on the Air and
Radiation Docket Web site.
E-mail: a-and-r-docket@epa.gov. Include Docket ID Number
EPA-HQ-OAR-2010-0505 in the subject line of the message.
Facsimile: (202) 566-9744.
Mail: Attention Docket ID Number EPA-HQ-OAR-2010-0505,
1200 Pennsylvania Ave., NW., Washington, DC 20460. Please include a
total of two copies. In addition, please mail a copy of your comments
on the information collection provisions to the Office of Information
and Regulatory Affairs, Office of Management and Budget (OMB), Attn:
Desk Officer for the EPA, 725 17th Street, NW., Washington, DC 20503.
Hand Delivery: United States Environmental Protection
Agency, EPA West (Air Docket), Room 3334, 1301 Constitution Ave., NW.,
Washington, DC 20004, Attention Docket ID Number EPA-HQ-OAR-2010-0505.
Such deliveries are only accepted during the Docket's normal hours of
operation, and special arrangements should be made for deliveries of
boxed information.
Instructions: Direct your comments to Docket ID Number EPA-HQ-OAR-
2010-0505. The EPA's policy is that all comments received will be
included in the public docket without change and may be made available
online at https://www.regulations.gov, including any personal
information provided, unless the comment includes information claimed
to be confidential business information (CBI) or other information
whose disclosure is restricted by statute. Do not submit information
that you consider to be CBI or otherwise protected through https://www.regulations.gov or e-mail. The https://www.regulations.gov Web site
is an ``anonymous access'' system, which means the EPA will not know
your identity or contact information unless you provide it in the body
of your comment. If you send an e-mail comment directly to the EPA
without going through https://www.regulations.gov, your e-mail address
will be automatically captured and included as part of the comment that
is placed in the public docket and made available on the Internet. If
you submit an electronic comment, the EPA recommends that you include
your name and other contact information in the body of your comment and
with any disk or CD-ROM you submit. If the EPA cannot read your comment
due to technical difficulties and cannot contact you for clarification,
the EPA may not be able to consider your comment. Electronic files
should avoid the use of special characters, any form of encryption, and
be free of any defects or viruses. For additional information about the
EPA's public docket, visit the EPA Docket Center homepage at https://www.epa.gov/epahome/dockets.htm. For additional instructions on
submitting comments, go to section II.C of the SUPPLEMENTARY
INFORMATION section of this preamble.
Docket: All documents in the docket are listed in the https://www.regulations.gov index. Although listed in the index, some
information is not publicly available, e.g., 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. Publicly available docket
materials are available either electronically through https://www.regulations.gov or in hard copy at the U.S. Environmental
Protection Agency, EPA West (Air Docket), Room 3334, 1301 Constitution
Ave., NW., Washington, DC 20004. The Public Reading Room is open from
8:30 a.m. to 4:30 p.m., Monday through Friday, excluding legal
holidays. The telephone number for the Public Reading Room is (202)
566-1744, and the telephone number for the Air Docket is (202) 566-
1742.
FOR FURTHER INFORMATION CONTACT: Bruce Moore, Sector Policies and
Programs Division, Office of Air Quality Planning and Standards (E143-
01), Environmental Protection Agency, Research Triangle Park, North
Carolina 27711, telephone number: (919) 541-5460; facsimile number:
(919) 685-3200; e-mail address: moore.bruce@epa.gov.
SUPPLEMENTARY INFORMATION:
Organization of This Document. The following outline is provided to
aid in locating information in this preamble.
I. Preamble Acronyms and Abbreviations
II. General Information
A. Does this action apply to me?
B. Where can I get a copy of this document and other related
information?
C. What should I consider as I prepare my comments for the EPA?
D. When will a public hearing occur?
III. Background Information
A. What are standards of performance and NSPS?
B. What are NESHAP?
[[Page 52739]]
C. What litigation is related to this proposed action?
D. What is a sector-based approach?
IV. Oil and Natural Gas Sector
V. Summary of Proposed Decisions and Actions
A. What are the proposed revisions to the NSPS?
B. What are the proposed decisions and actions related to the
NESHAP?
C. What are the proposed notification, recordkeeping and
reporting requirements for this proposed action?
D. What are the innovative compliance approaches being
considered?
E. How does the NSPS relate to permitting of sources?
VI. Rationale for Proposed Action for NSPS
A. What did we evaluate relative to NSPS?
B. What are the results of our evaluations and proposed actions
relative to NSPS?
VII. Rationale for Proposed Action for NESHAP
A. What data were used for the NESHAP analyses?
B. What are the proposed decisions regarding certain unregulated
emissions sources?
C. How did we perform the risk assessment and what are the
results and proposed decisions?
D. How did we perform the technology review and what are the
results and proposed decisions?
E. What other actions are we proposing?
VIII. What are the cost, environmental, energy and economic impacts
of the proposed 40 CFR part 60, subpart OOOO and amendments to
subparts HH and HHH of 40 CFR part 63?
A. What are the affected sources?
B. How are the impacts for this proposal evaluated?
C. What are the air quality impacts?
D. What are the water quality and solid waste impacts?
E. What are the secondary impacts?
F. What are the energy impacts?
G. What are the cost impacts?
H. What are the economic impacts?
I. What are the benefits?
IX. Request for Comments
X. Submitting Data Corrections
XI. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review and
Executive Order 13563: Improving Regulation and Regulatory Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation and Coordination With
Indian Tribal Governments
G. Executive Order 13045: Protection of Children From
Environmental Health and Safety Risks
H. Executive Order 13211: Actions Concerning Regulations 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
I. Preamble Acronyms and Abbreviations
Several acronyms and terms used to describe industrial processes,
data inventories and risk modeling are included in this preamble. While
this may not be an exhaustive list, to ease the reading of this
preamble and for reference purposes, the following terms and acronyms
are defined here:
ACGIH American Conference of Governmental Industrial Hygienists
ADAF Age-Dependent Adjustment Factors
AEGL Acute Exposure Guideline Levels
AERMOD The air dispersion model used by the HEM-3 model
API American Petroleum Institute
BACT Best Available Control Technology
BID Background Information Document
BPD Barrels Per Day
BSER Best System of Emission Reduction
BTEX Benzene, Ethylbenzene, Toluene and Xylene
CAA Clean Air Act
CalEPA California Environmental Protection Agency
CBI Confidential Business Information
CEM Continuous Emissions Monitoring
CEMS Continuous Emissions Monitoring System
CFR Code of Federal Regulations
CIIT Chemical Industry Institute of Toxicology
CO Carbon Monoxide
CO2 Carbon Dioxide
CO2e Carbon Dioxide Equivalent
DOE Department of Energy
ECHO Enforcement and Compliance History Online
e-GGRT Electronic Greenhouse Gas Reporting Tool
EJ Environmental Justice
EPA Environmental Protection Agency
ERPG Emergency Response Planning Guidelines
ERT Electronic Reporting Tool
GCG Gas Condensate Glycol
GHG Greenhouse Gas
GOR Gas to Oil Ratio
GWP Global Warming Potential
HAP Hazardous Air Pollutants
HEM-3 Human Exposure Model, version 3
HI Hazard Index
HP Horsepower
HQ Hazard Quotient
H2S Hydrogen Sulfide
ICR Information Collection Request
IPCC Intergovernmental Panel on Climate Change
IRIS Integrated Risk Information System
km Kilometer
kW Kilowatts
LAER Lowest Achievable Emission Rate
lb Pounds
LDAR Leak Detection and Repair
MACT Maximum Achievable Control Technology
MACT Code Code within the NEI used to identify processes included in
a source category
Mcf Thousand Cubic Feet
Mg/yr Megagrams per year
MIR Maximum Individual Risk
MIRR Monitoring, Inspection, Recordkeeping and Reporting
MMtCO2e Million Metric Tons of Carbon Dioxide Equivalents
NAAQS National Ambient Air Quality Standards
NAC/AEGL National Advisory Committee for Acute Exposure Guideline
Levels for Hazardous Substances
NAICS North American Industry Classification System
NAS National Academy of Sciences
NATA National Air Toxics Assessment
NEI National Emissions Inventory
NEMS National Energy Modeling System
NESHAP National Emissions Standards for Hazardous Air Pollutants
NGL Natural Gas Liquids
NIOSH National Institutes for Occupational Safety and Health
NOX Oxides of Nitrogen
NRC National Research Council
NSPS New Source Performance Standards
NSR New Source Review
NTTAA National Technology Transfer and Advancement Act
OAQPS Office of Air Quality Planning and Standards
OMB Office of Management and Budget
PB-HAP Hazardous air pollutants known to be persistent and bio-
accumulative in the environment
PFE Potential for Flash Emissions
PM Particulate Matter
PM2.5 Particulate Matter (2.5 microns and less)
POM Polycyclic Organic Matter
PPM Parts Per Million
PPMV Parts Per Million by Volume
PSIG Pounds per square inch gauge
PTE Potential to Emit
QA Quality Assurance
RACT Reasonably Available Control Technology
RBLC RACT/BACT/LAER Clearinghouse
REC Reduced Emissions Completions
REL CalEPA Reference Exposure Level
RFA Regulatory Flexibility Act
RfC Reference Concentration
RfD Reference Dose
RIA Regulatory Impact Analysis
RICE Reciprocating Internal Combustion Engines
RTR Residual Risk and Technology Review
SAB Science Advisory Board
SBREFA Small Business Regulatory Enforcement Fairness Act
SCC Source Classification Codes
SCFH Standard Cubic Feet Per Hour
SCFM Standard Cubic Feet Per Minute
SCM Standard Cubic Meters
SCMD Standard Cubic Meters Per Day
SCOT Shell Claus Offgas Treatment
SIP State Implementation Plan
SISNOSE Significant Economic Impact on a Substantial Number of Small
Entities
S/L/T State and Local and Tribal Agencies
SO2 Sulfur Dioxide
SSM Startup, Shutdown and Malfunction
STEL Short-term Exposure Limit
TLV Threshold Limit Value
TOSHI Target Organ-Specific Hazard Index
TPY Tons per Year
TRIM Total Risk Integrated Modeling System
TRIM.FaTE A spatially explicit, compartmental mass balance model
that
[[Page 52740]]
describes the movement and transformation of pollutants over time,
through a user-defined, bounded system that includes both biotic and
abiotic compartments
TSD Technical Support Document
UF Uncertainty Factor
UMRA Unfunded Mandates Reform Act
URE Unit Risk Estimate
VCS Voluntary Consensus Standards
VOC Volatile Organic Compounds
VRU Vapor Recovery Unit
II. General Information
A. Does this action apply to me?
The regulated industrial source categories that are the subject of
this proposal are listed in Table 1 of this preamble. These standards
and any changes considered in this rulemaking would be directly
applicable to sources as a Federal program. Thus, Federal, state, local
and tribal government entities are not affected by this proposed
action.
Table 1--Industrial Source Categories Affected by This Proposed Action
------------------------------------------------------------------------
NAICS code Examples of regulated
Category \1\ entities
------------------------------------------------------------------------
Industry........................... 211111 Crude Petroleum and
Natural Gas
Extraction.
211112 Natural Gas Liquid
Extraction.
221210 Natural Gas
Distribution.
486110 Pipeline Distribution
of Crude Oil.
486210 Pipeline
Transportation of
Natural Gas.
Federal government................. ........... Not affected.
State/local/tribal government...... ........... Not affected.
------------------------------------------------------------------------
\1\ North American Industry Classification System.
This table is not intended to be exhaustive, but rather provides a
guide for readers regarding entities likely to be affected by this
action. To determine whether your facility would be regulated by this
action, you should examine the applicability criteria in the
regulations. If you have any questions regarding the applicability of
this action to a particular entity, contact the person listed in the
preceding FOR FURTHER INFORMATION CONTACT section.
B. Where can I get a copy of this document and other related
information?
In addition to being available in the docket, an electronic copy of
this proposal will also be available on the EPA's Web site. Following
signature by the EPA Administrator, a copy of this proposed action will
be posted on the EPA's Web site at the following address: https://www.epa.gov/airquality/oilandgas.
Additional information is available on the EPA's Residual Risk and
Technology Review (RTR) Web site at https://www.epa.gov/ttn/atw/rrisk/oarpg.html. This information includes the most recent version of the
rule, source category descriptions, detailed emissions and other data
that were used as inputs to the risk assessments.
C. What should I consider as I prepare my comments for the EPA?
Submitting CBI. Do not submit information containing CBI to the EPA
through https://www.regulations.gov or e-mail. Clearly mark the part or
all of the information that you claim to be CBI. For CBI information on
a disk or CD ROM that you mail to the EPA, mark the outside of the disk
or CD ROM as CBI and then identify electronically within the disk or CD
ROM the specific information that is claimed as CBI. In addition to one
complete version of the comment that includes information claimed as
CBI, a copy of the comment that does not contain the information
claimed as CBI must be submitted for inclusion in the public docket. If
you submit a CD ROM or disk that does not contain CBI, mark the outside
of the disk or CD ROM clearly that it does not contain CBI. Information
not marked as CBI will be included in the public docket and the EPA's
electronic public docket without prior notice. Information marked as
CBI will not be disclosed except in accordance with procedures set
forth in 40 CFR part 2. Send or deliver information identified as CBI
only to the following address: Roberto Morales, OAQPS Document Control
Officer (C404-02), Environmental Protection Agency, Office of Air
Quality Planning and Standards, Research Triangle Park, North Carolina
27711, Attention Docket ID Number EPA-HQ-OAR-2010-0505.
D. When will a public hearing occur?
We will hold three public hearings, one in the Dallas, Texas area,
one in Pittsburgh, Pennsylvania, and one in Denver, Colorado. If you
are interested in attending or speaking at one of the public hearings,
contact Ms. Joan Rogers at (919) 541-4487 by September 6, 2011. Details
on the public hearings will be provided in a separate notice and we
will specify the time and date of the public hearings on https://www.epa.gov/airquality/oilandgas. If no one requests to speak at one of
the public hearings by September 6, 2011, then that public hearing will
be cancelled without further notice.
III. Background Information
A. What are standards of performance and NSPS?
1. What is the statutory authority for standards of performance and
NSPS?
Section 111 of the Clean Air Act (CAA) requires the EPA
Administrator to list categories of stationary sources, if such sources
cause or contribute significantly to air pollution, which may
reasonably be anticipated to endanger public health or welfare. The EPA
must then issue performance standards for such source categories. A
performance standard reflects the degree of emission limitation
achievable through the application of the ``best system of emission
reduction'' (BSER) which the EPA determines has been adequately
demonstrated. The EPA may consider certain costs and nonair quality
health and environmental impact and energy requirements when
establishing performance standards. Whereas CAA section 112 standards
are issued for existing and new stationary sources, standards of
performance are issued for new and modified stationary sources. These
standards are referred to as new source performance standards (NSPS).
The EPA has the authority to define the source categories, determine
the pollutants for which standards should be developed, identify the
facilities within each source category to be covered and set the
emission level of the standards.
CAA section 111(b)(1)(B) requires the EPA to ``at least every 8
years review and, if appropriate, revise'' performance standards unless
the ``Administrator determines that such review is not appropriate in
light of readily available information on the efficacy'' of the
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standard. When conducting a review of an existing performance standard,
the EPA has discretion to revise that standard to add emission limits
for pollutants or emission sources not currently regulated for that
source category.
In setting or revising a performance standard, CAA section
111(a)(1) provides that performance standards are to ``reflect the
degree of emission limitation achievable through the application of the
best system of emission reduction which (taking into account the cost
of achieving such reduction and any nonair quality health and
environmental impact and energy requirements) the Administrator
determines has been adequately demonstrated.'' In this notice, we refer
to this level of control as the BSER. In determining BSER, we typically
conduct a technology review that identifies what emission reduction
systems exist and how much they reduce air pollution in practice. Next,
for each control system identified, we evaluate its costs, secondary
air benefits (or disbenefits) resulting from energy requirements and
nonair quality impacts such as solid waste generation. Based on our
evaluation, we would determine BSER. The resultant standard is usually
a numerical emissions limit, expressed as a performance level (i.e., a
rate-based standard or percent control), that reflects the BSER.
Although such standards are based on the BSER, the EPA may not
prescribe a particular technology that must be used to comply with a
performance standard, except in instances where the Administrator
determines it is not feasible to prescribe or enforce a standard of
performance. Typically, sources remain free to elect whatever control
measures that they choose to meet the emission limits. Upon
promulgation, an NSPS becomes a national standard to which all new,
modified or reconstructed sources must comply.
2. What is the regulatory history regarding performance standards for
the oil and natural gas sector?
In 1979, the EPA listed crude oil and natural gas production on its
priority list of source categories for promulgation of NSPS (44 FR
49222, August 21, 1979). On June 24, 1985 (50 FR 26122), the EPA
promulgated an NSPS for the source category that addressed volatile
organic compound (VOC) emissions from leaking components at onshore
natural gas processing plants (40 CFR part 60, subpart KKK). On October
1, 1985 (50 FR 40158), a second NSPS was promulgated for the source
category that regulates sulfur dioxide (SO2) emissions from
natural gas processing plants (40 CFR part 60, subpart LLL). Other than
natural gas processing plants, EPA has not previously set NSPS for a
variety of oil and natural gas operations.
B. What are NESHAP?
1. What is the statutory authority for NESHAP?
Section 112 of the CAA establishes a two-stage regulatory process
to address emissions of hazardous air pollutants (HAP) from stationary
sources. In the first stage, after the EPA has identified categories of
sources emitting one or more of the HAP listed in section 112(b) of the
CAA, section 112(d) of the CAA calls for us to promulgate national
emission standards for hazardous air pollutants (NESHAP) for those
sources. ``Major sources'' are those that emit or have the potential to
emit (PTE) 10 tons per year (tpy) or more of a single HAP or 25 tpy or
more of any combination of HAP. For major sources, these technology-
based standards must reflect the maximum degree of emission reductions
of HAP achievable (after considering cost, energy requirements and
nonair quality health and environmental impacts) and are commonly
referred to as maximum achievable control technology (MACT) standards.
MACT standards are to reflect application of measures, processes,
methods, systems or techniques, including, but not limited to, measures
which, (1) reduce the volume of or eliminate pollutants through process
changes, substitution of materials or other modifications, (2) enclose
systems or processes to eliminate emissions, (3) capture or treat
pollutants when released from a process, stack, storage or fugitive
emissions point, (4) are design, equipment, work practice or
operational standards (including requirements for operator training or
certification) or (5) are a combination of the above. CAA section
112(d)(2)(A)-(E). The MACT standard may take the form of a design,
equipment, work practice or operational standard where the EPA first
determines either that, (1) a pollutant cannot be emitted through a
conveyance designed and constructed to emit or capture the pollutant or
that any requirement for or use of such a conveyance would be
inconsistent with law or (2) the application of measurement methodology
to a particular class of sources is not practicable due to
technological and economic limitations. CAA sections 112(h)(1)-(2).
The MACT ``floor'' is the minimum control level allowed for MACT
standards promulgated under CAA section 112(d)(3), and may not be based
on cost considerations. For new sources, the MACT floor cannot be less
stringent than the emission control that is achieved in practice by the
best-controlled similar source. The MACT floors for existing sources
can be less stringent than floors for new sources, but they cannot be
less stringent than the average emission limitation achieved by the
best-performing 12 percent of existing sources in the category or
subcategory (or the best-performing five sources for categories or
subcategories with fewer than 30 sources). In developing MACT
standards, we must also consider control options that are more
stringent than the floor. We may establish standards more stringent
than the floor based on the consideration of the cost of achieving the
emissions reductions, any nonair quality health and environmental
impacts and energy requirements.
The EPA is then required to review these technology-based standards
and to revise them ``as necessary (taking into account developments in
practices, processes, and control technologies)'' no less frequently
than every 8 years, under CAA section 112(d)(6). In conducting this
review, the EPA is not obliged to completely recalculate the prior MACT
determination. NRDC v. EPA, 529 F.3d 1077, 1084 (D.C. Cir. 2008).
The second stage in standard-setting focuses on reducing any
remaining ``residual'' risk according to CAA section 112(f). This
provision requires, first, that the EPA prepare a Report to Congress
discussing (among other things) methods of calculating risk posed (or
potentially posed) by sources after implementation of the MACT
standards, the public health significance of those risks, and the EPA's
recommendations as to legislation regarding such remaining risk. The
EPA prepared and submitted this report (Residual Risk Report to
Congress, EPA-453/R-99-001) in March 1999. Congress did not act in
response to the report, thereby triggering the EPA's obligation under
CAA section 112(f)(2) to analyze and address residual risk.
CAA section 112(f)(2) requires us to determine for source
categories subject to MACT standards, whether the emissions standards
provide an ample margin of safety to protect public health. If the MACT
standards for HAP ``classified as a known, probable, or possible human
carcinogen do not reduce lifetime excess cancer risks to the individual
most exposed to emissions from a source in the category or subcategory
to less than 1-in-1 million,'' the EPA must promulgate
[[Page 52742]]
residual risk standards for the source category (or subcategory), as
necessary, to provide an ample margin of safety to protect public
health. In doing so, the EPA may adopt standards equal to existing MACT
standards if the EPA determines that the existing standards are
sufficiently protective. NRDC v. EPA, 529 F.3d 1077, 1083 (D.C. Cir.
2008). (``If EPA determines that the existing technology-based
standards provide an ``ample margin of safety,'' then the Agency is
free to readopt those standards during the residual risk rulemaking.'')
The EPA must also adopt more stringent standards, if necessary, to
prevent an adverse environmental effect,\1\ but must consider cost,
energy, safety and other relevant factors in doing so.
---------------------------------------------------------------------------
\1\ ``Adverse environmental effect'' is defined in CAA section
112(a)(7) as any significant and widespread adverse effect, which
may be reasonably anticipated to wildlife, aquatic life or natural
resources, including adverse impacts on populations of endangered or
threatened species or significant degradation of environmental
qualities over broad areas.
---------------------------------------------------------------------------
Section 112(f)(2) of the CAA expressly preserves our use of a two-
step process for developing standards to address any residual risk and
our interpretation of ``ample margin of safety'' developed in the
National Emission Standards for Hazardous Air Pollutants: Benzene
Emissions from Maleic Anhydride Plants, Ethylbenzene/Styrene Plants,
Benzene Storage Vessels, Benzene Equipment Leaks, and Coke By-Product
Recovery Plants (Benzene NESHAP) (54 FR 38044, September 14, 1989). The
first step in this process is the determination of acceptable risk. The
second step provides for an ample margin of safety to protect public
health, which is the level at which the standards are set (unless a
more stringent standard is required to prevent, taking into
consideration costs, energy, safety, and other relevant factors, an
adverse environmental effect).
The terms ``individual most exposed,'' ``acceptable level,'' and
``ample margin of safety'' are not specifically defined in the CAA.
However, CAA section 112(f)(2)(B) preserves the interpretation set out
in the Benzene NESHAP, and the United States Court of Appeals for the
District of Columbia Circuit in NRDC v. EPA, 529 F.3d 1077, concluded
that the EPA's interpretation of subsection 112(f)(2) is a reasonable
one. See NRDC v. EPA, 529 F.3d at 1083 (D.C. Cir., ``[S]ubsection
112(f)(2)(B) expressly incorporates EPA's interpretation of the Clean
Air Act from the Benzene standard, complete with a citation to the
Federal Register''). (D.C. Cir. 2008). See also, A Legislative History
of the Clean Air Act Amendments of 1990, volume 1, p. 877 (Senate
debate on Conference Report). We notified Congress in the Residual Risk
Report to Congress that we intended to use the Benzene NESHAP approach
in making CAA section 112(f) residual risk determinations (EPA-453/R-
99-001, p. ES-11).
In the Benzene NESHAP, we stated as an overall objective:
* * * in protecting public health with an ample margin of
safety, we strive to provide maximum feasible protection against
risks to health from hazardous air pollutants by, (1) protecting the
greatest number of persons possible to an individual lifetime risk
level no higher than approximately 1-in-1 million; and (2) limiting
to no higher than approximately 1-in-10 thousand [i.e., 100-in-1
million] the estimated risk that a person living near a facility
would have if he or she were exposed to the maximum pollutant
concentrations for 70 years.
The Agency also stated that, ``The EPA also considers incidence
(the number of persons estimated to suffer cancer or other serious
health effects as a result of exposure to a pollutant) to be an
important measure of the health risk to the exposed population.
Incidence measures the extent of health risk to the exposed population
as a whole, by providing an estimate of the occurrence of cancer or
other serious health effects in the exposed population.'' The Agency
went on to conclude that ``estimated incidence would be weighed along
with other health risk information in judging acceptability.'' As
explained more fully in our Residual Risk Report to Congress, the EPA
does not define ``rigid line[s] of acceptability,'' but considers
rather broad objectives to be weighed with a series of other health
measures and factors (EPA-453/R-99-001, p. ES-11). The determination of
what represents an ``acceptable'' risk is based on a judgment of ``what
risks are acceptable in the world in which we live'' (Residual Risk
Report to Congress, p. 178, quoting the Vinyl Chloride decision at 824
F.2d 1165) recognizing that our world is not risk-free.
In the Benzene NESHAP, we stated that ``EPA will generally presume
that if the risk to [the maximum exposed] individual is no higher than
approximately 1-in-10 thousand, that risk level is considered
acceptable.'' 54 FR 38045. We discussed the maximum individual lifetime
cancer risk (or maximum individual risk (MIR)) as being ``the estimated
risk that a person living near a plant would have if he or she were
exposed to the maximum pollutant concentrations for 70 years.'' Id. We
explained that this measure of risk ``is an estimate of the upper bound
of risk based on conservative assumptions, such as continuous exposure
for 24 hours per day for 70 years.'' Id. We acknowledge that maximum
individual lifetime cancer risk ``does not necessarily reflect the true
risk, but displays a conservative risk level which is an upper-bound
that is unlikely to be exceeded.'' Id.
Understanding that there are both benefits and limitations to using
maximum individual lifetime cancer risk as a metric for determining
acceptability, we acknowledged in the 1989 Benzene NESHAP that
``consideration of maximum individual risk * * * must take into account
the strengths and weaknesses of this measure of risk.'' Id.
Consequently, the presumptive risk level of 100-in-1 million (1-in-10
thousand) provides a benchmark for judging the acceptability of maximum
individual lifetime cancer risk, but does not constitute a rigid line
for making that determination.
The Agency also explained in the 1989 Benzene NESHAP the following:
``In establishing a presumption for MIR, rather than a rigid line for
acceptability, the Agency intends to weigh it with a series of other
health measures and factors. These include the overall incidence of
cancer or other serious health effects within the exposed population,
the numbers of persons exposed within each individual lifetime risk
range and associated incidence within, typically, a 50-kilometer (km)
exposure radius around facilities, the science policy assumptions and
estimation uncertainties associated with the risk measures, weight of
the scientific evidence for human health effects, other quantified or
unquantified health effects, effects due to co-location of facilities
and co-emission of pollutants.'' Id.
In some cases, these health measures and factors taken together may
provide a more realistic description of the magnitude of risk in the
exposed population than that provided by maximum individual lifetime
cancer risk alone. As explained in the Benzene NESHAP, ``[e]ven though
the risks judged ``acceptable'' by the EPA in the first step of the
Vinyl Chloride inquiry are already low, the second step of the inquiry,
determining an ``ample margin of safety,'' again includes consideration
of all of the health factors, and whether to reduce the risks even
further.'' In the ample margin of safety decision process, the Agency
again considers all of the health risks and other health information
considered in the first step. Beyond that information, additional
factors relating to the appropriate level
[[Page 52743]]
of control will also be considered, including costs and economic
impacts of controls, technological feasibility, uncertainties and any
other relevant factors. Considering all of these factors, the Agency
will establish the standard at a level that provides an ample margin of
safety to protect the public health, as required by CAA section 112(f).
54 FR 38046.
2. How do we consider the risk results in making decisions?
As discussed in the previous section of this preamble, we apply a
two-step process for developing standards to address residual risk. In
the first step, the EPA determines if risks are acceptable. This
determination ``considers all health information, including risk
estimation uncertainty, and includes a presumptive limit on maximum
individual lifetime [cancer] risk (MIR) \2\ of approximately 1-in-10
thousand [i.e., 100-in-1 million].'' 54 FR 38045. In the second step of
the process, the EPA sets the standard at a level that provides an
ample margin of safety ``in consideration of all health information,
including the number of persons at risk levels higher than
approximately 1-in-1 million, as well as other relevant factors,
including costs and economic impacts, technological feasibility, and
other factors relevant to each particular decision.'' Id.
---------------------------------------------------------------------------
\2\ Although defined as ``maximum individual risk,'' MIR refers
only to cancer risk. MIR, one metric for assessing cancer risk, is
the estimated risk were an individual exposed to the maximum level
of a pollutant for a lifetime.
---------------------------------------------------------------------------
In past residual risk determinations, the EPA presented a number of
human health risk metrics associated with emissions from the category
under review, including: The MIR; the numbers of persons in various
risk ranges; cancer incidence; the maximum noncancer hazard index (HI);
and the maximum acute noncancer hazard. In estimating risks, the EPA
considered source categories under review that are located near each
other and that affect the same population. The EPA provided estimates
of the expected difference in actual emissions from the source category
under review and emissions allowed pursuant to the source category MACT
standard. The EPA also discussed and considered risk estimation
uncertainties. The EPA is providing this same type of information in
support of these actions.
The Agency acknowledges that the Benzene NESHAP provides
flexibility regarding what factors the EPA might consider in making our
determinations and how they might be weighed for each source category.
In responding to comment on our policy under the Benzene NESHAP, the
EPA explained that: ``The policy chosen by the Administrator permits
consideration of multiple measures of health risk. Not only can the MIR
figure be considered, but also incidence, the presence of noncancer
health effects, and the uncertainties of the risk estimates. In this
way, the effect on the most exposed individuals can be reviewed as well
as the impact on the general public. These factors can then be weighed
in each individual case. This approach complies with the Vinyl Chloride
mandate that the Administrator ascertain an acceptable level of risk to
the public by employing [her] expertise to assess available data. It
also complies with the Congressional intent behind the CAA, which did
not exclude the use of any particular measure of public health risk
from the EPA's consideration with respect to CAA section 112
regulations, and, thereby, implicitly permits consideration of any and
all measures of health risk which the Administrator, in [her] judgment,
believes are appropriate to determining what will `protect the public
health.' ''
For example, the level of the MIR is only one factor to be weighed
in determining acceptability of risks. The Benzene NESHAP explains ``an
MIR of approximately 1-in-10 thousand should ordinarily be the upper
end of the range of acceptability. As risks increase above this
benchmark, they become presumptively less acceptable under CAA section
112, and would be weighed with the other health risk measures and
information in making an overall judgment on acceptability. Or, the
Agency may find, in a particular case, that a risk that includes MIR
less than the presumptively acceptable level is unacceptable in the
light of other health risk factors.'' Similarly, with regard to the
ample margin of safety analysis, the Benzene NESHAP states that: ``EPA
believes the relative weight of the many factors that can be considered
in selecting an ample margin of safety can only be determined for each
specific source category. This occurs mainly because technological and
economic factors (along with the health-related factors) vary from
source category to source category.''
3. What is the regulatory history regarding NESHAP for the oil and
natural gas sector?
On July 16, 1992 (57 FR 31576), the EPA published a list of major
and area sources for which NESHAP are to be published (i.e., the source
category list). Oil and natural gas production facilities were listed
as a category of major sources. On February 12, 1998 (63 FR 7155), the
EPA amended the source category list to add Natural Gas Transmission
and Storage as a major source category.
On June 17, 1999 (64 FR 32610), the EPA promulgated MACT standards
for the Oil and Natural Gas Production and Natural Gas Transmission and
Storage major source categories. The Oil and Natural Gas Production
NESHAP (40 CFR part 63, subpart HH) contains standards for HAP
emissions from glycol dehydration process vents, storage vessels and
natural gas processing plant equipment leaks. The Natural Gas
Transmission and Storage NESHAP (40 CFR part 63, subpart HHH) contains
standards for glycol dehydration process vents.
In addition to these NESHAP for major sources, the EPA also
promulgated NESHAP for the Oil and Natural Gas Production area source
category on January 3, 2007 (72 FR 26). These area source standards,
which are based on generally available control technology, are also
contained in 40 CFR part 63, subpart HH. This proposed action does not
impact these area source standards.
C. What litigation is related to this proposed action?
On January 14, 2009, pursuant to section 304(a)(2) of the CAA,
WildEarth Guardians and the San Juan Citizens Alliance filed a
Complaint alleging that the EPA failed to meet its obligations under
CAA sections 111(b)(1)(B), 112(d)(6) and 112(f)(2) to take actions
relative to the review/revision of the NSPS and the NESHAP with respect
to the Oil and Natural Gas Production source category. On February 4,
2010, the Court entered a consent decree requiring the EPA to sign by
July 28, 2011,\3\ proposed standards and/or determinations not to issue
standards pursuant to CAA sections 111(b)(1)(B), 112(d)(6) and
112(f)(2) and to take final action by February 28, 2012.
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\3\ On April 27, 2011, pursuant to paragraph 10(a) of the
Consent Decree, the parties filed with the Court a written
stipulation that changes the proposal date from January 31, 2011, to
July 28, 2011, and the final action date from November 30, 2011, to
February 28, 2012.
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D. What is a sector-based approach?
Sector-based approaches are based on integrated assessments that
consider multiple pollutants in a comprehensive and coordinated manner
to manage emissions and CAA requirements. One of the many ways we can
address sector-based approaches is by reviewing multiple regulatory
programs together whenever possible, consistent with all
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applicable legal requirements. This approach essentially expands the
technical analyses on costs and benefits of particular technologies, to
consider the interactions of rules that regulate sources. The benefit
of multi-pollutant and sector-based analyses and approaches includes
the ability to identify optimum strategies, considering feasibility,
cost impacts and benefits across the different pollutant types while
streamlining administrative and compliance complexities and reducing
conflicting and redundant requirements, resulting in added certainty
and easier implementation of control strategies for the sector under
consideration. In order to benefit from a sector-based approach for the
oil and gas industry, the EPA analyzed how the NSPS and NESHAP under
consideration relate to each other and other regulatory requirements
currently under review for oil and gas facilities. In this analysis, we
looked at how the different control requirements that result from these
requirements interact, including the different regulatory deadlines and
control equipment requirements that result, the different reporting and
recordkeeping requirements and opportunities for states to account for
reductions resulting from this rulemaking in their State Implementation
Plans (SIP). The requirements analyzed affect criteria pollutant, HAP
and methane emissions from oil and natural gas processes and cover the
NSPS and NESHAP reviews. As a result of the sector-based approach, this
rulemaking will reduce conflicting and redundant requirements. Also,
the sector-based approach facilitated the streamlining of monitoring,
recordkeeping and reporting requirements, thus, reducing administrative
and compliance complexities associated with complying with multiple
regulations. In addition, the sector-based approach promotes a
comprehensive control strategy that maximizes the co-control of
multiple regulated pollutants while obtaining emission reductions as
co-benefits.
IV. Oil and Natural Gas Sector
The oil and natural gas sector includes operations involved in the
extraction and production of oil and natural gas, as well as the
processing, transmission and distribution of natural gas. Specifically
for oil, the sector includes all operations from the well to the point
of custody transfer at a petroleum refinery. For natural gas, the
sector includes all operations from the well to the customer. The oil
and natural gas operations can generally be separated into four
segments: (1) Oil and natural gas production, (2) natural gas
processing, (3) natural gas transmission and (4) natural gas
distribution. Each of these segments is briefly discussed below.
Oil and natural gas production includes both onshore and offshore
operations. Production operations include the wells and all related
processes used in the extraction, production, recovery, lifting,
stabilization, separation or treating of oil and/or natural gas
(including condensate). Production components may include, but are not
limited to, wells and related casing head, tubing head and ``Christmas
tree'' piping, as well as pumps, compressors, heater treaters,
separators, storage vessels, pneumatic devices and dehydrators.
Production operations also include the well drilling, completion and
workover processes and includes all the portable non-self-propelled
apparatus associated with those operations. Production sites include
not only the ``pads'' where the wells are located, but also include
stand-alone sites where oil, condensate, produced water and gas from
several wells may be separated, stored and treated. The production
sector also includes the low pressure, small diameter, gathering
pipelines and related components that collect and transport the oil,
gas and other materials and wastes from the wells to the refineries or
natural gas processing plants. None of the operations upstream of the
natural gas processing plant are covered by the existing NSPS. Offshore
oil and natural gas production occurs on platform structures that house
equipment to extract oil and gas from the ocean or lake floor and that
process and/or transfer the oil and gas to storage, transport vessels
or onshore. Offshore production can also include secondary platform
structures connected to the platform structure, storage tanks
associated with the platform structure and floating production and
offloading equipment.
There are three basic types of wells: Oil wells, gas wells and
associated gas wells. Oil wells can have ``associated'' natural gas
that is separated and processed or the crude oil can be the only
product processed. Once the crude oil is separated from the water and
other impurities, it is essentially ready to be transported to the
refinery via truck, railcar or pipeline. We consider the oil refinery
sector separately from the oil and natural gas sector. Therefore, at
the point of custody transfer at the refinery, the oil leaves the oil
and natural gas sector and enters the petroleum refining sector.
Natural gas is primarily made up of methane. However, whether
natural gas is associated gas from oil wells or non-associated gas from
gas or condensate wells, it commonly exists in mixtures with other
hydrocarbons. These hydrocarbons are often referred to as natural gas
liquids (NGL). They are sold separately and have a variety of different
uses. The raw natural gas often contains water vapor, hydrogen sulfide
(H2S), carbon dioxide (CO2), helium, nitrogen and
other compounds. Natural gas processing consists of separating certain
hydrocarbons and fluids from the natural gas to produced ``pipeline
quality'' dry natural gas. While some of the processing can be
accomplished in the production segment, the complete processing of
natural gas takes place in the natural gas processing segment. Natural
gas processing operations separate and recover NGL or other non-methane
gases and liquids from a stream of produced natural gas through
components performing one or more of the following processes: Oil and
condensate separation, water removal, separation of NGL, sulfur and
CO2 removal, fractionation of natural gas liquid and other
processes, such as the capture of CO2 separated from natural
gas streams for delivery outside the facility. Natural gas processing
plants are the only operations covered by the existing NSPS.
The pipeline quality natural gas leaves the processing segment and
enters the transmission segment. Pipelines in the natural gas
transmission segment can be interstate pipelines that carry natural gas
across state boundaries or intrastate pipelines, which transport the
gas within a single state. While interstate pipelines may be of a
larger diameter and operated at a higher pressure, the basic components
are the same. To ensure that the natural gas flowing through any
pipeline remains pressurized, compression of the gas is required
periodically along the pipeline. This is accomplished by compressor
stations usually placed between 40 and 100 mile intervals along the
pipeline. At a compressor station, the natural gas enters the station,
where it is compressed by reciprocating or centrifugal compressors.
In addition to the pipelines and compressor stations, the natural
gas transmission segment includes underground storage facilities.
Underground natural gas storage includes subsurface storage, which
typically consists of depleted gas or oil reservoirs and salt dome
caverns used for storing natural gas. One purpose of this storage is
for load balancing (equalizing the receipt and delivery of natural
gas). At an underground storage site, there are typically other
processes,
[[Page 52745]]
including compression, dehydration and flow measurement.
The distribution segment is the final step in delivering natural
gas to customers. The natural gas enters the distribution segment from
delivery points located on interstate and intrastate transmission
pipelines to business and household customers. The delivery point where
the natural gas leaves the transmission segment and enters the
distribution segment is often called the ``citygate.'' Typically,
utilities take ownership of the gas at the citygate. Natural gas
distribution systems consist of thousands of miles of piping, including
mains and service pipelines to the customers. Distribution systems
sometimes have compressor stations, although they are considerably
smaller than transmission compressor stations. Distribution systems
include metering stations, which allow distribution companies to
monitor the natural gas in the system. Essentially, these metering
stations measure the flow of gas and allow distribution companies to
track natural gas as it flows through the system.
Emissions can occur from a variety of processes and points
throughout the oil and natural gas sector. Primarily, these emissions
are organic compounds such as methane, ethane, VOC and organic HAP. The
most common organic HAP are n-hexane and BTEX compounds (benzene,
toluene, ethylbenzene and xylenes). Hydrogen sulfide (H2S)
and sulfur dioxide (SO2) are emitted from production and
processing operations that handle and treat ``sour gas.'' Sour gas is
defined as natural gas with a maximum H2S content of 0.25
gr/100 scf (4ppmv) along with the presence of CO2.
In addition, there are significant emissions associated with the
reciprocating internal combustion engines and combustion turbines that
power compressors throughout the oil and natural gas sector. However,
emissions from internal combustion engines and combustion turbines are
covered by regulations specific to engines and turbines and, thus, are
not addressed in this action.
V. Summary of Proposed Decisions and Actions
Pursuant to CAA sections 111(b), 112(d)(2), 112(d)(6) and 112(f),
we are proposing to revise the NSPS and NESHAP relative to oil and gas
to include the standards and requirements summarized in this section.
More details of the rationale for these proposed standards and
requirements are provided in sections VI and VII of this preamble. In
addition, as part of these rationale discussions, we solicit public
comment and data relevant to several issues. The comments we receive
during the public comment period will help inform the rule development
process as we work toward promulgating a final action.
A. What are the proposed revisions to the NSPS?
We reviewed the two NSPS that apply to the oil and natural gas
industry. Based on our review, we believe that the requirements at 40
CFR part 60, subpart KKK, should be updated to reflect requirements in
40 CFR part 60, subpart VVa for controlling VOC equipment leaks at
processing plants. We also believe that the requirements at 40 CFR part
60, subpart LLL, for controlling SO2 emissions from natural
gas processing plants should be strengthened for facilities with the
highest sulfur feed rates and the highest H2S
concentrations. For a more detailed discussion, please see section
VI.B.1 of this preamble.
In addition, there are significant VOC emissions from oil and
natural gas operations that are not covered by the two existing NSPS,
including other emissions at processing plants and emissions from
upstream production, as well as transmission and storage facilities. In
the 1984 notice that listed source categories (including Oil and
Natural Gas) for promulgation of NSPS, we noted that there were
discrepancies between the source category names on the list and those
in the background document, and we clarified our intent to address all
sources under an industry heading at the same time. See 44 FR 49222,
49224-49225.\4\ We, therefore, believe that the currently listed Oil
and Natural Gas source category covers all operations in this industry
(i.e., production, processing, transmission, storage and distribution).
To the extent there are oil and gas operations not covered by the
currently listed Oil and Natural Gas source category, pursuant to CAA
section 111(b), we hereby modify the category list to include all
operations in the oil and natural gas sector. Section 111(b) of the CAA
gives the EPA broad authority and discretion to list and establish NSPS
for a category that, in the Administrator's judgment, causes or
contributes significantly to air pollution which may reasonably be
anticipated to endanger public health or welfare. Pursuant to CAA
section 111(b), we are modifying the source category list to include
any oil and gas operation not covered by the current listing and
evaluating emissions from all oil and gas operations at the same time.
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\4\ The Notice further states that ``The Administrator may also
concurrently develop standards for sources which are not on the
priority list.'' 44 FR at 49225.
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We are also proposing standards for several new oil and natural gas
affected facilities. The proposed standards would apply to affected
facilities that commence construction, reconstruction or modification
after August 23, 2011. These standards, which include requirements for
VOC, would be contained in a new subpart, 40 CFR part 60, subpart OOOO.
Subpart OOOO would incorporate 40 CFR part 60, subpart KKK and 40 CFR
part 60, subpart LLL, thereby having in this one subpart, all standards
that are applicable to the new and modified affected facilities
described above. We also propose to amend the title of subparts KKK and
LLL, accordingly, to apply only to affected facilities already subject
to those subparts. Those operations would not become subject to subpart
OOOO unless they triggered applicability based on new or modified
affected facilities under subpart OOOO.
We are proposing operational standards for completions of
hydraulically fractured gas wells. Based on our review, we identified
two subcategories of fractured gas wells for which well completions are
conducted. For non-exploratory and non-delineation wells, the proposed
operational standards would require reduced emission completion (REC),
commonly referred to as ``green completion,'' in combination with pit-
flaring of gas not suitable for entering the gathering line. For
exploratory and delineation wells (these wells generally are not in
close proximity to a gathering line), we proposed an operational
standard that would require pit flaring. Well completions subject to
the standards would be limited to gas well completions following
hydraulic fracturing operations. These completions include those
conducted at newly drilled and fractured wells, as well as completions
conducted following refracturing operations at various times over the
life of the well. We have determined that a completion associated with
refracturing performed at an existing well (i.e., a well existing prior
to August 23, 2011) is considered a modification under CAA section
111(a), because physical change occurs to the existing well resulting
in emissions increase during the refracturing and completion operation.
A detailed discussion of this determination is presented in the
Technical Support Document (TSD) in the docket. Therefore, the proposed
standards would apply to completions at new gas wells that are
fractured or
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refractured along with completions associated with fracturing or
refracturing of existing gas wells. The modification determination and
resultant applicability of NSPS to the completion operation following
fracturing or refracturing of existing gas wells (i.e., wells existing
before August 23, 2011 would be limited strictly to the wellhead, well
bore, casing and tubing, and any conveyance through which gas is vented
to the atmosphere and not be extended beyond the wellhead to other
ancillary components that may be at the well site such as existing
storage vessels, process vessels, separators, dehydrators or any other
components or apparatus.
We are also proposing VOC standards to reduce emissions from gas-
driven pneumatic devices. We are proposing that each pneumatic device
is an affected facility. Accordingly, the proposed standards would
apply to each newly installed pneumatic device (including replacement
of an existing device). At gas processing plants, we are proposing a
zero emission limit for each individual pneumatic controller. The
proposed emission standards would reflect the emission level achievable
from the use of non-gas-driven pneumatic controllers. At other
locations, we are proposing a bleed limit of 6 standard cubic feet of
gas per hour for an individual pneumatic controller, which would
reflect the emission level achievable from the use of low bleed gas-
driven pneumatic controllers. In both cases, the standards provide
exemptions for certain applications based on functional considerations.
In addition, the proposed rule would require measures to reduce VOC
emissions from centrifugal and reciprocating compressors. As explained
in more detail below in section VI.B.4, we are proposing equipment
standards for centrifugal compressors. The proposed standards would
require the use of dry seal systems. However, we are aware that some
owners and operators may need to use centrifugal compressors with wet
seals, and we are soliciting comment on the suitability of a compliance
option allowing the use of wet seals combined with routing of emissions
from the seal liquid through a closed vent system to a control device
as an acceptable alternative to installing dry seals.
Our review of reciprocating compressors found that piston rod
packing wear produces fugitive emissions that cannot be captured and
conveyed to a control device. As a result, we are proposing operational
standards for reciprocating compressors, such that the proposed rule
would require replacement of the rod packing based on hours of usage.
The owner or operator of a reciprocating compressor affected facility
would be required to monitor the duration (in hours) that the
compressor is operated. When the hours of operation reaches 26,000
hours, the owner or operator would be required to change the rod
packing immediately. However, to avoid unscheduled shutdowns when
26,000 hours is reached, owners and operators could track hours of
operation such that packing replacement could be coordinated with
planned maintenance shutdowns before hours of operation reached 26,000.
Some operators may prefer to replace the rod packing on a fixed
schedule to ensure that the hours of operation would not reach 26,000
hours. We solicit comment on the appropriateness of a fixed replacement
frequency and other considerations that would be associated with
regular replacement.
We are also proposing VOC standards for new or modified storage
vessels. The proposed rule, which would apply to individual vessels,
would require that vessels meeting certain specifications achieve at
least 95-percent reduction in VOC emissions. Re