A
(Mm* #%•<*«<*•»
fewn«w»qi|rr-
Petroleum Refmery
oEm MACT Standard
Guidance
-
(Revtied to includt RuN Amendment*)
Revised Document
-------
EPA-456/B-00-001
Petroleum Refinery MACT
Standard Guidance
(Revised to include Rule Amendments)
Prepared for:
Office of Air Quality Planning and Standards
US Environmental Protection Agency
Research Triangle Park, NC 27711
Prepared by:
Eastern Research Group
November, 2000
Revised Document
-------
Petroleum Refinery MACTStandard Guidance
Notice
The statements in this document are intended solely as
guidance. This document is not intended, nor can It be relied
on, to create any rights enforceable by any party in litigation
with the United States. EPA and State officiate may decide to
follow the guidance provided In this document, or to act at
variance with the guidance, based on an analysis of specific
site circumstances. This guidance may be revised without
public notice to reflect changes in EPA's policy.
Mentions of trade names or commercial products in this
document or associated references does not constitute an
endorsement or recommendation for use.
November 1, 2000
i
-------
Petroleum Refinery MACTStandard Guidance
Acknowledgments
The Petroleum Refinery MACT Standard Guidance document was originally prepared by
Science Applications International Corporation under the direction of Rafael Sanchez of
EPA's Office of Enforcement and Compliance Assurance, under EPA contract number
68-C4-0072. This document has now been updated to include rule amendments as of
November, 2000, see below*.
The US Environmental Protection Agency's Manufacturing, Energy and Transportation
Division in the Office of Enforcement and Compliance Assurance would like to express
thanks and appreciation to everyone who helped make the Petroleum Refinery MACT
Standard Guidance possible.
Special thanks to the Petroleum Refinery MACT Review Members: Fred Weeks, EPA
Region 1; Harish Patel, EPA Region 2; Paul Dressel, EPA Region 3; Mirza Baig, EPA
Region 4; Kathy Keith, EPA Region 5; Martin Brittain, EPA Region 6; Bill Peterson, EPA
Region 7; Scott Whitmore, EPA Region 8; John Kim, EPA Region 9; Doug Hardesty &
Andrea Longhouse, EPA Region 10; Jim Durham and Larry Brockman, EPA OAQPS, and
Mary Lalley, ERG, Inc.
* This updated document was prepared by the Environmental Research Group Inc. under
the direction of Larry Brockman of EPA's Office of Air Quality Planning and Standards,
under Task Order 68-D6-011.
November 1, 2000
-------
Petroleum He finery MACT Standaro Quids nc
How to Download this Document Electronically from the Interne
This document is electronically available through the EPA Public Access serve- .v ire
following Web site: http://www-epa.aov/envirosense/oeca/metd/ref.html or from EPA
Unified Air Toxics Website's .Petroleum Refinery webpage:
http://www.eDa.aov/ttn/uatw/petrefine/petrefpa.html
Additional Resources
Applicability Determination Index (ADI):
http://134.67.104.12/cfdocs/adiwww/adiwww.html-ssi
Additional information and guidance on the applicability of the MACT J ca
be obtained through the EPA's Applicability Determination Index (ADI/ The AD: ,5
a database that contains memoranda issued by EPA on the applicability anc:
compliance issues associated with the New Source Performance Standards
(NSPS), National Emissions Standards for Hazardous Air Pollutants (wit>-
categories for both NESHAP, Part 61, and MACT, Part 63), and
chlorofluorocarbons (CFC). Recently issued determinations are added *>; the
database on a quarterly basis.
The National Compliance Assistance Clearinghouse is your guide to
compliance information on the Internet. It provides quick access to
compliance tools, contacts, and planned activities from across EPA as we!'
as other compliance assistance providers. To find out more about the
Clearinghouse, go to www.epa.Qov/clearinahouse
Contact List
EPA Regional Contact List (see Appendix H)
iii
-------
Petroleum Refinery MACTStandard Guidance
Table of Contents
Paae
Introduction 1-1
The Petroleum Refinery MACT Standard: An Overview 2-1
2.1 Applicability of the Rule 2-2
2.2 How Does a Facility Determine the Emission Points to Which
the Control Requirements Apply? 2-3
2.3 What Are the Control Requirements? 2-5
2.4 When Must A Facility Comply? ; 2-6
2.5 Conclusions ¦ 2-13
General Standards 3-1
3.1 What are the Performance Testing Requirements That Must Be
Met By All Regulated Emission Points? 3-1
3.2 What are the Monitoring Requirements For All Regulated
Emission Points? 3-2
3.3 What are the Reporting Requirements For All Regulated Emission
Points? 3-1
3.3.1 What are the Requirements For Permit Applications? 3-2
3.3.2 What are the Requirements for Applications for Approval of
Construction or Reconstruction? 3-3
3.3.3 What are the Requirements for Notification of Compliance
Status (NCS)? 3-3
3.3.4 What are Periodic Reports, and When Are They Required? 3-4
3.3.5 What are the Requirements for Startup, Shutdown, and
Malfunction Plan and Reports? 3-4
3.3.6 What are Reports Required for Special Situations? 3-5
3.3.7 When can Facilities Submit Requests for Extension of
Compliance? 3-6
3.3.8 What are the Requirements for Applications for a Performance
Test Waiver? 3-6
3.4 What are the Recordkeeping Requirements? 3-6
November 1, 2000
IV
-------
Petroleum Refinery MACTStandard Guidance
pgci
3.5 Conclusions 5
4. Emission Points Subject to the Regulation
4.1 What are the Requirements for Miscellaneous Process Vents? .
4.1.1 What are the Control Requirements for Miscellaneous
Process Vents? 4-1
4.1.2 What are the Testing Requirements for Miscellaneous
Process Vents? ^
4.1.3 What are the Monitoring Requirements for Miscellaneous
Process Vents?
4.1.4 What are the Reporting Requirements for Miscellaneous
Process Vents?
4.1.5 What are the Recordkeeping Requirements for Miscellaneous
Process Vents? 4-9
4.2 What are the Requirements for Storage Vessels? 4-10
4.2.1 What are the Control Requirements for Storage Vessels? . . .4-11
4.2.2 What are the Testing Requirements for Storage Vessels? . . . 4-11
4.2.3 What are the Monitoring and Inspection Requirements for
Storage Vessels? .4 1?
4.2.4 What are the Reporting Requirements for Storage
Vessels? 4-14
4.2.5 What are the Recordkeeping Requirements for Storage
Vessels? 4-18
4.3 What are the Requirements for Wastewater Streams? 4 ¦ 1 p
4.3.1 What are the Control Requirements for Wastewater
Streams? 4 n:
4.3.2 What are the Testing Requirements for Wastewater
Streams? '--K
4.3.3 What are the Monitoring Requirements for Wastewater
Streams? - :t-
4.3.4 What are the Reporting and Recordkeeping Requirement?
for Wastewater Streams? 4-1 £¦
4.4 What are the Requirements for Gasoline Loading Racks? 4 -1c
November 1 20'
V
-------
Petroleum Refinery MACTStandard Guidance
Em&
4.4.1 What are the Control Requirements for Gasoline Loading
Racks? 4-20
4.4.2 What are the Testing and Monitoring Requirements for
Gasoline Loading Racks? 4-20
4.4.3 What are the Reporting and Recordkeeping Requirements
for Gasoline Loading Racks? 4-22
4.5 What are the Requirements for Marine Tank Vessel Loading? 4-22
4.5.1 What are the Control Requirements for Marine Tank
Vessel Loading? 4-22
4.5.2 What are the Testing and Monitoring Requirements for
Marine Tank Vessel Loading? 4-23
4.5.3 What are the Reporting and Recordkeeping Requirements
for Marine Tank Vessel Loading? 4-23
4.6 What are the Requirements for Equipment Leaks? 4-23
4.6.1 What are the Control Requirements for Equipment Leaks? 4-23
4.6.2 What are the Testing, Inspection, and Monitoring
Requirements for Equipment Leaks? 4-23
4.6.3 What are the Reporting and Recordkeeping Requirements
for Equipment Leaks? 4-24
4.7 Emissions Averaging 4-24
4.7.1 Emissions Averaging Applicability 4-24
4.7.2 Emissions Averaging Credit/Debit System 4-25
4.7.3 Approval of Emissions Averaging Plan 4-26
4.7.4 Testing, Monitoring, Reporting, and Recordkeeping for
Emissions Averaging 4-26
4.7.5 Recordkeeping for Emissions Averaging 4-27
4.8 Conclusions 4-27
5. Interrelationship of the Petroleum Refinery MACT Standard with
Other Regulations 5-1
November 1, 2000
VI
-------
Petroleum Refinery MACT Standard Guidance
Paoe
Tables
Tabie 2-1 Applicability of the Petroleum Refinery MACT Standard 2-3
Table 2-2 Control Applicability Criteria for Emission Points 2-4
Table 2-3 Control Requirements for Process Units/Emission Points 2-6
Table 4-1 Monitoring Requirements for Combustion Devices 4-5
Table 4-2 Monitoring Requirements for Miscellaneous Process
Vents with Bypass Lines — : 4-5
Table 4-3 40 CFR Part 63, Subpart CC( Table 10 Parameters 4-7
Table 4-4 Additional Recordkeeping Requirements 4-10
Table 5-1 Overlap of the Petroleum Refinery MACT Standard
(40 CFR 63 Subpart CC) with Existing Regulations 5-4
November 1, 2000
vii
-------
Petroleum Refinery MACTStandard Guidance
Paoe
Figures
Figure 2-1 Emission Points within an Affected Source 2-2
Figure 2-2 Determination of Applicability for Miscellaneous Process Vents 2-7
Figure 2-3 Determination of Applicability for Storage Vessels 2-8
Figure 2-4 Determination of Applicability for Wastewater Streams 2-9
Figure 2-5 Determination of Applicability for Gasoline Loading Racks 2-10
Figure 2-6 Determination of Applicability for Marine Tank Vessel Loading 2-11
Figure 2-7 Determination of Applicability for Equipment Leaks 2-12
Appendices
Appendix A. Hazardous Air Pollutants A-1
Appendix B. Organic Hazardous Air Pollutants B-1
Appendix C. U.S. Petroleum Refineries Affected by the Petroleum Refinery
Standards C-1
Appendix D. Additional Resources for Petroleum Refining MACT Standard
Guidance Document D-1
Appendix E. Definitions E-1
Appendix F. Compliance Checklist for the Petroleum Refinery MACT
Standard (40 CFR Part 63, Subpart CC) F-1
November 1, 2000
viii
-------
Petroleum Refinery MACTStandard Guidance
to-
Appendix G. Recent Changes to the MACT Standard G-
Appendix H. EPA Regions and Regional Contacts For the Petroleum Refiner,
MACT Standard Implementation H-i
Technical Report Data
Nf-vembei ' 21
ix
-------
I
Petroleum Refinery MACTStandard Guidance
I. Introduction
In August 1995, the United States Environmental Protection Agency (EPA) promulgated
the National Standards for Hazardous Air Pollutants (NESHAP) for petroleum refineries
that were originally proposed in July 1992. These standards require petroleum refineries,
that are major sources of Hazardous Air Pollutants (HAPs), to meet emission standards
reflecting the application of the maximum achievable control technology (MACT). The
affected sources at petroleum refineries are defined to include all process vents, storage
vessels, marine tank vessel loading operations, gasoline rack operations, equipment
leaks, and wastewater treatment systems located at the refinery. This manual was
developed to assist refineries in determining the applicability of these new standards to
their operations, and to provide guidance to assist facilities in achieving and maintaining
compliance.
The manual is presented in five chapters. Chapter 1 states the purpose, scope, and layout
of the document. Chapter 2 summarizes the major parts of the regulation, applicability of
the regulation to specific process units, applicable control requirements, and processes
not covered under the new rule. Chapter 3 discusses general standards applicable to all
process units. Chapter 4 builds on the genera! requirements, and discusses requirements
specific to each type of process unit and for facilities that use emissions averaging.
Finally, Chapter 5 shows where the new Petroleum Refinery MACT standard overlaps with
existing regulations.
November 1, 2000
1-1
-------
Petroleum Refinery MACTStandard Guidance
2. The Petroleuh Refinery MACT Standard: An Overview
The maximum achievable control technology (MACT) standard for petroleum refineries
stems from the Clean Air Act Amendments (the Act) of '1990. Under the Act, EPA is
required to regulate emissions of 188 listed hazardous air pollutants (HAPs), also known
as air toxics. On July 16,1992, EPA published a list of source categories (industry
groups) that emit one or more of these HAPs. For listed categories of "major" sources
(those ;hat emit 10 tons annually or more of a listed pollutant or 25 tons or more of a
combination of pollutants annually- see Appendix I of this document for additional
information on "major sources), the Act requires EPA to develop standards that will require
the application of maximum achievable control technology.
The list of industry groups to be regulated includes petroleum refineries, because they are
a major source of HAP emissions. Consequently, the MACT standard was developed to
help control this source of emissions.
The Petroleum Refinery MACT standard applies to petroleum refining process units and
related emission points. The standard MACT includes testing, monitoring, reporting,
recordkeeping, and control requirements. Requirements in the MACT standard include
control of HAP emissions from the following emission points within petroleum refining
process units: process vents, storage vessel loading, wastewater collection and treatment
systems, gasoline loading racks, marine tank vessel
loading, and equipment leaks. There are two
general approaches to comply with the MACT
standard's control requirements:
(1) Implement controls on all emission points that
meet the criteria for control in the rule; or
(2) Use a method called emissions averaging.
This method allows the facilities flexibility to
choose certain emission points for control in
order to achieve the required emissions
reductions in the most cost-effective manner. In
some situations, facilities may find it more cost-
November 1, 2000
Who Will Be Affected By The
Petroleum Refinery MACT
Standard?
There are approximately 165
petroleum refineries as of
January 1,1997 in the United
States, all of which are
anticipated to be major
sources of HAPs, and
therefore, may be subject to
this regulation.
2-1
-------
Petroleum Refinery MACTStandard Guidance
effective to overcontrol certain emission points and undercontrol others, so r i tr,c
overall result would be greater emissions reductions at less control cost. Tnt M AC "i
standard spells out how facilities may use emissions averaging and which emissio<
points may be included. This approach can only be used for existing sources A
detailed explanation of emissions averaging is found in Chapter 4 of this manual.
Blinder the Petroleum Refinery MACT standard, the term "source" refers to trie
entire refinery, whereas under New Source Performance Standards {NSPS;
and State Implementation Plans (SIPs), sources are most commonly process
units. The MACT standard applies only to major sources. Under the MACT
standard, there are different requirements depending on whether the facility is an exis, /
source or a new source. The MACT Standard defines existing and new source^ a-
follows:
Existing sources - sources that commenced construction on or before July 14 1994
New sources - sources that commenced construction after July 14,1994. A process unit
constructed at an existing source is subject to new source requirements if the new unit has
the potential to emit 10 tons per year (tpy) or more of any one HAP or25tpy o> 'no e 0?
total HAPs. Otherwise it is subject to the requirements applicable to existing sources. A
change to an existing source or an addition of an emission point is subject to existing
source standards, unless it is a reconstructed source, which is subject to new s.n.roe
standards.
This chapter provides an overview of the major elements of the rule, including genera1
applicability, control requirements, and compliance deadlines. General information or
testing, monitoring, reporting, and recordkeeping is given in Chapter 3 and a detailed
discussion of individual emission points is found in Chapter 4.
2.1 Applicability of the Rule
Noverr^p" "
2-2
-------
Petroleum Refinery MACTStandard Guidance
The affected source is the combination of all the emission points located at a refinery, and
each point is considered part of the single affected source. The MACT standard also
applies only to major sources as defined by Section 112(a) of the Clean Air Act with the
potential to emit hazardous air pollutants. For clarification on whether a source is a major
source, see Appendix E. Figure 2-1 gives an example of each of the emission points
FIGURE 2-1. Emission Points Within an Affected Source
Finished Product
Storage Vessels
Miscellaneous
Process I
Vents
Gasoline
Loading
Rack
Raw Matenai
Storage Vesse'
Finished Product
Storage Vessel
Wastewater
4 Streams
—
within an affected source. TABLE 2-1 presents the emission points to which the
Petroleum Refinery MACT standard applies. If any of the points in TABLE 2-1 is not
located at the refinery, the MACT standard does not apply.
TABLE 2-1. Applicability of the Petroleum Refinery MACT Standard
The Rule Applle* To
The Rules Does Not Apply To
November 1, 2000
-------
Petroleum Refinery MACT Standsrd Guidance
Refineries that are major HAP sources under
either of the following definitions;
Potential to emit > 10 tons per year (tpy) of
any of the 188 HAPs in Appendix A of this
manual; or
Potential to emit i 25 tpy of total HAPs
Refining process units at refineries that are
major sources and emit or contain any of the
28 HAPs in Appendix B of this manual
The following emission points within
petroleum refining process units at major
sources;
Miscellaneous process vents that contain *
20 ppmv total organic HAP
Storage vessels (pressure vessels and
vessels < 40 m3 are exempt)
Wastewater streams and treatment
operations
Equipment containing or contacting a fluid is
> 5% by weight total organic HAPs.
The following emission points if located at
refineries that are major sources:
Marine vessel loading operations
Gasoline loading racks in SIC 2911
Storage vessels and equipment leaks
associated with bulk gasoline terminals in SIC
2911,
Refineries that are not major > ¦-, , e;
Equipment that does not err. • ;d -
any of the HAPs in Append - i, : * i- •
manual
Catalytic cracking and reform ng ca^ >•=
regeneration vents
Sulfur recovery plant vents
Research and development 1a ¦ .fi-
ll nits processing natural ga
Units for recycling discarded ¦
Shale oil extraction units
Ethylene processes
Units subject to the hazardous organic
NESHAP (HON) [40 CFR 63 SubDB'ts. h
G, H, and I]
Storm water from segregate;' stem-. wa;e-
sewers
Spills
Equipment in organic HAP service < 300
hours during the calendar yea-
2.2 How Does A Facility Determine the Emission Points to Which the
Control Requirements Apply?
The introduction to this chapter presented how a facility determines if it is classified as an
existing or newsource. Once this determination has been made, a facility must assess
whether it meets the criteria for requiring controls on its emission points. TABLE 2-2
2-4
-------
Petroleum Refinery MACTStandard Guidance
presents the control applicability criteria for each type of emission point. Emission points
that meet these criteria are called Group 1 emission points, while all other emission points
are called Group 2 emission points. Group 1 emission points are subject to all applicable
requirements of the MACT standard. Group 2 emission points are not subject to the
control or monitoring requirements of the MACT standard. However, Group 2
emission points are subject to certain recordkeeping requirements.
TABLE 2-2. Control Applicability Criteria for Emission Points
Emission
For Existing Sources, Controls Must
For New Sources, Controls Must Be
points
Be Used If:
Used If:
Miscellaneous
(1) Organic HAP concentration 2 20
(1) Organic HAP concentration > 20
Process
ppmv, and
ppmv, and
Vents
(2) Total VOC emissions ^ 33 kg/day.
(2) Total VOC emissions 2 6.8 kg/day
Storage
(1) Capacity ^ 177 m3, and
(1) Capacity> 151 m3, and
Vessels
(2) Vapor pressure > 10.4 kPa
(2) Vapor pressure > 3.4 kPa (maximum),
(maximum) and > 8.3 kPa (annual
and
average), and
(3) Organic liquid HAP concentration >
(3) Organic liquid HAP concentration >
2% by weight (annual average).
4°/t by weight (annual average).
OR
(1) Capacity ^ 76 and < 151 m3, and
(2) Vapor pressure > 77 kPa (maximum),
and
(3) Organic liquid HAP concentration >
2% by weight (annual average).
November 1, 2000
2-5
-------
Petroleum Refinery MACT Standard Guidana
Emission
points
For Existing Sources, Controls Must
Be Used If;
For Haw Sources, Controls Must Be
Used If:
Wastewater
Streams
(1) Total annua! benzene loading * 10
megagrams per year, and
(2} Flow rate 2 .02 liters per minute, and
(3) Benzene concentration 2 10 ppm by
weight, and
(4) Not exempt from controls under 40
CFR 61 Subpart FF.
(1) Total annual benzene lome 1C
megagrams per year, and
(2) Flow rate 2 .02 liters per mmjte. ana
(3) Benzene concentration if: d,
weight, and
(4) Not exempt from controls a"'}*-- t'
CFR 61 Subpart FF.
Gasoline
Loading
Racks
Part of bulk gasoline terminal located at
facilities designated under SIC 2911 with
gasoline throughput > 75,700 liters per
day.
Part of bulk gasoline termina seated a
facilities designated under SIC 29"w-:
gasoline throughput > 75,70r 1-
day.
Marine Tank
Vessel
Loading
(1) Vapor pressure of liquid loaded 2
10.3 kPa, and
(2) Emission > 9.1 megagrams of any
HAP or > 22.7 megagrams of total
HAP per year after August 18, 1999.
{1) Vapor pressure of liquid ioa-jec "0,;-
kPa
(2) No parallel emission rate ft-
new sources.
Equipment
Leaks
Equipment containing or contacting fluid
that is 5% by weight total organic HAPs.
Equipment containing or contact ig fu-
that is 5% by weight total orga-, c HAP;
Included at the end of this chapter in Figure 2-2 through 2-6 are decision flowcharts wnic
show how a facility can determine first if it is subject to the MACT standard, ana second if
Group 1 or Group 2 requirements apply. Decision flowcharts have been included tor ear.,
emission point that is potentially subject to the MACT standard (i.e., miscellaneous
process vents, storage vessels, wastewater streams, gasoline loading racks, r >ar.r,e
vessel loading, and equipment leaks).
23 What Are the Control Requirements?
Mover: >be 1,20
2-6
-------
Petroleum Refinery MACTStandard Guidance
TABLE 2-3 summarizes the control requirements for emission points meeting the criteria
in TABLE 2-2, Please note that while TABLE 2-3 provides an inclusive (as of
September 1997) summary of the control requirements for these emissions points,
specific requirements can be found in the referenced section of the Code of
Federal Regulations.
2.4 When Must A Facility Comply?
The MACT standard specifies the dates by which each emission point at new and existing
sources must be in compliance with the control requirements. All emission
points at new sources must be in compliance at startup or by August 18,1995, whichever
is later.
There is a specific compliance date for each emission point at existing sources.
Miscellaneous process vents and gasoline loading racks have a compliance date of
August 18,1998. Wastewater streams also have a compliance date of August 18,1998,
and sources should be in compliance with the benzene waste operations NESHAP found
in 40 CFR 61 Subpart FF.
Fixed roof storage vessels must be in compliance by August 18,1998 as well; however,
the preamble suggests compliance by August 18, 1999 if the tank must be replaced.
November 1, 2000
2-7
-------
Petroleum Refinery MACTStandard Guidance
TABLE 2-3. Control Requirements for Process Units/Emission Point?
Emission points
I
Control Requirements
Miscellaneous Process
Vents
Reduce organic HAPs by 98% or to 20 ppmv using incinerator
boilers, process heaters, or other devices; or
• Use a flare.
Storage Vessels
Comply with storage vessel NESHAP [40 CFR 63 Sure, '" C
which requires:
Internal floating roof with specified seals; or
External floating roof with specified seals; or
External floating roof converted to internal floating roof v.,.*
specified seals; or j
Closed vent system with 95% efficient control device, ]
Wastewater Streams
|
Comply with benzene waste operations NESHAP [40 CFR 6* Suhcar i
FF], which requires:
Reducing benzene mass emissions by 99% using swp.ufcsb.:
followed by another treatment process (e.g., steam stnpo ng t - j
biotreatment); and |
Reducing emissions from vents from stream strippers, otner
management, or treatment units by 95% with a contr ¦ c .'-t >•
20 ppmv at the outlet of the control device.
Gasoline Loading Racks
Comply with gasoline distribution NESHAP [40 CFR 63 Sub;x-<". n,,
which requires: i
;
Reducing emissions of total organic compounds to if '• r.i" -
per liter of gasoline loaded; and
Loading only in vapor tight cargo tanks that have bee- teste,, r
assure vapor tightness.
Marine Tank Vessel
Loading
Comply with marine tank vessel loading NESHAP [40 CFP ¦ Sun: >
Y], which requires:
Reducing HAP by 97% for existing sources
Reducing HAP by 98% for new sources.
2-8
-------
Petroleum Refinery MACTStandard Guidance
Emission points
Control Requirements
Equipment Leaks
Comply with equipment leak rules [40 CFR 63 Subpart H or 40 CFR 60
Subpart VV] for existing sources and [40 CFR 63 Subpart H] for new
sources, which require:
Leak detection and repair with specified leak definitions and
monitoring frequencies
Equipment specifications for some types of equipment.
November 1, 2000
2-9
-------
FIGURE 2-2. Determination of Applicability for Miscellaneous Process Vents
No
Yes
No
Yes
No
No
Yes
¦Existing
New-
No-
¦Yes
•Yes
No-
Group 1 miscellaneous
process vent*
Group 1 miscellaneous
process vent*
Group 2 miscellaneous
process vent*
Group 2 miscellaneous
process vent*
Is vent associated with an existing or new source?
Miscellaneous
process vent
provision
does not apply
Is organic HAP concentration > 20 ppmv, and
total VOC emissions > 33 kg/day?
Existing Source:
Is organic HAP concentration > 20 ppmv, and total
VOC emissions >6.8 kg/day?
New Source:
Does the vent contain a gas stream with 20 ppm by volume organic HAP and is it
continuously or periodically discharged during normal operations?
Note: The above list gives examples of where vent or gas streams may originate and may not be all inclusive.
Does the vent or gas stream come from: caustic wash accumulators, distillation lower condensers/
accumulators, Hash/knockout drums, reactor vessels, scrubber overheads, stripper overheads, vacuum
accumulators, blowdown condensers/accumulators, and delayed coker vents?
Note: The above list gives examples of vent or gas streams and may not be all inclusive.
- directly discharged to the atmosphere or
- routed to a control device prior to discharge to the atmosphere or
- diverted to a product recovery prior to control or discharge to the atmosphere?
Is the vent/gas stream:
Gas streams routed to a fuel gas system
Relief valve discharges
Leaks from equipment regulated under 40 CFR 63.648
Episodic or nonroutine releases such as maintenance or upsets
In situ sampling systems (onstream analyzers)
Catalytic cracking unit catalyst regeneration vents
Catalytic reformer regeneration vents
Sulfur plant vents
Vents from control devices
Vents from any stripping operations applied to comply with the wastewater provisions of 40 CFR
63 Subpart CC, G, or FF
Coking unit vents associated with coke drum depressuring at or below a coke drum outlet pressure
of 15 pounds per square inch gauge, deheading, draining, ordecoking (coke cutting) or pressure
testing after decoking
Vents from storage vessels
Emissions from wastewater collection and conveyance systems?
Does the vent or gas stream come from:
* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points
2 -10
November 1, 2000
-------
FIGURE 2-3. Determination of Applicability for Storage Vessels
¦No-
Yes
Yes
No
Yes
No
Yes
No
Yes
No
Yes
No
¦Existing
•New-
¦Yes
-No-
¦Yes
¦No-
Storage vessels
provision does
not apply
Group 1 storage
vessel*
Group 2 storage
vessel*
Group 1 storage
vessel*
Group 2 storage
vessel*
Is tank associated with an
existing or new source?
Is it used as a bottoms receiver
tank?
Is it used as a wastewater
storage tank?
Does it have a capacity less than
40 cubic meters?
Storage
vessels
provision
does
not
apply
Is it permanently attached to a
motor vehicle such as a truck,
railcar, barge or ship?
Is it a tank or other vessel that is used to
store organic liquids? (i.e., is this a storage
vessel "as described in the rule"?)
Is it a pressure vessel designed to operate
in excess of 204.9 kilopascals and without
emission to the atmosphere?
Is capacity > 177 m3 and vapor pressure > 10.4
kPa (maximum) and > 8.3 kPa (annual average),
and liquid HAP content > 4% by weight
(annual average)?
Existing Source:
Is capacity >151 m3 and vapor pressure > 3.4 kPa
(maximum), and liquid HAP content > 2% by weight
(annual average)?
OR
Is capacity between 76 and 151 m3, and vapor
pressure >77 kPa (maximum), and liquid HAP >2%
by weight (annual average)?
New Source:
* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.
2-1fCa)
November 1, 2000
-------
FIGURE 2-4. Determination of Applicability for Wastewater Streams
Yes
No—~
Yes
/ Applicability
criteria are the
same for
existing and
\ new sources
•Yes'
Group 2 wastewater
stream*
Group 1 wastewater
stream*
Wastewater provision
does not apply
Is discharged into any individual drain
system?
Is it water or wastewater that, during production or processing:
Comes into direct contact with or results
from the production or use of any raw
material, intermediate product, finished
product, byproduct, or waste product?
Does refinery have a total annual benzene
loading > 10 megagrams per year, and a
flow rate > 0.02 liters per minute, and
benzene concentration > 10 ppm by
weight, and subject to control requirements
under 40 CFR 61 Subpart FF?
[Examples of wastewater are: feed tank drawdown; water formed during a chemical reaction or used as a
reactant; water used to wash impurities from organic products or reactants; water used to cool or quench
organic vapor streams through direct contact; and condensed steam from jet ejector systems pulling vacuum
on vessels containing organics.]
* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.
2 -J7(h)
November 1, 2000
-------
FIGURE 2-5. Determination of Applicability for Gasoline Loading Racks
No-
Yes
No-
Yes
Applicability
criteria are the
same for
existing and
new sources
•Yes'
No-
Group 2 gasoline
loading rack*
Group 1 gasoline
loading rack*
Gasoline loading racks
provision does not apply
Is it a gasoline loading rack
classified under SIC 2911?
Does it have a gasoline throughput >
75,700 liters (20,000 gallons) per day?
loading arms, pumps, meters, shutoff valves,
relief valves, or
other piping and valves necessary to fill
gasoline cargo tanks?
Is it any of the following:
* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.
2-It Cc)
November 1, 2000
-------
Petroleum Refinery MACTStandaro Guida;
FIGURE 2-6. Determination of Applicability for Marine Tank Vessel Loading
'No-
Yes
Existing-
¦New-
•Yes-
No-
¦Yes-
No-
Group 1 marine tank
vessel loading*
Group 1 marine tank
vessel loading*
Group 2 marine tank
vessel loading*
Group 2 marine tank
vessel loading*
Marine tank vessel
loading provision
does not apply
Is it a land- or sea-based terminal or
structure that loads liquid commodities in
bulk onto marine tank vessels?
Is marine tank vessel loading associated
with an existing or new source?
Is vapor pressure of liquid loaded> 10.3 kPa?
New Source:
Is vapor pressure of liquid loaded> 10.3 kPa arid
emissions > 9.1 megagrams of any one HAP or >
22.7 megagrams of total HAP per year?
Existing Source:
" See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points
J ———-
Nli.Prn-7 " ,
2-12
-------
Petroleum Refinery MACT Standard Guidance
November 1, 2000
2-13
-------
Petroleum Refinery MACTStandard Guidance
FIGURE 2-7. Determination of Applicability for Equipment Leaks
Yes1
No
Yes
Equipment
leaks
provision
does not
apply
Equipment leaks provision applies
Is it a vent from a wastewater system
drain, tank mixer or sample valve on a
storage tank?
Is it an emission of organic hazardous air
pollutants from a pump, compressor,
pressure relief device, sampling connectior
system, open-ended valve or line, valve,
or instrumentation system "in organic
hazardous air pollutant service" (equipmeni
containing or contacting fluicfc 5% by
weight total organic HAP)?
* See Chapter 4 (or applicable requirements for Group 1 and Group 2 emission points
f
Novennfap' ~ ?C»"
2-14
-------
Petroleum Refinery MACT Standard Guidance
Floating roof storage vessels have a compliance date of August 18,2005, or the next
scheduled maintenance and degassing after August 18,1998, whichever is first.
Marine tank vessel loading must be in compliance by August 18,1999, unless used in
emissions averaging. If used to generate credit in an emissions average, it must comply
by August 18,1998, unless a case-by-case 1-year extension is granted.
A compliance late of A jgust 18,1998 is set for equipment leaks. Sources have the
option of complying with 40 CFR 60 Subpart W or 40 CFR 63 Subpart H, which allows for
3 phases of emissions reductions. (See Chapter 4 for more detailed information on
compliance dates for equipment leaks.)
2.5 Conclusions
Chapter 2 provided an overview of the MACT Standard answering the questions of which
facilities must comply; what facilities must do to comply, and when must they comply. The
overview defined the applicability of the MACT Standard to affected sources, and the
various types of emission points associated with the affected sources. Chapter 2 also
defined the control requirements applicable to the various emission points, noting which
points are required to maintain control equipment, and the types of control or associated
emission limit. Finally, Chapter 2 provided compliance deadlines for each category of
emission point. After reviewing the applicability determination flow charts in Chapter 2, a
facility should be able to determine whether the general requirements to be discussed in
Chapter 3, or the specific requirements in Chapter 4 will apply.
November 1, 2000
2-15
-------
Petroleum Refinery MACT Standard Guidance
3. General Standards
Once the refinery has determined which of its emission points are required to comply with
the Petroleum Refinery MACT standard (MACT standard), the refinery must determine the
specific requirements applicable to each emission point. While the control requirements
are specific to each type of emission point at the refinery, the MACT standard also
contains general provisions that are applicable to
all emission points. These general requirements
include performance testing, monitoring', reporting,
and recordkeeping. In addition, some reporting
requirements apply only to refineries conducting
certain activities.
Chapter 3 discusses the general requirements
applicable to all emission points at refineries.
Chapter 4 describes the control requirements
applicable only to specific emission points, as well
as emissions averaging - an alternative method to controlling emissions.
3.1 What are the Performance Testing Requirements That Must Be Met By
All Regulated Emission points?
All facilities are required to conduct an initial performance test of certain pollution control
equipment. (No performance tests are required for floating roofs or process heaters > 44
MW with vent introduced into the flame zone.) These initial performance tests must be
approved by EPA. To conduct the test, the facility must:
• Notify regulatory authority 30 days prior to conducting a performance test [40 CFR
63.642(d)(2)]
• Conduct tests at maximum representative operating capacity, with controls operating at
either maximum or minimum representative operating conditions for monitored
parameters, whichever result in lower emission reduction [40 CFR 63.642 (d)(3)].
General requirements for all
emission points include:
performance testing, monitoring,
reporting (including permit
applications and notifications of
compliance status), and
recordkeeping.
November 1, 2000
3-1
-------
Petroleum Refinery MACTStandard Guidance
3.2 What are the Monitoring Requirements For All Regulatid Emission
points?
Monitoring is required for some Group 1 emission points. Requirements range frorr once
an hour for miscellaneous process vents routed to a flare, to no monitoring requirements
for Group 1 storage vessels equipped with an external floating roof. Specific monitoring
requirements for each process unit are presented in Chapter 4.
3.3 What are the Reporting Requirements For All Regulated Emission
Points?
Reporting requirements range from permit applications, and initial notification o<
compliance status, to those requesting compliance extensions. With the exceptor
periodic reports, all reports are one-time submittals, or one time per incident submittals
The following types of information/reports must be submitted, where applicable fc r ea~-
emission point to the appropriate EPA Regional Office [40 CFR 63.13](See Appendix H
for a list of EPA Regional Offices);
• Permit Applications
• Applications for Approval of Construction or Reconstruction
• Notification of Compliance Status
• Periodic Reports
• Startup, Shutdown, and Malfunction Reports
• Reports Required for Special Situations
• Requests for Extension of Compliance
• Applications for a Performance Test Waiver.
Novftrriber
3-2
-------
Petroleum Refinery MACTStandard Guidance
Each of these requirements is presented in the following subsections.
3 J.I What are the Requirements For Permtt Applications?
All owners or operators of a source subject to
the rule are required to apply for a one-time Part
70 or Part 71 operating permit from the
appropriate authority. A source may apply for
the permit from either EPA or its State authority,
depending on whether EPA has approved a
State operating permit program. [40 CFR
63.642(a)]
The source must apply for a permit
from its state if EPA has approved
a State operating permit program
under Part 70. The source must
apply for a permit from its EPA
Regional Office if the State does
not have an EPA operating permit
program under Part 71.
November 1, 2000
3-3
-------
Petroleum Refinery MACTStandard Guidance
3.3.2 What are the Requirements for
Applications for Approval of
Construction or Reconstruction?
All new or reconstructed sources are
required to submit an application for
approval of construction or reconstruction.
Existing sources are not required to submit
the application, unless new construction or
reconstruction occurs at the source.
General application requirements include
[40 CFR 63.5(d)]:
• Applicant's name and address
• Notification of intent to construct a new
major affected source
• Source description and address
• Identification of relevant standard that is
the basis of the application
Construction means the on-site
fabrication, erection, or installation of a
affected source.
Reconstruction means the
replacement of components of an
affected or a previously unaffected
stationary source to the extent that
(1) The fixed capital cost of the nev.
component exceeds 50 percent of
the fixed capital cost that would De
required to construct a comparable
new source; and
(2) It is technologically and economically
feasible for the reconstructed source
to meet the relevant standard(s)
established by the Administrator (or
a state) pursuant to section 112 of
the Ciean Air Act.
• Expected commencement and completion dates of construction or reconstruction
• Anticipated date of startup
• Determination of rule applicability for each process unit (e.g., distillation units storage
vessels, flexible operation units)
• Actual or expected type and quantity of HAPs emitted
• Additional relevant information as requested by the Administrator.
Novei n^er :
3-4
-------
Petroleum Refinery MACT Standard Guidance
333 What are the Requirements for Notification of Compliance Status (NCS)?
All refineries are required to inform EPA of their compliance status with respect to the
MACT standard. Facilities must submit a NCS report within 150 days after each
applicable compliance deadline. (See Section 2.4 of this manual for compliance dates.)
There are two exceptions: When a new Group 1 emission point is added or a floating roof
storage vessel is brought into compliance, the NCS may be included in the next periodic
report.1 The report must identify each emission point and method of compliance. This
information may be included as a separate report, as an operating permit application, or ii
an amendment to an operating permit application. [40 CFR 63.654(f)] NCS report
requirements include the following:
• Determination of rule applicability to flexible operation units and storage vessels and
distillation units for which use varies from year to year [40 CFR 63.654(h)(6)]1
• Information on individual emission points to demonstrate compliance, such as range of
monitored parameters. [40 CFR 63.654(f)(1) and (f)(3)]
• Results of continuous monitoring system performance evaluations. [40 CFR
63.654(f)(4)]
• If initial performance tests are required, one example complete test report for each test
method used must be submitted. For additional tests using the same method, only the
results must be submitted. [40 CFR 63.654 (f)(2)]
33.4 What are Periodic Reports, and When are They Required?
Periodic reports are required only if compliance exceptions occur within any 6-month
reporting period. If compliance exceptions do occur, periodic reports must be submitted.
The reports must be submitted within 60 days after the end of each 6- month period. If
1This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18,
1998, For more information, see Appendix G,
November 1, 2000
I
3-5
-------
Petroleum Refinery MACTStandard Guidana
facilities use emissions averaging, reports must be submitted quarterly. [40 CFR
63.654(g)]
Periodic reports must include information on compliance exceptions, such as c. descnptK".-'
and cause of the exception and corrective action taken. (See Chapter 4 for each type c'
emission point.) If a performance test is done for an emission point that is addec c»
changed from Group 2 to Group 1, include the results, such as percent emission -
reduction or concentration, in the next periodic report. [40 CFR 63.654(g)(7)]
3.3.5 What are the Requirements for Startup,
Shutdown, and Malfunction Plan and
Reports?
The cessation of a process
unit for maintenance,
repair, or equipment
replacement
Any malfunction cf a
process unit.
All refineries must develop and implement a startup,
shutdown, and malfunction plan (SSMP) for the entire
facility, with the exception of wastewater stream
management units. An SSMP is not required for
wastewater stream management units unless they
receive streams subject to 40 CFR Part 63 Subpart G.
The malfunction plan must describe procedures for
operating and maintaining the source during periods
of startup, shutdown, and malfunction. In addition, the
plan must include a program of corrective action for
malfunction of process and air pollution control equipment used to comply with ne reievar
standard. EPA typically defines malfunctions as rare, unforeseeable occurrer ;
does not allow for facilities to operate in malfunction for extended periods of tin?
If corrective actions to address the malfunction are consistent with the startup, sh*/ jo-,--
and malfunction plan, submit a statement to this effect in the semi-annual repc . MO (J ^
63.10(d)(5)(l)]
A Startup, Shutdown, and
Malfunction Report is
required to document
• The start of operation of &
process unit for productio-
Nr . fmb
-------
Petroleum Refinery MACT Standard Guidance
If a malfunction occurs and corrective actions arenet consistent with the startup, shutdown,
and malfunction plan, this must be reported in the next periodic report.1
If a malfunction does not occur during a reporting period, a startup, shutdown, and
malfunction report is not required.
33.6 What are Reports Required for Special Siiuations?
The MACT standard has detailed requirements for testing, monitoring, and recordkeeping.
However, the rule allows for flexibility in meeting these requirements. If facilities intend to
use alternative procedures or devices, additional reports and approvals are required. For
these facilities, the following information must be submitted 18 months before the
compliance date for existing sources, or with the. application for approval of construction
for new sources:
• Request for approval to monitor an alternative control device operating parameter, with
supporting justification [40 CFR 63.654(h)(4)]
• Request for approval to use data compression systems instead of keeping hourly
records, with supporting information [40 CFR 63.654(h)(5)]
* Request to use other alternative monitoring methods, with supporting justification [40
CFR 63.654(h)(5)(iv) and 63.8(f)(4)(ii)]
* Request to establish an alternative emission standard, with a test plan or results of
testing and monitoring. [40 CFR 63.6(g)(2)] (If EPA finds the alternative standard
equivalent to the MACT standard, EPA will request public comment and publish a
Federal Register notice allowing its use.)
33.7 When Can Facilities Submit Requests for Extension of Compliance?
1This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18,
1998. For more information, see Appendix G.
November 1, 2000
3-7
-------
Petroleum Refinery MACI Standard Guidance
An extension of compliance may be requested if emission reductions have bee - r^-e ,'eo
early, or if the source is unable to comply with the relevant standard. Requests f
extension of compliance are allowed only for existing sources and must be sub'-uue.; c.
least 12 months before the compliance date, or 18 months prior if emissions averaging i.-,
used. [40 CFR 63.6(l)(2-3)] (See Chapter 2, Section 2.4 for compliance dates '
Requests must include the following;
• Description of controls to be installed
• Compliance schedule
• Interim emission control steps.
33.8 What are the Requirements for Appucations for a Performance Test? Waiver7
If a facility is unable to conduct a performance test for reasons such as technics c
economic infeasibility, an extension of compliance has been requested, or other reasons,
the facility must submit an application for waiver of a performance test to the Adminis'ra»or
The application must include information justifying the request and detailing the
infeasibility. [40 CFR 63.7(h)(3)(iii)]
3.4 What are the Recordkeeping Requirements?
All refineries are required to keep records of reports submitted, monitoring result- a-
other records for at least 5 years. [40 CFR 63.642(e) and 63.654(l)(4)] In additsor
records must be kept so that they are accessible within 24 hours of request in hard-
copy or computer-readable form. If acceptable to the Administrator, reports ma , L •
submitted on electronic media. [40 CFR 63.642(e)] The following records mu?' r
maintained on site:
• Records of the occurrence and duration of each startup, shutdown, or manure,:
operation and air pollution control equipment [40 CFR 63.10(b)(2)(l-ii)]
• Records of actions that are consistent and inconsistent with the startup, shut i nv
malfunction plan [40 CFR 63.10(b)(2)(iv-v)]
No\ p" |>p.
3-8
-------
Petroleum Refinery MACT Standard Guidance
• Records of continuous monitoring system calibration checks (if continuous monitoring
is required) [40 CFR 63.10(b)(x)j
• Records for storage vessels [40 CFR 63.654(l)(l)]
• Complete test reports and reported results for any required performance tests
[64.654(l)(2)]
• Values of continuously monitored parameters [40 CFR 63.654(l)(3)]
• Any additional records required by permit.
3.5 Conclusions
Chapter 3 discussed the general requirements of the MACT Standard (i.e., those
requirements applicable to all regulated emission points). The chapter presented the
requirements for performance testing, monitoring, reporting, and recordkeeping that apply
to all regulated emission points. For each of these requirements, Chapter 3 discussed
only those requirements that apply to every emission point. Additional requirements
applicable to individual emission points are discussed in Chapter 4.
November 1, 2000
3-9
-------
Petroleum Refinery MACT Standard Guidance
4. Emission Points Subject to the Regulation
This chapter summarizes the detailed testing, monitoring, reporting and recordkeeping
requirements specific to each emission point regulated by the MACT standard. In
addition, control requirements for each emission point are described. Unless otherwise
noted, the requirements in Chapter 4 apply only to Group 1 emissions points. With few
exceptions, Group 2 emissions points are subject only to record keeping requirements.
Chapter 4 discusses each of the regulated emission points (i.e., miscellaneous process
vents, storage vessels, wastewater streams, gasoline loading racks, marine tank vessel
loading, and equipment leaks) presenting the applicable requirements. Chapter 4
concludes with a discussion emissions averaging and how this technique can be used by
existing sources in lieu of complying with the applicable control requirements for the
individual emission points. Please note that this chapter does not discuss the
details of all of the MACT Standard requirements for each of these regulated
emissions points. In particular, in the discussion of storage vessels, wastewater
streams, gasoline loading racks, marine tank vessels and equipment leaks this chapter
references other sections of the federal code of regulations to which the refinery may be
required to comply. For further detail on the referenced sections, see the
appropriate section of the Code of Federal Regulations.
4.1 What are the Requirements for Miscellaneous Process Vents?
Once the refinery has determined which process vents are subject to the MACT standard,
the refinery must then determine the requirements applicable to each vent. These
requirements include controls, monitoring, reporting, and recordkeeping. To determine if a
process vent is subject to the MACT standard, refer to the applicability flowchart for
miscellaneous process vents in Chapter 2.
4.I.I What are the Control Requirements for Miscellaneous Process Vents?
If a vent meets the applicability criteria, it must be controlled by:
• Using a flare; or
November 1, 2000
4-1
-------
Petroleum Refinery MACTStandard Guidanct
• Reducing organic HAPs by 98% or to 20 ppmv using incinerators, boile's process
heaters, or other devices; or
• If a boiler or process heater is used, the vent stream must be introduced into the
flame zone of the control device, or in a location such that the required percent
reduction or concentration is achieved.
The following sections discuss the applicable testing, monitoring, reporting anc
recordkeeping requirements associated with each of these control methods.
4.1.2 What are the Testing Requirements for Miscellaneous Process Vents?
The MACT standard requires that
miscellaneous process vents be controlled by
routing the vents to a flare, incinerator, boiler,
process heater, other approved device, or
bypass lines. Some control devices for
miscellaneous process vents are required to
be tested during a one-time initial
performance test, and in follow-up tests in the
event of process changes. This performance
test must confirm that control equipment is
operating properly, and that emissions are
within specified limits. While some of the
components of the test are similar for all
miscellaneous process vents, the MACT
standard also applies testing requirements based on the control device as descnoeri
below.
Initial Performance Tests
Miscellaneous Process Vents are
to be Controlled if:
• It is an existing source, and the
vent contains 20 ppmv or more
of organic HAPs, and emits 33
kg/day or more of VOCs
• It is a new source, and the ven!
contains 20 ppmv or more of
organic HAPs, and emits 6.8
kg/day or more of VOCs.
Novernbe; 1
4-2
-------
Petroleum Refinery MACTStandard Guidance
Initial performance tests are required for vents routed to a flare and vents using other
approved control devices. When performance tests are required, the test measures
whether equipment is operating according to manufactuier specifications, or whether
equipment is meeting a specified emissions reduction. Vents routed to a flare have
testing requirements designed to measure whether equipment is operating properly, while
other categories of process vents must have more sophisticated equipment that measures
the level of emissions from each controlled vent. Performance tests are not required to
determine percent reduction when a
flare is used.
For vents routed to a flare, the initial
performance test must show that the
flare is operating properly, and that
the emission rate does not exceed
the capacity of the flame to control the
emissions. Based on these criteria,
the initial performance test is required
to measure the following:
• Emissions visibility (There
should be no visible
emissions.)
• Net heat value of combusted gas.
• Flow rate of gases being combusted.
For vents routed to an incinerator or a boiler or process heater < 44 Megawatts (MW) (150
MMBtu/hr) where the vent streams are net introduced into the flame zone of the boiler or
process heater, the initial performance test must show compliance with the requirement to
reduce organic HAPs by 98% or to 20 ppmv. [40 CFR 63.645 and 63.116 except (d) and
(e)]. The organic HAP concentration and percent reduction may be measured either as
total organic HAP or as total organic compounds (TOC) minus methane and ethane. The
sampling point varies depending on whether the facility is measuring total organic HAP or
TOC.
November 1, 2000
Performance tests are riot required for:
• Vents routed to a boiler or process
heater * 44 MW (150 MMBtu/hr)
• Vent streams that are introduced into the
flame zone of the boiler or process
heater
• A control device for which a
performance test was conducted for
determination of compliance with an
NSPS if no process changes have been
made.
4-3
-------
Petroleum Refinery MACTStandard Guidance
Determining Compliance Using Total Organic HAP
Sample sites must be located at both the inlet and
outlet of the control device, but the inlet sampling site
must be located after the final product recovery
device. If a process vent stream is introduced with
the combustion air or as a secondary fuel into a
boiler or process heater with a design capacity < 44
MW, selection of the location of the inlet sampling
site is required to ensure the measurement of total
organic HAP or TOG (minus methane and ethane)
concentrations in all process vent streams and
primary and secondary fuels introduced into the
boiler or process heater.
Determining Compliance Using TOC
As noted above, for vents that must show organic
HAP reduction, owners and operators can measure
that reduction either as total organic HAP or as TOC
minus methane and ethane. To measure the
reduction as TOC minus methane and ethane, the
refinery first must determine TOC according to the
procedures specified below.
Calculating the TOC
Emissions Rate:
TOC can be calculated us^n-
Method 18 or Method 25A cr j
40 CFR 60 Appendix A or a;
other method or data validate-; (
according to the protocol in j
Method 301 of 40 CFR c" !
Appendix A. When selecting ,
the sampling site, refineries are J
required to use Test Methods i
or 1 A of 40 CFR 60 Appendix
A, as appropriate. Additional
guidance on using these
methods can be found in 41
CFR 63(f), (g), and (h)
Samples must be taken:
• After the last product recovery device, but
• Prior to the inlet of any control device, and
• Prior to any dilution of the process vent stream and release to the atmosp* iere
Test Method 1 describes appropriate testing for sample and velocity traverses u
stationary sources. Test Method 1A describes appropriate testing for sample ann vp ecu>
Nov>~:rpbf-- ' v"
4-4
-------
Petroleum Refinery MACTStandard Cuidance
traverses for stationary sources with small stacks or ducts. Traverse site selection
methods are not needed for vents smaller than 0.10 meter in diameter.
Follow-up Tests to Process Changes
For Group 2 process vents, whenever the
refinery conducts a process change, the TOC
emission rate must be recalculated to determine
whether the vent remains a Group 2 process
vent or becomes a Group 1 process vent.
Recalculation may be based on vent stream flow
rate and TOC measurements as specified for
initial performance tests or best engineering
assessment practices.
4.1.3 What are the Mohftoring
Requirements for Miscellaneous
Process Vents?
Monitoring devices are not required for boilers
or process heaters > 44MW or in which all vent
streams are introduced into the flame zone. The type and frequency of monitoring
depends on the type of combustion device. All continuous monitoring devices must be
installed, calibrated, maintained, and operated according to manufacturer specifications.
Table 4-1 lists the type of monitoring required for each combustion device. Refineries with
Group 1 miscellaneous process vents may request approval to monitor parameters other
than those listed in Table 4-1 if the refinery uses a control device other than an incinerator,
boiler, process heater, or flare, or wants to monitor a parameter other than those specified
in the table. Refineries that use a vent system with bypass lines have separate
requirements that are described in Table 4-2.
For facilities using other approved control devices, or requesting to monitor other
parameters, a site-specific determination can be requested from the permitting authority.
November 1, 2000
What Constitutes a Process
Change?
Process changes include, but are
not limited to, changes in production
capacity, production rate, or catalyst
type; wheneverthere is replacement,
removal, or addition of recovery
equipment; and debottlenecking
activities.
Process changes donol include
process upsets, unintentional,
temporary process changes, or
changes that are within the range on
which the original calculation was
based.
4-5
-------
Petroleum Refinery MACTStandard Qui 3b'.a
Novemhc. J
4-6
-------
Petroleum Refinery MACTStandard Guidance
TABLE 4-1. Monitoring Requirements for Combustion Devices
Combustion Device
Type of Monitoring Required
Monitoring Location
Flare
Device capable of continuously
detecting the presence of a pilot
flame (including, but not limited
to a thermocouple, an ultraviolet
beam sensor, or an infrared
sensor)
Not specified
Incinerators other than catalytic
incinerators
Temperature monitoring device
with a continuous recorder
In the firebox or in the duct
work immediately downstream
of the firebox in a position
before any substantial heat
exchange occurs
Catalytic incinerators
Temperature monitoring device
with a continuous recorder
In the gas stream immediately
before and after the catalyst
bed
Boiler or process heater with a
design heat input capacity s 44
megawatts, or any boiler or
process heater in which all vent
streams are introduced into the
flame zone
No monitoring required
Not applicable
Boiler or process heater with a
design heat input capacity < 44
megawatts where the vent
streams are not introduced into
the flame zone
Temperature monitoring device
with a continuous recorder
In the firebox
TABLE 4-2. Monitoring Requirements for Miscellaneous Process Vents
with Bypass Lines
Type of Bypass Line Control
Type of Monitoring Required
Monitoring Location
November 1, 2000
4-7
-------
Petroleum fie finery MACT Standard Outdance
Refineries that use a vent system
with bypass line valves that have
not been sealed or secured
Flow indicator that determines at
least every hour whether a vent
stream flow is present
At the entrance to a'1
bypass line that a .. .. . e-
the vent stream awn fmr
the control device >
atmosphere
Refineries that use a vent system
with bypass lines, where the
valves have been secured in the
closed position with a car-seal or
a lock-and key-type configuration
Visual inspection at least every
other month to ensure that the
valve is maintained in the closed
position and the vent stream is
not diverted through the bypass
line
At the valve
4.1.4 What are the Reporting Requirements for Miscellaneous Process Yents?
Reporting requirements for miscellaneous
process vents include some requirements
applicable to all control devices, and additional
reporting based on the specific control device.
This section discusses the two reports with
specific requirements for miscellaneous
process vents: Notice of Compliance Status
reports, and Periodic reports.
Notice of Compuance Status Report
As noted in Chapter 3, all refineries are required
to submit a Notice of Compliance Status report.
The NCS may be submitted in an operating
permit application, an amendment to an
operating permit application, a separate
submittal, or any combination of the three. If the
required information has been submitted at an
earlier date, or at different times, and/or in
different submittals, later submittals may refer to
earlier submittals instead of duplicating and
resubmitting previously submitted information.
When Are NCS. Reports
Required?
Notice of Compliance Status reports
are required at startup, or within 150
days of an applicable compliance
deadline. If the refinery submits an
NCS report prior to the compliance
deadline, it does not need to submit
an additional report within 150 days
of the deadline. It does, however
need to send a letter to the
Administrator referencing the earlie^
notification.
For example, if a new facility submits j
an NCS report at startup in 1995 :•
is required to submit a letter referring
to the NCS (and noting that nc
process changes have occurred,
when an applicable 1998
compliance deadline occurs.
November 1 23-
4-8
-------
Petroleum Refinery MACT Standard Guidance
Information required to be included in the NCS depends on the type of emission point. For
all miscellaneous process vents, the NCS must identify each vent, whether the process
vent is Group 1 or Group 2, and, for each Group 1 vent that is not included in an emissions
average, the method of compliance (e.g., use of a flare or other control device meeting the
requirements of the MACT standard). [40 CFR 63.643(a)]
In addition, miscellaneous process vents with control devices required to be tested under
the MACT standard must submit information on each testing method, and results of the
performance test since there are different requirements for each test and test method
used. Supporting information required for each test method used is indicated in the box
below. Test results must include the following information:
• The percentage reduction of organic
HAPs or TOC or the outlet
concentration of organic HAPs or TOC
(ppm by volume on a dry basis
corrected to 3 percent oxygen),
determined as specified in 40 CFR
63.116(c)
• For vents controlled by flares, all-visible
emission readings, heat content
determinations, flow rate
measurements, and exit velocity
determinations made during the
compliance determination [40 CFR
63.654(f)(1)(iv)(A)]
• For vents controlled by flares, a
statement of whether a flame was
present at the pilot light over the full
period of the compliance determination
[40 CFR 63.654(0(1 )(iv)(B)]
Required Supporting Information
For Each Test Method Used:
D
Sampling site description
2)
Description of sampling and
analysis procedures, and any
modifications to standard
procedures
3)
Quality assurance procedures
4)
Record of operating conditions
during the test
5)
Record of preparation of
standards
6)
Record of calibrations
7)
Raw data sheets for field
sampling
8)
Raw data sheets for field and
laboratory analyses
9)
Documentation of calculations
10)
Any other information required
by the test method.
November 1, 2000
4-9
-------
Petroleum Refinery MACTStandard Guidance
• The value of the monitored parameter specified in 40 CFR 63 Subpart CC
10 (shown in Table 4-3), or a site specific parameter approved by the pe mn.r •
authority, averaged over the full period of the performance test.
Results of a prior performance test can be used if that test was conducted using the
methods specified in 40 CFR 63.645 and test conditions were representative of current
operating conditions.
TABLE 4-3. 40 CFR Part 63, Subpart CC, Table 10 Parameters
Control Device
Parameters to be Monitored
Thermal incinerators
Firebox temperature
Catalytic incinerators
Temperature upstream and downstream of the ca:j /?• be:
Boiler or process heater with a design
heat capacity < 44 MW where the vent
stream is noi introduced into the flame
zone
Firebox temperature
Flare
Presence of a flame at the pilot light
All Control Devices
Presence of flow diverted to the atmosphere from the eontr.->
device, or monthly inspections of sealed valves
Specific NCS Reports For Vents Controlled By a Flare
In addition to the above requirements, vents controlled by a flare are required to include
performance test results applicable to the specific testing of the flare. For vents routed ic a
flare, the NCS report must include the following performance test information
• AH visible readings
• Heat content determinations
• Flow rate measurements
• Exit velocity determinations
November 1 20
4-10
-------
Petroleum Refinery MACTStandard Guidance
• A statement of whether a flame was present at the pilot light over the full period of the
compliance determination
• If a parameter other than the presence of a pilot flame is monitored, the acceptable
range for the parameter and the rationale (including'any supporting data or
calculations) for the range.
Specific NCS Reports For Vents Routed to an
Incinerator or Boiler or Process Heater < 44
MW Where the Vent Streams are NOT
Introduced Into the Flame Zone.
In addition to the above requirements, vents
routed to an incinerator or boiler or process
heater < 44 MW where the vent streams are not
introduced into the flame zone must include the
following in the NCS report:
• Average firebox temperature (or gas
stream temperature for catalytic
incinerators) over the duration of the
performance test
• Acceptable range for the daily average
firebox temperature and rationale for the
range
• Times at which an operating day begins and ends.
Periodic Reports
When Are Periodic Reports Required?
November 1, 2000
Do NCS Reports Have to be
Submitted If the Same Test is
Conducted for Multiple
Emission points?
Vents forwhich initial performance
tests are required must also submit
one complete test report for each
test method used for each emission
point. If the refinery uses the same
method for additional tests, the
additional test results must be
submitted, but additional complete
test reports are not required.
4-11
-------
Petroleum Refinery MACTStandard Guidance
Periodic reports are required only if the refinery experiences any compliance except'uns c
periods of excess emissions. Periods of excess emissions are defined as showr. in
box on the following page. Compliance exceptions include any of the exceptions
described in Section 3.3. Compliance exceptions and periods of excess emissions ac
not include periods of startup, shutdown, malfunction, performance testing and monitoring
system calibration.
If Periodic Reports Are Required, When Must They Be Submitted?
Periodic reports must be submitted no later than 60 days after the end of each 6-month
period when any compliance exceptions occur. (The first 6-month period begins on the
date the NCS report is required to be submitted.) Quarterly reporting is requireo ' tne
refinery uses emissions averaging, which is discussed in Section 4.7 below.
What Must Be Included In Periodic Reports?
Generat contents of periodic reports are described in Chapter 3. For miscellaneous
process vents, periodic reports must also include excess emissions for the operating
parameters applicable to the vents (either parameters in Table 4-4 of this manual, or
others specified by the permitting authority).
What is a Period of Excess Emissions?
1) An operating day when the daily average value of a monitored parameter, excepi presence
of a flare or pilot flame, is outside the range specified in the NCS.
2) For each vent routed to a flare, operating days when all plot flames of a flare are abser
3) An operating day when monitoring data required to be recorded (see section 4.1.6) is j
available for less than 75% of the operating hours. |
!
4) For approved data compressions systems, an operating day when the monitor operatec to; J
less than 75% of the operating hours or a day when less than 18 monitoring values were !
recorded. i
November 1, 2000
4-12
-------
Petroleum Refinery MACTStandard Guidance
4.1.5 What are the Recordkeeping Requirements for Miscellaneous Process Vents?
As with the reporting requirements for miscellaneous process vents, there are also
overlapping recordkeeping requirements for the various control devices, as well as some
recordkeeping requirements specific to individual control devices. For all control devices,
it is necessary to retain for 5 years all information that must be reported.
In addition to information that must be reported, refineries may be required to maintain
records applicable to specific process vents as shown in Table 4-4.
TABLE 4-4. Additional Recordkeeping Requirements
Control Device
Required Records
Control devices for which an initial
performance test is required (flare,
incinerator, and boiler or process
heater < 44 MW where the vent
streams are not introduced into the
flame zone)
Complete test report for initial performance test results
• Times and duration of periods when monitoring devices
are not operating
Vents routed to a flare
• Record of each pilot flame determination (or alternate
parameter upon request and approval)
Vents routed to an incinerator or
boiler or process heater < 44 MW
where the vent streams are noi
introduced into the flame zone
• Record of each firebox temperature value or a block
average of values for periods of one hour or less
• Record of the daily average of firebox temperature.
However, if all hourly temperature values are within the
range reported in the NCS, the facility may record that
all values are within the range instead of daily average
values.
For additional information on general recordkeeping requirements applicable to
miscellaneous process vents and all other process units, refer to Section 3.4 of this
manual.
4.2 What are the Requirements for Storage Vessels?
November 1, 2000
4-13
-------
Petroleum Refinery MACTStandard Guidance
Group 1 storage vessels covered by the MACT standard include vessels storing orgs-,!:
liquids that contain organic HAPs. In order to determine if a storage vessel is subject to tht
MACT standard, refer to the applicability flowchart for storage vessels in Chapter 2
The HAP weight percent criteria may be determined using engineering judgement or tes;
results. The vapor pressure criteria may be determined by using one of the following
• Information in standard reference texts
• Methods described in API publication 2517 (Evaporative Loss from Externa; Floating-
Roof Tanks)
• Tests conducted using ASTM Method D2879-83
• Any other approved method.
4.2.1 What are the Control Requirements for Storage Vessels?
Storage vessels, that store a liquid with a maximum true vapor pressure of total organic
HAPs < 76.6 kPa, must be controlled by one of the following control methods [40 CFR
63.119(a)(1)]:
Floating Roofs
(1) Internal floating roof with specified seals; or
(2) External floating roof with specified seals; or
(3) External floating roof converted to internal floating roof with specified seals, (i.e . fixed
roof installed above the external floating roof)
Closed Vent Systems
November 1 200^
4-14
-------
Petroleum Refinery MACTStandard Guidsnce
(4) Closed vent system routed to a flare or other control device that reduces HAP
emissions by 95% or to 20 ppmv.
Storage vessels that store a liquid with a maximum true vapor pressure of total organic
HAPs > 76.6 kPa must be controlled by a closed vent system and control device. [40 CFR
63.119(a)(2)] In addition, work practices, as specified in 40 CFR 63.119(b) through (e),
must be followed for each of the control methods.
The above control methods apply to both existing and new sources. For storage vessels
at new sources, deck fitting controls, as specified in 40 CFR 63.119(c)(2)(l) through (xii),
must be installed on all floating roof tanks. In addition, the control requirements of 40 CFR
63.119(b)(5) and (b)(6) also apply.
As indicated above, the four control methods for storage vessels generally fit into two
categories for testing, monitoring, reporting, and recordkeeping requirements. The first
three methods fall under the category of floating roofs, while the last item is in the category
of closed vent systems with control device. Although some of the requirements described
below are specific to individual control methods within the two categories, most of the
requirements apply to all control methods within each of the two categories.
4.2.2 What are the Testing Requirements for Storage Vessels?
As with other emission points, certain storage vessels are required to be tested during an
initial performance test, and follow-up tests in the event of process changes. This initial
test is required to ensure that the control equipment is operating properly, and that
emissions are within specified limits.
For storage vessels equipped with a closed vent system routed to control device, an initial
performance test must be performed. However, there are no testing requirements for
storage vessels equipped with a floating roof.
iNmAL Performance Tests
Closed Vent System Routed to a Flare
November 1, 2000
4-15
-------
Petroleum Refinery MACTStandard Guid3nct
For storage vessels equipped with a closed vent system routed to a flare, testing
requirements include an initial performance test or compliance determination, as specifier
in 40 CFR 63.11(b), to ensure compliance with the control requirement to reduce tota:
organic HAP emissions by 95% or to 20 ppmv. The test must include the
measurement/determination of the following:
• Emissions visibility
• Net heat value of combusted gas
• Flow rate of gases being combusted
• Exit velocity.
Closed Vent System Routed to a Control Device Other Than a Flare
For storage vessels equipped with a closed vent system routed to a control device other
than a flare, testing requirements include either an initial design evaluation, as specified ir
40 CFR 63.120(d)(1 )(l), or an initial performance test, as specified in 40 CFR
63.120(d)(1 )(ii).
4.2.3 What are the MoNnoRiNG and Inspection Requirements for Storage Vessels?
For storage vessels that must apply controls, there are monitoring and inspection
requirements to ensure continuing compliance with the control requirements. The
requirements vary according to the control method used, with similarities for all closed ven,
systems and similarities for all floating roofs.
Monitoring Requirements
For storage vessels equipped with a closed vent system, the facility must monitor tht
parameters proposed in the Notice of Compliance Status report to ensure that the contro:
device is being properly operated and maintained. There are no monitoring requirement-
for storage vessels equipped with floating roofs.
November 1, 200''
4-16
-------
Petroleum He finery MACT Standard Gu id a nee
Inspection Requirements
Closed Vent Systems
Inspections of control equipment are also required periodically to demonstrate compliance
with the control requirements. For a closed vent system routed to a control device, the
facility must inspect the closed vent system, as specified in 40 CFR 63.148, every 12
months.
Floating Roofs
Storage vessels with floating roofs may have a single-seal system or a double-seal
system. For vessels with a double seal, the requirements for the secondary (outer) seal do
not apply when gaps in the primary (inner) seal are being measured. For storage vessels
equipped with a fixed roof and an internal floating roof or an external floating roof converted
to an internal floating roof, the following inspection requirements apply for each type of seal
system:
Single-Seal System
/ Visually inspect the internal floating roof and primary seal through manholes and
roof hatches at least once every 12 months after initial fill, or at least every 12
months after the compliance date.
/ Visually inspect the internal floating roof and primary seal each time the storage
vessel is emptied and degassed and at least once every 10 years after the
compliance date.
/ Visually inspect gaskets, slotted membranes, and sleeve seal (if any) each time
the storage vessel is emptied and degassed and at least once every 10 years after
the compliance date (new source only).
Double-Seal System
/ Visually inspect the internal floating roof, primary seal, and secondary seal each
time the vessel is emptied and degassed and at least once every 5 years after the
compliance date; or
November 1, 2000
4-17
-------
Petroleum Refinery MACTStandard Guidance
/ Visually inspect the internal floating roof and the secondary seal through mannoies
and roof hatches at least once every 12 months after initial fill, or at least ever> 12
months after the compliance date; and
/ Visually inspect the internal floating roof, primary seal, and secondary seal each
time the vessel is emptied and degassed and at least once every 10 years after the
compliance date.
For storage vessels equipped with an external floating roof, the facility must visually inspect
the external floating roof, the primary and secondary seals, and fittings each time tne
vessel is emptied and degassed. In addition, the following inspection requirements appK
for each type of seal system:
Single-Seal System
/ Measure the gaps between the vessel wall and the primary seal by the compliance
date and at least once a year, until a secondary seal is installed. When a
secondary seal is installed, measure gaps between the vessel wall and both the
primary and secondary seal within 90 calendar days of installation, and then comply
with the double-seal inspection requirements below. [40 CFR 63.120(b)(1)(ii)]
Double-Seal System
/ Measure the gaps between the vessel wall and the primary seal during hydrostatic
testing or by the compliance date and at least once every 5 years thereafter
/ Measure the gaps between the vessel wall and the secondary seal by the
compliance date and at least once a year.
4.2.4 What are the Reporting Requirements for Storage Vessels?
Reporting requirements for storage vessels include Notice of Compliance Status reports,
periodic reports, and internal inspection notification. As with testing and monitonng
reporting requirements for storage vessels include some requirements applicable to at,
four control methods, some requirements applicable to the two general control categories
{i.e., closed vent systems and floating roofs), and some requirements specific to individua
November 1 ?00f
4-18
-------
Petroleum Refinery MACTStandard Guidance
control methods. The following subsections discuss the specific information required for
storage vessels in each of these reports.
Notice of Compliance Status Report
Section 3.3.3 of this manual lays out the basic requirements for a NCS report. The MACT
standard sets out additional NCS requirements for storage vessels equipped with closed
vent systems, but not for storage vessels with floating roofs.
Closed Vent System Routed to a Flare
For storage vessels equipped with a closed vent system routed to a flare, the NCS must
also contain the results of the initial performance test, including:
« Flare design, such as steam-assisted, air-assisted, or non-assisted
• Visible emissions readings
• Heat content determinations
• Flow rate measurements
• Exit velocity determinations
• Periods during the compliance determination when the pilot flame is absent.
Closed Vent System Routed to a Control Device Other Than a Flare
For storage vessels equipped with a closed vent system routed to a control device other
than a flare, the NCS must also include;
• Description of the parameter(s) to be monitored to ensure proper operation and
maintenance of the control device
• Explanation of the parameter selection
• Frequency of monitoring
November 1, 2000
4-19
-------
Petroleum Refinery MACTStandard Guidance
Design evaluation documentation, as specified in 40 CFR 63.120(d)(1)(l), or
results of the initial performance test including identification of emission point;
sharing the control device.
Periodic Reports
As mentioned previously in this
section and in Chapter 3,
periodic reports are only
required if compliance
exceptions occur. The
information required in
periodic reports falls into the 2
general categories of control
methods: closed vent systems
and floating roofs, with a few
additional requirements for
external floating roofs.
Closed Vent Systems
Routed To Any Control
Device
For storage vessels equipped
with a closed vent system
routed to a control device,
periodic reports must include a
description of the following:
* Routine maintenance
for the control device
that was performed
during the previous 6
months
What Are Compliance Exceptions For Storage
Vessels?
Compliance exceptions refer to the following failures
or defects in the control equipment:
* Floating roof not resting on the surface of the liquid
inside the vessel and not resting on the leg
supports
• Liquid floating on the floating roof
• Seal detached from the floating roof
• Holes, tears, or other oponings in the seal or
seal fabric
• Visible gaps between the seal and the wall of
the vessel
• Gaskets no longer close off the liquid surface
from the atmosphere
• Slotted membrane has more than a 10% open
area (new source only).
Compliance exceptions also include occurrences
when monitored parameters are outside the
parameters established in the NCS.
November 1, 20C'
4-20
-------
Petroleum He finery MACT Standard Guidance
• Routine maintenance anticipated for the control device for the next 6 months
• For a control device that is a flare, each occurrence and cause when the
requirements specified in 40 CFR 63.11(b) are not met
• For a control device other than a flare, each occurrence and cause of monitored
parameters being outside the ranges documented in the NCS.
Floating Roofs
For storage vessels equipped with any type of floating roof, periodic reports must contain
the results of each inspection in which a failure was detected. Periodic reports must
include the following information:
• Date of inspection
• Identification of the storage vessel
• Description of the failure
• Nature and date of repair or date the vessel was emptied.
If a failure or defect is detected during inspection, the facility must repair or empty and
remove the vessel from service within 4'5 days. If the vessel cannot be repaired or emptied
within 45 days, the facility may utilize up to 2 extensions of up to 30 additional days each. If
an extension is used, periodic reports must also include the following information:
• Description of the failure
• Statement that alternate storage capacity is unavailable
• Schedule of actions that will ensure that the control equipment will be repaired or
the vessel will be emptied as soon as possible.
Additional reporting requirements for storage vessels equipped with an external floating
roof include notifying the Administrator 30 days in advance of any gap measurement.
Results of each gap measurement in which the requirements of 40 CFR 63.120(b)(3), (4),
(5), or (6) are not met must also be reported in the periodic reports. Such results must
include the following information:
November 1, 2000
4-21
-------
Petroleum Refinery MACT Standard Guidance
• Date of seal gap measurement
• Raw data and calculations described in 63.120(b)(5) or (6)
• Description of seal conditions that are not met
• Nature and date of repair or date the vessel was emptied.
Periodic reports should also include a Notification of Compliance Status (NCS) report if s
floating roof storage vessel is brought into compliance during the reporting period 1
The NCS must include the following information:
• The method of compliance for each storage vessel brought into compliance
• The expected compliance date for all floating roof storage vessels subject to control
requirements that are not yet in compliance (floating roof storage vessels have unti'
August 15, 2005 or the next scheduled emptying and degassing to be brought into
compliance).
• For floating roof vessels that are in compliance, the actual compliance date
Internal Inspection Notification
The third category of reporting directly applicable to storage vessels is notifying the
Administrator of scheduled internal inspections and refilling of empty storage vessels with
organic HAPs. Refineries are required to notify the Administrator at least 30 calendar
days prior to filling or refilling each storage vessel with organic HAPs. The 30-da>
notification is required except if:
• The internal inspection required by 40 CFR 1209(a)(2), 63.1299(a)(3), en
63.120(b)(10) is not planned, and
• The owner/operator of the refinery could not have known about the inspection 30
calendar days in advance of refilling the vessel with organic HAPs.
1This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18
1998. For more information, see Appendix G.
November 1. 2000
4-22
-------
Petroleum Refinery MACTStandard Guidance
If the inspection is not planned and the owner/operator could not have known about it in
advance, the Administrator (nust be notified at least 7 calendar days prior to refilling the
storage vessel. Notification may be made by telephone and immediately followed by
written documentation demonstrating why the inspection was unplanned. The notification
may also be made in writing provided that it is received by the Administrator at least 7
calendar days prior to the refilling.
If tie State or local permitting authority has received delegation of the Refinery MACT (not
all states have as of August 1997), they can waive the notification requirements for all or
some storage vessels at petroleum refineries. The State or local permitting authority may
also grant permission to refill storage vessels sooner than 30 days after submitting the
required notification under 40 CFR 64.654(h)(2)(i)(A) or sooner than 7 days after
submitting the notification under 40 CFR 64.654(h)(2)(i)(B) on a case-by-case basis.
4.2.5 What are the Recordkeeping Requirements for Storage Vessels?
There are recordkeeping requirements common to all storage vessels, as well as some
recordkeeping requirements specific to the different control methods. For all storage
vessels, it is necessary to maintain records of Group 1 or Group 2 determinations, vessel
dimensions, and analysis of capacity. In addition, all information required to be reported
must be retained for 5 years.
Closed Vent Systems Routed To Any Control Device
For storage vessels equipped with a closed vent system routed to a control device,
additional recordkeeping requirements include:
• Complete test report for initial performance test results
• Measured values of monitored parameters
• Planned routine maintenance performed, including:
November 1, 2000
4-23
-------
Petroleum Refinery MACTStandard Guidance
- The first time of day and date the control requirements arenci met at the beamni - _
of the planned routine maintenance, and
- The first time of day and date the control requirements are met at the conclusion, cr
the planned routine maintenance.
Floating Roofs
For storage vessels equipped with any type of floating roof, recordkeeping requirements
include retaining records of each inspection performed. [40 CFR 63.123(c) and (e)] '"or
storage vessels equipped with an external floating roof, additional requirements involve
retaining records of each seal gap measurement, including date, raw data obtained in tne
measurement, and the calculations described in 40 CFR 63.120(b)(3) and (4)
4.3 What are the Requirements for Wastewater Streams?
In order to determine if a wastewater stream is subject to the MACT Standard, refer to the
applicability flowchart for wastewater streams in Chapter 2. Refineries in compliance -viU
the benzene waste NESHAP [40 CFR 61 Subpart FF] are considered to be in compliance
with the refinery MACT standard. Provisions of the benzene waste NESHAP apply to the
following wastewater streams at petroleum refineries:
(1) Total benzene loading ^ 10 Mg per year, and
(2) Flow rate ^ .02 liters per minute, and
(3) Benzene concentration ^ 10 ppm by weight, and
(4) Not exempt from controls under the benzene waste NESHAP.
4.3.1 What are the Control Requirements for Wastewater Streams?
Wastewater streams meeting the applicability criteria above are required to comply wiU
the control requirements of the benzene waste NESHAP [40 CFR 61 Subpart FF] F her-'
control requirements include the following:
• Wastewater streams must reduce benzene mass emissions by 99% by using
suppression followed by steam stripping, biotreatment, or other treatment process
November 1 2Ci0
4-24
-------
Petroleum Refinery MACTStandard Guidance
• Vents from steam strippers and other waste management or treatment units must
have a control device that achieves 95% emission reduction or 20 ppmv at the
outlet of the control device.
43.2 What are the Testtng Requirements for Wastewater Streams?
All wastewater streams must comply with the testing requirements of the benzene waste
NESHAP found in 40 CFR 61.340 through 61.355. These sections also specify the
frequency for which testing must be done. If required, periodic measurements of benzene
concentration in the wastewater must be performed.
4.3.3 What are the Monitoring Requirements for Wastewater Streams?
All wastewater streams must also comply with the monitoring requirements of the benzene
waste NESHAP found in 40 CFR 61.340 through 61.355. If required, monitoring of the
process or control device operating parameters must be performed.
4.3.4 What are the Reporting and Recordkeeping Requirements for Wastewater
Streams?
All wastewater streams must comply with the reporting requirements of the benzene waste
NESHAP found in 40 CFR 61.356 and 61.357. [40 CFR 63.654(a)] In addition, all
information required to be reported must be retained for 5 years. [40 CFR 63.654(l)(4)]
Since affected sources should already be in compliance with 40 CFR 61 Subpart FF, they
will not need to make any changes to their current reporting and recordkeeping
procedures.
4.4 What are the Requirements for Gasoline Loading Racks?
In order to determine if a gasoline loading rack is subject to the MACT standard, refer to
the applicability flowchart for gasoline loading racks in Chapter 2.
4.4.1 What are the Control Requirements for Gasoline Loading Racks?
November 1, 2000
4-25
-------
Petroleum Refinery MACTStandard Guidance
Gasoline loading racks that are subject to the MACT standard must be in compliance w:'.r
the gasoline distribution facilities NESHAP found in 40 CFR 63 Subpart R, which requires
the following:
(1) Reduce emissions of total
organic compounds (TOC) to 10
milligrams per liter of gasoline
loaded; and
(2) Load gasoline only in vapor tight
cargo tanks that have been tested
to assure vapor tightness.
4.4.2 What are the Testing and
MoNrTORiNG Requirements
for Gasoune Loading Racks?
For all gasoline loading racks subject
to the MACT standard, the facility
must comply with the testing and
monitoring requirements of the
gasoline distribution facilities
NESHAP. These tests are found in
40 CFR 63.425(a) through (c)
(performance tests), 63.425(e)
(annual certification), 63.425(f) (leak
detection tests), 63.425(g) (nitrogen
pressure decay field tests), 63.425(h)
(continuous performance pressure
decay test) and 63.427 (continuous
monitoring).
Procedure For Initial Performance Testing
of Gasoline Loading Racks:
Initial performance tests must determine a
monitored operating parameter value for the
vapor processing system using the following
procedure:
1) During the performance test, continuously
record the operating parameters under 40
CFR 63.427.
2) Determine an operating parameter value
based on the parameter data monitored
during the performance test, supplemented
by engineering assessments and the
manufacturer's recommendations, and
3) Provide for the Administrator's approval the
rationale for the selected operating
parameter value, and monitoring frequency
and averaging time. This includes data and
calculations used to develop the value and a
description why the value, monitoring
frequency, and averaging time demonstrate
continuous compliance with the emission
standard in 40 CFR 63.422(b) or
60.112b(a)(3)(ii).
November 1, 200C
4-26
-------
Petroleum Refinery MACTStandard Guidance
Initial Performance Test
The initial performance test is required to be conducted according to the test methods and
procedures in 40 CFR 60.503, except a reading of 500.ppm must be used to determine
the level of leaks to be repaired under 40 CFR 60.503.
For follow-up tests (required to be conducted following process changes), the refinery is
required to document the reasons for any change in the operating parameter value since
the previous test.
What If A Closed Vent System Is Used To Control Emissions?
If a closed vent system and control device, as specified in 40 CFR 60.112b(a)(3), is
required to comply with the control requirements for gasoline loading racks, initial
performance tests are required. [40 CFR 63.423]
What If a Flare Is Used To Control Emissions?
If a flare is used, and emissions from the gasoline loading rack cannot be measured using
the methods specified in 40 CFR 60.503, the refinery is required to comply with the
provisions of 40 CFR 63.11 (b).
Annual Certification Tests
In addition to the initial performance test, gasoline cargo tanks are required to be tested
annually to certify that emissions controls are functioning properly. The annual
performance test must be conducted according to the vacuum and pressure tests
described in Method 27 of 40 CFR 60 Appendix A.
Leak Detection Tests
During loading operations, the facility is required to
conduct a leak detection test for gasoline cargo
tanks according to Method 21 of 40 CFR 60
November 1, 2000
How Are teaks Defined
for gasoline cargo tanks?
A leak is defined as a
reading of 21,000 ppm or
more propane.
4-27
-------
Petroleum Refinery MACTStandard Guidana
Appendix A. The tests are required to be conducted on each compartment dun no
loading of that compartment, or while the compartment is still under pressure. In adcM to
Method 21, the following additional requirements for the test apply [40 CFR 63.425'
• To eliminate a positive instrument drift, the dwell time for each leak detection ma>
not exceed two times the instrument response time. The instrument must be purgec
with ambient air between each leak detection, and the duration of the purge must
be in excess of two instrument response times.
~ The facility must attempt to block the wind from the area being monitorea snrj
record the highest detector reading and location for each leak.
ADomoNAL Testing Requirements
Cargo tanks with manifolded product lines are required to conduct a nitrogen pressure
decay field test on each compartment of each tank. This test is described in 40 CFR
63.425(g). A continuous performance pressure decay test, as described in 40 CFR
63.425 (h), is also required.
Continuous Monitoring
Gasoline loading racks are required to be in compliance with the continuous mcinStorinc
requirements of 40 CFR 63.427(a) and (b). The continuous monitoring system must be
installed, calibrated, certified, operated and maintained according to manufacture,
specifications. The location where the continuous monitoring system must be installed
depends on the type of system used (e.g., carbon adsorption, refrigeration condenser,
thermal oxidation, or flare).
4.4.3 What are the Reporting and Recordkeeping Requirements for Gasoline
Loading Racks?
For gasoline loading racks, the facility must comply with the reporting and reco dkeepin..
requirements of the gasoline distribution facilities NESHAP found in 40 CFR 63.428(D).
(c), (g)(1), and (h)(1) through (h)(3). The initial notification report under 40 CFR 63.428(a;
November * 2PC'
4-28
-------
Petroleum Refinery MACTStandard Guidance
is to be submitted with the initial NCS for the refinery, 150 days after the compliance date.1
All required records must be retained for 5 years.
4.5 What are the Requirements for Marine tank vessel loading?
In order to determine if marine tank vessel loading is subject to the MACT standard, refer
to the applicability flowchart for marine tank vessel loading in Chapter 2.
4.5.1 What are the Control Requirements for Marine tank vessel loading?
Marine tank vessel loading operations that are subject to the MACT standard must be in
compliance with the marine tank loading NESHAP found in 40 CFR 63 Subpart Y, which
requires the following.
Existing Sources: • Collect vapors discharged during loading
• Load only in vapor tight vessels
• Reduce collected HAP emissions by 97% or use vapor
balancing.
New Sources: ~ Same as existing sources, except reduce collected HAP
by 98% or use vapor balancing.
4.5.2 What are the Testing and Monitoring Requirements for Marine Tank Vessel
Loading?
For all marine tank vessel loading operations subject to the MACT Standard, the refinery
must comply with the testing and monitoring requirements of the marine tank loading
NESHAP found in 40 CFR 63.560 through 63.567.
1This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18,
1998. For more information, see Appendix G.
November 1, 2000
4-29
-------
Petroleum Refinery MACTStandard Guidance
4.5.3 What are the Reporting and Recordkeeping Requirements for Marine tan*
VESSEL LOADING?
For all marine tank vessel loading subject to the MACT standard, the refinery must comply
with the reporting and recordkeeping requirements of the marine tank loading NESH'r
found in 40 CFR 63.566, 63.567(a) and (c) through (I). The Initial Notification Repon. unde
40 CFR 63.567(b) is not required. All required records must be retained for 5 yes"i-
4.6 What are the Requirements for Equipment Leaks?
In order to determine if an equipment leak is subject to the MACT standard contro:
requirements, refer to the applicability flowchart for equipment leaks in Chaptef 2 Tne L
HAP service criterion is determined using test methods and procedures specified in 40
CFR 63.180.
4.6.1 What are the Control Requirements for Equipment Leaks?
For equipment leaks at existing sources, the facility must comply with either of the
following equipment leaks provisions:
(1) 40 CFR 60 Subpart W (synthetic organic chemical manufacturing industry (SGCMi1
equipment leaks NSPS), or
(2) Modified 40 CFR 63 Subpart H (hazardous organic NESHAP (HON) negotiated
regulation).
For equipment leaks at new sources, the facility must comply with modified 40 CFR 6S
Subpart H.
4.6.2 What are the Testing, Inspection, and Monttoring Requirements for
Equipment Leaks?
For al! equipment leaks subject to the MACT standard, the refinery must compiy with the
testing, inspection, and monitoring requirements for equipment leaks in 40 CFR 60.1046
NoverrDe" " ?000
4-30
-------
Petroleum Refinery MACTStandard Guidance
and 60.1047 (40 CFR 60 Subpart W), or 40 CFR 63,162 through 63.180 (40 CFR 63
Subpart H).
4.6.3 What are the Reporting and Recordkeeping Requirements for Equipment
Uaks?
For all equipment leaks subject to the MACT Standard, the refinery must comply with the
reporting and recordkeeping requirements for equipment leaks found in 40 CFR 60.1048
and 60.1049 (40 CFR 60 Subpart W) (except that the name rather than the signature of
the person deciding to delay repair must be recorded)1, or 40 CFR 63.181 and 63.182
(40 CFR 63 Subpart H) (except for 63.182(b), (c)(2), and (c)(4)).
4.7 Emissiohs Averaging
The Petroleum Refinery NESHAP [40 CFR 63 Subpart CC] is stated as a source-wide
emissions allowance, as represented by the equation in 40 CFR 63.642. As mentioned in
Chapter 2, there are 2 general approaches for petroleum refineries to comply with the
MACT standard's control requirements for achieving the emissions allowance:
(1) Implement controls on all emission points, as discussed in the previous sections of this
chapter; or
(2) Use a method called emissions averaging, which allows flexibility in applying controls.
Emissions averaging allows facilities to overcontrol some emission points and
undercontrol others in order to achieve the required emissions reductions in the most cost-
effective manner. Additional flexibility is provided by permitting the use of emissions
averaging among petroleum refineries, gasoline distribution facilities, and marine terminal
loading operations located at the same site. Emissions averaging can only be used for
existing sources.
1This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18,
1998. For more information, see Appendix G.
November 1, 2000
4-31
-------
Petroleum Refinery MACTStandard Guidance
4.7.1 Emissions Averaging Appucabiutv
Emissions averaging is allowed for miscellaneous process vents, storage vessels,
wastewater streams, gasoline loading racks, and marine tank vessel loading operation:- ¦
SIC 2911 at a refinery. Emissions averaging is not allowed across sources, such as
across different plant sites or'between refinery and HON sources (i.e., units having a
hazardous organic air pollutant as its primary product) at the same plant site. In additu;.
an emissions estimation is only required for points included in emissions averages, not fo>
all points in the source.
A limitation on the emissions averaging provision is that States have the authority to
disallow emission averaging and require the application of standard control requirement'
to all emission points.
4.7.2 Emissions Averaging Credit/Debit System
Emissions averaging provides a credit/debit system for calculating emissions to comply
with the overall emissions allowance. Facilities receive credits for overcontrol of emission
. points - control above what is required in Subpart CC, and debits for undercontrol of
emission points - control below what is required in Subpart CC. Emission credits ano
debits are calculated on a mass basis using equations in 40 CFR 63.652(g) and (h) to
estimate emissions based on actual operations. Credits calculated must be greater thai ;
or equal to debits calculated on an annual basis. [40 CFR 63.652(e)(3)] In addition,
debits may not exceed credits by more than 30% in any one quarter. [40 CFR 652(e)(4)
The following emission points can be used to generate emissions averaging credits [40
CFR 63.652(c)(1) through (3)]:
• Group 2 emission points
• Group 1 emission points controlled by technology with a higher nominal efficient,
than the reference control technology
November ". 2f;C
4-32
-------
Petroleum Refinery MACTStandard Guidance
• Emission points from which emissions are reduced by pollution reduction
measures, alone or in conjunction with other controls, that get more emission
reduction than required
The following emission points cannot be used to generate emissions averaging credits [40
CFR 63.652(d)]:
• Emission points already controlled on or before November 15,1990, unless the
level of control was increased after November 15,1990. If so, credit is allowed for
the increase only
• Group 1 emission points that are controlled by a reference control technology,
unless the technology has been approved for use in a different manner and a higher
nominal efficiency has been assigned. For example, it is not allowable to claim that
an internal floating roof meeting only the specifications stated in the reference
control technology definition in 40 CFR 63.641 applied to a storage vessel is
achieving greater than 95 percent control
• Emission points on shutdown process units
• Emission points controlled to comply with a State or other Federal rule, unless the
level of control has been increased after November 15, 1990 above what is
required by the State or other Federal rule. If so, credit is allowed for the increase
only.
Debits are generated if the required level of control of a Group 1 emission point, such as
98% for miscellaneous process vents and 95% for storage vessels, is not achieved. [40
CFR 63.652(g)] (See Table 2.3 for required level of control.) Debits and credits are
calculated using formulas found in 40 CFR 63.652(g) and (h). Calculations may not
include emissions from the following:
• Wastewater that is not process wastewater or wastewater streams treated in
biological treatment units. Group 1 wastewater streams cannot be left
undercontrolled or uncontrolled to generate debits [40 CFR 63.652(d)(4)]
November 1, 2000
4-33
-------
Petroleum Refinery MACT Standard Guidance
• More than 20 individual emission points in addition to those controlled by poiiutic-
prevention measures. Where pollution prevention measures are used, no more
than 25 emission points total may be included in the average [40 CFR 63.652(f); 1)}
• Emission points during periods of startup, shutdown, and malfunction [40 CFR
63.652(f)(2)]
• Emission points for which continuous monitors are used and excess emissions
occur. [40 CFR 63.652(f)(3)] For these periods, the monthly credits and debits wi:
be adjusted as specified in 40 CFR 63.652(f)(3)(f) through (iii).
4.7.3 Approval of Emissions Averaging Plan
Facilities that wish to use emissions averaging to comply with the source-wide emissions,
allowance, must submit for approval an emissions averaging plan in the Implementation
Plan or Operating Permit Application. The plan must demonstrate that the credits will be
sufficient to offset the debits under representative operating conditions. [40 CFR
63.652(e)(3)(l)] The plan may include use of innovative technologies, different from the
reference control technology, provided that the innovative technologies achieve greater
than the level of control required for a Group 1 emission point. In addition, the facility must
include a risk assessment in the plan of any hazards or risks of the plan, such as the risk
from one large emission point versus the risk from combined emission points. Such
hazards and risks must be reviewed and compared to point-by-point compliance
4.7.4 Testing, Monitoring, Reporting, and Recordkeeping for Emissions Averaging
For each emission point included in an emissions average, facilities must perform testmr.
monitoring, reporting, and recordkeeping equivalent to the requirements for Group 1
emission points that are not included in emissions averaging. [40 CFR 63.653(a)! See
Chapter 3 for general requirements and previous sections in this chapter for emission
point specific requirements. One additional requirement is to maintain the monthly
calculations of debits and credits.
4.7.5 Recordkeeping for Emissions Averaging
Novembet 200.
4-34
-------
Petroleum Refinery MACTStandard Guidance
Requirements for emissions averaging include maintaining the following:
« Initial performance test results (if applicable)
• Monthly debits, credits, and calculations using E'PA-specified calculation
procedures
« Operating parameter monitoring results.
4.8 Conclusions
Chapter 4 completed the discussion of requirements of the MACT standard by detailing
requirements that are specific to each emission point, and discussed the alternative
compliance method of emissions averaging. This chapter explained the requirements for
emissions from miscellaneous process vents, storage vessels, wastewater streams,
gasoline loading racks, marine tank vessel loading, and equipment leaks. For each type
of emission point, the chapter discussed control requirements, followed by an explanation
of testing, monitoring, reporting and record keeping requirements. The chapter concluded
by discussing how a facility could use emissions averaging to meet the requirements of the
standard, rather than control each emission point.
November 1, 2000
4-35
-------
Petroleum Refinery MACTStandard Guidance
5. Interrelationship of the Petroleum Refinery MACT
Standard with Other Regulations
This chapter summarizes the interrelationship between the MACT standard and other
regulations. As described in previous chapters, the MACT standard requires that HAP
emissions be controlled from various emission points within the petroleum refinery. Some
of these emission points may also be subject to other existing regulations including the
New Source Performance Standards (NSPS) or other NESHAPs. It was not EPA's intent
to have redundant regulations that put an undue burden on the owner/operator of a
petroleum refinery, but to allow sources to comply with only the most stringent regulation
which will demonstrate compliance with all applicable regulations.
The applicability of 40 CFR 63 Subpart CC versus 40 CFR 63 Subpart G, hazardous
organic NESHAP (HON), or some other MACT standard, to an emission point is
determined by the primary product produced at the unit The primary product is that
produced in the greatest mass or volume by the unit. For instance, if the unit produces a
hazardous organic as the primary product, then it is subject to the HON. If a unit is integral
to the petroleum refinery's operations, and produces hazardous organics in small
quantities, it is subject to the petroleum refining MACT standard.
EPA has also included a SIC code reference for petroleum refining (SIC 2911) in the
MACT Standard in order to clarify the applicability of the rule and reduce the potential
confusion of regulatory overlap.
The following describes the relationship of the MACT standard to existing regulations for
each process unit and related emission points:
Miscellaneous Process Vents: There are no existing regulations governing
miscellaneous process vents. Both Group 1 and Group 2 have to comply with the MACT
standard.
Storage Vessels: For storage vessels, there is an overlap between the MACT standard
and the following NSPS:
November 1, 2000
5-1
-------
Petroleum Refinery MACT Standard 6u ida nee
* 40 CFR 60 Subpart K, performance standards for petroleum liquid storage , essels
that were built or have undergone some kind of modification after June 11 1 c~3
but before May 19,1978
Novembe'
5-2
-------
Petroleum Refinery MACTStandard Guidance
• 40 CFR 60 Subpart Ka, performance standards for petroleum liquid storage
vessels that were built or have undergone some kind of modification after May 18,
1978, but before July 7, 1984
• 40 CFR 60 Subpart Kb, performance stahdards'for volatile organic storage vessels
that have been modified after July 23,1984.
The control requirements in the MACT standard reference the storage vessel provisions in
40 CFR 63 Subpart G. The MACT standard is applicable to all new Group 1 storage
vessels and to existing facilities not governed by 40 CFR 60 Subpart Kb. For Group 2
storage vessels, if the control requirements of Subparts K, Ka or Kb do not apply, the
vessel is subject to Subpart CC. All units that are not subject to Subparts K, Ka or Kb are
subject to the MACT Standard.
Owners/operators of internal floating roof or external floating roof tanks are allowed to
defer upgrading their seals to meet the NESHAP requirements until the next scheduled
inspection and maintenance activity or within 10 years, whichever comes first.
Wastewater Streams: For wastewater streams, the following regulations are cross-
referenced in the MACT standard.
• 40 CFR 60 Subpart QQQ, performance standards for VOC emissions from
petroleum refinery wastewater systems
• 40 CFR 61 Subpart FF, benzene waste operations NESHAP (BWON)
• 40 CFR 63 Subpart G, synthetic organic chemical manufacturing industry (SOCMI)
NESHAP (Subpart G).
New and existing sources in compliance with BWON are in compliance with the MACT
standard. The MACT standard is applicable only to Group 1 streams that are subject to 40
CFR 60 Subpart QQQ. For wastewater stream management units that receive streams
subject to the BWON and streams subject to 40 CFR Part 63 Subpart G, the MACT
standard clarifies which provisions of the BWON and which provisions of Subpart G must
be complied with. The specific provisions of each regulation that apply are specified in
November 1, 2000
5-3
-------
Petroleum Refinery MACT Standard Guidance
§63.640(o)(2). Alternately, the owner/operator may comply with all of the requiren-e-T- ;/
Subpart G only.1
Gasoline Storage Racks: Existing sources are governed by 40 CFR 63 Subpa-. R
gasoline distribution facilities.NESHAP, which is referenced in the MACT stances Ne.-
sources are subject to 40 CFR Part 60 Subpart XX, but are required to comply only with,
the requirements of the MACT standard.1
Marine Tank Vessel Loading: These sources are subject to 40 CFR 63 Subpart \
marine tank loading NESHAP, which is referenced in the MACT standard.
Equipment Leaks: For equipment leaks, the following regulations are cross-reference:
in the MACT standard;
• 40 CFR 60 Subpart W, performance standards for equipment leaks from SOCA'
process units
• Modified 40 CFR 63 Subpart H, HON negotiated equipment leak stands-c
There are no group designations for equipment leaks. New sources must comply with the
40 CFR 63 Subpart H at startup, whereas existing sources can choose to comply witt.
either 40 CFR 60 Subpart W or 40 CFR 63 Subpart H. Also, the MACT standard doe.
not apply to units that are also subject to provisions of the HON.
Table 5-1 presents a summary of the existing regulations that may be applicable to eac^
emission point controlled under the MACT standard.
Conclusions
Chapter 5 discussed the relationship between the MACT Standard and existing
regulations. As was indicated in this chapter, the MACT Standard overlaps with certa
requirements for storage vessels, wastewater streams, gasoline storage racks, marine
1 This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on Auqjs* "8
1998. For more information, see Appendix G.
N overrules i, 20C'
5-4
-------
Petroleum Refinery MACTStandard Guidance
tank vessel loading, and equipment leaks. Miscellaneous process vents are the one type
of emission point for which there are no existing requirements, and thus no overlap. This
chapter also described other federal standards with which refineries are required to
comply that are referenced in the MACT standard.
November 1, 2000
5-5
-------
TABLE 5-1. Overlap of the Petroleum Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations
Source
Category
Source
Type
Source
Group
Existing Regulation
Must Comply With
Comment:
Miscellaneous
Process
Vents
New/
Existing
1 12
N/A
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries
No existin
j regulatu
Storage
Vessels
Existing
1
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart G
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
2
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquid
storage
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
If subject
requireme
Subpart K
"X?
cfTjontrol
f*of 40 (
p^Ka
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
=s
=>o
New
1
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart G
sP
n»
«-^l
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
2
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
-H
ST
40 CFR 60 Subpart Kb: NSPS
for volatile orqamn liquids
40 CFR 60 Subpart Kb: NSPS
for volatile organs storage
V.W'S
If subject
rpquireme
Subpart K
•"¦J
cgtontrol
•Sin 4ft i
•F*~
s
Cu
=3
-------
TABLE 5-1. Overlap of the Petroleum Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations
Source
Category
Source
Type
Source
Group
Existing Regulation
Must Comply With
Comments
Miscellaneous
Process
Vents
New/
Existing
1 12
N/A
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries
No existing regulation
Storage
Vessels
Existing
1
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries, which references 40
CFR 63 Subpart G
40 CFR 60 Subpart Kb:
NSPS for volatile organic
liquids
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
2
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquid
storage
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
If subject to control
requirements of 40 CFR 60
Subpart K or Ka
40 CFR 60 Subpart Kb:
NSPS for volatile organic
liquids
40 CFR 60 Subpart Kb: NSPS
for volatile organic liquids
New
1
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 63 Subpart CC:
NESHAP for petroleum
40 CFR 60 Subpart Kb:
NSPS for volatile organic
liquids
refineries, which references 40
CFR 63 Subpart G
2
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
40 CFR 60 Subpart K or Ka:
NSPS for petroleum liquids
-------
>
TABLE 5-1. Overlap of the Petroleum Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations (continued)
Source
Category
Source
Type
Source
Group ;
¦:v/¦ Existing Regulation
; Must Comply With
Comments
Wastewater
Streams
New/
Existing
1
40 CFR 61 Subpart FF:
benzene waste operations
NESHAP (BWON)
40 CFR 61 Subpart FF:
benzene waste operations
NESHAP (BWON)
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems only
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries
•
2
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems
1 / 2
40 CFR 63 Subpart G:
NESHAP for SOCMI process
vents, storage vessels, transfer
40 CFR 63 Subpart G: 63.133
- 63.137 & 63.140
For equipment used in
storage and conveyance of
wastewater streams
operations, and wastewater
40 CFR 61 Subpart FF and
40 CFR 63 Subpart G: 63.138
-63.139
For treatment and control
of wastewater streams
40 CFR 63 Subpart G: 63.143
-63.148
For monitoring and
inspection of equipment,
reporting, and
recordkeeping
requirements
OR
40 CFR 63 Subpart G: 63.133
- 63.148 & 63.151 -63.152
Alternately, comply with
only the requirements of
Subpart G.1
-------
TABLE 5-1. Overlap of the Petroleufn Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations (continued)
Source
Category
Source
Type
Source
Group
; Existing Regulation
Must Comply With
Comments
Gasoline
Loading
Racks
New/
Existing
N/A
40 CFR 63 Subpart R:
gasoline distribution facilities
NESHAP
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries, which references 40
CFR 63 Subpart R
New
N/A
40 CFR 60 Subpart XX; New
Source Standard for Bulk
Gasoline Terminals
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries, which references
40 CFR 63 Subpart R1
Equipment
Leaks
Existing
N/A
40 CFR 60 Subpart W:
NSPS for equipment leaks
OR
40 CFR 63 Subpart H: HON
equipment leaks
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries, which references 40
CFR 63 Subpart H
40 CFR 60 Subpart W: NSPS
for equipment leaks
The new petroleum
refinery NESHAP allows
owners and operators of
existing sources to choose
between the two
regulations.
New
N/A
40 CFR 63 Subpart H: HON
equipment leaks
40 CFR 63 Subpart CC:
NESHAP for petroleum
refineries, which references 40
CFR 63 Subpart H
New sources do not have a
choice like existing
sources.
1 This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18,1998. For more information, see
Appendix G.
z
o
<
CD
3
cr
(D
—t
IV)
o
o
o
-------
TABLE 5-1. Overlap of the Petroleum Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations (continued)
Source
Category
Source
Type
Source
Group
Existing Regulation
Must Comply With
Comment;
Wastewater
Streams
New/
Existing
1
40 CFR 61 Subpart FF:
benzene waste operations
NESHAP (BWON)
40 CFR 61 Subpart FF:
benzene waste operations
NESHAP (BWON)
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems only
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries
2
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems
40 CFR 60 Subpart QQQ:
NSPS for VOC emissions from
petroleum refinery wastewater
systems
""O
1 12
40 CFR 63 Subpart G:
NESHAP for SOCMI process
vents, storage vessels, transfer
operations, and wastewater
40 CFR 63 Subpart G: 63.133 -
63.137 & 63.140
For equip
storage ar
wastewafc
r3»t usee
tfteonvey
Stream;
40 CFR 61 Subpart FF and
40 CFR 63 Subpart G: 63.138-
63.139
For treatrr
wastewati
f$5*and c
Catream;
=3
40 CFR 63 Subpart G: 63.143-
63.148
For moniti
inspectior
reporting,
recordkee
igflg and
requi
OR
Si
=3
40 CFR 63 Subpart G: 63.133-
63.148 & 63.151 - 63.152
Altematel
only the r<
Subpart G
'gaomply
(foremen
-------
TABLE 5-1. Overlap of the Petroleum Refinery MACT Standard (40 CFR 63 Subpart CC)
with Existing Regulations (continued)
Source
Category
Source
Type
Source
Group
Existing Regulation
Must Comply With
Comment;
Gasoline
Loading
Racks
New/
Existing
N/A
40 CFR 63 Subpart R:
gasoline distribution facilities
NESHAP
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart R
New
N/A
40 CFR 60 Subpart XX: New
Source Standard for Bulk
Gasoline Terminals
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart R1
Equipment
Leaks
Existing
N/A
40 CFR 60 Subpart W: NSPS
for equipment leaks
OR
40 CFR 63 Subpart H: HON
equipment leaks
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart H
40 CFR 60 Subpart W: NSPS
for equipment leaks
The new f
NESHAP
and opera
sources t<
the two re
9^leum
jJlijws ow
:S^.of ex
Jioose 1
g^tions.
n>
New
N/A
40 CFR 63 Subpart H: HON
equipment leaks
40 CFR 63 Subpart CC:
NESHAP for petroleum refineries,
which references 40 CFR 63
Subpart H
New soun
choice lik
sources.
=3
3&do nol
i^isting
S
1 This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18, 1998. For more information,
Appendix G.
—1
£>
&
SL
5
cL
rx>
=3
<""N
T,
-------
Petroleum Refinery MACTStindsrd Guidme
Appendix A. Hazardous Air Pollutants (HAPs)
Chemical Name
CAS Number
Acetaldehyde
75070
Acetamide
60355
Acetonitrile
75058
Acetophenone
98862
2-Acety!aminofIuorene
53963
Acrolein
107028
Acrylamide
79061
Acrylic acid
79107
Acrylonitrile
107131
Allyl chloride
107051
4-Aminobiphenyl
92671
Aniline
62533
o-Anisidine
90040
Asbestos
1332214
Benzene (including benzene from gasoline)
71432
Benzidine
92875
Benzotrichloride
98077
Benzyl chloride
100447
Biphenyl
92524
Bis(2-ethylhexyl)phthalate (DEHP)
117817
November 1, 2000
A-1
-------
Petroleum Refinery MACT Standard Guidance
Chemical Name
CAS Number j
Bis(chloromethyl)ether
542881
Bromoform
75252
1,3-Butadiene
10699C
Calcium cyanamide
156627
Captan
133062
Carbaryl
63252
Carbon disulfide
7515C
Carbon tetrachloride
56235
Carbonyl sulfide
463581
Catechol
120809
Chloramben
133904
Chlordane
57749
Chlorine
7782505
Chloroacetic acid
79118
2-Chloroacetophenone
532274
Chlorobenzene
108907
Chlorobenzilate
510156
Chloroform
67663
Chloromethyl methyl ether
107302
Chloroprene
126998
Cresols/Cresylic acid (isomers and mixture)
1319773
o-Cresol
95487
Nuverr.ber 1, 200f
A-2
-------
Petroleum Refinery MACT Standard Guidance
Chemical Name
CAS Number
m-Cresol
108394
p-Cresol
106445
Cumene
98828
2,4-D, salts and esters
94757
DDE
3547044
Diazomethane
334883
Dibenzofurans
132649
1,2-Dibromo-3-chloropropane
96128
Dibutylphthalate
84742
1,4-Dichlorobenzene(p)
106467
3,3-Dichlorobenzidene
91941
Dichloroethyl ether (Bis(2-chloroethyl)ether)
111444
1,3-Dichloropropene
542756
Dichlorvos
62737
Diethanolamine
111422
N,N-Diethyl aniline (N,N-Dimethylaniline)
121697
Diethyl sulfate
64675
3,3-Dimethoxybenzidine
119904
Dimethyl aminoazobenzene
60117
3,3-Dimethyl benzidine
119937
Dimethyl carbamoyl chloride
79447
Dimethyl formamide
68122
November 1, 2000
A-3
-------
Petroleum Refinery MACT Standard Guidance
Chemical Name
CAS Number
1,1-Dimethyl hydrazine
57147
Dimethyl phthalate
131113
Dimethyl sulfate
77781
4,6-Dinitro-o-cresol, and salts
534521
2,4-Dinitrophenol
51285
2,4-Dinitrotoluene
121142
1,4-Dioxane (1,4-Diethyleneoxide)
123911
1,2-Diphenylhydrazine
122667
Epichlorohydrin (l-Chloro-2,3-epoxypropane)
106898
1,2-Epoxybutane
106887
Ethyl acrylate
140885
Ethyl benzene
100414
Ethyl carbamate (Urethane)
51796
Ethyl chloride (Chloroethane)
75003
Ethylene dibromide (Dibromoethane)
106934
Ethylene dichloride (1,2-Dichloroethane)
107062
Ethylene glycol
107211
Ethylene imine (Aziridine)
151564
Ethylene oxide
75218
Ethylene thiourea
96457
Ethylidene dichloride (1,1-Dichloroethane)
75343
Formaldehyde
50000
Novembe' ' 200;
A-4
-------
Petroleum Refinery MACTStandard Guidance
Chemical Name
CAS Number
Heptachlor
76448
Hexachlorobenzene
118741
Hexachlorobutadiene
87683
Hexachlorocyclopentadiene
77474
H sxachloroethane
67721
Hexamethylene-1,6-diisocyanate
822060
Hexamethylphosphoramide
680319
Hexane
110543
Hydrazine
302012
Hydrochloric acid
7647010
Hydrogen fluoride (Hydrofluoric acid)
7664393
Hydroquinone
123319
[sophorone
78591
Lindane (all isomers)
58899
Maleic anhydride
108316
Methanol
67561
Methoxychlor
72435
Methyl bromide (Bromomethane)
74839
Methyl chloride (Chloromethane)
74873
Methyl chloroform (1,1,1-Trichloroethane)
71556
Methyl ethyl ketone (2-Butanone)
78933
Methyl hydrazine
60344
November 1, 2000
A-5
-------
Petroleum Refinery MACTStandard Guidance
Chemical Name
CAS Number
Methyl iodide (lodomethane)
74884
Methyl isobutyl ketone (Hexone)
108101
Methyl isocyanate 1
624839
Methyl methacrylate
80626
Methyl tert butyl ether
1634044
4,4-Methylene bis(2-chloroaniline)
101144
Methylene chloride (Dichloromethane)
75092
Methylene diphenyl diisocyanate (MDI)
101688
4,4-Methylenedianiline
101779
Naphthalene
91203
Nitrobenzene
98953
4-Nitrobiphenyl
92933
4-Nitrophenol
100027
2-Nitropropane
79469
N- N itroso- N-methylurea
684935
N-Nitrosodimethylamine
62759
N-Nitrosomorpholine
59892
Parathion
56382
Pentachloronitrobenzene (Quintobenzene)
82688
Pentachlorophenol
87865
Phenol
108952
p-Phenylenediamine
106503
NovemDet ", 2000
A-6
-------
Petroleum Refinery MACTStandard Guidance
Chsmfca! Name
CAS Number
Phosgene
75445
Phosphirie
7803512
Phosphorus
7723140
Phthalic anhydride
85449
Polychlorinated biphenyls (Aroclors)
1336363
1,3-Propane sultone
1120714
beta-Propioiactone
57578
Propionaldehyde
123386
Propoxur (Baygon)
114261
Propylene dichloride (1,2-Dichloropropane)
78875
Propylene oxide
75569
1,2-Propylenimine (2-Methyl aziridine)
75558
Quinoline
91225
Quinone
106514
Styrene
100425
Styrene oxide
96093
2.3,7,8-Tetrachlorodibenzo-p-dioxin
1746016
1,1,2,2-T etrachloroethane
79345
Tetrachloroethylene (Perchloroethylene)
127184
Titanium tetrachloride
7550450
Toluene
108883
2,4-Toluene diamine
95807
November 1, 2000
A-7
-------
Petroleum Refinery MACT Standard Guidance
Chemical Name
CAS Number j
2,4-Toluene diisocyanate
58484S
o-Toluidine
95534
Toxaphene (chlorinated camphene)
8001352
1,2,4-T richlorobenzene
120821
1,1,2-T richloroethane
79005
Trichloroethylene
79016
2,4,5-Trichlorophenol
95954
2,4,6-Trichlorophenol
88062
Triethylamine
121448
Trifiuralin
1582098
2,2,4-T rimethylpentane
540841
Vinyl acetate
108054
Vinyl bromide
593602
Vinyl chloride
75014
Vinylidene chloride (1,1-Dichloroethylene)
75354
Xylenes (isomers and mixture)
1330207
o-Xylenes
95476
m-Xylenes
108383
p-Xylenes
106423
Antimony Compounds
0
Arsenic Compounds (inorganic including arsine)
0
Beryllium Compounds
0
Novembe* V 2^^
A-8
-------
Petroleum Refinery MACTStandard Guidance
Chemical Name
CAS Number
Cadmium Compounds
0
Chromium Compounds
0
Cobalt Compounds
0
Coke Oven Emissions
0
Cyanide Compounds1
0
Glycol ethers2
0
Lead Compounds
0
Manganese Compounds
0
Mercury Compounds
0
Fine mineral fibers3
0
Nickel Compounds
0
Polycyfic Organic Matter4
0
Radionuclides (including radon)5
0
Selenium Compounds
0
Note- For all listings above which contain the word 'compounds' and for glycol ethers, the following applies:
Unless otherwise specified, these listings are defined as including any unique chemical substance that
contains the name chemical {i.e., antimony, arsenic, etc.) as part of that chemical's infrastructure
1 X'CN where X=H" or any other group where a formal dissociation may occur. For example KCN or
Ca(CN)2.
2 Includes mono- and di-ehters or ethylene glycol, diethylene glycol, and triethylene glycol
R-{OCH2CH2)„-OR' where n=1, 2, or 3; R=alkyl or aryi groups; R'=R, H, or groups which, when
removed, yield glycol ethers with the structure: R-(OCH2CH)„-OH. Polymers are excluded from the
glycol category.
November 1, 2000
A-9
-------
Petroleum Refinery HACTStandard Guidance
3 Includes mineral fiber emissions from facilities manufacturing or processing glass, rock r:r s-ag
(or ther mineral derived fibers) of average diameter 1 micrometer or less.
* Includes organic compounds with more than one benzene ring, and which have a boiling po.n: gre-:
than or equal to 100eC,
5 A type of atom which spontaneously undergoes radioactive decay.
November 1 20 v.
A-10
-------
Petroleum Refinery MACTStandard Guidance
Appendix B. Organic Hazardous Air Pollutants
(Organic HAPs)
Chemical Name
CAS Number
Benzene
71432
Biphenyl
92524
Butadiene (1,3)
10990
Carbon disulfide
75150
Carbonyl sulfide
463581
Cresol (mixed isomers)
1319773
Cresol (m-)
108394
Cresol (o-)
95487
Cresol (p-)
106445
Cumene
98828
Dibromoethane (1,2) (ethylene debromide)
106934
Dichloroethane (1,2)
107062
Diethanolamine
111422
Ethylbenzene
100414
Ethylene glycol
107211
Hexane
110543
Methanol
67561
Methyl ethyl ketone (2-butanone)
78933
November 1, 2000
B-1
-------
Petroleum Refinery MACTStandard Guidance
Chemical Name
CAS Number j
Methyl isobutyl ketone (hexone)
108101
Methyl tert butyl ether
1634044
Naphthalene
91203
Phenol
108952
Toluene
108883
Trimethylpentane (2,2,4)
540841
Xylene (mixed isomers)
1330207
Xylene (m-)
108383
Xylene (o-)
95476
Xylene (p-)
106423
November * 200C
B-2
-------
Petroleum Refinery MACT Standard Guidance
Appendix C. U.S. Petroleum Refineries Affected by the
Petroleum Refinery Standards
Facility Name
Cfty
State
1994 Capacity
Units*
Tesoro Alaska Petroleum
Kenai
AK
72,000
Arco Alaska Inc.
' Kuparuk
AK
12,000
Mapco Inc.
North Pole
AK
128,200
Petro Star Inc
North Pole
AK
10,000
Arco Alaska Inc.
Prudhoe Bay
AK
15,000
Petro Star Inc.
Valdez
AK
26,300
Coastal Mobile Refining Co.
Chickasaw/Mobile Bay
AL
16,500
Shell Oil Products Co.1
Saraland
AL
76,000"
Hunt Refining Company Inc.
T uscaloosa
AL
33,500
Lion Oil Co. Inc
El Dorado
AR
51,000
Cross Oil & Refining Co Inc.
Smackover
AR
6,200
Berry Petroleum Co
Stephens
AR
6,700
Anchor Refining Co
McKittirck
CA
10,000*
Kern Oil & Refining Co
Bakersfield
CA
21,400
San Joaquin Refining Co. Inc.
Bakers fie Id
CA
24,300
Sunland Refining Corp
Bakersfield
CA
12,000
Texaco Refining and Marketing Inc.
Bakersfield
CA
56,000
Exxon Corporation
Benecia
CA
128,000
Huntway Refining Co.
Benecia
CA
8,600
Chevron USA Products Co.
El Segundo
CA
230,000
November 1, 2000
C-1
-------
Petroleum Refinery MACTStandard Guidance
Facility Nam®
City
Stats
1994 Capacity
Units*
Atlantic Richfield Co.
Carson
CA
255. oc r
Unocal Corp.
Los Angeles/Wilmington
CA
118.75C"
Shell Martinez Refining Co.
Martinez
CA
146.9;;:
November 1 2Ci(X
C-2
-------
Petroleum Refinery MACTStandard Guidance
Facility Name
City ,
Stats
1994 Capacity
Units*
Tosco Corporation
Martinez
CA
160,000
Witco Corporation
Oildale
CA
0
Tenby Inc.
Oxnard
CA
4,000
Paramount Petroleum Corp.
Paramount
CA
46,500
Chevron USA Products Co.
Richmond
CA
230,000
Santa Maria Refining Co 2
Santa Maria
CA
10,000*
Unocal Corp.
San Francisco/Santa Maria
CA
103,645"
Lunday Thagard Co
South Gate
CA
8,100
Mobile Oil Corp.
Torrance
CA
130,000
Huntway Refining Co
Wilmington
CA
5,500
Texaco Refining and Marketing
Wilimington
CA
64,000
Ultramar Inc.
Wilmington
CA
68,000
Conoco Inc
Commerce City
CO
57,500
Total Petroleum Inc 3
Denver
CO
28,000*
Star Enterprise
Delaware City
DE
140,000
Young Refining Corporation
Douglasville
GA
5,540
Citgo Asphalt Refining Co.
Savannah
GA
28,000
BHP Hawaii Inc.
Kapolei
HI
93,500
Chevron USA Products Co
Barbers Point
HI
54,000
Clark Oil & Refining Corp
Blue Island
IL
80,515
Clark Oil & Refining Corp.
Hartford
IL
62,500
Mobil Oil Corporation
Joliet
IL
188,000
Indian Refining Partnership
Lawrenceville
IL
80,750
November 1, 2000
C-3
-------
Petroleum Refinery MACTStandard Guidanct
Facility Name
City
State
1994 Capacity
Units"
Uno-Ven Company
Lemont -
IL
14 7 X 7
Marathon Oil Company
Robinson
IL
175.00C
Shell Wood River Refining Co.4
Wood River
IL
2' 1.00C
Laketon Refining Corp
Laketon
IN
1 —r
Novembe1 207
C-4
-------
Petroleum Refinery MACT Standard Guidance
Facility Nam®
City
State
1994 Capacity
Units*
Countrymark Cooperative Inc.
Mount Vernon
IN
22,000
Amoco Oil Co,
Whiting
IN
410,000
Farmland Industries Inc.
Coffeyville
KS
68,600
Texaco Refining and Marketing Inc.
El Dorado
KS
94,600
National Coop Refinery Assoc.
Mc Pherson
KS
75,600
Ashland Petroleum Co,
Russell/Catlettsburg
KY
213,400
Somerset Refinery Inc.
Somerset
KY
5,500
Exxon Corporation
Baton Rouge
LA
424,000
BP Exploration & Oil Inc.
Belle Chasse
LA
231,500
Mob;i Oil Corporation
Chalmette
LA
170,000
Cana! Refining Co.
Church Point
LA
9,500
Star Enterprise
Convent
LA
225,000
Calumet Lubricants Co.
Cotton Valley
LA
7,800
Marathon Oil Company
Garyviile
LA
255,000
Basis Petroleum, Inc.5
Krotz Springs
LA
67,100*
Calcasieu Refining Co.
Lake Charles
LA
12,500
Citgo Petroleum Corporation
Lake Charles
LA
305,000
American International Refining Inc.6
Lake Charles
LA
27,600*
Cit-Con Oil Corp.
Lake Charles
LA
7,350
Murphy Oil USA Inc
Meraux
LA
100,000
Shell Norco Refining Co.
Norco
LA
215,000
Placid Refining Co.
Port Allen
LA
48,500
Calumet Lubricants Co. Ltd.
Princeton
LA
8,200
November 1, 2000
C-5
-------
Petroleum Refinery MACTStandard Guidance
Facility Nam#
City
State
1394 Capacity
Units*
Atlas Processing Co. Div. Of Pennzoil
Shreveport
LA
46,200
Shell Chemical Co.7
St. Rose
LA
40,000"
Conoco Inc.
Westlake
LA
191,00f
Lakeside Refining Co.
Kalamazoo
Ml
5.600'
November 1, 2000
C-6
-------
Petroleum Refinery MACT Standard Cuidsnce
Facility Nam*
City
Stats
1994 Capacity
Units*
Total Petroleum Inc.
Alma
Ml
45,600
Marathon Oil Company
Detroit
Ml
70,000
Koch Refining Company LP
Rosemount
MN
230,000
Ashland Petroleum Co.
Saint Paul Park
MN
67,100
Southland Oil Company
Lumberton
MS
5,800
Chevron USA Products Co
Pascagoula
MS
295,000
Southland Oil Company
Sandersville
MS
11,000
Ergon Inc.
Vicksburg
MS
23,000
Conoco Inc.
Billings
MT
49,500
Exxon Co.
Billings
MT
44,000
Montana Refining Co
Great Falls
MT
7,000
Cenex
Laurel
MT
41,450
Amoco Oil Co
Mandan
ND
58,000
Tosco Refining Co.8
Linden
NJ
240,000*
Citgo Asphalt Refining Co.
Paulsboro
NJ
40,000
Mobil Oil Corp.
Paulsboro
NJ
126,000
Chevron USA Products Co.
Perth Amboy
NJ
80,000
Amerada Hess Corporation
Port Reading
NJ
0
Coastal Eagle Point Oil Co.
Westville
NJ
125,000
Navajo Refining Company
Artesia
NM
57,000
Giant Refining Co -
Bloomfield
NM
16,800*
Giant Refining Co.
Gallup
NM
20,800
Petro Source Refining Partners
Eagle Springs
NV
7,000
November 1, 2000
C-7
-------
Petroleum Refinery MACTStandard Guidance
Facility Nam*
City
Stata
1994 Capacity
Units'
Ashland Petroleum Co.
Canton
OH
6C f'C.
BP Oil Co.
Lima
OH
16- or.;
BP Oil Co.
Toledo (Oregon)
OH
13G.00C
Sun Refining & Marketing Co.10
Toledo
OH
'25 CO'
November *, 200"
C-8
-------
Petroleum Refinery MACTStandard Guidance
Facility Nam*
City
State
1994 Capacity
Units*
Total Petroleum Inc
Ardmore
OK
68,000
Conoco Inc.
Ponca City
OK
140,000
Sinclair Oil Corporation
Tulsa
OK
54,000
Sun Refining & Marketing Co.
Tulsa
OK
85,000
Gary-Williams Co.1'
Wynnewood
OK
45,000*
Chevron USA Products Co 11
Portland (Willbridge)
OR
15,000*
Witco Corporation
Bradford
PA
10,000
Sun Refining & Marketing Co
Marcus Hook
PA
175,000
Sun Refining & Marketing Co.
Philadelphia-Girard Pt13
PA
177,000*
Sun Refining & Marketing Co.
Philadelphia-Pt. Breeze14
PA
130,000*
Pennzoil Products Company
Rouseville
PA
15,700
United Refining Inc
Warren
PA
60,000
Mapco Petroleum Inc
Memphis
TN
89,000
Pride Companies L P
Abilene
TX
42,750
Exxon Co. USA
Baytown
TX
396,000
Mobil Oil Corporation
Beaumont
TX
315,000
Fina Oil and Chemical Co
Big Spring
TX
55,000
Phillips Petroleum Company
Borger
TX
110,000
Howell Hydrocarbons & Chemicals Inc.
Channelview
TX
1,400
Citgo Petroleum Corp 16
Corpus Christ!
TX
130,000*
Coastal Refining & Marketing Inc.
Corpus Christi
TX
95,000
Koch Refining Company Inc.
Corpus Christi
TX
255,000
Neste Trifinery Petroleum Services
Corpus Christi
TX
27,000
November 1, 2000
C-9
-------
Petroleum Refinery MACTStandard Guidance
Faculty Nam«
City
State
f
1994 Capar't>
Units
Valero Refining Company
Corpus Christi
TX
29.90'
Deer Park Refining Ltd. Partnership
Deer Park
TX
215\yV
Chevron USA Products Co.
El Paso
TX
8' C".
Basis Petroleum, Inc.16
Houston
TX
57,60 *
C-10
-------
Petroleum Refinery MACT Standard Guidance
Facility Nam*
City
State
1894 Capacity
Units*
Lyondell-Citgo Refining Co.
Houston
TX
265,000
Shell Odessa Refining Co,
Odessa
TX
28,600
Crown Central Petroleum Corp.
Pasadena
TX
100,000
Clark Oil & Refining Corp,17
Port Arthur
TX
185,000*
Fina Oil and Chemical Co.
Port Arthur
TX
175,000
Star Enterprise
Port Arthur/Neches
TX
235,000
Age Refining & Marketing
San Antonio
TX
6,000
Diamond Shamrock Corp.
Three Rivers
TX
Diamond Shamrock Corp.
Sunray (Mckee)
TX
132,000
Phillips Petroleum Company
Sweeny
TX
185,000
Amoco Oil Company
Texas City
TX
433,000
Marathon Oil Company
Texas City
TX
70,000
Basis Petroleum Inc.18
Texas City
TX
125,400*
La Gloria Oil & Gas Co.
Tyler
TX
55,000
Big West Oil Company
Salt Lake City
UT
24,000
Amoco Oil Company
Salt Lake City
UT
44,000
Chevron USA Products Co
Salt Lake City
UT
45,000
Cry sen Refining Inc
Woods Cross
UT
12,500
Phillips Petroleum Company
Woods Cross
UT
25,000
Amoco Oil Company
Yorktown
VA
53,000
Hess of Virgin Islands Corp.
St. Croix
VI
505,000
Shell Anacortes Refin Co 19
Anacortes
WA
108,200*
Texaco Refining and Marketing
Anacortes
WA
136,000
November 1, 2000
e-11
-------
Petroleum Refinery HACTStandard Guidance
Facility Name
City
State
1994 Capacity ;
Units
Atlantic Richfield Company
Ferndale
WA
165,OX'
Tosco Corporation
Femdale
WA
95,c:-
Chevron USA Products Co.20
Seattle
SNA
C
Sound Refining Inc.
Tacoma
WA
:1.£0:
Novemb' ¦ 0 U",
C-12
-------
Petroleum Refinery MACTStandard Guidance
Facility Name
City
State
1994 Capacity
Units*
US Oil & Refining Co.
Tacoma
WA
32,400
Murphy Oil USA Inc.
Superior
Wl
33,200
Quaker State oil Refining Corp.
Newell
WV
11,500
Frontier Refining Inc.
Cheyenne
WY
38,670
Little America Refining Co.
Evansville/Casper
WY
24,500
Wyoming Refining Co
Newcastle
WY
12,555
Sinclair Oil Corporation
Sinclair
WY
54,000
* Barrels/Calendar day {one barrel=42 U.S. Gallons). Data extracted from Report 1 -Comparative Profile
Petroleum Refining. EPA Regional or State Reviewers, Regional Review Draft. 10/25/96.
+ Charge Capacity, b/cd. Data extracted from Oil and Gas Journal. Dec. 23, 1996, pp. 85-94.
Endnotes
1. Formerly LL&E Petroleum Marketing
2 Formerly Conoco
3 Formerly Colorado Refining
4. Possibly same refinery as Shell Oil Company in Roxana Wood River
5. Formerly Phibro Energy USA Inc.
6. Leases Gold Line Refining Ltd.
7. Formerly St. Rose Refining Inc.
8. Formerly Bayway Refining Company
9. Formerly Bloomfield Refining Company
10. Same as Sun Company Inc. (r &M)
11 Same as Kerr-Mcgee Refining Corp.
12. Same as Chevron U.S.A. Inc.
13. Previously combined with Point Breeze Refinery
14. Previously combined with Girard Point Refinery
15. Same as Citgo Refining and Chemical Inc.
16. Previously Phibro Energy USA Inc.
17. Formerly Chevron USA Inc.
18. Formerly Diamond Shamrock Corp. in Three Rivers, TX
19. Formerly Shell Oil Company
November 1, 2000
C-13
-------
20 Same as Chevron USA Inc.
Petroleum Refinery MACTStandard Guidance
Noverr'L>f>r 1 2001
C-14
-------
Petroleum Refinery MACT Standard Guidance
Appendix D. Additional Resources for Petroleum Refining
MACT Standard Guidance Document
Documents/Reports available on the Internet:
Clean Air Act signed rules
134.67.104.12/html/caa/rules.htm
Includes compressed files of the Clean Air Act.
Sector Notebook: Profile of the Petroleum Refining Industry. EPA Office of
Compliance. September 1995.http://es.inel.gov/.
This sector notebook provides general information on the petroleum refining industry,
including: industrial processes, chemical releases and transfer profile, and pollution
prevention opportunities. The report also summarizes applicable federal statutes and
regulations, provides a compliance and enforcement history, and presents compliance
assurance and initiatives for the industry.
Air Toxics Regulations: Petroleum Refining. Final Air Toxics Rule for the
Petroleum Refining Industry. July 28,1995.
www.epa.gov/oar/oaqps/airtox/fsrefine.html
Document written following EPA's issuance of final regulation to reduce emissions of
air toxics from petroleum refineries. Discusses health and environmental benefits of
new rule and flexibility of rule for the industry. Provides background and cost of
information, discusses who will be affected, and includes a FACT sheet.
AIRS Facility Subsystem (AFS Data) - USA Emissions Ranking Report - VOC
www. e p a. g o v/a i rs/afsd-voc. h tm I
November 1, 2000
D-1
-------
Petroleum Refinery MACTStandard Guidance
This report ranks the 100 largest stationary sources of volatile organic compounds
(VOC) emissions in the United States, as of February 28,1997.
AIRS Facility Subsystem (AFS Data) - USA Emissions Ranking Report - CO
www.epa.gov/airs/afsd-co.html
This report ranks the 100 largest stationary sources of carbon monoxide {CO,
emissions in the United States, as of February 28,1997.
Noverrbe; " 2000
D-2
-------
Petroleum Refinery MACTStandard Guidance
National Ambient Air Quality Standards (NAAQS)
wvvvv.epa.gov/airs/criteria.html
Document lists EPA's national standards set for the six principal pollutants, called
"criteria" pollutants.
EPA Operating Permits Program - Information
www.epa.gov/oar/oaqps/permits/
Provides a mechanism for gathering all the federal, state, and local requirements
applicable to air pollution sources. Answers questions like: What are the
requirements? What guidance has been prepared? Who are responsible for
implementing the permits programs? What is the approval status for each of the state
and local permitting authorities? What changes are coming?
Environment Canada
www.ns.doe.ca/soe/ch4-31 .html
State of the Environment in Atlantic Region report. Includes chapters describing
process releases from petroleum refining and presents data on air emissions from
refineries.
Center for Transportation and Analysis
vAvw-cta.ornl.gov/data/tedb15Ztab21.htm
Includes the table Refinery Yield of Petroleum Products from a Barrel of Crude Oil,
1978-1993(a).
Websites
U.S. EPA Office of Air and Radiation (OAR):
OAR Homepage
www.epa.gov/oar/
November 1, 2000
D-3
-------
Petroleum Refinery MACTStandard Guidance
Includes information on prevention and air toxics. Lists publications, regulations ?r"?
resources. Provides search tool.
OAR Regulations
www.epa.gov/oar/oarregul.html
Contains information on Clean Air Act documents, Clean Air Act operating permits
program, ozone depletion regulations, OAQPS air regulations - schedule, stoxica
regulations - fact sheets, and other regulations, including the federal register online
OAR Resources
www.epa.gov/oar/oarrsrc.html
Lists various services, networks, webpages, databases, software, and contacts that
may be useful.
U.S. EPA Office of Air Quality Planning and Standards (OAQPS):
Transfer Technology Network 2000 (TTN 2000) Home Page
www.epa.gov/oar/ttn_bbs.html
Provides access to various electronic bulletin board systems containing information
about many areas of air pollution science, technology, regulation, measurement, and
prevention. Serves as a public forum for the exchange of technical information and
ideas among users and EPA staff. Includes tools to: 1) estimate air polluta-.
emissions, 2) download computer code for regulatory models, 3) read summaries o;
details of the Clean Air Act, 4) find a course offered by the Air Pollution Trailing
Institute, or 5) seek technical support in implementing air pollution programs
Unified Air Toxics Website: Home Page
www.epa.gov/oar/oaqps/airtox/
Contains basic facts, summaries of EPA regulations, information on pollutants anc
sources of pollutants, technical resources, EPA program and contacts, and state an::
local programs.
November " ATiC
D-4
-------
Petroleum Refinery MACT Standard Guidance
Unified Air Toxics Website: Pollutants & Sources
wA'w.epa.gov/oar/oaqps/airtox/polIsour.html
Provides a list of 188 toxic air pollutants to be regulated by EPA, defines the types of
sources of pollutants, and provides a list of 174 categories of industrial and
commercial sources that emit toxic air pollutants.
Unified Air Toxics Website: EPA Programs
www.epa.gov/oar/oaqps/airtox/epaprogs.html
Describes the following three programs: Hazardous Air Pollutants Strategic
Implementation Plan, National Emission Standards for Hazardous Air Pollutants
(NESHAP), and Maximum Achievable Control Technology (MACT) Standards.
Publications
www.epa.gov/oar/oaqps/publicat.html
Contains air quality and emissions trend reports, newsletters, fact sheets, and various
guides to evaluating exposure to air pollutants.
American Petroleum Institute (API)
www.api.org/
Representing the Nation's oil and gas industries. Contains industry data, facts about
the petroleum industry, and publications such as: NO* Emissions from Petroleum
Industry Operations, October 1979; Petroleum Emission Factor Information Retrieval
System (PEFIRS), July 1993; The Cost Effectiveness of Carbon Dioxide from
Petroleum Sources, July 1991; and, Electric Exchange of Environmental Compliance
Information. A Proposed Approach, August 1995.
One of many documents available from API is the Summary of Question and Answer
Sessions for American Petroleum Institute's Refinery MACT Rule Workshop.
October 23-24, 1995,
November 1, 2000
D-5
-------
Petroleum Refinery MACTStandard Guidance
Appendix E. Definitions
Affected source means the combination of all emission points at a petroleum refinery.
Each point is considered part of the single affected source.
Boiler means any closed combustion device that extracts useful energy in the form of
steam and is not an incinerator.
Closed vent system means a system that is not open to the atmosphere and is
composed of piping, ductwork, connections, and, if necessary, flow inducing devices that
transport gas and vapor from an emission point to a control device or back into the
process. If gas or vapor from regulated equipment is routed to a process (e.g., petroleum
refinery fuel gas system), the process is not considered a closed vent system and is not
subject to the closed vent system standards.
Combustion device means an individual unit of equipment such as a flare, incinerator,
process heater, or boiler used for the combustion of organic hazardous air pollutant (HAP)
vapors.
Construction means the on-site fabrication, erection, or installation of an affected source.
Control device means any equipment used for recovering, removing, or oxidizing
hazardous organic pollutants (HAPs). Such equipment includes, but is not limited to,
absorbers, carbon absorbers, condensers, incinerators, flares, boilers, and process
heaters.
Deck fitting controls means the fittings that pass through or are attached to the deck or
roof of a floating roof tank, and include hatches, gauge floats, and support columns.
Controls may be installed to minimize evaporative losses from the fittings.
Double-seal system means a floating roof having both primary and secondary seals.
Dwell time means the time feeds spend in a reactor (allowing for reactions to occur) or the
time feeds or products spend in a tank.
November 1, 2000
E-1
-------
Petroleum Refinery MACTStandard Guidance
Emissions averaging means a method of complying with emission limitations, w.nereb,
the affected source may create emission credits by reducing emissions from specific
points to a level below that required by the relevant standard, and those credits a- used
offset emissions from points that are not controlled to the level required by the rele vant
standard.
November 1 20n-'
E-2
-------
Petroleum Refinery MACTStandard Guidance
Emission point means an individual miscellaneous process vent, storage vessel,
wastewater stream, or equipment leak associated with a petroleum refining process unit;
an individual storage vessel or equipment leak associated with a bulk gasoline terminal or
pipeline breakout station classified under SIC 2911; a gasoline loading rack classified
under SIC 2911; or a marine tank vessel loading operation located at a petroleum refinery.
Existing source means a source that commenced construction on or before July 14,
1994,
External floating roof means a pontoon-type or double-deck-type cover that rests on the
liquid surface in a storage vessel or waste management unit with no fixed roof.
Firebox means a chamber (e.g., boiler) where fuels are burned.
Fixed roof means a cover that is mounted on a storage vessel or waste management unit
in a stationary manner and that does not move with fluctuations in liquid level.
Flame zone means the portion of a combustion chamber of a boiler or process heater
occupied by the flame envelope.
Flare means a device used in refineries to combust undesirable volatile gases (e.g.,
methane, ethane, hydrogen sulfide) from process units. Flares also take momentary
surges in gas manufacturing by burning the excess. When burned, these gases are
converted to more favorable compounds which can be emitted into the air.
Flow indicator means a device that indicates whether gas is flowing, or whether the valve
position would allow gas to flow, in a line.
Gasoline means any petroleum distillate or petroleum distillate/alcohol blend having a
Reid vapor pressure of 27.6 kilopascals or greater that is used as a fuel for internal
combustion engines.
Hazardous organic pollutant or HAP means one of the 188 chemicals listed in section
112(b) of the Clean Air Act, and listed in Appendix A of this manual.
November 1, 2000
E-3
-------
Petroleum Refinery MACT Standard Guidance
Incinerator means an enclosed combustion device that is used for destroying org?-
compounds. Auxiliary fuel may be used to heat waste gas to combustion temperas. •*-.
Any energy recovery section is a separate section following the combustion section an^
the two are joined by ducts or connections carrying flue gas.
Internal floating roof means a cover that rests or floats on the liquid surface (but no:
necessarily in complete contact with it) inside a storage vessel or waste management uni:
that has a permanently affixed roof.
Major source means a source that has the potential to emit 10 tons per year o- more
annually of any of the 188 listed hazardous air pollutants (HAPs), or 25 tons per year oi
more annually of any combination of HAPs.
Malfunction means any sudden, infrequent, and not reasonably preventable fai'jie o' ai
pollution control equipment, process equipment, or a process to operate in a norma 0'
usual manner. Failures that are caused in part by poor maintenance or careless operatic'
are not malfunctions.
Maximum achievable control technology or MACT means demonstrated technologies
which may be used to achieve acceptable air emissions limits for specific compounds
Maximum true vapor pressure means the equilibrium partial pressure exerted by tne
stored liquid at the temperature equal to the highest calendar-month average of the liquic
storage temperature for liquids stored above or below the ambient temperature or at the
local maximum monthly average temperature as reported by the National Weather Service
for liquids stored at the ambient temperature.
New source means a source that commenced construction after July 14, 1994.
Organic hazardous air pollutant or organic HAP means any of the 28 organ!.
chemicals listed in Appendix B of this manual.
Primary seal means the seal that slides against a wall of a floating roof tank a? tne rocf ir
raised and lowered. It closes the annular space between the roof and tank wal' and can be
constructed of metal or polymer.
November ', ?0C\"
E-4
-------
Petroleum Refinery MACTStandard Guidance
Process heater means an enclosed combustion device that primarily transfers heat
liberated by burning fuel directly to process streams or to heat transfer liquids other than
water,
Process unit means the equipment assembled and connected by pipes or ducts to
process raw and/or intermediate materials and to manufacture an intended product. A
process unit includes any associated storage vessels, and includes, but is not limited to,
chemical manufacturing process units and petroleum refining process units.
Reconstruction means the replacement of components of an affected or a previously
unaffected stationary source to the extent that:
(1) The fixed capital cost of the new component exceeds 50 percent of the fixed capita!
cost that would be required to construct a "comparable new source; and
(2) It is technologically and economically feasible for the reconstructed source to meet
the relevant standard(s) established by the Administrator (or a state) pursuant to
Section 112 of the Clean Air Act.
Recovery device means an individual unit of equipment capable of and used for the
purpose of recovering chemicals for use, reuse, or sale. Recovery devices include, but are
not limited to. absorbers, carbon absorbers, and condensers.
Secondary seal means the seal that provides addition evaporative loss control. It is
mounted on the roof rim or tank wall over the primary seal.
Single-seal system means a floating roof having one continuous sea! that completely
covers the space between the wall of the storage vessel and the edge of the floating roof.
Total organic compound or TOC means those compounds, excluding methane and
ethane, measured according to the procedures of method 18 of 40 CFR 60 Appendix A.
Method 25A may be used alone or in combination with Method 18 to measure TOC as
provided in 40 CFR 63.645.
November 1, 2000
-------
Petroleum Refinery MACTStandard Guidance
APPENDIX F. Compliance Checklist for the
Petroleum Refinery MACT Standard
40 CFR Part 63, Subpart CC
November, 2000
November 1, 2000
F-1
-------
Petroleum Refinery MACTStandard Guidance
Table of Contents
I GENERAL APPLICABILITY F-4
II APPLICABILITY FOR SPECIFIC EMISSION POINTS F-5
A. Miscellaneous Process Vents F-5
B. Storage Vessels F-6
C. Wastewater Streams F-8
D. Gasoline Loading Racks F-8
E. Marine Tank Vessel Loading F-8
F Equipment Leaks F-9
III. COMPLIANCE DEADLINES F-9
A. All new sources F-10
B. Existing Miscellaneous Process Vents and Gasoline Loading Racks F-10
C Existing Wastewater Streams F-10
D. Existing Storage Vessels F-10
E. Marine Tank Vessel Loading Operations F-10
F. Equipment Leaks F-10
IV. GENERAL STANDARDS F-10
A. Performance Testing F-10
B Operating Permits F-11
C. Application for Approval of Construction or Reconstruction F-11
D Notification of Compliance Status (NCS) Reports F-11
E Periodic Reports F-11
F. Startup, Shutdown and Malfunction Plans and Reports F-12
G. Reports Required for Special Situations F-13
H Requests for Extension of Compliance F-13
I Applications for a Performance Test Waiver F-14
J. Recordkeeping F-14
V. REQUIREMENTS FOR MISCELLANEOUS PROCESS VENTS F-15
A. Miscellaneous Process Vents Control Requirements F-15
B. Miscellaneous Process Vents Testing Requirements F-15
C. Miscellaneous Process Vents Monitoring Requirements F-17
D. Miscellaneous Process Vents Reporting Requirements F-18
VI. REQUIREMENTS FOR STORAGE VESSELS F-21
A. Control Requirements for Storage Vessels F-21
November 1, 2000
F-2
-------
Petroleum Refinery MACTStandard Guidance
B. Testing Requirements for Storage Vessels F-.7.
C. Monitoring and Inspection Requirements for Storage Vessels for Storage Vessels
Required to Apply Controls K-<_.
D. Reporting Requirements for Storage Vessels Equipped with Closed
Vent Systems F-2-
E. Recordkeeping Requirements for Storage Vessels F-?"-
VII, REQUIREMENTS FOR WASTEWATER STREAMS F-28
A. Control Requirements for Wastewater Streams F-2c
B. Testing and Monitoring Requirements for Wastewater Streams
C. Reporting and Recordkeeping Requirements for Wastewater Streams F-2f
VIII, REQUIREMENTS FOR GASOLINE LOADING RACKS F-2i
A Control Requirements for Gasoline Loading Racks F-Z?
B Testing and Monitoring Requirements for Gasoline Loading Racks F-?b
C. Reporting and Recordkeeping Requirements for Gasoline Loading Racks > i'
IX REQUIREMENTS FOR MARINE TANK VESSEL LOADING , f-i'-
A. Control Requirements for Marine Tank Vessel Loading F-3
B. Testing and Monitoring Requirements for Marine Tank Vessel Loading r-"*'
C. Reporting and Recordkeeping Requirements for Marine Tank
Vessel Loading F-2"
X REQUIREMENTS FOR EQUIPMENT LEAKS F-;<'
A. Control Requirements for Equipment Leaks F-.V
B. Testing, Inspection, and Monitoring Requirements for Equipment Leaks F-3:
C. Reporting and Recordkeeping Requirements for Equipment Leaks f- .
XI EMISSIONS AVERAGING - .
A. Emissions Averaging Applicability . F-32
B. Emissions Averaging Credit/Debit System f:-31
C. Approval of Emissions Averaging Plan
D Testing, Monitoring, Reporting, and Recordkeeping for Emissions
Nevernbe' ' 2'f
F-3
-------
Petroleum Refinery MACTStandard Guidance
I. GENERAL APPLICABILITY
1, Is the refinery a major HAP source?
[ ] Potential to emit > 10 tons per year (tpy) of any of the 188 HAPs listed in §
112(b) of the Clean Air Apt; or
[ ] Potential to emit 2 25 tpy of total HAPs,
Yes[ ] No[
]
2, Do the refining process units at refineries that are major HAP sources emit or
contain any of the following 28 organic HAPs? Please check the substances
below that apply
[ ] Benzene [ ] Ethylene glycol
[ ] Biphenyl [ ] Hexane
[ ] Butadiene (1,3) [ ] Methanol
[ ] Carbon disulfide [ ] Methyl ethyl ketone (2-butanone)
[ ] Carbonyl sulfide [ ] Methyl isobutyl ketone (hexone)
[ ] Cresol (mixed isomers) [ ] Methyl tert butyl ether
[ ] Cresol (m-) j J Naphthalene
[ ] Cresol (0-) [ ] Phenol
[ ] Cresol (p-) [ j Toluene
[ ] Cumerte f J Trimetnylpentane (2.2.4)
[ ] Dibromoethane (1,2) [ ] Xylene (mixed isomers)
(ethylene dibromide) [ } Xylene (m-)
[ ] Dichloroethane (1,2) [ ] Xylene (0-)
[ ] Diethanolamine [ ] Xylene (p-)
[ ] Ethylbenzene
Yes[ ] No [
]
3. Are any of the following emission points located within petroleum refining
process units? Please check the emission points below that apply.
[ ] Miscellaneous process vents that contain s 20 ppmv total organic HAP
[ j Storage vessels (pressure vessels and vessels < m3 are exempt)
[ j Wastewater streams and treatment operations
[ ] Equipment containing or contacting a fluid that is > 5% by weight total
organic HAPs
Yes [ ] No [
]
November 1, 2000
F_4
-------
Petroleum Refinery HACTStandard Guidance
4 Are any of the following emission points located at a refinery that is a major
source'' Please check the emission points below that apply.
Yes
[ ] Marine vessel loading operations
J
[ ] Gasoline loading racks in SIC 2911
[ ] Storage vessels and equipment leaks associated with bulk gasoline
terminals in SIC 2911
Novfn-bB! ' 20'-'
F-5
-------
Petroleum Refinery MACTStandard Guidance
II. APPLICABILITY FOR SPECIFIC EMISSION POINTS
A. Miscellaneous Process Vents
1 Does the vent contain a aas stream with > 20 DDmv oraanic HAP and is it
continuously or Deriodicallv discharaed durina normal oDerations?
Yes[ ) No[
1
2. Is the vent or gas stream any of the following? Please check the descriptions
below that apply.
f I Directlv discharaed to the atmoSDhere
f l Routed to a control device Drior to discharae to the atmosDhere
f l Diverted to a Droduct recoverv Drior to control or discharae to the
atmosphere
Note. The above list gives examples of vent or gas streams and may not be all
inclusive.
Yes[ ] No [
]
3. Does the vent or gas stream come from any of the following? Please check the
items below that apply.
[ ] Gas streams routed to a fuel gas system
[ ] Relief valve discharges
[ ] Leaks from equipment regulated under 40 CFR 63.648
[ ] Episodic or nonroutine releases such as maintenance or upsets
[ ] In situ sampling systems (on stream analyzers)
[ ] Catalytic cracking unit catalyst regeneration vents
[ ] Catalytic reformer regeneration vents
[ ] Sulfur plant vents
[ ] Vents from control devices
[ ] Vents from any stripping operations applied to comply with the wastewater
provisions of 40 CFR 63 Subpart CC, G, or FF
[ ] Coking unit vents associated with coke drum, depressuring at or below a
coke drum outlet pressure of 15 pounds per square inch gauge, deheading,
draining, or decoking (coke cutting) or pressure testing after decoking
[ ] Vents from storage vessels
[ ] Emissions from wastewater collection and conveyance systems
Note: If the answer to question 3 is "Yes", the miscellaneous process vents
provision does not apply.
Yes[ ] No [
]
November 1, 2000
F-6
-------
Petroleum Refinery MACTStandard Guidance
4 Does the vent or gas stream come from any of the following? Please check the
items below that apply
[ ] Caustic wash accumulators [ ] Stripper overheads
[ ] Distillation lower condensers/ [ ] Vacuum accumulators
accumulators
[ ] Blowdown condenser/ [ ] Delayed coker vents
accumulators
[ ] Flash/knockout drums [ ] Reactor vessels
[ ] Scrubber overheads
Note. The above list gives examples of where vent or gas streams originate and
may not be all inclusive.
Yes: j No
]
5. Is the vent associated with an existing or new source?
[ ] Existing source
[ ] New source
Existing sources - sources that commenced construction on or before July 14,
1994.
New sources- sources that commenced construction after July 14, 1994. A
process unit constructed at an existing source is subject to new source
requirements if the new unit has the potential to emit 10 tons per year (tpy) or more
of any one HAP or 25 tpy or more of total HAPs. Otherwise it is subject to existing
source standards. A change to an existing source or an addition of an emission
point is subject to existing source standards, unless it is a reconstructed source,
which is subject to new source standards.
For an existing source:
6 Is the organic HAP concentration > 20 ppmv, and total VOC emissions s 33
kg/day?
Note: If the answer to question 6 is "Yes", it is a Group 1 miscellaneous process
vent. If the answer is "No", it is a Group 2 miscellaneous process vent.
Yes [ IV
]
No /pThfi' ¦ ?0O>,
F-7
-------
Petroleum Refinery MACTStandard Guidance
For a new source:
7 Is the organic HAP concentration s 20 ppmv, and total VOC emissions > 6,8
kg/day9
Note; If the answer to question 7 is "Yes", it is a Group 1 miscellaneous process
vent. If the answer Is "No", it is a Group 2 miscellaneous process vent.
Yes[ ] No [
]
B, Storage Vessels
1 Is it a tank or other vessel used to store oraanic liauids?
Yes[ ] No [
I
2 Is it permanently attached to a motor vehicle such as a truck, rail car. barge, or
ship"?
Yes[ ] No [
]
3. Is it a pressure vessel designed to operate in excess of 204.9 kPa and without
emission to the atmosphere''
Yes[ ] No [
]
4. Does it have a capacity less than 40 m3?
Yes[ ] No [
I
5 Is it used as a bottoms receiver tank?
Yes [ ] No[
]
6 Is it used as a wastewater storage tank''
Yes [ ] No[
]
Note: If any of the answers to questions 2 through 6 is "Yes", the storage vessels provision does not
apply
November 1, 2000
F-8
-------
Petroleum Refinery MACT Standard Qui da net
7, Is tank associated with an existing or new source9
[ ] Existing source
[ ] New source
Existing sources - sources that commenced construction on or before July 14,
1994,
New sources - sources that commenced construction after July 14, 1994, A
process unit constructed at an existing source is subject to new source
requirements if the new unit has the potential to emit 10 tons per year (tpy) or more
of any one HAP or 25 tpy or more of total HAPs, Otherwise it is subject to existing
source standards. A change to an existing source or an addition of an emission
point is subject to existing source standards, unless it is a reconstructed source,
which is subject to new source standards.
!
For an existing source.
8 Is the capacity > 177 m3 arid vapor pressure > 10.4 kPa (maximum) and 2 8.3
kPa (annual average) and liquid HAP content > 4% by weight (annual average)?
Note: If the answer to question 8 is "Yes", it is a Group 1 storage vessel. If the
answer is "No", it is a Group 2 storage vessel.
i
Yes , N.-
]
For a new source:
9 Is the capacity > 151 m3 and vapor pressure 2 3.4 kPa (maximum) and
liquid HAP content > 2% by weight (annual average)?
OR
10. Is the capacity between 76 and 151m3 and vapor pressure 2 77 kPa (maximum)
and liquid HAP > 2% by weight (annual average)?
Note: If the answer to question 9 or 10 is "Yes", it is a Group 1 storage vessel. If
both answers are "No", it is a Group 2 storage vessel.
Yes' No ,
]
Ye.- No
I
November ' 20!"
F-9
-------
Petroleum Refinery MACTStandard Guidance
C, Wastewater Streams
1. Is it water or wastewater that, during production or processing:
Comes into direct contact with or results from the Production or use of anv raw
material, intermediate produfct, finished product, byproduct, or waste product?
Is discharged into any individual drain system?
Yes[ ] No[
1
Yes[ ] No [
]
2 Does refinery have a total annual benzene loading 2 10 megagrams per year,
and a flow rate j 0.02 liters per minute, and benzene concentration 2 10 ppm
by weight, and subject to control requirements under 40 CFR 61 Subpart FF?
Note: Wastewater streams applicability criteria are the Same for existing and new
sources If the answer to question 2 is "Yes", it is a Group 1 wastewater stream. If
the answer is "No', it is a Group 2 wastewater stream.
Yes[ ] No[
]
0. Gasoline Loading Racks
1. Is it any of the following equipment, which is necessary to fill gasoline cargo
tanks? Please check the equipment below that applies.
[ ] Loading arms [ ] Shutoff valves
[ ] Pumps [ ] Relief valves
[ ] Meters [ ] Other piping and valves
Yes[ ] No I
]
2 Is it a gasoline loading rack classified under SIC 2911?
Yes[] No [
]
3. Does it have a gasoline throughput > 75,700 liters (20,000 gallons) per day?
Note: Gasoline loading racks applicability criteria are the same for existing and new
sources. If the answer to question 3 is "Yes", it is a Group 1 gasoline loading rack.
If the answer is "No", it is a Group 2 gasoline loading rack
Yes[ ] No [
]
E. Marine Tank Vessel Loading
1. Is it a land- or sea-based terminal or structure that loads liquid commodities in
bulk onto marine tank vessel loading''
Yes[ ] No[
]
November 1, 2000
F-10
-------
Petroleum Refinery MACTStandard Quioana
2 Is vessel loading associated with an existing or new source?
!
[ ] Existing source
( ] New source
Existing sources - sources that commenced construction on or before July 14,
1994;
New sources - sources that commenced construction after July 14, 1994. A
process unit constructed at an existing source is subject to new source
requirements if the new unit has the potential to emit 10 tons per year (tpy) or more
of any one HAP or 25 tpy or more of total HAPs. Otherwise it is subject to existing
source standards. A change to an existing source or an addition of an emission
point is subject to existing source standards, unless it is a reconstructed source,
which is subject to new source standards.
For an existing source;
3. Is vapor pressure of liquid loaded > 10,3 kPa and emissions > 9.1 megagrams
of any one HAP or > 22.7 megagrams of total HAPs per year?
Yes; ] No '
1
Note: If the answer to question 3 is "Yes", it is a Group 1 marine tank vessel
loading. If the answer is "No*, it is a Group 2 marine tank vessel loading.
J
For a new source:
4. Is vapor pressure of liquid loaded > 10.3 kPa^
Ye? . N>"
1
Note: If the answer to question 4 is "Yes", it is a Group 1 marine tank vessel
loading. If the answer is "No", it is a Group 2 marine tank vessel loading.
F. Equipment Leaks
1, ts it a vent from a wastewater system drain, tank mixer, or sample valve on a
storage tank''
Yes Ni
1
Note: If the answer to question 1 is "Yes", the equipment leaks provision does not
apply
J
November ?0r:r
F-11
-------
Petroleum Refinery MACTStandard Guidance
2 Is it an emission of organic HAPs from any of the following which is/are "in
oraanic hazardous air Dollutant service" (eauiDment containina or contactina
fluid > 5% by weight total organic HAP):
pump''
compressor?
pressure relief device?
sampling connection system?
open-ended valve or line?
valve?
instrumentation system?
Note: Equipment leaks applicability criteria are the same for existing and new
sources.
Note to inspector. The applicability sections of this checklist (i.e., General
Applicability and Applicability for Specific Emission Points) determines whether the
Petroleum Refinery MACT Standard applies to a particular refinery, and whether it
applies to a particular emission point. Unless otherwise noted, refineries are
required to control emissions from all Group 1 emission points to which the MACT
standard applies. Group 2 emission points are subject only to recordkeeping
requirements unless otherwise noted in the inspection guide.
Yes[ ] No[
]
Yes[ ] No [
]
Yes[ ] No[
]
Yes[ ] No [
]
Yes[ ] No [
)
Yes[ ] No[
]
Yes[ ] No[
]
III. COMPLIANCE DEADLINES
A. All new sources
Were all emission points in compliance at startup or by August 18, 1995,
whichever was later?
Yes[ ) No[ ]
B. Existing Miscellaneous Process Vents and Gasoline Loading Racks
Were all emission points in compliance by August 18, 1998?
Yes[ ] No [ ]
C. Existing Wastewater Streams
1. Were all emission points in compliance by August 18, 1998?
Yes[ ] No[ ]
2. Are all wastewater streams in compliance with the benzene waste
operations NESHAP (40 CFR 61, Subpart FF)?
Yes[ ] No[ ]
November 1, 2000
F-12
-------
Petroleum He finery MACT Standard 6uid3nce
D. Existing Storage Vessels
1. Were all fixed roof vessels in compliance by August 18, 1998?
Yesi ; No ; ]
2. Were fixed roof vessels for which the tanks that must be replaced in
compliance by August 18, 1999?
Yes[ i No[ j
3. Were floating roof vessels in compliance by August 18, 2005, or the next
scheduled maintenance and degassing after August 18, 1998, whichever is
first?
Yes [ ' No, .
E. Marine Tank Vessel Loading Operations
1. Were operations in compliance by August 18, 1999?
Yes [ ] No[ ]
2. Are operations used to generate credit in an emissions average?
Yes[ ] No I ,
If yes, were operations in compliance by August 18, 1998?
.Yes[ Nu i j
If operations were aoi in compliance by August 18, 1998, was a case-by-
case 1-year extension granted?
Yes [ j Nc; j
F. Equipment Leaks
1. Were equipment leaks in compliance by August 18, 1998?
Yes [j No[ ]
2. For sources that are complying with 40 CFR 60 Subpart W or 40 CFR 63
Subpart H, are they meeting the deadlines in the 3 phases of emissions
reductions?
Ve^ _ No¦ j
IV. GENERAL STANDARDS TO ALL APPLICABLE EMISSIONS POINTS
A. Performance Testing
1. Did the facility conduct and initial performance test of all pollution control
equipment for which it is required?
(See Section I of this checklist for applicability. If the pollution control
equipment is required by the MACT standard, an initial performance test is
required. Note that no performance tests are required for floating roofs or
process heaters > 44 MW with vent introduced into the flame zone.)
Yer- [ N.7 : j
2. Was the initial performance test aDDroved bv EPA?
Yes , ] No [ ]
November 20CK
F-13
-------
Petroleum Refinery MACTStandard Guidance
3. Did the facility notify the reaulatorv authority 30 davs Drior to conductina
each performance test?
Yes[ ] No[ ]
4. Were the tests conducted at the maximum reDresentative ODeratina
cepecity9
Yes[ ] No[ ]
Were controls operating at either maximum or minimum representative
operating conditions for monitored parameters, whichever result in lower
emission reduction? [40 CFR 63.642 (d)(3)])
Yes [ ] No[ ]
B. Operating Permits
Did the owner or operator of the source subject to the standard apply for a one-
time Part 70 or Part 71 operating permit from the appropriate authority?
Yes [ ] No[ ]
C. Application for Approval of Construction or Reconstruction
If the source is a new or reconstructed source, did it submit an application for
approval of construction or reconstruction?
Yes [ ] No[ ]
D. Notification of Compliance Status (NCS) Reports
1. Did the facility submit a Notification of ComDliance Status fNCS) within
150 davs after each aDplicable comDliance deadline, or with the next
periodic report for new Group 1 emission points or floating roof storage
vessels brought into compliance after August 18, 1998?1
(See part III of this checklist for applicable compliance deadlines.)
Note: The NCS report may be included as a separate report, as an operating permit
application, or in an amendment to an operating permit application).
Yes [ ] No[ ]
2. Did the report identify each gmis^jpr) point and method of comDliance?
Yes [ ] No[ ]
3. Did the report include the following:
al Information on individual emission points to demonstrate cnmplianr.p
such as range of monitored parameters? [40 CFR 63.654(f)(1) and
(f)(3)]
Yes [ ] No[ ]
b) Results of continuous monitorina system performance evaluations? [40
CFR 63.654(f)(4)]
Yes [ ] No[ ]
November 1, 2000
F-14
-------
Petroleum Refinery MACT Standard Guidance
c) Determination of rule aoDlicabilltv to flexible operation units and storaae
vessels and distillation units for which use varies from year to year?
[40 CFR 63.654(h)(6)]1
Yes ' No ¦ '
4. If the facility was required to conduct initial performance tests, did it submit
one examDle comDtete test reDort for each test method used?
Note: For additional tests using the same method, only the results of the each
additional test must be submitted. [40 CFR 63.654 (f)(2)]
Yes[1 Nu [ j
E. Periodic Reports
1. Have any compliance exceptions occurred within any 6-month reporting
period?
Yes[ _ Nc , )
a) If yes, has the facility submitted periodic reports within 60 days
after the end of each 6- month period?
Ye.- N, , ,
b) If the facility uses emissions averaging, has the facility submitted
reports quarterly? [40 CFR 63.654(g)]
Yes[ ] No [ j
2. Were any new Group 1 emission points added or did any Group 2 emission
points become Group 1 emission points during the last 6-month period?
Yes; ' No[ ;
a) If yes, was an NCS report included with the periodic report?
Yes[ ] No[ ]
3. Were any floating storage vessels brought into compliance during the last
6-month period?
Yes[ • No ? }
a) If yes, was an NCS report Included with the periodic report?
Yes [ No[ )
'This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on Aug
For more information, see Appendix G.
F. Startup, Shutdown and Malfunction Plans and Reports
1. Has the facility developed and implemented a startup, shutdown, and
malfunction plan for the entire facility?
Note: The plan is not required to include wastewater.
ust 18 1998
Yes * ' ;
a^ If ves, does the malfunction olan describe Drocedures for ODeratina and
mamtainina the source durina periods of startuD. shutdown, and
malfunction?
Yes t hi. [ |
November 1. 2C'C
F-15
-------
Petroleum Refinery MACTStandard Guidance
M Dorr the Dlan also include a Droaram of corrective action for
malfunction of process and air pollution control equipment used to
comply with the relevant standard?
Note: EPA typically defines malfunctions as rare, unforeseeable.occurrences and
does not allow for facilities to operate in malfunction for extended periods of time.
Ves [ ] No[ ]
2. Has the facility prepared a Startup, Shutdown, and Malfunction Report to
document each:
a) Start of operation of a process unit for production?
Ves [ ] No [ ]
tA Cessation of a Drocess unit for maintenance. reDair. or equipment
replacement7
Yes [ ] No[ ]
cl Malfunction of a Drocess unit?
Yes [ ] No[ ]
3 Are corrective actions to address each malfunction consistent with the
startup, shutdown, and malfunction plan?
Yes [ ] No[ ]
a) If yes, has the facility submitted a statement to this effect in the semi-
annual report? [40 CFR 63.10(d)(5)(l)]
Yes [ ] No[ ]
b) If a malfunction occurs and corrective actions are not consistent with
the startup, shutdown, and malfunction plan, has the facility reported
this in the periodic report for the time period in which the malfunction
occurred'''
Note: If a malfunction does not occur during a reporting period, a startup, shutdown,
and malfunction report is not required.
Yes [ ] No[ ]
G. Reports Required for Special Situations
1. Does the facilitv use/intend to use alternative Drocedures fe.a.. Drocedures
other than those described in the MACT Standard) or devices to comply
with the MACT standard?
Yes [ ] No [ ]
a) If yes, has the facility submitted the following information 18 months
before the compliance date for existing sources, or with the approval of
construction for new sources:
Yes [ ] No [ ]
Request for aDDroval to monitor an alternative control device
operating parameter, with supporting justification? [40 CFR
63.654(h)(4)]
Yes [ ] No [ ]
November 1, 2000
F-16
-------
Petroleum Refinery MACT Standard Suidanct
'This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August 18 ',93?
For more information, see Appendix G.
• Reauest for aDDrovai to use data comDression svstems instead of
keeping hourly records, with supporting information? [40 CFR
63.654(h)(5)]
Yes [ ] Nc; ]
Request to use other alternative monitoring methods, with
supporting justification? [40 CFR 63.654(h)(5)(iv) and 63 8(f)(4)(ii))
Yes [ ] No[
Request to establish an alternative emission standard, with a test
plan or results of testing and monitoring? [40 CFR 63.6(g)(2)]
Note: If EPA finds the alternative standard equivalent to the MACT standard, EPA
will request public comment and publish a Federal Register notice allowing its use.
Prior to conducting the inspection, the inspector should determine whether EPA has
recently adopted any alternative standards equivalent to the MACT standard, with
which the facility intends to comply.
Yes : , No [
H. Requests for Extension of Compliance
1. Has the facility requested an extension of compliance either;
a) at least 12 months before the compliance date? or
Yes t j Nc[ :
b) 18 months prior if emissions averaging is used?
Note; Facilities may request an extension of compliance if emissions reductions
been achieved early, or is the source Is unable to comply with the relevant standard.
Requests for an extension of compliance can only be made for existing sources.
Yes : " Nc : ;
November " 200':
F-17
-------
Petroleum Refinery MACTStandard Guidance
2. If the facility submitted a request for an extension, did the request include
the following
a) Description of controls to be installed''
Yes [J No [ J
b) Compliance schedule?
Yes [ ] No[ ]
c) Interim emission control steps?
Yes [ ] No[ ]
I. Applications for a Performance Test Waiver
1 Is the facility unable to conduct a performance test for reasons such as
technical or economic infeasibility, or other reasons, has an extension of
compliance been requested?
Yes [ ] No[ ]
2. If yes, has the facility submitted an application for waiver of a performance
test to the Administrator?
Yes [ ] No [ ]
3 Did the application include information justifying the request and detailing
the infeasibility7 [40 CFR 63.7(h)(3)(iii)]
Yes [ ] No[ ]
J. Recordkeeping
1. Does the facility keep records of reports submitted, monitoring results, and
other records for at least 5 years? [40 CFR 63.642(e) and 63.654(l)(4)]
Yes [ ] No[ ]
2. Are records keDt so that thev are accessible within 24 hours of reauest in
either hard copy or computer-readable form? [40 CFR 63.642(e)]
Yes [ ] No[ ]
3. Are the following records maintained on site:
Records of the occurrence and duration of each startup, shutdown, or
malfunction of operation and air pollution control equipment? [40 CFR
63.10(b)(2)(l-ii)]
Yes [ ] No[ ]
• Records of actions that are consistent and inconsistent with the
startup, shutdown, and malfunction plan? [40 CFR 63.10(b)(2)(iv-v)]
Yes [ ] No[ ]
Records of continuous monitorina svstem calibration checks fif
continuous monitoring is required)? [40 CFR 63.10(b)(x)]
Yes [ ] No[ ]
Records for storage vessel??. [40 CFR 63.654(l)(1l]
Yes [ ] No[ ]
-
November 1, 2000
F-18
-------
Petroleum Refinery MACTStandard Guidance
• Comoiete test reDorts and reoorted results for anv reauired
performance tests? [64.654(1 )(2)]
Yes | j i\, _ !
• Values of continuously monitored parameters? [40 CFR
63.654(l)(3)]
Yes ,
Any additional records required by permit?
Yes [ ] .V i j
Nov&«nb«-- 1 200"
F-19
-------
Petroleum Refinery MACTStandard Guidance
V. REQUIREMENTS FOR MISCELLANEOUS PROCESS VENTS
A Miscellaneous Process Vents Control Requirements
1. Is the source an existing source, and the vent contains 20 ppmv or more of
organic HAPs, and emits 33 kg/day or more of total VOCs?
Yes J .] No [ ]
2. Is the source a new source, and the vent contains 20 ppmv or more of
organic HAPs, and emits 6.8 kg/day or more of VOCs?
Yes [ ] No[ ]
a) if yes to 1 or 2, does the facility control its Miscellaneous Process
Vents by:
Using a flare? or
Yes f] No[ ]
Reducing organic HAPs by 98% or to 20 ppmv using
incinerators, boilers, process heaters, or other devices? or
Yes [ ] No[ ]
If a boiler or process heater is used, the vent stream must be
introduced into the flame zone of the control device, or in a
location such that the required percent reduction or
concentration is achieved?
Yes [ ] No[ ]
B. Miscellaneous Process Vents Testing Requirements
1. Initial Performance Tests
a) Vents routed to a flare
Does the facility control Miscellaneous Process Vents emissions by
routing vents to a flare or by using other control devices?
Yes [ ] No [ ]
1) If the facility uses a flare, has the facility conducted an initial
performance test for each control device?
Yes [ ] No[ ]
2) Did the initial performance test show that the flare is operating
properly, and that the emission rate does not exceed the capacity
of the fiame to control the emissions?
Yes [ ] No [ ]
3) For vents routed to a flare, did the initial performance test measure
the following.
Emissions visibility?
Yes [ ] No[ ]
November 1, 2000
F-20
-------
Petroleum Refinery MACTStandard Guidance
Net heat value of combusted gas"?
Yes ' V _ i
Flow rate of gases being combusted''
Yer [ '
b) Vents routed to an Incinerator or a boiler or process heater < 44
MW
For vents routed to an incinerator or a boiler or process heater < 44 MW
(150 MMBtu/hr) where the vent streams are qq! introduced into the
flame zone of the boiler or process heater, did the initial performance
test show compliance with the requirement to reduce organic HAPs by
98% or to 20 pprnv"5 [40 CFR 63.645 and 63,116 except (d) and (e)]
Ye<> , , Nc ;
c) Vents routed to other control devices
Does the facility control Miscellaneous Process Vents emissions with:
1} Vents routed to a boiler or orocess heater > 44 MW f150
MMBtu/hr)? or
I
)
Yes i , Nc- [ ;
2) Vent streams that are introduced into the flame zone of the boiler or
process heater? or
Yes; , Nu: j
3) A control device for which a -performance test was conducted for
determination of compliance with an NSPS if no process changes
have been made?
Note: If the facility answered yes to any of these questions (B.1 .c) performance
tests are not required for these vents.
Ye; ; No
2. Sampling for Initial performance tests
a) Does the facility conduct performance test sampling and analysis
according to the prescribed EPA-approved methods?
!
Yea . . \ . j
3. Follow-up tests to process changes
a) Have any process changes occurred at the facility"'
Ye: V - •
1) If yes, for each process change affecting a Group 2 process vent,
did the facility recalculate the TOC emission rate to determine
whether the vent remains a Group 2 process vent or becomes a
Group 1 process vent?
Yes: ; No , '
Nov em be' " ?r>fT
F-21
-------
Petroleum Refinery MACTStandard Guidance
Was rpi-jalr.ulatinri based on vent stream flow rate and TOC
measurements as specified for initial performance tests or best
engineering assessment practices?
Note: That process changes include, but are not limited to, changes in production
capacity, production rate, or catalyst type; whenever there is replacement, removal,
or addition of recovery equipment; and debottlenecking activities.
(Process changes do qq! include process upsets, unintentional, temporary process
changes, or changes that are within the range on which the original calculation was
based,)
Yes[ ] No[ ]
C. Miscellaneous Process Vents Monitoring Requirements
1. Miscellaneous process vents routed to a flare
For miscellaneous process vents routed to a flare, is a monitoring device
capable of continuously detected the presence of a pilot flame (including, but
not limited to a thermocouple, an ultraviolet beam sensor, or an infrared
sensor) used"
Yes[ ] No [ ]
2. Miscellaneous process vents routed to Incinerators other than catalytic
Incinerators
For miscellaneous process vents routed to incinerators other than catalytic
incinerators, is a temDerature monitorina device with a continuous recorder
used7
Yes ['} No [ ]
Is the device located in the firebox or in the duct work immediatelv
downstream of the firebox in a position before anv substantial heat exchanoe
occurs'
Yes[ ] No[ ]
3, Miscellaneous Process Vents routed to catalytic incinerators
For Miscellaneous Process Vents routed to catalytic incinerators, is a
temperature monitonnq device with a continuous recorder used?
Yes [ J No[ ]
Is the device located in the gas stream immediately before and after the
catalyst Deti?
Yes [ ] No[ ]
November 1, 2000
F-22
-------
Petroleum Refinery MACTStandard Qumnct
4. Miscellaneous process vents routed to boiler or process heaters with a
design heat capacity <44 megawatts where the vent streams are not
Introduced Into the flame zone
For miscellaneous process vents routed to boiler or process heaters with a
design heat capacity <44 megawatts where the vent streams are not
introduced into the flame zone, is a temDerature monitorina device with a
continuous recorder used?
Yes¦ No t ;
Is the device located in the firebox?
Note ¦ No monitoring is required for boilers or process heaters.
Yes. \c ;
5, Refineries that use a vent system with bypass line valves that have not
been sealed or secured.
For refineries that use a vent system with bypass line valves that have not
been sealed or secured, is a flow indicator that determines at least everv hour
whether a vent stream flow is present used?
Yes [ , No
Is the indicator located at the entrance to any bypass line that could divert
the vent stream away from the control device to the atmosphere?
Yes [ 1 No i ]
6. Refineries that use a vent system with bypass lines, where the valves
have been secured In the closed position with a car-seal or a lock-and
key-type configuration.
For refineries that use a vent system with bypass lines, where the valves have
been secured in the closed position with a car-seal or a lock-and key-type
confiauration. are the valves visualiv insoected at least everv other month to
ensure that they are maintained in the closed position and the vent stream is
not diverted through the bypass line?
Ye, , ; Nc : j
7. Refineries using other approved control devices
For refineries using other approved control devices or requesting to monitor
other parameters, is the facility complying with any site-specific monitoring
requirements''
Ye: N,- K ,
Novembe- " 2r)?'
F-23
-------
Petroleum Refinery MACTStandard Guidance
D. Miscellaneous Process Vents Reporting Requirements
1. Notice of Compliance Status (NCS) reports
a) All miscellaneous process vents affected by the MACT standard
For miscellaneous process vents affected by the MACT standard, has the
refinery submitted an NCS report that identifies the following:
1) Each vent?
Yes[ ] No [ ]
2) Whether the process vent is Group 1 or Group 2?
Yes[ ] No[ ]
3) For each Group 1 vent that is not included in an emissions average,
the method of compliance (e.g., use of a flare or other control device
meeting the requirements of the MACT standard)? [40 CFR
63.643(a)]
Note. If the required information has been submitted at an earlier date, or at different
times, and/or in different submittals, later submittals may refer to earlier submittals
instead of duplicating and resubmitting previously submitted information.
Yes [ ] No[ ]
4) For miscellaneous process vents with control devices required to be
. tested under the MACT standard, did the NCS include information on
each testina method, and results of the Derformance test since there
are different requirements for each test and test method used?
Yes [ ] No[ ]
5) For each test method used, did the NCS include the following test
results.
a) The percentage reduction of organic HAPs or TOC or the outlet
concentration of organic HAPs or TOC (ppm by volume on a dry
basis corrected to 3 percent oxygen), determined as specified in 40
CFR 63.116(c)?
Yes [ ] No[ J
b) The value of the monitored parameter specified in 40 CFR 63
Subpart CC, Table 10 or a site specific parameter approved by the
permitting authority, averaged over the full period of the performance
test"?
Yes [ ] No[ ]
November 1, 2000
F-24
-------
Petroleum Refinery MACTStandard Guidance
6) For each test method used, does the NCS include the following
supporting information:
a) Sampling site description?
!
Yes[ No ;
b) Description of sampling and analysis procedures, and any
modifications to standard procedures?
Yes[ ] Nc [ j
c) Quality assurance procedures?
Yes [ ] fvi
d) Record of operating conditions during the test?
Yes [ ] Nc
e) Record of preparation of standards?
Yes : ; No; ¦
f) Record of calibrations?
Yes [ ' No: j
g) Raw data sheets for field sampling?
Yes [ Nc
h) Raw data sheets for field and laboratory analyses?
Yet [ j No[ ;
1) Documentation of calculations?
Yes [ j No; ]
j) Any other information required by the test method?
Yes [ ] No,
7) If the same test is conducted for multiple emission points, did the
facility submit the following:
a) one complete test report for each test method used for each
emission point?
Yes [ . Nc ( ]
b) for additional tests using the same method, the additional test
results?
Yes , Nj ^
8) Miscellaneous Process Vents Controlled by Flares
a) For vents controlled by flares, did the NCS include the following test
results,
all visible emission readings?
Yes i ; N;
heat content determinations7
Ye? Nc [ ,
flow rate measurements?
Yes [ . v.; ;
exit velocity determinations made during the compliance
determination? [40 CFR 63.654(f)(1)(iv)(A)]
Yes : _ No[
Novr-irhc-r 1, 200'
F-25
-------
Petroleum Refinery MACTStandard Guidance
bl For vents controlled bv flares, a statement of whether a flame was
Dresent at the Dilot liaht over the full Deriod of the compliance
determination? [40 CFR 63.654(f)(1)(iv)(B)]
Yes[ ] No[ ]
c) If a parameter other than the presence of a pilot flame is monitored,
the acceptable range for the parameter and the rationale (including
any supporting data or calculations) for the range?
Note ¦ Results of a prior performance test can be used if that test was conducted
using the methods specified in 40 CFR 63.645 and test conditions were
representative of current operating conditions.-
Yes[ ] No [ ]
9) Vents routed to an incinerator or boiler or process heater < 44
MW where the vent streams are Jifii introduced Into the flame
zone
In addition to the information required for all miscellaneous process
vents, do NCS reports for vents routed to an incinerator or boiler or
process heater < 44 MW where the vent streams are ooi introduced
into the flame zone include the following information:
a) Average firebox temperature (or gas stream temperature for
catalytic incinerators) over the duration of the performance test?
Yes [ ] No[ ]
b) Acceptable range for the daily average firebox temperature and
rationale for the range?
Yes [ ) No [ ]-
c) Times at which an operating day begins and ends?
Yes[ ] No [ ]
2. Periodic reports
a) Has the refinerv experienced anv comDliance exceDtions or periods of
excess emissions''
(Compliance exceptions and periods of excess emissions do not include
periods of startup, shutdown, malfunction, performance testing and
monitoring system calibration.)
Yes[ ] No [ ]
b) Has the refinerv submitted the aDDrooriate Deriodic reDorts reaardina the
compliance exceptions or periods of excess emissions?
Yes[ ] No [ ]
November 1, 2000
F-26
-------
Petroleum Refinery MACTStandard Guidance
1) Were the reports submitted no later than 60 days after the end of
each 6-month period when any compliance exceptions occur?
Note- The first 6-month period begins on the date the NCS report is required to be
submitted.
Yes :
2) If the refinery uses emissions averaging, were the reports submitted
quarterly?
Yes; , No .
3) For control devices for which an initial performance test is required
(flare, incinerator, and boiler or process heater < 44 MW where the
vent streams are not Introduced Into the flame zone), did the facility
submit the following Information in the periodic report;
Complete test report for initial performance test results''
Yet , rv.
• Times and duration of periods when monitoring devices are
not operating?
Yes[ ] No • .
4) Periodic Reports for vents routed to a flare
For vents routed to a flare, did the facility submit a record of each
pilot flame determination (or alternate parameter upon request and
approval) in the periodic report?
Yes [ ) No [ ]
5) Periodic Reports for vents routed to an Incinerator or boiler
or process heater < 44 MW where the vent streams are not
Introduced Into the flame zone
For vents routed to an incinerator or boiler or process heater < 44
MW where the vent streams are qq! introduced into the flame zone,
did the facility submit the following information in the periodic
report;
. Record of each firebox temDerature value or a block
average of values for periods of 1 hour or less"5
Yf- • ; , N'. :
• Record of the dailv averaae firebox temDerature?
Note: If all hourly temperature values are within the range reported in the NCS, the
facility may record that all values are within the range instead of daily average
values.
Ye;- ;
Ncvembc i 2rr,"
F-27
-------
Petroleum Refinery MACTStandard Guidance
Vi. REQUIREMENTS FOR STORAGE VESSELS
A. Control Requirements for Storage Vessels
1. For storage vessels with, floating roofs does the facility use one of the
following control devices?
Yes [] No[ ]
a) Internal floating roof with specified seals?
Yes [J No [ ]
b) External floating roof?
Yes[] No[ ]
c) Externa! floating roof converted to an internal floating roof (i.e., fixed roof
installed above the external floating roof)?
Yes i j No[ ]
2. For storage vessels with closed vent systems* does the facility use a closed
vent system routed to a flare or other control device that reduces HAP
emissions by 95% or to 20 ppmv?
Yes [ ] No [ ]
3. Are all storage vessels that store a liquid with a maximum true vapor
pressure of total organic HAPs * 76.6 kPa controlled by a closed vent
system and control device'' [40 CFR 63.119(a)(2)]
Yes [ ] No [ ]
- If yes, are. work practices, as specified in 40 CFR 63.119(b) through (e),
fo!lowed for each of the control methods?
Yes [ ] No [ ]
4. Storage vessels at new sources
a) In addition to the above control requirements, did storage vessels at new
sources also install deck fitting controls, as specified in 40 CFR
63.119(c)(2)(l) through (xii), on all floating roof tanks?
Yes [ ] No [ ]
b) Do storage vessels at new sources also apply the control requirements of
40 CFR 63 119(b)(5) and (b)(6)?
Yes [ ] No [ ]
B. Testing Requirements for Storage Vessels
1. Initial Performance Tests for Closed Vent Systems Routed to a Flare
a) For storage vessels equipped with a closed vent system routed to a flare,
has the facility conducted an initial performance test or compliance
determination, as specified in 40 CFR 63.11(b), to ensure compliance with
the control requirement to reduce total organic HAP emissions by 95% or
to 20 ppmv''
Yes[ ] No [ ]
November 1, 2000
F-28
-------
Petroleum Refinery MACTStandard Guidance
1) If yes. did She test include the measurement/determination of the
following
• Emissions visibility?
Yes ; ;
i
No |
• Net heat value of combusted gas?
Yes [ j
No ' ;
• Flow rate of gases being combusted?
Yes [
no ; '
• Exit velocity?
Yes • rv
2. Initial Performance Tests for Closed Vent Systems Routed to a Control
Device Other Than a Flare
a) For storage vessels equipped with a closed vent system routed to a
control device other than a flare, did the facility conduct either an initial
design evaluation, as specified in 40 CFR 63.120(d)(1)(l), or an initial
performance test, as specified in 40 CFR 63.120(d)(1 )(ii)?
Yes t
\> t ;
C. Monitoring and Inspection Requirements for Storage Vessels for Storage
Vessels Required to Apply Controls
1. Storage vessels equipped with a closed vent system
For storage vessels equipped with a closed vent system, does the facility
monitor the parameters proposed in the Notice of Compliance Status (NCS)
report to ensure that the control device is being properly operated and
maintained7
Yer '
Nc :
Note: There are no monitoring requirements for storage vessels equipped with
floating roofs.
2. Closed vent systems routed to a control device
Does the facility inspect closed vent systems routed to a control device every
12 months as specified in 40 CFR 63.148?
Yes
3. Storage Vessels with floating roofs
a) Do the storage vessels have a single-seal system or a double-seal
system''
Yes t
N.
Novembe'
F-29
-------
Petroleum Refinery MACTStandard Guidance
b) Storage vessels with a single seal system
For storage vessels with a single seal system and equipped with a fixed
roof and an internal floating roof or an external floating roof converted to an
internal floating roof, does the refinery conduct the following inspections:
¦h Visuallv insDect the internal floatina roof and Drimarv seal throuah
manholes and roof hatches at least once every 12 months after initial
fill, or at least every 12 months after the compliance date?
Yes[ ] No[ ]
2} Visuallv insDect the internal floatina roof and Drimarv seal each time
the storaae vessel is emDtied and deaassed and at least once everv
10 ye?rs after the compliance date?
Yes[ ] No [ ]
31 Visuallv insDect aaskets. slotted membranes, and sleeve seal Cif anvl
each time the storaae vessel is emDtied and deaassed and at least
once every 1Q ye?r§ after the compliance date (new source only)?
Yes[ ] No [ ]
c) Storage vessels with a double single seal system
For storage vessels with a double single seal system and equipped with a
fixed roof and an internal floating roof or an external floating roof converted
to an internal floating roof, does the refinery conduct the following:
11 Visuallv insDect the internal floatina roof, nrimarv seal and secondarv
seal each time the vessel is emptied and degassed and at least once
everv 5 vears after the comoiiance date? or
Yes[ ] No [ ]
2) Visuallv insDect the internal floatina roof and the secondarv seal
throuah manholes and roof hatches at least once everv 12 months
after initial fill, or at least every 12 months after the compliance date;
and
Yes[ ] No [ ]
3) Visuallv insDect the internal floatina roof, primarv seal and secondarv
seal each time the vessel is emptied and degassed and at least once
every 10 yeers after the compliance date?
Yes[ ] No [ ]
*
November 1, 2000
F-30
-------
Petroleum Refinery MACT Standard Guidance
d) Storage vessels equipped with an external floating roof
1) For storage vessels equipped with an external floating roof, does the
facilitv visuallv insDect the followina. each time the vessel is emDtied
and declassed:
- external floating roof?
Yes[ ] No[ ]
- the primary and secondary seals7
Yes ; N'j ;
- fittings7
Ye: 1 ; \t ;
2) For storage vessels equipped with an external floating roof, does the
facility conduct the following additional inspections:
• For single-seal systems, does the facility:
- Measure the gaps between the vessel wall and the primary seal
by the compliance date and at least once a year, until a
secondary seal is installed?
Yes ; j No „ ,
- When a secondary seal is installed, measure gaps between the
vessel wall and both the primary and secondary seal within 90
calendar days of installation, and then comply with the double-
seal inspection requirements? [40 CFR 63.120(b)(1 )(ii)]
Yes t j imu .
• For double-seal systems, does the facility:
- Measure the gaps between the vessel wall and the primary seal
during hydrostatic testing or by the compliance date and at
least once every 5 years thereafter?
Yes L No[ ;
- Measure the gaps between the vessel wall and the secondary
seal by the compliance date and at least once a year?
Ye? , Nc
NO'/P'T bf"* 1. 200"
F-31
-------
Petroleum Refinery MACT Standard Guidance
D. Reporting Requirements for Storage Vessels Equipped with Closed Vent
Systems
1. Notice of Compliance Status Reports
a) Storage vessels equipped with a closed vent system routed to a
flare
For storage vessels equipped with a closed vent system routed to a flare,
does the NCS contain the results of the initial performance test, including:
« Flare design, such as steam-assisted, air-assisted, or non-
assisted7
Yes [ ] No [ ]
• Visible emissions readings?
Yes [ ] No [ ]
• Heat content determinations''
Yes [ ] No[ ]
• Flow rate measurements'?
Yes [ ] No [ ]
• Exit velocity determinations?
Yes [ ] No[ ]
• Periods during the compliance determination when the pilot flame is
absent"
Yes [ ] No []
b) NCS Reports for storage vessels equipped with a closed vent
system routed to a control device other than a flare
For storage vessels equipped with a closed vent system routed to a
control device other than a flare, does the NCS also include:
• Description of the parameter(s) to be monitored to ensure proper
operation and maintenance of the control device?
Yes [ ] No []
• Explanation of the parameter selection?
Yes [ ] No{ )
• Frequency of monitoring?
Yes [ ] No[ ]
• Design evaluation documentation, as specified in 40 CFR
63.120(d)(1 )(l), or results of the initial performance test including
identification of emission points sharing the control device?
Yes [ ] No []
November 1, 2000
F-32
-------
Petroleum Refinery MACTStandard Guidance
2. Periodic Reports
a) Have any compliance exceptions regarding storage vessels occurred?
Yes l \c :
If yes, has the facility submitted the appropriate periodic reports for
storage vessels?
Yes[ , No; ;
b) Periodic Reports for storage vessels equipped with a closed vent
system routed to a control device
For storage vessels equipped with a-closed vent system routed to a
control device, do periodic reports include a description of the following.
• Routine maintenance for the control device that was performed
during the previous 6 months''
(
i
}
\
I
\
Yes ¦ ,
• Routine maintenance anticipated for the control device for the next
6 months?
Yes . , r,c ,
• For a control device that is a flare, each occurrence and cause
when the requirements specified in 40 CFR 63.11(b) are not met?
Yes ' ; 'V
• For a control device other than a flare, each occurrence and cause
of monitored parameters being outside the ranges documented in
the NCS?
Yes • No i ]
c) Periodic reports for storage vessels equipped with any type of
floating roof
For storage vessels equipped with any type of floating roof, do the
periodic reports contain the results of each inspection in which a failure
was detected, including:
1) Date of inspection?
i
Yes [ . , _ !
2) Identification of the storage vessel?
Yes „ . iso . i
3) Description of the failure?
Yes
4) Nature and date of repair or date the vessel was emptied9
d) Did the facility apply for an extension beyond the 45 day period for
correcting failures identified during inspections of storage vessels?
Ye$ [ ] No [ ;
Novembe« 20f
F-33
-------
Petroleum Refinery MACTStandard Guidance
1) If the facility applied for an extension, did the corresponding
periodic reports also include the following information
• Description of the failure?
Yes[ ] No[ ]
• Statement that alternate storage capacity is unavailable?
Yes[ ] No[ ]
• Schedule of actions that will ensure that the control
equipment will be repaired or the vessel will be emptied as
soon as possible?
Note If the vessel cannot be repaired or emptied within 45 days, the facility may
utilize up to 2 extensions of up to 30 additional days each.
Yes[ ] No I ]
e) Storage vessels equipped with art external floating roof
For storage vessels equipped with an external floating roof, did the
facility conduct any gap measurement?
Yes [ ] No( ]
1) If yes, did the facility notify the Administrator 30 days in advance of
the gap measurement9
Yes [ ] No[ ]
2) Were the requirements of 40 CFR 63.120(b)(3), (4), (5), or (6) not
met for any of the gap measurements?
Yes [ ] No[ ]
- If yes, were the results of the gap measurement in which the
requirements were not met included in the periodic reports?
Yes [J No[ ]
- Was the following information included in the reports.
• Date of seal gap measurement?
Yes [ ] No [ ]
• Raw data and calculations described in 63.120(b)(5) or (6)?
Yes [ ] No [ ]
• Description of seal conditions that are not met?
Yes I ] No[ ]
• Nature and date of repair or date the vessel was emptied?
Yes [ ] No[ ]
f) Floating Roof Storage Vessel Brought Into Compliance after
August 18, 1998.
Do the Periodic Reports include a NCS for each floating roof storage
vessel brought into compliance during the reporting period?1
Yes [ ] No[ ]
a) If yes, does the NCS include the method of compliance?
Yes [ ] No[ ]
November 1, 2000
F-34
-------
Petroleum Refinery MACTStandard Guidanct
b) If yes does the NCS include a list of all other floating roofs subject
to control requirements that are not yet in compliance and their
expected compliance date?
Yes ; ;
fv. t ;
c) If yes, for floating roof vessels brought into compliance, including
those brought into compliance during the last reporting period, does
the NCS include the actual date of compliance?
Yes [ ]
No; ]
3. Internal Inspection Notifications
al Did the facilitv notifv the Administrator of fillina or refillina of each storaae
vessel with organic HAPs?
Yes , ]
Nv : j
b) Did the facilitv notifv the Administrator at least 30 calendar davs nrior to
any scheduled internal inspections?
Yes [
j
- If not, was the internal inspection not planned? and
Yes [ j V '
- Could the owner/operator of the refinery not have known about the
inspection 30 calendar days in advance of refilling the vessel with
organic HAPs?
Yes ,
c) If the inspection is not planned and the owner/operator could not have
known about it in advance, did the facility notify the Administrator at
least 7 calendar days prior to refillinq the storaqe vessel?
Yes
\
i
v i
- If the notification was made by telephone, was it immediately
followed by written documentation demonstrating why the
inspection was unplanned?
Yes L
l\ c , '
1 This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on August *" 9
For more information, see Appendix G.
Noveuhe; ' /rY
F-35
-------
Petroleum Refinery MACTStandard Guidance
- If the notification was made in writing, was it is received by the
Administrator at least 7 calendar days prior to the refilling?
Note ¦ if the State or tocal permitting authority has received delegation of the Refinery
MACT (not all states have as of August 1997), they can waive the notification
requirements for all or some storage vessels at petroleum refineries. The State or
local permitting authority may also grant permission to refill storage vessels sooner
than 30 days after submitting the required notification under 40 CFR
64.654(h)(2)(l)(A) or sooner than 7 days after submitting the notification under 40
CF!1 64.654(h)(2)(i)(B) on a case-by-case basis.
Yes[ ] No[ 1
E. Recordkeeping Requirements for Storage Vessels
1) All Storage Vessels
- For all storage vessels, does the facility maintain records of Group 1 or
Group 2 determinations, vessel dimensions, and analysis of capacity for 5
years'5
Yes[ ] No []
- In addition, does the facility maintain all information required to be reported
for 5 years?
Yes[ ] No[ ]
2) Storage vessels equipped with a closed vent system routed to a
control device
For storage vessels equipped with a closed vent system routed to a control
device, does the facility also maintain the following records for 5 years:
a) Complete test report for initial performance test results'?
Yes[ ] No f ]
b) Measured values of monitored parameters?
Yes I] No [ }
c) Planned routine maintenance performed, including-
- The first time of day and date the control requirements are uoi met at the
beginning of the planned routine maintenance? and
Yes[ ] No []
- The first time of day and date the control requirements are met at the
conclusion of the planned routine maintenance''
Yes [ ] No[ ]
4) For storage vessels equipped with any type of floating roof, does the facility
retain records of each inspection oerformed? f4Q CFR 63.123c and fell
Yes [ ] No [ ]
November 1, 2000
F-36
-------
Petroleum Refinery MACT Standard Guidance
5) For storage vessels equipped with an external floating roof, does the facility
retain records of each seal gap measurement, includinq date, raw data
obtained in the measurement, and the calculations described in 40 CFR
63.120(b)(3) and (4)?
Yes , :
\ _
Nove'->fiP* i. 700'1
F-37
-------
Petroleum Refinery MACTStandard Guidance
VII, REQUIREMENTS FOR WASTEWATER STREAMS
A Control Requirements for Wastewater Streams
Note¦ If a refinery is in compliance with the benzene waste NESHAP [40 CFR 61
Subpart FF], it is considered to be in compliance with the refinery MACT standard.
Provisions of the benzene waste NESHAP apply to the following wastewater
streams at petroleum refineries:
(1) Total benzene loading > 10 Mg per year, and
(2) Flow rate ? .02 liters per minute, and
(3) Benzene concentration > 10 ppm by weight, and
(4) Not exempt from controls under the benzene waste NESHAP.)
1. Has the refinery reduced benzene mass emissions from wastewater streams
by 99% by using suppression followed by steam stripping, biotreatment. or
other treatment process?
Yes[ ] No[ ]
2 For vents from steam strippers and other waste management or treatment
units, does the facility utilize a control device that achieves 95% emission
reduction or 20 ppmv at the outlet of the control device?
Yes[ ] No[ ]
B. Testing and Monitoring Requirements for Wastewater Streams
1 Do all wastewater streams at the facility comply with the testing
requirements of the benzene waste NESHAP found in 40 CFR 61.340 through
61.355'?
Yes[ ] No [ ]
2. Is testing done at the required frequency?
Yes [ J No[ ]
3. If required, are periodic measurements of the benzene concentration in the
wastewater performed'?
Yes [ ] No[ ]
4. If required, does the facility conduct monitoring of the process or control
device operating parameter?
Yes[] No[ ]
C. Reporting and Recordkeeping Requirements for Wastewater Streams
1. Do all wastewater streams comply with the reporting requirements of the
benzene waste NESHAP found in 40 CFR 61.356 and 61.357? [40 CFR
63.654(a)]
Yes [ ] No[ ]
November 1, 2000
F-38
-------
Petroleum Refinery MACTStandard Guidance
2 In addition, is all information required to be reported retained for 5 years? [40
CFR 63.654{l){4)] Ye;-
Note: Since affected sources should already be in compliance with 40 CFR 61
Subpart FF, they will not need to make any changes to their current reporting and
recordkeeping procedures in order to comply with the Petroleum MACT standard
Noverrpf
F-39
-------
Petroleum Refinery MACTStandard Guidance
VIII. REQUIREMENTS FOR GASOLINE LOADING RACKS
A. Control Requirements for Gasoline Loading Racks
Is the facility in compliance with the gasoline distribution facilities NESHAP
found in 40 CFR 63 Subpart R, which requires the facility to:
1. Reduce emissions of total organic compounds (TOC) to 10 milligrams per
liter of gasoline loaded, and
2 Load gasoline only in vapor tight cargo tanks that have been tested to assure
vapor tightness?
Yes[ ] No [ ]
B. Testing and Monitoring Requirements for Gasoline Loading Racks
1. Is the facility in compliance with the testing and monitoring requirements of
the gasoline distribution facilities NESHAP found in 40 CFR 63.425(a)
through (c) (performance tests), 63.425(e) through (h) (annual certification),
63.425(f) (leak detection tests), 63.425(g) (nitrogen pressure decay field
tests), and 63.427 (continuous monitoring)?
Yes[ ] No[ ]
2. Initial Performance Tests
a) Did the facility conduct an initial performance test for gasoline racks
according to the test methods and procedures in 40 CFR 60.503 (except
using a reading of 500 ppm to determine the level of leaks to be repaired
under 40 CFR 60.503)?
Yes [' ] No [ ]
b) Did the facility conduct any follow-up tests following process changes?
Yes[ ] No[ ]
If yes, did the refinery document the reasons for any change in the
operating parameter value since the previous test?
Yes[ ] No[ ]
c) If the facility is using a closed vent system and control device as specified
in 40 CFR 60.112b(a)(3) to control emissions from gasoline loading racks,
did the facility conduct initial performance tests on the control devices?
[40 CFR 63.423]
Yes[ ] No[ ]
d) If the facility uses a flare to control emissions, and emissions from the
gasoline loading rack cannot be measured using the methods specified in
40 CFR 60.503, is the refinery in compliance with the provisions of 40
CFR 63.11(b)?
Yes [ ] No[ ]
November 1, 2000
F-40
-------
Petroleum Refinery MACT Standard Guidance
3. Annual Certification Tests
Does the facility conduct annual tests on gasoline cargo tanks to certify that
emissions controls are functioning properly?
Yes ,
If yes, is the annual performance test conducted according to the
vacuum and pressure tests described in Method 27 of 40 CFR 60
Appendix A?
Yes ; J NoJ i
Nlcw'imbe-' 1 200'
F-41
-------
Petroleum Refinery MACTStandard Guidance
4. Leak Detection Tests
During loading operations, does the facility conduct a leak detection test for
gasoline cargo tanks according to Method 21 of 40 CFR 60 Appendix A?
Yes[ ] No []
Are the teste conducted on each comDartment durina the loadina of
that comDartment. or white the compartment is still under pressure?
Yes[ ] No[ ]
b) In addition to Method 21, are the following requirements for the test
met [40 CFR 63,425]:
• To eliminate a positive instrument drift, does the dwell time for
each leak detection not exceed two times the instrument
response time?
Yes[ ] No [ ]
• Is the instrument purged with ambient air between each leak
detection?
Yes[ ) No[ ]
• Is the duration of the purge in excess of two instrument
response times?
Yes [ ] No[ ]
• Does the facility attempt to block the wind from the area being
monitored, and record the highest detector reading and location
for each leak?
Yes [ ] No[ ]
5. Additional Testing Requirements
a) For cargo tanks with manifolded product lines, does the facility conduct a
nitrogen pressure decay field test on each compartment of each tank?
(This test is described in 40 CFR 63.425(g).)
Yes [ ] No[ ]
b) Does the facility also conduct a continuous performance pressure decay
test, as described in 40 CFR*63.425 (h)"5
Yes [ ] No[ ]
6. Continuous Monitoring
Are gasoline loading racks in compliance with the continuous monitoring
requirements of 40 CFR 63.427(a) and (bp
Yes [ ] No [ ]
a) Is the continuous monitoring system installed, calibrated, certified,
operated and maintained according to manufacturer specifications?
Yes[) No { ]
November 1, 2000
F-42
-------
Petroleum Refinery HACTStandard Guidance
b) Is the location where the continuous monitoring system is installed
appropriate to the type of system used (e.g., carbon adsorption,
refrigeration condenser, thermal oxidation, or flare)?
Yes ; . No.
C. Reporting and Recordkeeping Requirements for Gasoline Loading Racks
1. Did the facility include the MCS for the gasoline loading racks in the initial
NCS for the refinery?
Yes j No ' j
2. For gasoline loading racks, does the facility comply with the reporting and
recordkeeping requirements of the gasoline distribution facilities NESHAP
found in 40 CFR 63.428(b), (c), (g)(1), and (h)(1) through (h)(3)?
Yes- V '
3 Does the facility retain all required records for 5 years?
Yes '
November * 2'TO
F-43
-------
Petroleum Refinery MACTStandard Guidance
IX. REQUIREMENTS FOR MARINE TANK VESSEL LOADING
A Control Requirements for Marine Tank Vessel Loading
Are all marine tank vessel loading operations that are subject to the MACT
standard in compliance with the marine tankloading NESHAP found in 40 CFR
63 Subpart Y, which requires the following;
1, For existing sources does the facility utilize controls that.
• Collect vapors discharged during loading?
Yes[ ] No[ ]
* Load only in vapor tight vessels9
Yes[ ] No[ ]
• Reduce collected HAP emissions by 97% or use vapor balancing?
Yes[ ] No[ ]
2 For new sources does the facility utilize controls'thaf
• Collect vapors discharged during loading7
Yes [J No[ ]
• Load only in vapor tight vessels?
Yes [ ] No[ ]
» Reduce collected HAP by 98% or use vapor balancing?
Yes [ ] No [ ]
B. Testing and Monitoring Requirements for Marine Tank Vessel Loading
For all marine tank vessel loading subject to the MACT Standard, does the
refinery comply with the testing and monitoring requirements of the marine tank
loading NESHAP found in 40 CFR 63.560 through 63.567-?
Note: The Initial Notification Report under 40 CFR 63.567(b) is not required.
Yes [ ] No [ 3
C, Reporting and Recordkeeping Requirements for Marine Tank Vessel
Loading
1. For all marine tank vessel loading subject to the MACT standard, does the
refinery comply with the reporting and recordkeeping requirements of the
marine tank loading NESHAP found in 40 CFR 63.566, 63.567(a) and (c)
through (I)?
Yes [ ] No[ ]
2. Does the facility retain all records required to be kept for 5 years?
Yes [ ] No[ ]
X. REQUIREMENTS FOR EQUIPMENT LEAKS
November 1, 2000
F-44
-------
Petroleum Refinery MACTStandard Guidance
A Control Requirements for Equipment Leaks
1. For equipment leaks at existing sources* does the facility comply with either
of the following equipment leaks provisions:
(a) 40 CFR 60 Subpart W (synthetic organic chemical manufacturing
industry (SOCMI) equipment leaks NSPS)? or
Yes [ ] No; j
(b) Modified 40 CFR 63 Subpart H (hazardous organic NESHAP (HON)
negotiated regulation)?
Ye? . N;' [ ]
2. For equipment leaks at new sources does the facility must comply with
modified 40 CFR 63 Subpart H?
Yes t Nc [
B. Testing, Inspection, and Monitoring Requirements for Equipment Leaks?
For all equipment leaks subject to the MACT standard, does the refinery
comply with the testing, inspection, and monitoring requirements for
equipment leaks in 40 CFR 60.1046 and 60.1047 (40 CFR 60 Subpart W), or
40 CFR 63.162 through 63.180 (40 CFR 63 Subpart H)?
Yes[ j No
C. Reporting and Recordkeeping Requirements for Equipment Leaks
For all equipment leaks subject to the MACT Standard, does the refinery
comply with the reporting and recordkeeping requirements for equipment
leaks found in 40 CFR 60.1048 and 60.1049 (40 CFR 60 Subpart W),
(except the name rather than the signature of the person deciding to delay
repair must be recorded)1, or 40 CFR 63.181 and 63.182 (40 CFR 63 Subpart
H) (except for 63.182(b), (c)(2), and (c)(4))7
Yes [ 1 Kc. „ ,
XI. EMISSIONS AVERAGING
A. Emissions Averaging Applicability
Did the facility conduct emissions averaging?
Ye^ U.
Noverrrip "
F-45
-------
Petroleum Refinery MAC!Standard Guidance
- If yes, did the facility conduct emissions averaging only for emission points at
a single refinery''
Note. Emissions averaging is not allowed across sources, such as across different
plant sites or between refinery and HON sources (i.e., units having a hazardous
organic air pollutant as its primary product) at the same plant site. In addition, an
emissions estimation is only required for points included in emissions averages, not
for all points in the source.
A limitation on the emissions averaging provision is that States have the authority to
disallow emissions averaging and require the application of standard control
requirements to all emission points.
Yes [ ] No[ ]
B. Emissions Averaging Credit/Debit System
1. Were emission credits and debits calculated on a mass basis usina
equations in 40 CFR 63.652(g) and (h) based on actual operations?
Yes [ ] No[ ]
2 Were credits calculated areater than or eaual to debits calculated on an
enni^i basi:?'? [40 CFR 63.652(e)(3)]
Yes [ ] No []
3 Did debits exceed credits by more than 30% in any one quarter? [40 CFR
652(e)(4)]
Yes [ ] No[ ]
'This requirement reflects an amendment to 40 CFR Part 63 Subpart CC made on Auc
For more information, see Appendix G.
4, Were any emission points other than the following used to generate
emissions averaging credits [40 CFR 63.652(c)(1) through (3)]:
» Group 2 emission points.
» Group 1 emission points controlled by technology with a higher nominal
efficiency than the reference control technology.
• Emission points from which emissions are reduced by pollution reduction
measures, alone or in conjunction with other controls, that get more
emission reduction than required?
just 18, 1998.
Yes[ ] No[ ]
November 1, 2000
F-46
-------
Petroleum Refinery MACTStandard Guidance
5 Did the facility use any of the following emission points to generate
emissions averaging credits [40 CFR 63.652(d)]:
• Emission points already controlled on or before.November 15, 1990,
unless the level of control was increased after November 15, 1990? {If so,
credit is allowed for the increase only.)
Yes { ] No[ ]
• Group 1 emission points that are controlled by a reference control
technology, unless the technology has been approved for use In a different
manner and a higher nominal efficiency has been assigned?
{For example, it is not allowable to claim that an internal floating roof meeting only
the specifications stated in the reference control technology definition in 40 CFR
63.641 applied to a storage vessel is achieving greater than 95 percent control.)
Ye? , No; '
• Emission points on shutdown process units?
Yes : j fw ;
* Emission points controlled to comply with a State or other Federal rule,
unless the level of control has been increased after November 15,1990
above what is required by the State or other Federal rule?
Note: If the facility used any of these emission points, credit is allowed for the
increase only.
Yes j No,
i
Note: Debits are generated if the required level of control of a Group 1 emission point, such as °:.t ' ;¦
miscellaneous process vents and 95% for storage vessels, is not achieved. [40 CFR 63.652{g (Set
Table 2.3 for required level of control.) Debits and credits are calculated using formulas fo..
Ye* , ;
• More than 20 individual emission points in addition to those controlled by
pollution prevention measures?
Yes , . ;
- Where pollution prevention measures are used, no more than 25
emission points total'? [40 CFR 63.652(f)(1)]
Yes , _ :\c . .
• Emission points during periods of startup, shutdown, and malfunction?
[40 CFR 63.652(f)(2)]
Yer. ; ;
Novembe- 21'
F-47
-------
Petroleum Refinery MACTStandard Guidance
• Emission points for which continuous monitors are used and excess
emissions occur? [40 CFR 63.652(f)(3)] (For these periods, the monthly
credits and cabits will be adjusted as specified in 40 CFR 63.652(f)(3)(l)
through (iii).)
Yes [ ] No [ ]
C. Approval of Emissions Averaging Plan
1. Did the facility submit for approval an emissions averaging plan in the
Implementation Plan or Operating Permit Application''
Yes [ ] No[ ]
2. Did the pian demonstrate that the credits will be sufficient to offset the debits
under representative operating conditions? {40 CFR 63,652(e){3)(l)J
Note: The plan may include use of innovative technologies, different from the
reference control technology, provided that the innovative technologies achieve
greater than the level of control required for a Group 1 emission point.)
Yes [ ] No [ ]
3, Did the facilitv include a risk assessment in the Dlan of anv hazards or risks
of the plan, such as the risk from one large emission point versus the risk
from combined emission points?
Yes [ ] No[ ]
- Did the facility review such hazards and risks and compare them to point-
by-point compliance?
Yes [ ] No[ ]
D. Testing, Monitoring, Reporting, and Recordkeeping for Emissions
Averaging
1. For each emission point included in an emissions averaae. did the refinerv
perform testing, monitoring, reporting, and recordkeeping equivalent to the
requirements for Group 1 emission points that are not included in emissions
averaging? [40 CFR 63.653(a)]
Yes [ ] No [ ]
2. In addition, did the facilitv maintain the monthlv calculations of debits and
credits?
Yes [ ] No[ ]
3, Does the facility maintain the following records for emissions averaging:
• Initial performance test results (if applicable)?
Yes [ ] No[ ]
¦ Monthly debits, credits, and calculations using EPA-specified calculation
procedures''
Yes [ ] No [ ]
• Operating parameter monitoring results?
Yes [ ] No [ ]
November 1, 2000
F-48
-------
Petroleum Refinery MACTStandard Guidance
Ncverroei " 200C
F-49
-------
Petroleum Refinery MACTStandard Guidance
Appendix G. Recent Changes
On August 18, 1998, EPA amended the MACT standard. A summary of the changes
made through the amendments is provided in the preamble to the amendments'
(63 FR 44135) and below.
Startup, Shutdown and Malfunction Plans for Wastewater (Section 3.3.5)
The MACT standard was revised to clarify that a Startup, Shutdown Malfunction Plan
(SSMP) is not required for wastewater stream management units (unless the owner or
operator elects to comply with 40 CFR Part 63, Subpart G.) The MACT standard
references the Benzene Waste Operations NESHAP for wastewater requirements. The
EPA did not intend to add additional requirements for wastewater beyond the Benzene
Waste Operations NESHAP.
Wastewater stream control requirements (Section 2, Table 2-3 and Section 5 Table
5-1)
Previously, wastewater stream management units that received streams subject to the
MACT standard and 40 CFR Part 63, Subpart G (the HON) were required to comply with a
combination of requirements from 40 CFR Part 61, Subpart FF (the Benzene Waste
Operations NESHAP) and Subpart G. The standard was revised to allow
owners/operators the option to comply with only the requirements of Subpart G for
wastewater stream management units that receive both streams subject to Subpart G and
the MACT standard.
Startup, Shutdown and Malfunction Reports (Section 3.3.5)
Previously, refineries were required to report an action taken that is inconsistent with the
SSMP within two days of commencing the action and within seven days of completing the
action. These requirements have been replaced with the requirement to report actions
taken that are inconsistent with the SSMP in the next periodic report.
November 1, 2000
G-1
-------
Petroleum Refinery MACTStandard Guidance
Clarification of Requirements for Installation and Calibration of Continuous
Monitoring Systems (CMS)
Previously, the MACT standard required a continuous monitoring system (CMS) to be
installed and calibrated according to manufacturer's specifications. This requirement has
been revised to allow procedures other than those specified by the manufacturer to be
followed.
Requirement to Record Signature Owner or Operator When Equipment Lea^
Repairs are Delayed (Section 4.6.3)
Previously, when an equipment leak was detected and could not be repaired wiv
15 days, the signature of the owner or operator (or designate) whose decision it was tnr.t
repair could not be affected was to be recorded. This requirement has been revise tc.
allow the name of the owner or operator (or designate) to be recorded instead
Exemption of Secondary Seal From Requirements During Primary Seal Gap
Measurements (Section 4.2.3)
The MACT standard was revised to extend the provision exempting secondary seais frcr.
seal gap requirements during primary seal gap measurements to storage vessels subject
to the Petroleum Refineries NESHAP that are to comply with Subpart Kb of 40 CFR Par
60. The EPA has determined the provision provides a necessary clarification that was not
considered in development of Subpart Kb.
Documentation of Compliance (Section 3.3.3 and 4.4.3)
Refineries with co-located gasoline loading racks that are subject to the MACT stands^
are generally required to comply with the requirements of the Gasoline Distribution MACT
(40 CFR Part 63 Subpart R), The Gasoline Distribution MACT references notifies:
requirements of the General Provisions. It was not clear when the Notification of
Compliance status was required for gasoline loading racks at petroleum refinerier Tht
requirement has been clarified to state that any notifications of compliance status requ're;
Noveioor- 1 2(-0£
G-2
-------
Petroleum Refinery MACTStandard Guidance
by the Gasoline Distribution MACT for gasoline loading racks co-located at refineries are
to be submitted within 150 days of the Petroleum Refinery NESHAP compliance date.
Revision of Notification of Compliance Status (NCS) Report Requirement for New
Group 1 Emission Point (Section 3.3.3)
Previously, facilities were required to provide a NCS report for a new Group 1 emission
point within 150 days of the change or addition of that point. The reporting requirements
are amended to allow the NCS report to be p rovided in the periodic report for the reporting
period in which the Group 1 emission point is added.
Semiannual Reporting of Inspection Results (Section 4.2.4)
For storage vessels complying with the reporting requirements of the MACT standard, if a
failure is detected during an inspection, it is required to be reported in the next periodic
report. Previously, for storage vessels complying with Subpart Kb or Subpart Ka, if a
failure is detected during an inspection, a report is to be provided to the Administrator
within 30 days or 60 days, respectively. Now, when a failure is detected during an
inspection of a storage vessel subject to the Petroleum Refineries NESHAP that is to
comply with Subpart Kb or Subpart Ka, the failure is to be reported in the next periodic
report.
Extensions for EFR Seal Gap Measurements
As discussed previously, storage vessels subject to the MACT standard and a new source
performance standard (40 CFR Part 60 Subpart K, Ka or Kb) are only required to comply
with one of the standards. Procedures are specified for external floating roof storage
vessels that must comply with the MACT standard to allow seal gap measurements to be
delayed if it is determined that it is unsafe to perform the measurement. Provisions allow
the gap measurements to be delayed for 30 days while the unsafe conditions are
corrected. If the unsafe conditions cannot be corrected within that time period, the vessel
is to be emptied within 45 days of the determination that the roof is unsafe. The owner or
operator may use up to two extensions of 30 days each to empty the tank. These
provisions have been extended to storage vessels complying with Subparts Ka and Kb.
November 1, 2000
-------
Petroleum Refinery MACTStandard Guidance
Extensions for Storage Vessel Repairs
In the MACT standard, when an internal floating roof is discovered to not meet trie
requirements of the standard, it must be repaired or the associated storage vesse! taken
out of service and emptied within 45 days. If a storage vessel cannot be emptied or
repaired within 45 days, the owner or operator may use up to two extensions of 30 days
each. If an extension is utilized, the owner or operator must, in the next periodic repot
identify the vessel, provide a description of the failure, document that alternate storage
capacity is unavailable, and specify a schedule of actions that will ensure that the centre
equipment will be repaired or the vessel will be emptied as soon as possible. Tnsf
requirement has been extended to vessels complying with Subpart Kb, which coes no-
include provisions to be followed in the event that a failure is detected during an inspects:
of a storage vessel control device and the storage vessel cannot be repaired or emptieo
within 45 days.
Definition of Gasoline (Appendix E)
A definition for gasoline was added to the definitions in the MACT standard. The definition
was taken from 40 CFR Part 60 Subpart XX Standards of Performance for Bu!>- r->a$r.i«r e
Terminals.
Report of Determination of Applicability for Flexible Operation Units and for
Distillation Columns and Storage Vessels for Which Use Varies (Section 3.3.3;
The MACT standard was revised to allow applicability determinations for flexible operation
units and distillation columns and storage vessels for which use varies to be reports r
initial Notification of Compliance Status report (rather than 18 months prior tc thf.
compliance date).
Compliance of Agitators with Equipment Leaks Provisions (Figure 2-7)
Currently, owners and operators of refineries can comply with the equipment leak:-
provisions of the MACT standard by complying with the equipment leaks prov^:-;rl ;. e'
Subpart H. Some of the referenced provisions of Subpart H refer to agitators ir, heavy
liquid service. It is possible that, due to the references to agitators in Subpart H, the MAC.T
standard could be interpreted as applying to agitators. The MACT standard was revised
Noveif-tiR' * ?00f.
G-4
-------
Petroleum Refinery MACTStandard Guidance
to specifically state that owners and operators are not required to comply with Subpart H.
for agitators in heavy liquid service.
Overlap of Subparts XX and R for Gasoline Loading Racks (Section 5)
The current MACT standard requires gasoline loading racks located at refineries to be in
compliance with the control requirements of 40 CFR Part 63 Subpart R National Emission
Standards for Gasoline Distribution Facilities. New gasoline loading racks are also
subject to 40 CFR Part 60 Subpart XX New Source Performance Stardard (NSPS) for
Bulk Gasoline Terminals. It is currently possible for a gasoline loading rack at a petroleum
refinery to be subject to both Subparts R and XX. The MACT Standard was revised to
require petroleum refineries with gasoline loading racks subject to both Subparts R and
XX to comply with the control requirements of Subpart R.
Corrections to Miscellaneous Process Vent Equations
Following promulgation of the Petroleum Refineries NESHAP, two errors were discovered
in two equations to be used to calculate kilograms per day of volatile organic compounds
(VOC) in miscellaneous process vent streams. These errors have been corrected.
Revision of Notification of Compliance Status Report Requirement for Existing
Group 1 Storage Vessels Brought Into Compliance After August 18,1998
(Sections 3.3.3 and 4.2.4)
The MACT standard allows floating roof storage vessels to be brought into compliance up
to 10 years after August 18, 1998, the compliance date for other emission points. A
Notification of Compliance Status (NCS) report is required to be submitted when these
vessels are brought into compliance. Previously, it was not clear when the NCS report is
to be submitted. The MACT standard has been revised to require a NCS report to be
submitted for storage vessels brought into compliance after August 18,1998 with the
periodic report for the reporting period in which the vessel was brought into compliance.
The report will include a list of all Group 1 storage vessels and either the actual or
anticipated date of compliance for each vessel.
November 1, 2000
G-5
-------
Petroleum Refinery MACTStandard Guidance
Appendix H. EPA Regions and Regional Contacts for the
Petroleum Refinery MACT Standard Implementation
No Petroleum Refineries in ' John York
EPA Region 1 EPA Region VK6EN-AT1
1445 Ross Avenue, Suite 700
Dallas, TX 75202-2733
PH: (214) 665-7289
FAX: (214) 665-7446
Umesh Dholakia
EPA Region II
290 Broadway
New York, NY 10007-1866
PH: (212) 637-4023/4065
FAX: (212) 637-3901/3998
Bill Peterson
EPA Region VII. ARTD/APCO
726 Minnesota Avenue •
Kansas City, KS 66101
PH: (913) 551-7881
FAX: (913) 551-7065
Patrick Foley
' Region IIU3AT12)
841 Chestnut Building
Philadelphia, PA 19107
PH: (215)814-2098
FAX: (215) 566-2114
Leonardo Ceron
EPA Region IV (AR-4)
Atlanta Federal Ctr.
61 Forsyth St.
Atlanta, GA 30303-3104
PH: (404)562-9129
FAX: (404) 562-9095
Kathy Keith
EPA Region V (AE-17J^
Tami Thomas-Burton
EPA Region VIII (8 ENF-T)
999 18th Street, Suite 500
Denver, CO 80202-2405
PH: (303)312-6581
FAX: (303) 312-6409
Cyntia Steiner
EPA Region IX(AIR-5
75 Hawthorne Street
San Francisco, CA 94105
PH: (415)744-1139
FAX: (415) 744-1076
Kai-Hon Shum
EPA Region X(QAQ-107)
November 1, 2000
H-1
-------
Petroleum Refinery MACTStandard Guidance
77 W. Jackson Blvd.
Chicago, 1L 60604
PH: (312) 353-6956
FAX: (312) 353-8289
1200 Sixth Avenue
Seattle, WA 98101
PH: (206) 553-2117
FAX: (206) 553-0110
Jim Durham
(Technical Lead)
OAQPS. MD-13
RTP, NIC 27711
PH: 919-541-5672
FAX: 919-541
Larry Brockman
(Guidance Documents)
QAQP5, md-12
RTP, NC 27711
PH: 919-541-5394
Rafael Sanchez
(Compliance Assistance)
USEPA, OECA (2223-A)
1200 Pennsylvania Avenue, NW
Washington, DC 20044
FAX: 919-541-2664
PH: 202-564-7028 -FX -00r
j
November " ?'•
1-1
-------
Petroleum Refinery MACTStandard Guidance
TECHNICAL REPORT DATA
(Please read Instructions on reverse before completing)
1. REPORT NO.
EPA-456/B-00-
001
2
3. RECIPIENT'S ACCESSION
NO.
4 TITLE AND SUBTITLE
Petroleum Refinery MACT Standard Guidance
5. REPORT DATE
November, Z000
6. PERFORMING
ORGANIZATION CODE
7 AUTHOR (Si
8. PERFORMING
ORGANIZATION REPORT NO.
9 PERFORMING ORGANIZATION NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning and Standards
Research Triangle Park, NC Z7711
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
12 SPONSORING AGENCY NAME AND ADDRESS
Director
Office of Air Quality Planning and Standards
Office of Air and Radiation
U.S. Environmental Protection Agency
Research Triangle Park, NC Z7711
13. TYPE OF REPORT AND
PERIOD COVERED
Revision/Final
14. SPONSORING AGENCY
CODE
EPA/200/04
15. SUPPLEMENTARY NOTES
November 1, 2000
I-2
-------
Petroleum Refinery MACTStandard Guidance
16 ABSTRACT
This document can help you (both the regulated community and regulators) understau;1
the requirements for the Petroleum Refinery MACT Standard by helping you determin:
the following "hings:
• if the rule applies to your plant and process
¦ what emission points are subject to the rule
¦ the control, testing, monitoring, and reporting requirements
• dates b> which you much meet requirements, contacts, how to get more
information, etc
17 KEY WORDS AND DOCUMENT ANALYSIS
a DESCRIPTORS
b. IDENTIFIERS/OPEN ENDED TERMS
C l!
SA
T!
Fir
d
C,-
Of
P
Air Pollution control
18 DISTRIBUTION STATEMENT
Release Unlimited
19. SECURITY CLASS (Report)
Unclassified
2.
(!'
P,-\
C.I
12
5
20. SECURITY CLASS (Page)
Unclassified
2:
p^
u
F
November J /CC,
1-3
-------
n<^ r 01 III 2220 1 (Rev. 4-773 PREVIOUS EDITION IS OBSOLETE
Petroleum Refinery MACTStandard Guidance
November 1, 2000
M
------- |