Expansion of RCRA Comparable Fuel Exclusion, 33284-33334 [E7-11130]
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Federal Register / Vol. 72, No. 115 / Friday, June 15, 2007 / Proposed Rules
ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Part 261
[EPA–HQ–RCRA–2005–0017; FRL–8324–2]
RIN 2050–AG24
Expansion of RCRA Comparable Fuel
Exclusion
Environmental Protection
Agency (EPA).
ACTION: Proposed rule.
AGENCY:
SUMMARY: EPA is proposing to expand
the comparable fuel exclusion under the
rules implementing subtitle C of the
Resource Conservation and Recovery
Act (RCRA) for fuels that are produced
from hazardous waste but which
generate emissions that are comparable
to emissions from burning fuel oil when
such fuels are burned in an industrial
boiler. Such excluded fuel would be
called emission-comparable fuel (ECF).
ECF would be subject to the same
specifications that currently apply to
comparable fuels, except that the
specifications for certain hydrocarbons
and oxygenates would not apply. The
ECF exclusion would be conditioned on
requirements including: Design and
operating conditions for the ECF boiler
to ensure that the ECF is burned under
the good combustion conditions typical
for oil-fired industrial boilers; and
conditions for tanks storing ECF which
conditions are typical of those for
storage of commercial fuels, and are
tailored for the hazards that ECF may
pose.
Comments must be received on
or before August 14, 2007. Under the
Paperwork Reduction Act, comments on
the information collection provisions
must be received by OMB on or before
July 16, 2007.
ADDRESSES: Submit your comments,
identified by Docket ID No. EPA–HQ–
RCRA–2005–0017, by one of the
following methods:
• https://www.regulations.gov: Follow
the on-line instructions for submitting
comments.
• E-mail: rcra-docket@epa.gov.
• Fax: 202–566–9744.
• Mail: RCRA Docket, Environmental
Protection Agency, Mailcode: 2822T,
1200 Pennsylvania Ave., NW.,
Washington, DC 20460. Please include a
total of two copies. We request that you
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DATES:
also send a separate copy of your
comments to the contact person listed
below (see FOR FURTHER INFORMATION
CONTACT). In addition, please mail a
copy of your comments on the
information collection provisions to the
Office of Information and Regulatory
Affairs, Office of Management and
Budget (OMB), Attn: Desk Officer for
EPA, 725 17th St., NW., Washington, DC
20503.
• Hand Delivery: RCRA Docket, EPA
Docket Center (2822T), EPA West, Room
3334, 1301 Constitution Ave., NW.,
Washington, DC. Such deliveries are
only accepted during the Docket’s
normal hours of operation, and special
arrangements should be made for
deliveries of boxed information. Please
include a total of two copies. We request
that you also send a separate copy of
each comment to the contact person
listed below (see FOR FURTHER
INFORMATION CONTACT).
Instructions: Direct your comments to
Docket ID No. EPA–HQ–RCRA–2005–
0017. EPA’s policy is that all comments
received will be included in the public
docket without change and may be
made available online at https://
www.regulations.gov, including any
personal information provided, unless
the comments include information
claimed to be Confidential Business
Information (CBI) or other information
the disclosure of which is restricted by
statute. Do not submit information that
you consider to be CBI or otherwise
protected through https://
www.regulations.gov or e-mail. Send or
deliver information identified as CBI to
the following address: Ms. LaShan
Haynes, RCRA Document Control
Officer, EPA (Mail Code 5305P),
Attention Docket ID No. EPA–HQ–
RCRA–2005–0017, 1200 Pennsylvania
Avenue, NW., Washington, DC 20460.
Clearly mark the part or all of the
information that you claim to be CBI.
The https://www.regulations.gov Web
site is an ‘‘anonymous access’’ system,
which means EPA will not know your
identity or contact information unless
you provide it in the body of your
comment. If you send an e-mail
comment directly to EPA without going
through https://www.regulations.gov,
your e-mail address will be
automatically captured and included as
part of the comment that is placed in the
public docket and made available on the
Internet. If you submit an electronic
Category
NAICS code
Any industry that generates or combusts hazardous waste as
defined in the proposed rule.
comment, EPA recommends that you
include your name and other contact
information in the body of your
comment and with any disk or CD–ROM
you submit. If EPA cannot read your
comment due to technical difficulties
and cannot contact you for clarification,
EPA may not be able to consider your
comment. Electronic files should avoid
the use of special characters, any form
of encryption, and be free of any defects
or viruses. For additional information
about EPA’s public docket, visit the EPA
Docket Center homepage at https://
www.epa.gov/epahome/dockets.htm.
We also request that interested parties
who would like information they
previously submitted to EPA to be
considered as part of this action identify
the relevant information by docket entry
numbers and page numbers.
Docket: All documents in the docket
are listed in the https://
www.regulations.gov index. Although
listed in the index, some information is
not publicly available, e.g., CBI or other
information whose disclosure is
restricted by statute. Certain other
material, such as copyrighted material,
will be publicly available only in hard
copy. Publicly available docket
materials are available either
electronically in https://
www.regulations.gov or in hard copy at
the RCRA Docket, EPA/DC, EPA West,
Room 3334, 1301 Constitution Ave.,
NW., Washington, DC. The Public
Reading Room is open from 8:30 a.m. to
4:30 p.m., Monday through Friday,
excluding legal holidays. The telephone
number for the Public Reading Room is
(202) 566–1744, and the telephone
number for the RCRA Docket is (202)
566–0270.
FOR FURTHER INFORMATION CONTACT:
Mary Jackson, Hazardous Waste
Minimization and Management
Division, Office of Solid Waste,
Mailcode: 5302P, Environmental
Protection Agency, 1200 Pennsylvania
Ave., NW., Washington, DC 20460;
telephone number: (703) 308–8453; fax
number: (703) 308–8433; e-mail address:
jackson.mary@epa.gov.
SUPPLEMENTARY INFORMATION:
General Information
A. Does This Action Apply to Me?
Categories and entities potentially
affected by this action include:
SIC code
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327
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Examples of potentially regulated entities
Waste Management and Remediation
Services.
Non-metallic Mineral Products Manufacturing.
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Category
NAICS code
SIC code
325
324
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333
326
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89
95
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1. Submitting CBI. Do not submit this
information to EPA through https://
www.regulations.gov or e-mail. Clearly
mark the part or all of the information
that you claim to be CBI. For CBI
information in a disk or CD ROM that
you mail to EPA, mark the outside of the
disk or CD ROM as CBI and then
identify electronically within the disk or
CD ROM the specific information that is
claimed as CBI. In addition to one
complete version of the comment that
includes information claimed as CBI, a
copy of the comment that does not
contain the information claimed as CBI
must be submitted for inclusion in the
public docket. Information so marked
will not be disclosed except in
accordance with procedures set forth in
40 CFR part 2.
2. Tips for Preparing Your Comments.
When submitting comments, remember
to:
• Identify the rulemaking by docket
number and other identifying
information (subject heading, Federal
Register date and page number).
49
50
51
512, 541, 812
512, 514, 541, 711
924
336
928
334
B. What Should I Consider as I Prepare
My Comments for EPA?
33
38
306
488, 561
421
422
This table is not intended to be
exhaustive, but rather provides a guide
for readers regarding entities likely to be
impacted by this action. This table lists
examples of the types of entities EPA is
now aware could potentially be
regulated by this action. Other types of
entities not listed could also be affected.
To determine whether your facility,
company, business, organization, etc., is
affected by this action, you should
examine the applicability criteria in this
proposed rule. If you have any questions
regarding the applicability of this action
to a particular entity, consult the person
listed in the preceding FOR FURTHER
INFORMATION CONTACT section.
28
29
38
• Follow directions—The agency may
ask you to respond to specific questions
or organize comments by referencing a
Code of Federal Regulations (CFR) part
or section number.
• Explain why you agree or disagree;
suggest alternatives and substitute
language for your requested changes.
• Describe any assumptions and
provide any technical information and/
or data that you used.
• If you estimate potential costs or
burdens, explain how you arrived at
your estimate in sufficient detail to
allow for it to be reproduced.
• Provide specific examples to
illustrate your concerns, and suggest
alternatives.
• Explain your views as clearly as
possible, avoiding the use of profanity
or personal threats.
• Make sure to submit your
comments by the comment period
deadline identified.
3. Docket Copying Costs:
You may copy a maximum of 100
pages from any regulatory docket at no
charge. Additional copies are 15 cents/
page.
4. How Do I Obtain a Copy of This
Document and Other Related
Information?
In addition to being available in the
docket, an electronic copy of today’s
proposed rule will also be available on
the Worldwide Web (WWW). Following
the Administrator’s signature, a copy of
this document will be posted on the
WWW at https://www.epa.gov/hwcmact.
This Web site also provides other
information related to the NESHAP for
hazardous waste combustors.
5. Index of Contents
The information presented in this
preamble is organized as follows:
Part One: Background and Summary
I. Statutory Authority
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Examples of potentially regulated entities
Chemical Manufacturing.
Petroleum and Coal Products Manufacturing.
Primary Metals Manufacturing.
Machinery Manufacturing.
Plastic and Rubber Products Manufacturing.
Administration and Support Services.
Scrap and waste materials.
Wholesale Trade, Non-durable Goods,
N.E.C.
Business Services, N.E.C.
Services, N.E.C.
Air, Water and Solid Waste Management.
Transportation Equipment Manufacturing.
National Security.
Computer and Electronic Products Manufacturing.
Miscellaneous Manufacturing.
II. Background
A. What Is the Intent of This Proposed
Rule?
B. Who Would Be Affected by This
Proposed Rule?
C. What Is the Relationship Between the
Proposed Rule and the Existing
Exclusion for Comparable Fuel?
1. What Modifications to the Comparable
Fuel Exclusion May Be Warranted?
2. How Has EPA Involved Stakeholders in
Discussions Regarding Potential
Revisions to the Comparable Fuel
Exclusion?
III. Summary of the Proposed Rule
A. What Are the Conditions for Exclusion
of Emission-Comparable Fuel (ECF)?
B. What Changes Is EPA Proposing to the
Conditions for Existing Comparable
Fuel?
Part Two: Rationale for the Proposed Rule
I. What Is the Rationale for Excluding
Emission-Comparable Fuel From the
Definition of Solid Waste?
A. Why Would the Specifications Be
Waived Only for Hydrocarbons and
Oxygenates?
B. Do Available Data and Information
Support a Comparable Emissions
Finding?
1. Evaluation of Organic Emissions Data for
Hazardous Waste Boilers
2. Evaluation of RCRA Risk Assessments
3. Comparative Risk Assessment for
Dioxin/Furan
II. What Conditions Would Apply to
Burners of Emission-Comparable Fuel?
A. Why Isn’t a DRE Performance Test a
Critical Requirement To Ensure Good
Combustion Conditions?
B. What Is the Rationale for the Proposed
Burner Conditions?
1. ECF Must Be Burned in a Watertube
Steam Industrial or Utility Boiler That Is
Not Stoker-Fired
2. CO Monitoring
3. The Boiler Must Fire at Least 50%
Primary Fuel
4. The Boiler Load Must Be 40% or Greater
5. The ECF Must Have an As-Fired Heating
Value of 8,000 Btu/lb or Greater
6. ECF Must Be Fired Into the Primary Fuel
Flame Zone
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7. The ECF Firing System Must Provide
Proper Atomization
8. Dioxin/Furan Controls for Boilers
Equipped With an ESP or FF
III. What Restrictions Would Apply to
Particular Hydrocarbons and
Oxygenates?
A. What Is the Rationale for the Relative
Hazard Characterization Scheme?
B. What Are the Results of the Relative
Hazard Ranking?
C. What Firing Rate Restrictions Would
Apply to Benzene and Acrolein?
IV. What Conditions Would Apply to
Storage of ECF?
A. What Are the Proposed Storage
Conditions?
1. Tank Systems, Tank Cars and Tank
Trucks
2. Underground Storage Tank Systems
3. Closure of Tank Systems
4. Waiver of RCRA Closure for RCRA
Tanks That Become ECF Tanks
5. Management of Incompatible Waste
Fuels and Other Materials
B. What Other Options Did We Consider?
1. Other Options We Considered to
Establish Storage Conditions for ECF
2. Consideration of Storage Controls for
Currently Excluded Comparable Fuels
V. How Would We Assure That The
Conditions Are Being Satisfied?
A. What Recordkeeping, Notification and
Certificate Conditions Would Apply to
Generators and Burners?
1. Waste Analysis Plans
2. Sampling and Analysis
3. Speculative Accumulation
4. Notifications
5. Burner Certification
6. Recordkeeping
7. Transportation
8. Ineligible RCRA Hazardous Waste Codes
B. What If I Fail To Comply With
Conditions of the Exclusion?
C. How Would Spills and Leaks Be
Managed?
D. What Would Be the Time-Line for
Meeting the Proposed Conditions?
VI. What Clarifications and Revisions Are
Proposed for the Existing Conditions for
Exclusion of Comparable Fuel?
VII. What Are the Responses to Major
Comments of the Peer Review Panel?
A. What Are the Reponses to Major
Comments Regarding the Comparable
Emissions Rationale?
B. What Are the Reponses to Major
Comments Regarding the Application of
the WMPT To Rank Comparable Fuel
Constituents?
Part Three: State Authority
I. Applicability of the Rule in Authorized
States
II. Effect on State Authorization
Part Four: Costs and Benefits of the Proposed
Rule
I. Introduction
II. Baseline Specification
III. Analytical Methodology, Primary Data
Sources, and Key Assumptions
IV. Key Analytical Limitations
V. Findings
Part Five: Statutory and Executive Order
Reviews
I. Executive Order 12866: Regulatory
Planning and Review
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II. Paperwork Reduction Act
III. Regulatory Flexibility Act
IV. Unfunded Mandates Reform Act of
1995
V. Executive Order 13132: Federalism
VI. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
VII. EO 13045 ‘‘Protection of Children
From Environmental Health Risks and
Safety Risks’’
VIII. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
IX. National Technology Transfer
Advancement Act
X. Executive Order 12898: Federal Actions
To Address Environmental Justice in
Minority Populations and Low-Income
Populations
Part One: Background and Summary
I. Statutory Authority
These regulations are proposed under
the authority of sections 2002, 3001,
3002, 3003, and 3004 of the Solid Waste
Disposal Act of 1970, as amended by the
Resource Conservation and Recovery
Act of 1976 (RCRA), as amended by the
Hazardous and Solid Waste
Amendments of 1984 (HSWA), 42
U.S.C. 6921, 6922, 6923, and 6924.
II. Background
A. What Is the Intent of This Proposed
Rule?
Section 40 CFR 261.38 states that
secondary materials (i.e., materials that
otherwise would be hazardous wastes)
which have fuel value and whose
hazardous constituent levels are
comparable to those found in the fossil
fuels which would be burned in their
place are not solid wastes, and hence
not hazardous wastes. We are proposing
to amend the comparable fuel exclusion
by expanding the exclusion to include
fuels that are produced from a
hazardous waste but which generate
emissions when burned in an industrial
boiler that are comparable to emissions
from burning fuel oil. In other words,
the fuels would be comparable from an
emissions standpoint but not a physical
standpoint. The revised rule would
establish a new category of excluded
waste-derived fuel called emissioncomparable fuel (ECF).
The quantity of waste fuels excluded
under this approach would increase
substantially the amount of hazardous
waste fuels that would eligible for
exclusion from the RCRA hazardous
waste regulations. Specifically, we
estimate that approximately 13,000 tons
per year of waste fuels are currently
excluded under the existing comparable
fuel exclusion, while we project that up
to an additional 107,000 tons per year
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may be excluded under the exclusion
being proposed today.
These additional hazardous secondary
materials could be burned for energy
recovery without imposing unnecessary
regulatory costs on generators, primarily
the manufacturing sector. However, the
expanded comparable fuel exclusion
may not substantially increase the
amount of hazardous waste burned for
energy recovery because high Btu
wastes, even though not currently
excluded from RCRA, are currently
burned in industrial furnaces and
incinerators for their fuel value.
Nonetheless, continuing to regulate
these waste-derived fuels as hazardous
wastes would treat a potentially
valuable fuel commodity (especially
considering the increasing value of
fuels) as a waste without a compelling
basis.
B. Who Would Be Affected by This
Proposed Rule?
Entities that generate, burn, and store
ECF are potentially affected by this
proposal. The basic structure of the
proposal is that ECF is no longer a solid
(and hazardous) waste, and hence that
each of these entities would not be
subject to subtitle C regulation when
managing ECF. Thus, generators of
hazardous waste fuels that meet the
conditions of the ECF exclusion could
manage these fuels without being
subject to subtitle C regulation assuming
that the management conditions are
satisfied. Burners, which are limited to
certain industrial boilers (including
utility boilers), could burn ECF
provided the boilers meet the design
and operating conditions in the
proposed rule, as discussed in Part II,
Section II. Generators would benefit
from lower operating costs because of
lower (or eliminated) waste
management fees and because these
fuels would substitute for fuels which
would otherwise be purchased. In
addition, entities storing ECF would not
be subject to subtitle C standards
provided they satisfy the management
conditions tailored to ECF, as discussed
in Part Two, Section IV.
Commercial hazardous waste
combustors that are currently managing
waste fuels that qualify as ECF, on the
other hand, might find themselves
unable to continue to charge hazardous
waste management fees for the excluded
waste fuels. Consequently, commercial
hazardous waste combustors might lose
the waste management revenues for
those diverted fuels and may need to
meet their heat input requirements by
using other waste fuels or fossil fuels.
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C. What Is the Relationship Between the
Proposed Rule and the Existing
Exclusion for Comparable Fuel?
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On June 19, 1998 (63 FR 33782 and
§ 261.38), EPA promulgated standards to
exclude from the regulatory definition
of solid waste certain hazardous wastederived fuels that meet specification
levels for hazardous constituents and
physical properties that affect burning
which are comparable to the same levels
in fossil fuels. EPA’s goal was to
develop a comparable fuel specification
which is useable by the regulated
community, but assures that an
excluded waste-derived fuel is similar
in composition to commercially
available fuel and therefore poses no
greater risk than burning fossil fuel.
During the eight years that the
comparable fuel exclusion has been part
of the hazardous waste regulations,
several stakeholders have pointed out
that many hazardous wastes with fuel
value do not satisfy the terms of the
exclusion. Independently, in 2003, EPA
began examining the effectiveness of the
current comparable fuel program as part
of an effort to promote the energy
conservation component of the Resource
Conservation Challenge 1 to determine
whether other hazardous wastes could
be appropriately excluded as
comparable fuel.
As part of this effort, we contacted the
American Chemistry Council (ACC) in
early 2003 to determine how much
waste is currently excluded as
comparable fuel and whether there were
additional quantities of other high Btu
wastes that could potentially be
considered comparable fuel. ACC
conducted a survey of its members and
provided results to EPA in late 2003
indicating that approximately 13,000
tons per year of waste fuels are currently
excluded, but that approximately
190,000 tons per year of additional
waste fuels could potentially be
excluded under revisions to the
exclusion.2
Therefore, ACC recommended that
EPA consider approaches to address the
following barriers perceived as
excluding additional quantities of waste
fuels:
• Analytic Issues: High analysis cost
and matrix interferences hamper
meeting the detection limit
requirements for nondetected analytes
in many waste fuel matrices.
1 See https://www.epa.gov/epaoswer/osw/
conserve/strat-plan/strat-plan.htm#rccplan.
2 Letter from American Chemistry Council (Carter
Lee Kelly, Leader, Waste Issues Team, and Robert
A. Elam, Director, Regulatory Affairs, Waste Issues
Team) to Robert Springer and Matt Hale, USEPA,
dated November 24, 2003.
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• Over-Rigid Specifications: Wastes
containing nonhalogenated organics and
oxygenates do not result in emissions
greater than burning waste fuel meeting
the specification if the combustor
operates under good combustion
conditions.
• Blending: The current exclusion
bans blending to meet hazard
constituent specifications. Flexibility is
needed on blending of streams
containing low levels of constituents,
such as chromium and manganese
attributable to corrosion from stainless
steel vessels and pipes.
1. What Modifications to the
Comparable Fuel Exclusion May Be
Warranted?
We are proposing in this action to
expand the exclusion for comparable
fuel to establish a new category of
excluded fuel—emission-comparable
fuel (ECF). This proposal would exclude
waste fuels that generate emissions,
when burned in an industrial boiler,
which are comparable to emissions from
burning fuel oil. ECF would be subject
to the same hazardous constituent and
other specifications in Table 1 to
§ 261.38 that currently apply to
comparable fuels, except that the
specifications for certain hydrocarbons
and oxygenates would not apply. The
exclusion would be based on the
rationale that ECF has substantial fuel
value, that the hydrocarbon and
oxygenate constituents no longer subject
to a specification add fuel value, and
that emissions from burning ECF in an
industrial boiler operating under good
combustion conditions are likely not to
differ from emissions from burning
fossil fuels under those same
conditions. As a result, the current
specifications limiting the hydrocarbons
and oxygenates appear to be
unnecessary.
The exclusion would be conditioned
on the ECF being burned and stored
under certain conditions, including: (1)
Design and operating conditions for the
ECF boiler that ensure that the ECF is
burned under the good combustion
conditions typical for oil-fired industrial
boilers; and (2) conditions for storage in
tanks which are comparable to those for
storage of fuels and organic liquids and
which are tailored for the hazards that
ECF may pose given that ECF can have
higher concentrations of certain
hydrocarbons and oxygenates than fuel
oil and gasoline.
We are not proposing revisions to the
comparable fuel exclusion to address
the analytical and blending
recommendations raised by ACC.
a. Why Are We Not Proposing
Revisions To Address Analytic
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Concerns? The specifications in Table 1
to § 261.38 for volatile organic
compounds that were not detected in
fuel oil or gasoline were based on the
low levels of detection achievable for
fuel oil rather than the much higher
levels of detection achievable for
gasoline. Given that only benzene,
toluene, and naphthalene were detected,
EPA used this approach for most of the
volatile organic compounds. EPA
acknowledged this deviation from
establishing the specification for
nondetected compounds as the highest
level of detection in a benchmark fuel
and explained that the levels of
detection for volatile compounds in
gasoline were inflated because of matrix
effects. ACC suggested that EPA
consider the fact that many waste fuels
may pose the same matrix effects as
gasoline, such that the fuel oil-based
specifications would not be reasonably
achievable.
We believe that it would not be
appropriate to consider increasing the
specifications for all volatile organic
compounds and base them on the higher
levels of detection in gasoline rather
than fuel oil levels of detection because
most of the compounds would simply
not be expected to be found in fuel oil
or gasoline. Rather, only certain
hydrocarbons would be expected to be
in these fuels. We could potentially also
consider oxygenates, however, because
they are within a class of compounds
that are added to fuels to enhance
combustion. It appeared, however, that
this revision would not likely result in
additional hazardous waste fuel being
conditionally excluded. There were very
few, if any, waste fuels that meet the
specifications for all volatile
compounds, except for the enumerated
hydrocarbons and oxygenates, and that
also could meet revised, higher
specifications for the hydrocarbons and
oxygenates based on the levels of
detection in gasoline. Consequently, we
are not pursuing this approach further
but, nonetheless, solicit comment on
such an approach.
b. Why Are We Not Proposing
Revisions To Address Blending
Concerns? A condition of the existing
comparable fuel exclusion is that
blending to meet the specification
(except for viscosity) is prohibited to
preclude dilution to avoid treatment.3
ACC noted that waste fuels often
contain incidental contamination of
metals, such as chromium and
manganese from corrosion of stainless
steel vessels and pipes, and that
blending to meet the specifications for
3 See
63 FR at 33795, and existing § 261.38(c)(3–
4).
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low levels of metals appears reasonable.
We believe that blending to meet the
specifications for metals is explicitly
prohibited because it would be
inconsistent with the section 3004(m)
hazardous waste treatment provisions
(which, although not directly
applicable, articulate important overall
statutory objectives) which require
hazardous constituents to be removed or
destroyed by treatment, not diluted. See
63 FR at 33795.
We believe, however, that blending to
meet the specification for organic
compounds that may be present in fuel
oil or gasoline—hydrocarbons—or that
are within a class of compounds that are
added to fuels to enhance combustion—
oxygenates—could be considered. These
compounds would not be diluted to
avoid treatment; they would still be
treated by combustion. However, it
appears that there were very few, if any,
additional waste fuels that would be
excluded under such a blending
provision. Nonetheless, we solicit
comment on such an approach and its
applicability to additional waste fuels.
2. How Has EPA Involved Stakeholders
in Discussions Regarding Potential
Revisions to the Comparable Fuel
Exclusion?
On December 15, 2005, EPA convened
a public meeting of stakeholders to
discuss potential revisions to the
comparable fuel exclusion under 40
CFR 261.38.4 Meeting notes are
available in the docket for this
rulemaking.5 Participants in the
stakeholder meeting raised several
issues during the meeting and our
responses are included in the meeting
notes. In addition, several participants
submitted written comments after the
meeting. These comments and our
responses are available in the docket to
today’s proposal.6
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III. Summary of the Proposed Rule
Today’s proposed rule would expand
the comparable fuel exclusion by
conditionally waiving the specifications
for certain hydrocarbons and oxygenates
4 See e-mail from Jim Berlow, USEPA, to Jim Pew,
Earthjustice; Melvin Keener, Coalition for
Responsible Waste Incineration; David Case,
Environmental Technology Council; Michael
Benoit, Cement Kiln Recycling Coalition; Barbara
Simcoe, Association of State and Territorial Solid
Waste Management Officials; and Robert Elam,
American Chemistry Council, dated November 23,
2005.
5 See memorandum from Bob Holloway, USEPA,
to Docket Number RCRA 2005–0017, entitled
‘‘Meeting Notes—Comparable Fuel Stakeholder
Meeting on Dec. 15, 2005,’’ dated January 4, 2006.
6 USEPA, ‘‘Response to Comments on the
December 15, 2005 Stakeholder Meeting Regarding
Expanding the Comparable Fuel Exclusion,’’ May
2007.
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listed in Table 1 to § 261.38. This
excluded waste fuel would be called
emission-comparable fuel. We are also
proposing to clarify the regulatory status
of existing comparable fuel that no
longer meets the conditions of the
exclusion.
A. What Are the Conditions for
Exclusion of Emission-Comparable Fuel
(ECF)?
ECF is a fuel derived from hazardous
waste but which would be excluded
from the RCRA hazardous waste
regulations if it meets prescribed
specifications and management
conditions. The ECF specifications
would be the same as those that are
applicable to comparable fuel, except
the specifications for particular
hydrocarbons and oxygenates would not
apply. See proposed § 261.38(a)(2). The
exclusion would apply from the point
that ECF meets the specifications.
Special conditions of the exclusion
specific to ECF would include the
following design and operating
conditions for the ECF burner: (1) The
burner must be a watertube steam boiler
other than a stoker-fired boiler; (2)
carbon monoxide (CO) must be
monitored continuously, must be linked
to an automatic ECF feed cutoff system,
and must not exceed 100 ppmv on an
hourly rolling average (corrected to 7%
oxygen); (3) the boiler must fire at least
50% primary fuel on a heating value or
volume basis, whichever results in a
higher volume of primary fuel, and the
primary fuel must be fossil fuel or tall
oil with a heating value not less than
8,000 Btu/lb; (4) the boiler load must be
40% or greater; (5) the ECF must have
an as-fired heating value of 8,000 Btu/
lb or greater; (6) ECF must be fired into
the primary fuel flame zone; (7) the ECF
firing system must provide proper
atomization; and (8) if the boiler is
equipped with an electrostatic
precipitator (ESP) or fabric filter (FF)
and does not fire coal as the primary
fuel, the combustion gas temperature at
the inlet to the ESP or FF must be
continuously monitored, must be linked
to the automatic ECF feed cutoff system,
and must not exceed 400 °F on an
hourly rolling average. See proposed
§ 261.38(c)(2). (Please note that we
specifically request comment on these
proposed conditions, as discussed later.)
The principal conditions that would
apply to ECF boilers—waterwall steam
boiler, low CO, burning high Btu
primary fuel that is properly atomized,
operating at boiler loads above 40%—
reflect design and operating conditions
typical for oil-fired industrial boilers
that operate under good combustion
conditions.
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In addition, ECF must be stored in
tanks, tank cars, or tank trucks. See
proposed § 261.38(c)(1). These tank
systems, tank cars, and tank trucks
would be excluded from regulation if
they meet conditions similar to those
which apply to fuel oil (the product
most analogous to ECF), along with
additional conditions necessary to
minimize the potential for releases to
the environment accounting for the
differences between ECF and fuel oil.
These include: (1) Certain provisions of
the Spill Prevention, Control, and
Countermeasures (SPCC) requirements
applicable to oil under §§ 112.2, 112.5,
112.7, and 112.8; (2) secondary
containment and leak detection
requirements for tank systems,
including use of liners, vaults, or
double-walled tanks; (3) preparedness
and prevention, emergency procedures,
and response to release provisions
adopted from requirements applicable
to tank systems that store hazardous
waste, and (4) fugitive air emission
technical controls adopted from Subpart
EEEE, Part 63, for organic liquids
distribution (which would apply not
only to any hazardous air pollutants
among the oxygenates and
hydrocarbons, but also would apply to
the 11 oxygenates for which there
would be no specification in this
proposed rule and which are hazardous
constituents under RCRA having
significant vapor pressure but which are
not hazardous air pollutants under the
CAA). Underground tanks storing ECF
are subject to the applicable
requirements of 40 CFR Part 280. A
further condition of the exclusion is that
the generator must document in the
waste analysis plan how precautions
will be taken to prevent mixing of ECF
and other materials which could result
in adverse consequences from
incompatible materials. In addition, to
be excluded, ECF would need to meet
all of the conditions applicable to
existing comparable fuel, including: (1)
The specifications under Table 1 to
261.38, except for the specifications for
certain hydrocarbons and oxygenates;
(2) prohibition on blending to meet the
specifications, except for viscosity; 7 (3)
notifications to state RCRA and Clean
Air Act (CAA) Directors and public
notification; (4) waste analysis plans; (5)
sampling and analysis conditions; (6)
prohibition on speculative
accumulation; (7) recordkeeping; (8)
7 ECF must have a heating value of 5,000 Btu/lb
or greater as-generated (or after bona fide
treatment), but must have a heating value of 8,000
Btu/lb, as fired. Thus, ECF with an as-generated
heating value below 8,000 Btu/lb may be blended
with other fuels to achieve a heating value of 8,000
Btu/lb.
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burner certification to the generator; and
(9) ineligible waste codes.
ECF that has lost its exclusion
because of failure to satisfy a condition
of the exclusion must be managed as a
hazardous waste from the point of ECF
generation.8 In addition, ECF that is
spilled or leaked and cannot be burned
under the conditions of the exclusion is
a waste (it is a hazardous waste if it
exhibits a characteristic of hazardous
waste or if the ECF were derived from
a listed hazardous waste) and must be
managed in accordance with existing
federal and state regulations.
Furthermore, if an ECF tank system
ceases to be operated to store ECF
product, but has not been cleaned by
removing all liquids and accumulated
solids within 90 days of cessation of
ECF storage operations, the tank system
would become subject to the RCRA
subtitle C hazardous waste regulations.9
(This is the same principle that applies
to any product storage unit when it goes
out of service. See § 261.4(c).) Liquids
and accumulated solids removed from a
tank system that ceases to be operated
for storage of ECF product are waste
(they are hazardous wastes if they
exhibit a characteristic of hazardous
waste or if the ECF were derived from
a listed hazardous waste).
rwilkins on PROD1PC63 with PROPOSALS2
B. What Changes Is EPA Proposing to
the Conditions for Existing Comparable
Fuel?
The proposed rule would restructure
the current conditions for comparable
fuel (and syngas fuel) to make the
regulatory language more readable given
that the regulation must accommodate
the proposed exclusion for ECF.
Consequently, we are redrafting the
entire section for clarity. In addition, we
are making technical corrections to
several provisions of the rule.10 We
regard these language changes as purely
technical, and thus will accept comment
only on whether the suggested language
change expresses the current meaning of
8 Please note that we request comment on
whether the final rule should include a ‘‘reasonable
efforts’’ provision that would provide that the
failure of an off-site, unaffiliated burner to meet the
proposed conditions or restrictions of the exclusion
would not mean the material was considered waste
when handled by the generator, as long as the
generator can adequately demonstrate that he has
made reasonable efforts to ensure that the material
will be managed by the burner under the conditions
of the exclusion. See discussion in Part Two,
Section V.B of the preamble.
9 If the tank is used to actively accumulate
hazardous waste after being taken out of service as
an ECF product tank, the tank may be eligible for
the provisions under § 262.34 that waive the permit
requirements for generator tanks that accumulate
hazardous waste for not more than 90 days.
10 See memorandum from Bob Holloway, USEPA,
to Docket ID No. EPA–HQ–RCRA–2005–0017, dated
January 10, 2007.
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the provision. We are not reexamining,
reconsidering, or otherwise reopening
these provisions for comment.
We are, however, proposing to amend
several provisions that apply to
comparable fuel for the same reasons
that we are proposing to apply the
amended provisions to ECF. We
specifically request comment on
whether these clarifications and
conforming amendments are
appropriate:
• We are proposing to clarify the
consequences of failure to satisfy the
conditions of the existing comparable
fuel exclusion. The material must be
managed as hazardous waste from the
point of generation. In addition, we are
proposing to clarify that excluded fuel
that is spilled or leaked and that no
longer meets the conditions of the
exclusion must be managed as a
hazardous waste if it exhibits a
characteristic of hazardous waste or if it
was derived from a listed hazardous
waste when the exclusion was claimed.
See proposed § 261.38(d).
• We are proposing to clarify the
status of tanks that cease to be operated
as comparable fuel storage tanks. The
tank system becomes subject to the
RCRA hazardous waste facility
standards if not cleaned of liquids and
accumulated solids within 90 days of
ceasing operations as a comparable fuel
tank. In addition, we are proposing to
clarify that liquids and accumulated
solids removed from the tank after the
tank ceases to be operated as a
comparable fuel product tank must be
managed as hazardous waste if they
exhibit a characteristic of hazardous
waste or if they were derived from a
listed hazardous waste when the
exclusion was claimed. See proposed
§ 261.38(b)(13).
• We are proposing to waive the
RCRA closure requirements for tank
systems that are used only to store
hazardous wastes that are subsequently
excluded as comparable fuel. See
proposed § 261.38(b)(14).
• We are proposing to clarify the
regulatory status of boiler residues,
including bottom ash and emission
control residue. Burning excluded fuel
that was derived from a listed hazardous
waste does not subject boiler residues to
regulation as derived-from hazardous
waste. See § 261.38(b)(12).
• We are proposing that the one-time
notice by the generator to regulatory
officials include an estimate of the
average and maximum monthly and
annual quantity of waste for which an
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33289
exclusion would be claimed.11 See
proposed § 261.38(b)(2)(i)(D).
Part Two: Rationale for the Proposed
Rule
I. What Is the Rationale for Excluding
Emission-Comparable Fuel From the
Definition of Solid Waste?
Emission-comparable fuel (ECF) is a
fuel derived from hazardous waste, but
which would be excluded from RCRA
hazardous waste regulation if it meets
prescribed specifications and
management conditions. The ECF
specifications would be the same as
those that currently apply to existing
comparable fuel, except the
specifications for particular
hydrocarbons and oxygenates would not
apply. See proposed § 261.38(a)(2).12
The exclusion would be based on the
rationale that ECF has fuel value, that
the hydrocarbon and oxygenate
constituents no longer subject to a
specification themselves have fuel
value, and that emissions from burning
ECF in an industrial boiler operating
under good combustion conditions are
likely not to differ from emissions from
burning fossil fuels under those same
conditions. Emissions from burning ECF
in an industrial boiler operating under
good combustion conditions would be
comparable to emissions from burning
fuel oil in an industrial boiler operating
under the same good combustion
conditions because operating a boiler
under good combustion conditions,
evidenced by carbon monoxide (CO)
emissions below 100 ppmv (on an
hourly rolling average), assures the
destruction of organic compounds
generally to trace levels, irrespective of
the type or concentration of the organic
compound in the feed.13 As
11 Providing an estimate of excluded quantities
would help regulatory officials establish inspection
and monitoring priorities. This requirement was an
oversight when the exclusion was initially
promulgated. We required the burner to issue a
public notice that included this information (see
existing § 261.38(c)(1)(ii)(D)), but we inadvertently
did not require the generator who claims the
exclusion to provide this information in his notice
to regulatory officials.
12 Table 1 to § 261.38 provides specifications for
37 hydrocarbons and oxygenates. For ECF, the
specifications would not apply for those
compounds, except for PAHs and naphthalene, as
discussed in Part Two, Section III, of the text. In
addition, there would be firing rate restrictions for
ECF that contained more than 2% benzene or
acrolein.
13 This assumes that fuels are fired into the flame
zone, thus avoiding total ignition failure. If a waste
fuel were inadvertently fired out of the flame zone,
the fuel may not even partially combust. If this were
to happen, CO levels could be low even though
organic emissions could be high. ECF boilers would
be required to fire ECF into the primary fuel flame
zone. Also see USEPA, ‘‘Draft Technical Support
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hydrocarbons are oxidized during
combustion, eventually (ideally) to
carbon dioxide and water, CO is formed
just prior to complete oxidation to
carbon dioxide. Because CO is difficult
to oxidize, it is the rate-limiting step in
the oxidation process. Thus, low CO
levels indicate good combustion and
low levels of organic compounds.
EPA has discretion to classify such
material as a fuel product, and not as a
waste. See generally Safe Foods and
Fertilizer v. EPA, 350 F. 3d 1263, 1269–
71 (D.C. Cir. 2004) (secondary materials
physically comparable to virgin
products which would be used in their
place, or which pose similar or
otherwise low risks when used in the
same manner as the virgin product,
need not be considered ‘‘discarded’’ and
hence need not be classified as solid
wastes). Given that ECF (including the
hydrocarbon and oxygenate portion)
would have legitimate energy value and
that emissions from burning ECF are
comparable to fuel oil when burned in
an industrial boiler under the good
combustion conditions typical of such
boilers, classifying such material as a
fuel product and not as a waste
promotes RCRA’s resource recovery
goals without creating a risk from
burning greater than those posed by
fossil fuel. Under these circumstances,
EPA can permissibly classify ECF as a
non-waste.
The conditional exclusion would be
an exclusion only from the RCRA
subtitle C regulations, and not from the
emergency, remediation and
information-gathering sections of the
RCRA statute [sections 3007, 3013, and
7003]. This is consistent with the
principle already codified for other
excluded hazardous secondary
materials—that the exclusion is only
from the RCRA regulatory provisions,
and not from these statutory authorities.
See § 261.1(b). We are restating this
principle here in the interest of clarity,
not to reopen the issue. The legal basis
for the distinction of the Agency’s
authority under these provisions is that
they use the broader statutory definition
of solid waste (and hazardous waste, as
well) and so need not (and should not)
be read as being limited by the
regulatory definition. See, for example,
50 FR at 627. See also Connecticut
Coastal Fishermen’s Assn. v. Remington
Arms, 989 F. 2d 1305, 1313–15 (2d Cir.
1993) (EPA may permissibly ascribe
different definitions to the term ’’solid
waste’’ for regulatory and statutory
purposes).
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Section 5.
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Although ECF could have higher
concentrations of particular
hydrocarbons and oxygenates than the
benchmark fossil fuels—fuel oil and
gasoline—that EPA used to establish the
specifications in Table 1 to § 261.38,
higher levels of hydrocarbons and
oxygenates in ECF do not imply that
burning ECF for energy recovery
constitutes waste management because:
(1) Hydrocarbons naturally occur in
virgin fuels 14 and oxygenates are a class
of compounds that are added to virgin
fuels to enhance combustion; 15 (2) the
hydrocarbons and oxygenates have a
heating value of 10,000 Btu/lb to 18,500
Btu/lb,16 which is comparable to the
range for virgin fuels (e.g., coal and fuel
oil); and (3) the hydrocarbons and
oxygenates produce emissions
comparable to virgin fuels when burned
under conditions typical of those under
which virgin fuels are burned.
We note, however, that ECF can pose
a greater hazard during storage than fuel
oil given that ECF can contain higher
concentrations of certain hazardous,
volatile hydrocarbons and oxygenates.
We are consequently proposing to
condition the exclusion on certain
storage conditions similar to those
applicable to commercial products and
commodities analogous to ECF, namely
fuel oil and other commercial organic
liquids. See discussion below in Part
Two, Section IV.
In addition, we are proposing to
condition the exclusion on requirements
for the design and operation of the ECF
burner to ensure that ECF is burned
under the good combustion conditions
typical of most fossil fuel boilers. See
discussion below in Part Two, Section
II. These conditions should ensure that
emissions from burning ECF remain
comparable to emissions from burning
fossil fuels.
A. Why Would the Specifications Be
Waived Only for Hydrocarbons and
Oxygenates?
We are proposing not to apply the
specifications for certain hydrocarbons
and oxygenates, but are proposing to
retain the specifications for metals and
14 We explained in the final comparable fuel rule
that it is reasonable to assume that the Table 1
hydrocarbons that we did not detect in fuel oil or
gasoline could in fact be present at levels up to the
detection limit. See 63 FR at 33791.
15 Examples of fuel oxygenates are: Ethanol;
methyl tert-butyl ether (MTBE), tert-amyl methyl
ether (TAME); diisopropyl ether (DIPE); ethyl tertbutyl ether (ETBE); tert-amyl alcohol (TAA); and
tert-butyl alcohol (TBA). For further discussion, see
USEPA, ‘‘Draft Technical Support Document for
Expansion of the Comparable Fuel Exclusion,’’ May
2007, Section 3.1.
16 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Section 2.2.
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the other categories of organic
compounds for which specifications are
provided under § 261.38. We would not
apply the specifications for these
hydrocarbons 17 because: (1) It is
reasonable to assume that these
compounds may be present in fossil
fuels (see 63 FR at 33791); and (2) when
they are burned under the good
combustion conditions typical for fossil
fuel-fired boilers, emissions from
burning these compounds would be
comparable to emissions from burning
fuel oil.
We also would not apply the
specifications for the listed oxygenates
because they are a class of organic
compounds that are added to fuels to
enhance combustion.18 These
compounds would burn cleanly under
the good combustion conditions typical
of a fuel oil-fired industrial boiler and
would generate only trace or
comparable levels of emissions.
It is appropriate to retain the
specifications for metals since they do
not contribute energy and are not
destroyed during the combustion
process. Given that the metal
specifications in Table 1 to § 261.38
reflect levels that can be present in fuel
oil, excess, noncontributing metals are
‘‘along for the ride,’’ suggesting
discarding. Moreover, metals emissions
would necessarily be higher than
emissions from fuel oil if the metals
specifications do not apply because oilfired boilers typically lack optimized
particulate control due to low metal
content of commercially available fuel
oils.
Also, it is appropriate to retain the
specifications for the other categories of
organic compounds listed under Table 1
to § 261.38—sulfonated organics,
nitrogenated organics, and halogenated
organic compounds. These organic
compounds, for the most part, are not
likely to be found in the benchmark
fuels—fuel oil and gasoline—we used to
establish the specifications. And, unlike
oxygenates, these organic compounds
are not within a class of compounds that
are added to fossil fuels to enhance
combustion. These hazardous
compounds also would appear to be
along for the ride when present at
concentrations higher than benchmark
17 Please note, however, that we are proposing to
retain the specifications for certain hydrocarbons:
PAHs (polycyclic aromatic hydrocarbons) and
naphthalene. See discussion in the text in Part Two,
Section III.
18 We acknowledge that oxygenates are added to
fuels burned in internal combustion engines rather
than fuels burned in industrial boilers. However,
oxygenates burn cleanly—they do not contain
halogens, sulfur, or nitrogen that would result in
emissions of halogen acids and sulfur and nitrogen
oxides.
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fuels, and consequently their
destruction via combustion can be
viewed as waste management.
B. Do Available Data and Information
Support a Comparable Emissions
Finding?
We investigated whether emissions
from burning ECF in an industrial boiler
operating under prescribed good
combustion conditions would be
comparable to emissions from burning
fuel oil in an industrial boiler operating
under good combustion conditions. We
evaluated organic emissions data from
watertube steam boilers (other than
stoker-fired boilers) burning hazardous
waste and compared those emissions
against emissions from oil-fired
industrial boilers. In addition, we
conducted two qualitative analyses of
the risk that ECF emissions may pose:
(1) Evaluation of RCRA risk assessments
for watertube steam boilers burning
hazardous waste to determine if organic
emissions had been found to pose a
hazard to human health and the
environment; and (2) a limited
comparative risk assessment for dioxin/
furan emissions.
As discussed below, we believe that
available data and information indicate
that emissions from burning ECF under
the proposed, prescribed conditions
would be comparable to emissions from
an oil-fired industrial watertube steam
boiler operating under good combustion
conditions.
rwilkins on PROD1PC63 with PROPOSALS2
1. Evaluation of Organic Emissions Data
for Hazardous Waste Boilers
In the absence of emissions data from
boilers burning ECF, we evaluated
organic emissions data from watertube
steam boilers burning hazardous waste
and compared those emissions against
emissions from oil-fired industrial
boilers. Using hazardous waste boiler
emissions as a surrogate for ECF boiler
emissions is a reasonable worst-case
because the exclusion would be
conditioned on the ECF boiler operating
under conditions relating to assuring
good combustion conditions that are at
least as stringent as those required of
boilers burning hazardous waste.19
19 See discussion in Part Two, Section II, of the
text describing the ECF boiler conditions. The CO
controls for ECF boilers plus the requirement to fire
ECF into the primary fuel flame zone are equivalent
to the controls on organic emissions for hazardous
waste boilers—CO controls and compliance with
the 99.99% destruction and removal efficiency
(DRE) standard. The other ECF boiler controls are
more restrictive than controls that apply to
hazardous waste boilers, but are appropriate to help
assure that an ECF boiler operates under good
combustion conditions given that ECF would be
burned under a conditional exclusion absent a
RCRA permit and the regulatory oversight typical
for a RCRA hazardous waste combustor, and absent
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We obtained organic emissions data
for 26 hazardous waste watertube steam
boilers which data were generated
during risk-burn testing required under
RCRA omnibus authority codified at
§ 270.32(b)(2). EPA requires this testing
as necessary on a site-specific basis to
ensure that emissions are protective of
human health and the environment. We
have data for 28 test conditions for the
26 boilers that provide 175 detected
measurements of organic compounds,
where a measurement is a three-run
set.20 We also have data for hazardous
organic compounds emitted from oilfired industrial boilers. Those data were
compiled in support of the NESHAP for
Industrial, Commercial, and
Institutional Boilers and Process Heaters
promulgated under Part 63, Subpart
DDDDD. See 69 FR 55218 (Sept. 13,
2004). We use oil-fired industrial boiler
emissions data for comparison because
fuel oil is the closest analogous fuel to
ECF, and ECF could be burned only in
industrial or utility boilers. See
discussion below in Section II.B.1.
We have emissions data for both
hazardous waste boilers and oil-fired
industrial boilers for 26 hazardous
organic compounds. We also have
hazardous waste boiler emissions data
for another 33 hazardous organic
compounds for which we do not have
oil-fired boiler emissions data for
comparison. We discuss our
investigation of these data below.
a. Hazardous Organic Compounds for
Which We Have Both Hazardous Waste
Boiler and Fuel Oil Boiler Emissions
Data. We have both hazardous waste
boiler and fuel-oil boiler emissions data
for 26 hazardous organic compounds.
The great majority of the hazardous
waste boiler test condition averages for
these compounds (150, or greater than
85%) were unequivocally comparable to
fuel oil emissions—the hazardous waste
emissions were below the oil emissions
95th percentile level. There were 24 test
condition averages, however, that
exceeded the oil emissions 95th
percentile level for 10 compounds.21
the extensive operating limits (e.g., combustion
chamber temperature, maximum load) that are
established subsequent to emissions testing to
demonstrate compliance with a destruction and
removal efficiency (DRE) standard.
20 A test condition is normally comprised of three
test runs conducted under identical (controllable)
operating conditions.
21 Please note that we have reanalyzed the oilfired boiler emissions data to identify the 95th
percentile benchmarks based on test condition
averages, rather than test runs, based on comments
submitted by one of the peer reviewers. As
discussed in Part Two, Section VII, although the
reanalysis resulted in several additional
exceedances of the oil emissions benchmarks, our
conclusion remains unchanged. It is reasonable to
conclude that ECF emissions will be either
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33291
Nonetheless, we do not believe that
these exceedances indicate that ECF
emissions would be higher than oil-fired
boiler emissions, as discussed below.
For 12 of the 24 exceedances,
laboratory contamination of the sample
was known or suspected. Specifically,
for nine exceedances—six for
dichloromethane, two for benzene, and
one for toluene—the constituent being
measured was found in the blank, while
there were three additional exceedances
for dichloromethane, a common lab
contaminant that is frequently found in
laboratory samples and in the
environment. For one of these test
conditions, the report indicated that
dichloromethane is a common
laboratory contaminant, implying that
the data may be suspect. For the other
two test conditions, laboratory
contamination was not discussed in the
test reports. Even if laboratory
contamination were not an issue for
these two tests, however, we note that
these hazardous waste boilers were not
operating under the conditions that are
proposed for an ECF boiler. Both boilers
were burning waste fuels with a heating
value below the 8,000 Btu/lb minimum
heating value that is proposed for ECF.
In addition, it is unclear if one boiler
was burning vent gas or natural gas as
the primary fuel. ECF must be burned
with at least 50% primary fuel that is
fossil fuel. Operating under conditions
less stringent than proposed for ECF
boilers could result in higher emissions
of organic compounds.
For seven exceedances, hazardous
waste boiler emissions were at trace
levels 22—there was a de minimis
increase in emissions. Test condition
averages were below 8 µg/dscm for the
exceedances for anthracene,
benzo[a]pyrene, ethylbenzene, fluorine,
2-methlynaphthalene, and
phenanthrene.
In addition, an exceedance for
acetaldehyde was at an emissions level
of 100 µg/dscm, while oil emission
levels for acetaldehyde are virtually
comparable at 70 µg/dscm. However, the
hazardous waste boiler emissions for
acetaldehyde were well below the 95th
percentile emissions for natural gas
boilers, 635 µg/dscm. This is relevant
because ECF may be burned with
natural gas as the primary fuel. Further,
generally comparable to oil emissions or at de
minimis levels.
22 Emissions of 8 µg/dscm for high molecular
weight compounds such as these are equivalent to
approximately 0.005 ppmv expressed as propane
equivalents. Thus, these are de minimis
concentrations considering that the hydrocarbon
emission limit for boilers burning hazardous waste
is 10 ppmv, expressed as propane equivalents. See
§ 63.1217(a)(5)(ii).
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rwilkins on PROD1PC63 with PROPOSALS2
we note that the hazardous waste boiler
was operating under conditions less
stringent than proposed for ECF
boilers—it was burning only 20%
natural gas as the primary fuel, while it
is proposed that ECF boilers fire at least
50% primary fuel. Thus, acetaldehyde
emissions may be higher than they
would have been if the boiler had the
hot, stable flame that burning 50%
natural gas (or fuel oil) would provide.
Finally, there were four exceedances
for benzene that we nonetheless believe
are comparable to fuel oil emissions.
Three of the exceedances were below
the highest fuel oil emission test run
level of 200 µg/dscm, while the fourth
exceedance was at a level of 260 µg/
dscm, just somewhat higher. More
importantly, for all four exceedances,
the hazardous waste boiler was not
operating under the conditions
proposed for an ECF boiler. For all four
exceedances, the hazardous waste fuel
had a heating value below 2,000 Btu/lb
compared to 8,000 Btu/lb that is
proposed for ECF. And, for one of the
exceedances, the hazardous waste fuel
had a viscosity of 165 cSt, while the
maximum viscosity for ECF would be 50
cSt. To reiterate, operating under
conditions less stringent than proposed
for ECF boilers could result in higher
emissions of organic compounds.
Notwithstanding this analysis of
available emissions data, we
acknowledge that, when ECF with
higher concentrations of certain
hydrocarbons and oxygenates than fuel
oil is burned even under good
combustion conditions, emissions of
hazardous organics may be somewhat
higher than those from burning fossil
fuel. This is because combustion is
generally a percent-reduction process.
Thus, even though good combustion
conditions may ensure a very high
destruction efficiency (e.g., 99.9999%
reduction), emission concentrations
may nonetheless increase as the feedrate
of an organic compound increases. We
believe, however, that these increases
would be de minimis because operating
under the good combustion conditions
proposed for ECF boilers ensures that
emissions of hazardous organic
compounds would generally be at trace
levels, and, as discussed below,
protective of human health and the
environment.23
23 Please note that a peer reviewer questioned
whether ECF emissions could, in fact, be expected
to be comparable to oil-fired boiler emissions given
the unlimited concentrations of the listed
hazardous compounds (i.e., benzene, toluene, and
the oxygenates) that may be present in ECF. We
respond to this comment in Part Two, Section VII
of the preamble.
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b. Compounds for Which We Only
Have Hazardous Waste Boiler Emissions
Data. We have hazardous waste boiler
emissions data for 33 hazardous organic
compounds for which we do not have
oil-fired boiler emissions data for
comparison. Average hazardous waste
boiler emissions for each of these
compounds are at trace levels—below
11 µg/dscm 24—except for bis(2ethylhexyl)phthalate and chloroform.
We have bis(2-ethylhexyl)phthalate
emissions data for 15 test conditions
(generally comprised of three runs)
representing 15 different boilers. Test
condition average emissions ranged
from 0.34 µg/dscm to 600 µg/dscm for
the boilers, with an average of 69 µg/
dscm. Although the highest test
condition average—600 µg/dscm—
appeared to be an outlier given that the
second highest average was 130 µg/
dscm and 12 test conditions were below
42 µg/dscm, we determined that it is not
a statistical outlier.25 Nonetheless, we
note that: (1) The boiler with the highest
emissions—600 µg/dscm—was not
operating under the conditions that are
proposed for an ECF boiler (which
could result in higher emissions)—the
primary fuel firing rate was
approximately 30% rather than a
minimum of 50%, and boiler load was
approximately 30% rather than a
minimum of 40%; and (2) bis(2ethylhexyl)phthalate is known to be a
common lab contaminant, and thus the
reported emissions levels may be
suspect.
For chloroform, we have emissions
data for 9 test conditions (generally
comprised of three runs) representing 9
different boilers. Test condition average
emissions ranged from 0.28 µg/dscm to
270 µg/dscm for the boilers, with an
average of 45 µg/dscm. Although the
highest test condition average—270 µg/
dscm—appeared to be an outlier given
that the second highest average was 85
µg/dscm and the remaining test
conditions did not exceed 16 µg/dscm,
we determined that it is not a statistical
outlier. We note, however, that the
boiler with the highest emissions—270
µg/dscm—was not operating under the
conditions that are proposed for an ECF
boiler—it burned a waste fuel with a
heating value below 8,000 Btu/lb and it
is not clear whether the boiler burned
process vent gas or natural gas as
primary fuel.
24 As discussed in footnote 22, emissions at this
low concentration are in the de minimis range.
25 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Appendix C.
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2. Evaluation of RCRA Risk Assessments
In addition to the analysis of emission
concentrations discussed above, we
reviewed the RCRA risk assessments 26
that had been completed by June 2006
for hazardous waste watertube steam
boilers other than stoker-fired boilers to
determine if organic emissions under
the good combustion conditions
required by the standards under Part
266, Subpart H, may result in
unacceptable risk to human health and
the environment. We determined that
such risk assessments had been
conducted at 13 facilities and decisions
on whether omnibus/additional permit
conditions are needed to ensure
emissions are protective have been
made for nine of those facilities. A
decision to include an omnibus permit
condition to address organic emissions
has been made for only two of the nine
facilities, however.
The first facility operated several
boilers equipped with a common
electrostatic precipitator. Risk-based
dioxin emission limitations and
associated testing and temperature
monitoring requirements were
established in the permit based upon a
finding that dioxin/furan emissions
during an isolated test event exceeded
risk levels of concern. During that test
event, artificial chlorine spiking into the
waste feed was conducted. During
subsequent testing under the permit
terms, chlorine spiking did not take
place and compliance with the riskbased dioxin/furan emission limitations
was demonstrated. Electrostatic
precipitator operating temperatures
during the subsequent tests ranged from
396 °F to 418 °F. We note, however, that
the chlorine specification proposed for
ECF would prohibit chlorine
concentrations from approaching the
levels present during the instances of
chlorine spiking at this facility. In
addition, we also note that today’s
proposal would require that ECF boilers
(other than coal-fired boilers) equipped
with an ESP or FF maintain a gas
temperature below 400 °F as a condition
of the exclusion. See discussion in
Section II below.
For the second facility where omnibus
permit conditions were imposed, there
was no finding of excess risk associated
with any organic constituents. Rather,
the omnibus permit conditions serve as
a trigger for a reassessment of risk if
emissions levels higher than those
considered in the initial risk assessment
were measured.
This analysis confirms our view that
organic emissions from hazardous waste
26 See
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boilers operating under good
combustion conditions required under
§§ 266.104 and 63.1217 are generally
protective. It also confirms our view that
organic emissions from ECF boilers
operating under the good combustion
conditions discussed in Section II below
should be protective.
3. Comparative Risk Assessment for
Dioxin/Furan
Finally, we also conducted an
abbreviated comparative risk assessment
for dioxin/furan emissions from boilers
burning hazardous waste and that meet
the design conditions for an ECF boiler
discussed below in Section II—a
watertube steam boiler that is not
stoker-fired. The abbreviated evaluation
used one component of the comparative
risk evaluation used to support the
Phase II hazardous waste combustor
MACT for boilers 27—the Margin of
Exposure (MOE) analysis.28 The
emission-adjusted MOE analysis uses
the risk ‘‘safety margins’’ (i.e., modeled
MOEs) determined from the MACT
Phase I comprehensive risk assessment
for hazardous waste incinerators 29 to
determine whether, considering
emissions alone, risks for a second
universe, here, the ECF boilers, could
rise to a level of concern.30 Smaller
MOEs correspond to a greater potential
for risk beyond the level of concern (i.e.,
1E–05 lifetime cancer risk). In this
analysis, we: (1) Revised the dioxin/
furan emissions data base for Phase II
hazardous waste boilers to establish a
data base of boilers that meet the ECF
boiler design conditions (i.e., by
eliminating boilers other than watertube
steam boilers that are not stoker-fired)
and by adding dioxin/furan emissions
data obtained during the evaluation of
risk burns for hazardous waste boilers,
as discussed above; (2) calculated point
estimates and confidence intervals for
the revised emissions data base; (3)
combined the Phase I incinerator data
base with the revised (i.e., ECF) boiler
data base and conducted tests for
common generalized percentiles; and (4)
27 See
70 FR at 59536–37 (October 12, 2005).
‘‘Assessment of the Potential Costs,
Benefits, & Other Impacts of the Hazardous Waste
Combustion MACT Final Rule Standards,’’
September 2005, Chapter 6.
29 RTI International, ‘‘Inferential Risk Analysis in
Support of Standards for Hazardous Air Pollutant
Emissions from Hazardous Waste Combustion,’’
June 2005, Section 1.
30 It must be emphasized that emission-adjusted
MOEs should not be construed as predictions of the
level of risk. Instead, they are only intended to
provide an indication of whether risks could exceed
a level of concern based on simplifying
assumptions and as such, are subject to some level
of uncertainty.
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28 USEPA,
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adjusted the MOE, if appropriate.31 The
analysis indicates that the emissionsadjusted MOEs representing the ECF
boilers are higher than the MOEs for the
Phase I incinerators. This suggests a
lower potential for risk for the ECF
boilers compared to hazardous waste
incinerators. This means that, within
the limitations of the analyses, dioxin/
furan emissions from ECF boilers pose
no greater hazard than the emissions
from hazardous waste incinerators, and
therefore, should remain within levels
that are protective.
Based on this information—
comparison of emissions concentrations
from hazardous waste boilers and oilfired boilers; evaluation of omnibus risk
assessments; and evaluation of dioxin/
furan risk—we conclude that emissions
from burning ECF in a boiler under the
conditions proposed today would be
comparable to fuel oil emissions and
would be generally protective of human
health and the environment. We
specifically request additional data and
comment on our analyses and
conclusions.
II. What Conditions Would Apply to
Burners of Emission-Comparable Fuel?
The ECF exclusion proposed today
would be conditioned on burning ECF
under conditions typical of a fuel oilfired industrial boiler operating under
good combustion conditions. The ECF
conditions would ensure that the boiler
maintains a hot, stable flame, and that
ECF is properly atomized and fired into
that flame. In addition, post-combustion
conditions would minimize the
potential for dioxin/furan formation by
controlling the combustion gas
temperature at the inlet to a dry
particulate matter control device for
boilers so-equipped. Accordingly, we
propose the following conditions: (1)
The burner must be a watertube steam
boiler other than a stoker-fired boiler;
(2) carbon monoxide (CO) must be
monitored continuously, must be linked
to an automatic ECF feed cutoff system,
and must not exceed 100 ppmv on an
hourly rolling average (corrected to 7%
oxygen); (3) the boiler must fire at least
50% primary fuel on a heat input or
volume basis, whichever results in a
higher volume of primary fuel, and the
primary fuel must be fossil fuel or tall
oil with a heating value not less than
8,000 Btu/lb; (4) the boiler load must be
40% or greater; (5) the ECF must have
an as-fired heating value of 8,000 Btu/
lb or greater; (6) ECF must be fired into
the primary fuel flame zone; (7) the ECF
31 See USEPA, USEPA, ‘‘Draft Technical Support
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Section 5.3.4.
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33293
firing system must provide proper
atomization; and (8) if the boiler is
equipped with an electrostatic
precipitator (ESP) or fabric filter (FF)
and does not fire coal as the primary
fuel, the combustion gas temperature at
the inlet to the ESP or FF must be
continuously monitored, must be linked
to the automatic ECF feed cutoff system,
and must not exceed 400 °F on an
hourly rolling average. These conditions
are consistent with oil-fired industrial
boiler design and operating conditions
that ensure good combustion (and postcombustion control of dioxin/furan) and
ensure that emissions from burning ECF
are comparable to fuel oil emissions.32
In addition, as discussed in the previous
section, such emissions would be at
levels which are protective of human
health and the environment.
The boiler design and operating
conditions that ensure a hot, stable
flame and good combustion of ECF (i.e.,
all of the conditions, except the
condition to minimize post-combustion
formation of dioxin/furan by limiting
the gas temperature at the inlet to the
ESP or FF) derive from extensive testing
that EPA conducted in the mid-1980’s to
identify design and operating
parameters that affect the combustion of
hazardous organic compounds in waste
fuels fired as supplementary fuel in
boilers. See 52 FR at 16995–96 (May 6,
1987). EPA used the results of that
testing to identify design and operating
conditions that would ensure that waste
fuel is properly atomized and fired into
a hot, stable flame to ensure destruction
of hazardous organics in the waste fuel
to trace levels and to minimize
formation of products of incomplete
combustion (PICs) to levels that would
not pose a hazard to human health or
the environment.
Those operating conditions also
reflect typical operations for an oil-fired
industrial boiler operating under good
combustion conditions: (1) As discussed
below, CO levels below 100 ppmv are
typically achieved by oil-fired industrial
boilers; (2) the oil fuel provides a hot,
stable flame; and (3) boilers generally
operate at loads greater than 40% and
can experience poor combustion
conditions at lower loads. The design
conditions—the boiler must be a
watertube steam boiler that is not
stoker-fired—also reflect industrial
32 Given that burning ECF under the proposed
conditions will destroy toxic organic compounds in
the ECF generally to trace levels, we are proposing
that burning excluded fuel that was derived from
a hazardous waste listed under §§ 261.31–261.33
does not subject boiler residues, including bottom
ash and emission control residues, to regulation as
derived-from hazardous waste. See proposed
§ 261.38(b)(12).
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boiler designs that help ensure optimum
combustion efficiency. See discussion
below in Section B.1.
A. Why Isn’t a DRE Performance Test a
Critical Requirement To Ensure Good
Combustion Conditions?
EPA concluded from the boiler testing
discussed above that: (1) Boilers cofiring
hazardous waste fuels with fossil fuels
where the hazardous waste provides
less than 50 percent of the boiler’s fuel
requirements can achieve 99.99 percent
destruction and removal efficiency
(DRE) of POHCs (principal organic
hazardous constituents) under a wide
range of operating conditions (e.g., load
changes, waste feed rate changes, excess
air rate changes); (2) when boilers are
operated at high combustion efficiency,
as evidenced by flue gas carbon
monoxide (CO) levels of less than 100
ppmv, DRE exceeds 99.99 percent; (3)
boilers clearly operating under poor
combustion conditions, as evidenced,
for example, by smoke emissions, still
achieved 99.99 percent DRE: (4)
emissions of PICs appeared generally to
increase as combustion efficiency
decreased as evidenced by increased
flue gas CO levels; and (5) emission of
total unburned hydrocarbons (i.e.,
quantified Part 261, Appendix VIII
pollutants, as well as unburned POHCs
and other unburned organic
compounds) may increase as
combustion efficiency decreases as
evidenced by an increase in flue gas CO
levels. See 52 FR at 16995.
These results confirm that a 99.99%
DRE regulatory requirement (coupled
with compliance with limits on
operating conditions established during
the DRE performance test) has limited
utility for ensuring that a combustor
operates under the good combustion
conditions necessary to destroy both
hazardous organics in the fuel feed and
PICs to levels that are protective of
human health.33 EPA has explained,
however, why a limit on carbon
monoxide emissions (i.e., 100 ppmv,
hourly rolling average) is a conservative
indicator of good combustion conditions
for boilers (and other combustors) that
will result in destruction of both POHCs
and PICs. See 52 FR at 16998; 70 FR at
59461–463. Of the four combustion
failure modes that EPA has identified—
total ignition failure, partial ignition
rwilkins on PROD1PC63 with PROPOSALS2
33 We
note that, for this reason, hazardous waste
boilers are currently exempt from the requirement
to demonstrate 99.99% DRE if the boiler complies
with specific design and operating conditions,
including the principal organic emission control
requirement of continuously monitoring CO and
compliance with a limit of 100 ppmv. See
§ 266.110. We note further that the ECF boiler
conditions proposed today are at least as stringent
as the conditions provided by § 266.110.
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failure, combustion air failure, and
rapid quench failure—only a total
ignition failure could result in low CO
and poor combustion of POHCs and
PICs.34 Total ignition failure could
potentially occur in a boiler if the fuel
firing gun inadvertently directed the
fuel to a location in the combustion
chamber away from the flame zone—
i.e., if the fuel were not fired into the
flame zone. The other combustion
failure modes result in high CO and
potentially high unburned organics: 35
partial ignition failure; combustion air
failure; and rapid quench failure. Thus,
it is important to ensure that waste fuels
are fired into the flame zone of a boiler
when relying on CO emission levels to
ensure good combustion conditions
(and that 99.99% DRE is achieved), as
proposed for ECF boilers.
B. What Is the Rationale for the
Proposed Burner Conditions?
From the discussion above, it could
be argued that the only controls needed
to ensure good combustion conditions
and destruction of hazardous organics
in ECF would be continuous monitoring
of carbon monoxide and a requirement
to fire ECF into the flame zone to avoid
total ignition failure. Notwithstanding
this view, we believe it is appropriate to
apply additional controls to help ensure
that an ECF boiler operates under the
good combustion conditions typical of
an oil-fired industrial boiler given that
ECF would be burned under a
conditional exclusion absent a RCRA
permit and the regulatory oversight
typical for a RCRA hazardous waste
combustor. The proposed conditions
would help ensure good combustion
conditions by requiring that ECF has
substantial heating value and that it is
fired into a hot, stable flame. There are
many industrial boilers that meet the
design criteria (i.e., watertube steam
boiler that is not stoker-fired) and the
operating conditions generally reflect
standard operating practice. The
proposed conditions consequently are
analogous to conditions under which
fuel oil, the commercial product for
which ECF substitutes, are burned.
Furthermore, more than 90% of the
candidate waste fuel streams identified
34 See USEPA, USEPA, ‘‘Draft Technical Support
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Appendix A.
35 Because CO is more thermally stable than other
intermediate combustion products, high CO
emissions may or may not be indicative of high PIC
emissions. If CO is low, however, combustion has
progressed to the point that PIC emissions will be
low (assuming total ignition failure is avoided).
Thus, CO is considered a conservative indicator of
good combustion. See 52 FR at 16998.
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by generators had heating values greater
than 8,000 Btu/lb.36
The rationale for each of the proposed
burner conditions is discussed below.
We specifically request comment on
each of these proposed conditions.
1. ECF Must Be Burned in a Watertube
Steam Industrial or Utility Boiler That Is
Not Stoker-Fired
A condition of the proposed exclusion
would require the ECF burner to be a
watertube steam boiler that does not fire
fuels using a stoker or spreader-stoker
feed system.37 ECF also must be burned
in a boiler rather than in an industrial
furnace, such as a cement kiln, because
the Agency conducted nonsteady-state
emissions tests (as part of the boiler
testing program discussed above) to
identify the parameters that affect
combustion efficiency only for boilers.
Industrial furnaces have a primary
purpose other than burning fuels most
efficiently and we have not determined
the operating conditions that would
ensure good combustion conditions
absent the regulatory oversight provided
by the RCRA hazardous waste permit
program.
The boiler must be a watertube,
nonstoker boiler because there is a
greater potential for poor distribution of
combustion gases and localized cold
spots in firetube and stoker boilers that
can result in poor combustion
conditions. In particular, stoker and
spreader-stoker boilers generally burn
solid fuels with a relatively large
particle size on a bed, thus making even
distribution of combustion air difficult.
See 56 FR at 7148.
The boiler must be a steam boiler
rather than a process heater because
process heaters can have a primary
purpose other than to burn fuels under
optimum combustion conditions. An
example is a process heater that
quenches combustion gases to reduce
gas temperatures to avoid overheating a
process fluid. Such operating conditions
could adversely affect combustion
efficiency by interrupting the complete
combustion of organic compounds.
Finally, the boiler must be an
industrial or utility boiler as currently
36 Letter from American Chemistry Council
(Carter Lee Kelly, Leader, Waste Issues Team, and
Robert A. Elam, Director, Regulatory Affairs, Waste
Issues Team) to Robert Springer and Matt Hale,
USEPA, dated November 24, 2003.
37 Stoker-fired boilers are designed to burn solid
fuels (including coal, wood, municipal wastes, etc.)
on a bed. Stokers are mechanical or pneumatic
devices that feed solid fuels onto a grate at the
bottom of the furnace and remove the ash residue
after combustion. See USEPA, USEPA, ‘‘Draft
Technical Support Document for Expansion of the
Comparable Fuel Exclusion,’’ May 2007, Section
3.3.2.
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required under the comparable fuel
exclusion. See proposed
§ 261.38(c)(2)(i). This would ensure that
ECF is burned in boilers that are capable
of handling this type of fuel (e.g., rather
than boilers at schools, apartments, or
hospitals) and that would be subject to
Federal, state, or local air emission
requirements.
We request comment on whether
there are other types of combustors (e.g.,
thermal oxidizer) that may be able to
burn ECF under the good combustion
conditions comparable to an industrial
watertube steam boiler (that is not of
stoker design). Any suggestions for other
types of combustors must include
supporting information in order for the
Agency to be able to consider it for final
action.
rwilkins on PROD1PC63 with PROPOSALS2
2. CO Monitoring
A condition of the proposed exclusion
would require that combustion gas CO
be monitored continuously, that the CO
recordings be linked to an automatic
ECF feed cutoff system, and that CO
emissions not exceed 100 ppmv on an
hourly rolling average (corrected to 7%
oxygen). As discussed above, low CO
emissions, coupled with firing ECF in
the primary fuel flame zone, are the
primary controls for ensuring that the
boiler is operating under good
combustion conditions.
EPA has used continuous CO
monitoring as an indicator of good
combustion for various types of
combustors, including boilers that burn
hazardous waste and boilers that do not
burn hazardous waste. See 70 FR at
59463–64 for a discussion of using CO
to control organic HAP under the
NESHAP for hazardous waste boilers,38
and 68 FR at 1671 for a similar
discussion in the context of the
NESHAP for boilers that do not burn
hazardous waste. We note that the
38 The NESHAP for hazardous waste boilers allow
sources to continuously monitor total hydrocarbons
and comply with a limit of 10 ppmv in lieu of
continuously monitoring CO and complying with a
limit of 100 ppmv. See §§ 63.1216(a)(5) and
63.1217(a)(5). We are not proposing a total
hydrocarbon alternative for ECF boilers, however,
because very few, if any, hazardous waste boilers
elect that alternative given the complexity of
maintaining a continuous hydrocarbon monitor. In
addition, boilers that are designed to rapidly
quench the combustion gas temperature and thus
cannot achieve CO levels below 100 ppmv have no
choice other than to monitor hydrocarbons if they
burn hazardous waste fuels. But, these boilers may
not be appropriate candidates for burning ECF even
if they achieve hydrocarbon levels below 10 ppmv
absent the regulatory oversight of a RCRA or Title
V permit given that they are not designed to achieve
optimum combustion efficiency. Nonetheless, we
request comment on whether the rule, if finalized,
should allow ECF boilers the option of
continuously monitoring hydrocarbons and
complying with a limit of 10 ppmv as an alternative
to CO monitoring.
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NESHAP for boilers that do not burn
hazardous waste (i.e., Industrial Boiler
NESHAP) requires continuous CO
monitoring only for new solid, liquid, or
gas boilers with a capacity greater than
100 MM Btu/hr. The CO limit is 400
ppmv corrected to 3% oxygen for oil
and gas boilers and 400 ppmv corrected
to 7% oxygen for solid fuel boilers, and
is based on a 30-day average. Boilers
with a capacity in the range of 10 MM
Btu/hr to 100 MM Btu/hr comply with
the CO limit based on a 3-run average
during periodic performance testing.
See Table 1 to Subpart DDDDD, Part 63.
EPA did not establish a CO limit for
existing boilers that do not burn
hazardous waste because: (1) CO
monitoring was not floor control given
that inadequate information was
available to conclude that 6% of the
sources were equipped with CO
monitors or that 6% of the sources were
subject to state standards for CO
monitoring; and (2) CO monitoring did
not appear to be cost-effective as a
beyond-the-floor control technique. For
new sources where MACT floor is based
on the performance of the single best
performing source within a category or
subcategory, EPA established CO
monitoring requirements based on the
most stringent state standards for CO
monitoring that applied to all large
boilers (i.e., greater than 10 MM Btu/hr)
in a subcategory (i.e., solid fuel, liquid,
and gas boilers) and to all fuel types
burned by boilers within the
subcategory (e.g., for solid fuel boilers,
coal, wood, and other biomass).39
Notwithstanding the 400 ppmv CO
limit (based on a 30-day average or
periodic performance testing 40)
applicable to new industrial boilers that
do not burn hazardous waste, a 100
ppmv limit (based on an hourly rolling
average) is appropriate for ECF burners
because: (1) The limited CO data in the
Industrial Boiler NESHAP data base
indicate that oil-fired boilers, the boiler
subcategory most analogous to a boiler
burning ECF, are achieving CO levels
below 100 ppmv; 41 (2) hazardous waste
39 See 68 FR at 1673 and the memorandum from
Jim Eddinger, EPA, to Docket No. OAR–2002–0058
entitled, ‘‘Revised MACT Floor Analysis for the
Industrial, Commercial, and Institutional Boilers
and Process Heaters National Emission Standards
for Hazardous Air Pollutants Based on Public
Comments,’’ dated February 2004, pp. 18–19.
40 The 30-day averaging period for the Industrial
Boiler NESHAP was adopted because boilers
burning biomass under certain conditions (e.g., wet
wood after a rain event) could not achieve the CO
limit over a shorter averaging period. This situation
is not relevant here. ECF boilers that burn fuel oil
or natural gas as primary fuel can readily achieve
a 100 ppmv CO limit over an hourly rolling average.
41 See USEPA, USEPA, ‘‘Draft Technical Support
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Section 3.4. Also, we note
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33295
fuels that are proposed to be excluded
as ECF are currently burned in boilers
subject to a 100 ppmv (hourly rolling
average) CO standard under RCRA
§ 266.104, also indicating that a CO
limit of 100 ppmv is readily achievable;
and (3) a tighter CO limit for ECF than
the CO limit that applies to industrial
boilers burning fossil fuels and
nonhazardous waste fuels is appropriate
given the greater potential for ECF
emissions to pose a hazard to human
health and the environment (i.e., it is
reasonable and appropriate to tailor the
management controls that apply to the
most analogous product, fuel oil, to
address the greater hazards posed by
potentially high concentrations of
hazardous organic compounds in
ECF).42
We similarly do not believe that
periodic rather than continuous CO
monitoring would be appropriate for
ECF boilers, even though periodic CO
monitoring is allowed under the
Industrial Boiler NESHAP to boilers in
the size range of 10 MM Btu/hr to 100
MM Btu/hr. As discussed above, low CO
emissions, combined with the
requirement to fire ECF into the primary
fuel flame zone, is the principal
indicator of good combustion
conditions. Periodic CO monitoring
would ensure good combustion
conditions only periodically—
combustion conditions could deteriorate
an hour, day, or week after the periodic
performance test. Given the potential
hazards that burning ECF under poor
combustion conditions can pose
compared to fossil fuels and
nonhazardous waste fuels, and given the
variability in combustion characteristics
that ECF may have over time relative to
the primary fuel, it is reasonable to
condition the exclusion on continuous
CO monitoring.43 Nonetheless, we
specifically request comment on
whether periodic rather than continuous
that EPA adopted the 400 ppmv CO limit for boilers
that do not burn hazardous waste to accommodate
the higher CO levels that can result from burning
solids, particularly wet biomass after rain events.
That scenario would not be applicable to a boiler
burning ECF. ECF boilers can readily achieve CO
levels below 100 ppmv.
42 The hazardous waste boiler emissions data we
analyzed as a surrogate for ECF emissions data to
determine if emission concentrations were
comparable to fuel oil emissions were derived from
hazardous waste boilers operating under a CO limit
of 100 ppmv. If those boilers operated at higher CO
levels and thus at lower combustion efficiency,
emissions of toxic organic compounds may have
been higher.
43 The Industrial Boiler NESHAP requires CO
monitoring, albeit periodic monitoring, for all new
boilers in the size range of 10 MM Btu/hr to 100
MM Btu/hr. The proposed continuous CO
monitoring conditions for ECF boilers, irrespective
of size, would apply only to those boilers that elect
to burn ECF.
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CO monitoring should be allowed for
ECF boilers in the size range of 10 MM
Btu/hr to 100 MM Btu/hr, consistent
with the Industrial Boiler NESHAP CO
monitoring provisions for new boilers.
Commenters must explain and provide
supporting information why periodic
monitoring is sufficient, including how
the owner or operator would ensure that
the boiler is operating under ‘‘good
combustion conditions’’ during those
times that the boiler is not being
monitored for CO in order for the
Agency to be able to consider it for final
action.
Finally, we propose to specify that the
CO monitor must be linked to an
automatic ECF feed cutoff system to
ensure that ECF is fired only when the
boiler is operating under good
combustion conditions—when CO
levels are below 100 ppmv on an hourly
rolling average. Linking the CO monitor
to an automatic ECF feed cutoff system
is appropriate given that emissions may
be neither comparable to fuel oil nor
protective if the boiler is not operating
under good combustion conditions. An
automatic feed cutoff system does not
appear to be cost-prohibitive and would
help assure effective combustion. We
propose to adopt the provisions for
automatic feed cutoff systems that apply
to boilers that burn hazardous waste—
§ 63.1206(c)(3)—and for the same
reasons. See USEPA, ‘‘Technical
Support Document for HWC MACT
Standards, Volume IV: Compliance with
the HWC MACT Standards,’’ July 1999,
Chapter 11.
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3. The Boiler Must Fire at Least 50%
Primary Fuel
A condition of the proposed exclusion
would require an ECF boiler to fire at
least 50% primary fuel on a heat input
or volume basis, whichever results in a
higher volume of primary fuel, and the
primary fuel must be fossil fuel or tall
oil with a heating value not less than
8,000 Btu/lb. These conditions would
ensure that a hot, stable flame is
provided to help ensure optimum
combustion conditions. Although a
primary fuel firing rate of 50% is at the
lower end of the range of reasonable
values—50% to 75% primary fuel—that
could have been selected, we believe it
is a reasonable condition because it
would ensure that the boiler is burning
primarily fossil fuel (or equivalent) and
so ensures a hot, stable flame.44 We also
44 ECF could be cofired with other fuels,
including waste fuels, that may not have
combustion characteristics comparable to fuel oil,
natural gas, or ECF. Thus, absent a condition that
at least 50% of the fuel must have a heating value
of 8,000 Btu/lb or greater, a hot, stable flame into
which ECF would be fired could not be assured.
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note that this condition would be
consistent with the primary fuel
requirement for hazardous waste boilers
under § 266.110 that elect to waive the
DRE performance standard under
operating conditions that ensure
optimum combustion efficiency.
The primary fuel would be required to
have a minimum heating value of 8,000
Btu/lb to reflect the low end of the range
of heating values for fossil fuels
normally fired in industrial boilers.
Most coal-fired industrial boilers burn
either subbituminous coal (with heating
values ranging from 8,300–11,500 Btu/
lb) or bituminous coal (with heating
values ranging from 10,500 to 14,000
Btu/lb). Lignite, a low-rank coal that
typically has a heating value below
8,000 Btu/lb, is not commonly burned
in industrial boilers.
Although we believe that the primary
fuel would generally be fossil fuel—oil,
natural gas, or coal (i.e., pulverized coal
burned in suspension)—it is reasonable
to allow other high-quality fuels as the
primary fuel. Consequently, tall oil
would also be allowed as a primary fuel.
Tall oil is fuel derived from vegetable
and rosin fatty acids and has a heating
value comparable to fuel oil.
We specifically request comment on
whether a condition to require a
minimum of 50% primary (generally
fossil) fuel is appropriate to maintain a
hot, stable flame to ensure good
combustion of ECF. Any comments
recommending an alternative minimum
limit for the primary fuel firing rate
must include supporting information in
order for the Agency to be able to
consider it for final action.
4. The Boiler Load Must Be 40% or
Greater
A condition of the proposed exclusion
would require the ECF boiler to operate
at 40% load (i.e., the heat input at any
time when ECF is fired must be at least
40% of the maximum rated boiler heat
input) or greater to ensure a hot, stable
flame. At low loads, higher excess air
rates are used to improve fuel/air
mixing. The increased excess air rates,
however, can also cool the flame zone
and even make the flame unstable (e.g.,
as a candle flame flickers in a breeze),
thereby increasing the likelihood of
flameout. These conditions can result in
reduced combustion efficiency.
Although a lower boiler load could have
been selected within the reasonable
range of 25% to 40% of maximum load,
we believe it is appropriate to adopt a
value at the high end of the range to be
conservative given that ECF can contain
concentrations of certain hydrocarbons
and oxygenates higher than the
specifications listed in Table 1 to
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§ 261.38. We also note that a minimum
load requirement of 40% would be
consistent with the requirement for
hazardous waste boilers under § 266.110
that elect to waive the DRE performance
standard under operating conditions
that ensure optimum combustion
efficiency.
We specifically request comment on
whether a condition on minimum boiler
load of 40 percent is appropriate to
maintain a hot, stable flame and thus
ensure good combustion conditions.
Any comments recommending an
alternative minimum boiler load must
include supporting information in order
for the Agency to be able to consider it
for final action.
5. The ECF Must Have an As-Fired
Heating Value of 8,000 Btu/lb or Greater
A condition of the proposed exclusion
would require the ECF to have an asfired heating value of 8,000 Btu/lb or
greater. This is a reasonable minimum
heating value that could have been
selected within the range of 5,000 Btu/
lb to 10,000 Btu/lb because: (1) It is the
minimum heating value of fossil fuels
normally fired in industrial boilers (i.e.,
subbituminous coal); and (2) it would
help ensure that a hot, stable primary
fuel flame is maintained. We also note
that more than 90% of the candidate
waste fuel streams identified by
generators had heating values greater
than 8,000 Btu/lb.45
Although ECF, like comparable fuel,
would need to have a heating value of
5,000 Btu/lb as-generated (or after bona
fide treatment as a hazardous waste), it
must have a minimum heating value of
8,000 Btu/lb as-fired. Accordingly, ECF
may be blended with fuels (including
comparable fuel) other than hazardous
waste to achieve an as-fired heating
value of at least 8,000 Btu/lb. However,
any fossil fuel used to blend ECF to
achieve the minimum 8,000 Btu/lb
heating value requirement could not be
counted to achieve the proposed
condition that the boiler must have a
minimum firing rate of 50% primary
fuel.
We specifically request comment on
whether a condition to require that ECF
have an as-fired heating value of 8,000
Btu/lb or greater is appropriate to help
ensure that the hazardous compounds
that may be present in the ECF at high
concentrations are destroyed to levels
comparable to oil-fired boiler emissions.
Any such comments on alternative ECF
heating values must include supporting
45 Letter from American Chemistry Council
(Carter Lee Kelly, Leader, Waste Issues Team, and
Robert A. Elam, Director, Regulatory Affairs, Waste
Issues Team) to Robert Springer and Matt Hale,
USEPA, dated November 24, 2003.
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information in order for the Agency to
be able to consider it for final action.
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6. ECF Must Be Fired Into the Primary
Fuel Flame Zone
As a condition of the proposed
exclusion, ECF must be fired into the
primary fuel flame zone to avoid,
potentially, total ignition failure—a
combustion failure mode characterized
by poor combustion, high emissions of
unburned organic compounds, but
potentially low CO emissions. Under
this combustion failure mode, organic
compounds in ECF would not be
exposed to the hot flame zone and may
be simply volatilized absent
combustion. Thus, under this failure
mode, low CO emissions may not be
indicative of good combustion
conditions.
As a practical matter, firing waste
fuels (or any fuels) directly into the
flame zone of the boiler is standard
operating practice. Directing the fuel
burner in a direction that avoided the
flame zone would normally occur only
inadvertently. Nonetheless, we believe
it is prudent to propose this condition
to highlight its importance in achieving
good combustion conditions.
We specifically request comment on
whether a condition to require that ECF
be fired into the primary fuel flame zone
is appropriate to help ensure that the
hazardous compounds that may be
present in the ECF at high
concentrations are destroyed to levels
comparable to oil-fired boiler emissions.
Any such comments must include
supporting information in order for the
Agency to be able to consider it for final
action.46
7. The ECF Firing System Must Provide
Proper Atomization
As a condition of the proposed
exclusion, the ECF firing system must
provide proper atomization to ensure
that the ECF droplets are not too large
for optimum volatilization. An organic
compound must be vaporized and
mixed with air before combustion can
occur. The quicker ECF and its
constituents are vaporized and the more
completely the volatilized compounds
are mixed with air, the more rapid and
efficient the combustion and destruction
of organic constituents. Firing systems
that atomize liquid fuels to form small
droplets increase the rate of
vaporization by providing a larger
surface area per volume of fuel to absorb
heat from the flame.
46 Please note that we also request comment on
conditions (other than proper atomization) that may
be appropriate for the ECF firing system in Part
Two, Section VII, in response to comments from a
peer reviewer.
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We are proposing to allow the use of
virtually all atomization systems
commonly used to fire liquid fuels.47
We are, however, proposing to restrict
the maximum size of solids that may be
present in liquid fuels that meet the
viscosity specification of 50 cSt—the asfired ECF must pass through a 200 mesh
screen. This would ensure that the
appropriate droplet size is achieved (to
ensure volatilization and destruction of
organic compounds) and minimize
plugging of the firing nozzle. The
acceptable atomization systems are air,
steam, mechanical, or rotary cup
atomization systems.48
a. Air or steam atomization. Air or
steam atomization systems use air or
steam to break up the fuel into small
droplets. Under ordinary operations,
high pressure steam or air provided at
30 to 150 psig produces much smaller
droplets than other atomization systems.
Because of the cost of providing high
pressure air and where steam is not
readily available, low pressure (1–5
psig) burners are sometimes used.
b. Mechanical atomization.
Mechanical atomizers break up the fuel
into small droplets by forcing it through
a small, fixed orifice. A strong cyclonic
or whirling velocity is imparted to the
fuel before it is released through the
orifice. Combustion air is provided
around the periphery of the conical
spray of fuel. The combination of
combustion air introduced tangentially
into the burner and the action of the
swirling fuel produces effective
atomization.
The size of the droplets produced by
mechanical atomization is a function
principally of the fuel viscosity and the
fuel pressure at the atomizing nozzle.
The pressure required to produce a
droplet size conducive to optimum
combustion efficiency depends on the
volatility of the fuel. Highly volatile
materials can volatilize rapidly, even
from larger droplets, and, thus, can be
fired at pressures of 75 to 150 psig. Less
volatile fuels may require an
atomization pressure as high as 1,000
psig to form droplets small enough to
rapidly volatilize.
Given that fuel pressure is an
important factor in determining droplet
size, we considered whether it would be
appropriate to propose to limit the
minimum fuel pressure as a condition of
47 A simple lance (essentially an open pipe
without any means of atomization), however, could
not be used to fire ECF.
48 Engineering Science, ‘‘Background Information
Document for the Development of Regulations to
Control the Burning of Hazardous Waste in Boilers
and Industrial Furnaces, Volume I: Industrial
Boilers,’’ January 1987, pp. 4–89 to 4–96.
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33297
the exclusion.49 Optimum fuel pressure
to produce an optimum droplet size,
however, is a function of fuel volatility
and fuel/air mixing. Thus, it is not
practicable to propose specific limits on
minimum fuel pressure. Rather, we are
proposing that the boiler owner or
operator be required to maintain fuel
pressure within the atomization system
design range considering the viscosity
and volatility of the waste fuel, the fuel/
air mixing system, and other
appropriate parameters. This approach
would allow the atomization system
manufacturer or designer (e.g., if
designed and fabricated on-site) the
necessary flexibility to determine an
acceptable fuel pressure considering the
specifics of the situation. If fuel pressure
is not maintained at appropriate levels
to ensure small droplet size and
optimum combustion efficiency or, if for
any other reason the boiler does not
achieve maximum combustion
efficiency, the boiler may not be able to
achieve CO levels below 100 ppmv.
c. Rotary cup atomization. The rotary
cup atomizer uses centrifugal force to
break up the fuel into droplets. It
consists of an open cup mounted on a
hollow shaft. The fuel is pumped at low
pressure through the hollow shaft to the
cup which is rotating at several
thousand revolutions per minute. A thin
film of the fuel is centrifugally torn from
the tip of the cup. As centrifugal force
drives the fuel off the cup, combustion
air is admitted in a rotation counter to
the direction of the cup. This counter
motion of the air breaks up the conical
sheets of fuel into droplets and provides
turbulence for mixing the droplets with
air.
Rotary cup atomizers are typically
used on smaller boilers (e.g., less than
30 MM Btu/hr heat input) because the
maximum capacity of the largest unit is
about 1,400 pounds of fuel per hour. In
addition, rotary cup atomizers are not
often installed on new boilers because it
is difficult to achieve optimum fuel/air
mixing over a wide range of fuel flow
rates. Rotary cup atomizers are used
because they are relatively inexpensive,
they can handle fuels with relative high
viscosities ranging up to 40 to 72 cSt,50
49 Mechanical atomizers are susceptible to
erosion of the orifices in the firing nozzle. Erosion
can increase the size of the orifice resulting in
decreased fuel pressure and increased droplet size.
Limits on minimum fuel pressure, thus, would
ensure that droplet size remains optimized during
the course of operations by either increasing fuel
pressure as the nozzle erodes and, more likely,
replacing an eroded firing nozzle.
50 ECF could not have a viscosity exceeding 50
cSt given that it would be subject to the same
specifications that apply to existing comparable
fuel, except that the specifications for certain
hydrocarbons and oxygenates would not apply.
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and they are relatively insensitive to
solid impurities in the fuel and can
handle waste fuels with solids that can
pass through a 34 to 100 mesh screen.51
Droplet size is related primarily to the
viscosity and flow rate of the fuel and
rotational speed of the cup. Resulting
combustion efficiency is related to
volatility of the fuel and fuel/air mixing.
Although it is impracticable to control
these variables in a regulatory context,
manufacturers and boiler owners and
operators have ample experience with
rotary cup atomizers to design units that
achieve efficient combustion. Thus, we
are proposing that owners and operators
demonstrate that the as-fired fuel has a
volatility within the design parameters
of the firing system and limit fuel flow
rates consistent with the design
parameters of the firing system. As
discussed above, relative to mechanical
atomization systems, if, in fact, the
device does not produce droplet sizes
and fuel/air ratios conducive to
maintaining high combustion efficiency,
the boiler may not be able to achieve CO
levels below 100 ppmv.
We specifically request comment on
whether these conditions for
atomization of ECF are appropriate to
help ensure that the hazardous
compounds that may be present in the
ECF at high concentrations are
destroyed to levels comparable to oilfired boiler emissions. Any such
comments must include supporting
information in order for the Agency to
be able to consider it for final action.52
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8. Dioxin/Furan Controls for Boilers
Equipped With an ESP or FF
If a boiler is equipped with an
electrostatic precipitator (ESP) or fabric
filter (FF) and does not fire coal as the
primary fuel,53 we are proposing that
the combustion gas temperature at the
inlet to the ESP or FF be continuously
monitored, be linked to the automatic
ECF feed cutoff system, and not exceed
51 We propose that ECF must be able to pass
through a 200 mesh (74 micron) sieve to ensure that
particles are small enough to ensure volatilization
and destruction of organic compounds.
52 Please note that we also request comment on
conditions that may be appropriate for the ECF
firing system in Part Two, Section VII, in response
to comments from a peer reviewer.
53 Note that oil-fired boilers are generally not
equipped with a particulate matter control device
and that the fraction that are so-equipped are
typically equipped with wet scrubbers rather than
an ESP or FF. Thus, we would expect that this
condition would only apply to a small percentage
of boilers that choose to burn ECF. See the
memorandum from Jim Eddinger, EPA, to EPA
Docket No. OAR–2002–0058, entitled, ‘‘Revised
MACT Floor Analysis for the Industrial,
Commercial, and Institutional Boilers and Process
Heaters National Emission Standards for Hazardous
Air Pollutants Based on Public Comments,’’ dated
February 2004, Section 6.4.2.
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400 °F on an hourly rolling average.
These proposed conditions would
ensure that the post-combustion,
heterogeneous surface-catalyzed
formation of dioxin/furan in an ESP or
FF is minimized so that emissions from
burning ECF remain at least comparable
to those from burning fossil fuels and
remain at levels that are protective of
human health and the environment.
We are basing these proposed
conditions on information and data
gathered from the recently promulgated
NESHAP standards for hazardous waste
combustors. See 70 FR 59402.
Specifically, we have determined that
the surface-catalyzed formation of
dioxins/furans across an ESP or FF can
be significant when gas temperatures
exceed 400 °F.54 When gas temperatures
are below 400 °F (and the combustor is
operating under good combustion
conditions as evidenced by CO below
100 ppmv), however, dioxin/furan
emissions are generally below 0.40 ng
TEQ/dscm, the emission standard for
most hazardous waste combustors.55
Boilers burning coal as the primary
fuel would not be required to monitor
combustion gas temperature at the inlet
to an ESP or FF as a condition of the
exclusion, however. We determined
during development of the NESHAP for
coal-fired boilers that burn hazardous
waste that sulfur contributed by the coal
is a dominant control mechanism
because the sulfur inhibits formation of
dioxins/furans.56 Please note, however,
that a peer reviewer questioned whether
the low sulfur coal that some ECF
boilers may burn would also inhibit
formation of dioxins/furans. We believe
that low sulfur coals would also inhibit
formation of dioxins/furans (and, thus,
a condition to limit the gas temperature
at the inlet to the ESP or FF would not
be needed), but request comment and
supporting information on opposing
views. See discussion in Section VII
below.
We are further proposing an hourly
averaging period for the temperature
limit, rather than a longer averaging
period, because there is a nonlinear
54 USEPA, ‘‘Technical Support Document for
HWC MACT Standards, Volume III: Selection of
MACT Standards and Technologies,’’ July 1999,
Section 3.0; USEPA, ‘‘Technical Support Document
for HWC MACT Standards, Volume IV: Compliance
with the HWC MACT Standards,’’ September 2005,
Section 3.2, and USEPA, ‘‘Technical Support
Document for HWC MACT Standards, Volume III:
Selection of MACT Standards,’’ September 2005,
Section 13.3.1.1.
55 See §§ 63.1217, 63.1219, and 63.1220. See also
USEPA, USEPA, ‘‘Draft Technical Support
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Section 5.
56 USEPA, ‘‘Technical Support Document for
HWC MACT Standards, Volume III: Selection of
MACT Standards,’’ September 2005, Section 14.1.1.
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relationship between gas temperature at
the ESP or FF and dioxin/furan
emissions. Consequently, a longer
averaging period would allow higher
temperatures to be offset by lower
temperatures, even though dioxin/furan
emissions at the higher temperatures
could be exponentially higher than
emissions at the lower temperatures,
and, thus, average dioxin/furan
emissions would be substantially higher
than if temperatures had been
maintained at the average
temperature.57
We also believe that there are factors
other than high gas temperature at the
inlet to an ESP or FF that may
contribute to the post-combustion
formation of dioxin/furan in boilers, but
these situations would not occur for
boilers burning ECF under the proposed
conditions. For example, we have
dioxin/furan emissions data for nine
three-run test conditions for eight
boilers burning liquid hazardous waste
fuel and equipped with wet scrubbers,
and two of the boilers have emissions
exceeding 0.40 ng TEQ/dscm.58
Although the wet scrubbers on these
boilers preclude surface-catalyzed
dioxin/furan formation across the
emission control device, the boilers
nonetheless have high dioxin/furan
emissions—1.4 ng TEQ/dscm and 0.44
ng TEQ/dscm. We note, however, that
both of these boilers are firetube boilers
and one burns waste fuel containing
60% by weight chlorine. Firetube
boilers would not be allowed to burn
ECF under the conditions proposed
today for reasons discussed above and,
in addition, the chlorine level in the
waste fuel for one of the boilers is orders
of magnitude higher than the
specification for chlorine in Table 1 to
§ 261.38.59 It is speculated that the
higher tube surface to combustion gas
57 USEPA, ‘‘Technical Support Document for
HWC MACT Standards, Volume IV: Compliance
with the HWC MACT Standards,’’ September 2005,
Section 2.2.3.
58 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,
May 2007, Section 5.
59 Although chlorine content of the feed is
generally not considered a primary factor in
formation of dioxin/furan (especially when other
factors may predominate, such as high gas
temperature at the inlet to the ESP or FF) because
extremely small amounts of chlorine are sufficient
to provide the chlorine for dioxin/furan formation,
we are nonetheless concerned enough about
chlorine content in the feed to require that
hazardous waste combustors operate within the
range of normal chlorine federate levels during
performance testing to document compliance with
the dioxin/furan emission standard. Thus, chlorine
content of the feed may be a significant factor that
could affect dioxin/furan formation. See USEPA,
‘‘Technical Support Document for HWC MACT
Standards, Volume IV: Compliance with the HWC
MACT Standards,’’ September 2005, Section 3.3.
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volume ratio for a firetube boiler
compared to a watertube boiler may
increase the possibility of combustion
gas flow over particulate matter that has
adhered to the tubes within the 400–750
°F temperature window, which is
conducive to surface-catalyzed
formation of dioxins/furans.
We also have dioxin/furan emissions
data for 11 three-run test conditions for
six different boilers that burn hazardous
waste and that are equipped with an
ESP or FF. Gas temperatures at the ESP
or FF were generally below 400 °F.60
Only two test conditions (from two
boilers) were above 0.4 ng TEQ/dscm.
One boiler (which would be ineligible to
burn ECF because it is a firetube boiler)
had emissions of 0.66 ngTEQ/dscm
during one test condition. This unit
burns mixed waste with levels of
chlorine and metals above the
specifications in Table 1 to § 261.38.
The second boiler (a watertube boiler),
however, had average emissions of 2.4
ng TEQ/dscm. Although the FF for this
boiler was operated slightly above 400
°F, we note that this boiler burned waste
fuel containing nickel at levels orders of
magnitude higher than the specification
identified in Table 1 to § 261.38. Nickel,
as well as copper and iron, have been
suggested to be responsible for the
catalytic reactions that lead to postcombustion formation of dioxins/
furans.61
Therefore, based on the data
described above, we believe that the
scenarios that resulted in high dioxin/
furan emissions when burning
hazardous waste fuels would not occur
for ECF boilers and that a proposed
condition that would limit the gas
temperatures at the inlet to a dry
particulate matter control device to
400 °F should control dioxin/furan
emissions generally to below 0.40 ng
TEQ/dscm.62 Moreover, we note that we
have dioxin/furan emissions data for 38
three-run test conditions representing
32 different boilers burning hazardous
waste fuel and not equipped with an
emissions control device where the test
condition average emissions were quite
low—below 0.10 ng TEQ/dscm. In
60 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,
May 2007, Section 5.3.3.
61 USEPA, ‘‘Technical Support Document for
HWC MACT Standards, Volume IV: Compliance
with the HWC MACT Standards,’’ September 2005,
p. 3–17.
62 We discussed previously in the text in Part
Two, Section I.B, that an abbreviated comparative
risk assessment for dioxin/furan emissions from
hazardous waste boilers that meet the design
conditions (i.e., watertube steam boiler that is not
stoker-fired) for an ECF boiler indicates that dioxin/
furan emissions from such a boiler are not likely to
pose a hazard to human health or the environment.
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addition, we have dioxin/furan
emissions data for 15 runs for oil-fired
industrial boilers (i.e., not burning
hazardous waste), and the average
emissions were 0.013 ng TEQ/dscm and
the maximum emissions were 0.042 ng
TEQ/dscm.63 This is further
confirmation indicating that dioxin/
furan emissions from boilers burning
ECF under the proposed conditions
should be quite low.
III. What Restrictions Would Apply to
Particular Hydrocarbons and
Oxygenates?
The toxicity, persistence and
bioaccumulation potential for the 37
hydrocarbons and oxygenates for which
specifications have been established in
Table 1 to § 261.38 varies over a wide
range. In addition, we acknowledge that
when ECF with potentially higher
concentrations of certain hydrocarbons
and oxygenates than fuel oil is burned,
even under good combustion
conditions, emissions of hazardous
organics maybe somewhat higher than
those from burning fossil fuel because
combustion is generally a percentreduction process. Therefore, to ensure
that the emissions from burning ECF as
a fuel under the conditions proposed
today remain protective, we propose to
retain the specifications for compounds
that can pose a high hazard—
naphthalene and PAHs—and to restrict
the firing rate of ECF containing
concentrations of compounds that can
pose a lower, but substantial hazard—
benzene and acrolein. See Safe Food
and Fertilizers, 353 F. 3d at 1271
(exclusion from the definition of solid
waste can be justified by low risk posed
by the recycling practice).
We explain below the rationale for the
approach we use to categorize the 37
hydrocarbons and oxygenates for which
specifications are established in Table 1
to § 261.38, according to their relative
hazard to human health and the
environment.
A. What Is the Rationale for the Relative
Hazard Characterization Scheme?
We categorized the 37 hydrocarbons
and oxygenates for which specifications
have been established in Table 1 to
§ 261.38 as to their relative hazard.64 We
assigned the highest hazard constituents
to Category A, the constituents that pose
intermediate hazard to Category B, and
the other constituents to Category C. As
63 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,
May 2007, Section 3.4.
64 Please note that we have conducted an
independent peer review of our ranking procedures.
See discussion in Part Two, Section VII, of the
preamble.
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mentioned above, we are proposing to
retain the specifications for the Category
A constituents, restrict the feedrate of
the Category B constituents, and not
apply the specifications in Table 1 to
the Category C constituents. We discuss
below the procedure for categorizing the
constituents.
First, we used the Waste
Minimization Prioritization Tool
(WMPT) 65 to rank the 37 hydrocarbons
and oxygenates. The WMPT is a peerreviewed methodology which provides
a screening-level assessment of potential
chronic (i.e., long-term) risks to human
health and the environment,
considering the chemicals’ toxicity,
persistence and bioaccumulation
potential.66
The WMPT scoring method produces
chemical-specific scores for a screeninglevel risk-based ranking of chemicals.67
The scoring method was designed to
generate an overall chemical score that
reflects the potential of a chemical to
pose risk to either human health or
ecological systems. A measure of human
health concern is derived, consistent
with the risk assessment paradigm, by
jointly assessing the chemical’s human
toxicity and potential for exposure.
Similarly, a measure of the ecological
concern is derived by jointly assessing
the chemical’s ecological toxicity and
potential for exposure. The WMPT uses
a small number of relatively simple
measures to represent the toxicity (e.g.,
oral Cancer Slope Factor) and exposure
potential (e.g., Bioaccumulation Factor)
of each chemical, consistent with a
screening-level approach and with other
systems of this type.
We then applied the procedures the
Agency used to develop the Priority
65 USEPA, ‘‘Waste Minimization Prioritization
Tool Background Document for the Tier III PBT
Chemical List,’’ 2000.
66 After several rounds of internal expert and
public comments, EPA used the current version of
the WMPT as the initial step in the process of
identifying the initial pool of priority chemicals
that are national priorities for voluntary pollution
prevention activities across the agency. EPA
determined the initial pool of priority chemical
candidates based on their rank. The rankings are
based on the higher of available scores for human
health concern (i.e., the sum of the scores for
persistence, bioaccumulation, and human toxicity)
and ecological concern (i.e., the sum of the scores
for persistence, bioaccumulation, and ecological
toxicity). The priority chemical candidate pool was
limited to those chemicals with WMPT scores of 8
or 9 (on a scale of 3 to 9). For a more detailed
description of the WMPT development process, see
USEPA, ‘‘Waste Minimization Prioritization Tool
Background Document for the Tier III PBT
Chemical List,’’ 2000. The specific use of the
current version of the WMPT rankings in
developing the RCRA Prioirity Chemicals List is
documented in the Tier III Chemical List Docket.
67 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Section 2.4.
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Chemicals List 68 from the WMPT
scoring. Thus, we assigned constituents
that scored an eight or nine to the high
hazard category—Category A.
Next, we considered whether any of
the remaining constituents, those that
did not receive a WMPT score of 8 or
9, present additional concerns for
materials managed as comparable fuels.
We did this by further analyzing the
data that WMPT used to generate
Human Toxicity scores for the
remaining constituents. We first
identified constituents that had WMPT
human toxicity scores based on
inhalation as the driving exposure
pathway. This is an appropriate
screening criterion given that the
inhalation pathway is particularly
important for evaluating the hazard
posed by air emissions. For such
constituents, we then determined
whether they posed a relatively high
human toxicity hazard or were a known
human carcinogen. If so, we assigned
the constituent to hazard Category B.
We assigned all other constituents to
hazard Category C.69
B. What Are the Results of the Relative
Hazard Ranking?
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We assigned 11 constituents to
Category A—the high hazard
constituents. These are constituents that
had WMPT scores of eight or nine,
consistent with the Agency’s procedures
for identifying priority chemicals.
Because the WMPT methodology
assigns all PAHs the highest score for
any PAH, we assigned a score of nine
to all PAHs. Ten of the 11 Category A
constituents are PAHs. The only
Category A constituent that is not a
PAH, but that scored an eight or nine,
was naphthalene.
In evaluating constituents to assign to
hazard Category B, we identified three
constituents that have WMPT human
toxicity scores based on inhalation as
the driving exposure pathway: Benzene,
acrolein, and phenol.
Benzene is a known human
carcinogen via the inhalation exposure
pathway. There are some chemicals
with sufficiently robust toxicological
databases that the Agency not only
generates a carcinogenic slope factor,
but also designates them ‘‘known
human carcinogens.’’ Consequently, we
believe it is reasonable to assign
68 See: https://www.epa.gov/epaoswer/hazwaste/
minimize/chemlist.htm.
69 We also qualitatively assessed the five
constituents with insufficient data to generate
complete, aggregate WMPT scores. Even assuming
worst-case values for their human toxicity score,
none of these constituents would have qualified for
Category A or B. Thus, we assigned them to
Category C.
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benzene to Category B to restrict the
feedrate (and thus emissions) of this
compound.
Acrolein has a WMPT human toxicity
score of three because it has very high
inhalation toxicity. Acrolein did not
have a higher aggregate WMPT score
because it had a low bioaccumulation
score. Nonetheless, exposure via
inhalation is of particular importance in
the context of assessing the hazard
posed by emissions from burning ECF.
Consequently, we believe it is
reasonable to assign acrolein to Category
B.
We did not assign phenol to Category
B because it has significantly lower
toxicity than benzene and acrolein.
Phenol has a WMPT human toxicity
score of two, rather than the highest
score of three. Further, phenol is not
known to be a carcinogen. EPA has
classified phenol as a Group D
carcinogen—not classifiable as to
human carcinogenicity, based on a lack
of data concerning carcinogenic effects
in humans and animals. Consequently,
we do not believe that phenol should be
assigned to hazard Category B even
though its WMPT human toxicity score
is based on the inhalation pathway. The
remaining constituents were assigned to
Category C.
C. What Firing Rate Restrictions Would
Apply to Benzene and Acrolein?
As discussed above, we believe that
benzene and acrolein pose a lower
hazard than PAHs and naphthalene, but
a greater hazard than the other
hydrocarbons and oxygenates for which
the specifications would not apply for
ECF. Accordingly, we propose to restrict
the firing rate of ECF that has benzene
or acrolein concentrations exceeding
2% by weight, as-fired, to 25% of the
heat input to the boiler (on a heat input
or volume input basis, which ever
results in the lower volume of ECF).
This ECF firing rate restriction would
reduce the feedrate of benzene and
acrolein and thus ensure that emissions
of these compounds remain at levels
comparable to emissions from burning
fuel oil in industrial boilers and
protective of human health and the
environment. Absent this firing rate
restriction, ECF with high
concentrations of benzene or acrolein
could be fired at a 50% firing rate—the
remaining 50% of the fuel must be
primary fossil fuel or equivalent. Thus,
the 25% firing rate restriction would
reduce the feedrate of benzene and
acrolein by half.
We selected a 25% firing rate
restriction because it is in the middle of
the range of values that could have been
reasonably considered—10% to 40%—
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given that the maximum firing rate for
any ECF is 50%. We selected a 2% or
greater benzene concentration as the
criterion for applying the firing rate
restriction because selecting a lower
concentration cutpoint would restrict
the composite benzene concentration in
total fuels to levels lower than would be
allowed if comparable fuel were burned
as 100% of the boiler fuel. Specifically,
we assumed that comparable fuel would
generally have a heating value of at least
10,000 Btu/lb if it were to comprise
100% of the boiler’s fuel. The
comparable fuel specification would
allow a benzene concentration of 4,100
mg/kg (or 0.41%) for a 10,000 Btu/lb
fuel. We further assumed the upper
range of heating values for the
comparable fuel would be 18,000 Btu/
lb. At that heating value, the comparable
fuel could contain 7,400 mg/kg (or
0.74%) benzene.
We then determined the benzene
concentration in ECF fired at a 25%
firing rate as a supplement to fuel oil
that would result in a composite fuel
benzene concentration equivalent to the
levels allowed if existing comparable
fuel were 100% of the boiler fuel.
Virtually all of the benzene would be
contributed by the ECF because fuel oil
contains negligible benzene.70 At a 25%
firing rate, the benzene concentration in
a 10,000 Btu/lb ECF would need to
exceed 1.6% for the benzene
concentration in the composite fuels
(i.e., ECF and fuel oil) to exceed 4,100
mg/kg, the benzene concentration in the
fuel if 10,000 Btu/lb comparable fuel
were fired as the sole fuel burned.
Similarly, at a 25% firing rate, the
benzene concentration in an 18,000 Btu/
lb ECF would need to exceed 3% for the
benzene concentration in the composite
fuels to exceed 7,400 mg/kg, the
benzene concentration in the fuel if
18,000 Btu/lb comparable fuel were
fired as the sole fuel burned.
Consequently, the reasonable range of
ECF benzene concentrations for
selecting the cutpoint to apply the 25%
firing rate restriction is 1.6% to 3%.71
We are proposing a cutpoint of 2%
because it generally correlates to the
average heating value of waste fuels—
11,000 Btu/lb.72
70 The comp fuel benzene spec in 261.38 (4,100
mg/kg at 10,000 Btu/lb) is based on levels of
benzene in gasoline. Benzene in crude oil is
concentrated in refined fractions, such as gasoline.
71 Expanding the fuel heating value range from
8,000 Btu/lb (the lowest heating value allowed for
ECF) to 20,000 Btu/lb (the highest heating value
known for waste fuels that may qualify as ECF)
would expand the benzene concentration cutpoint
range to 1.3% to 3.3%.
72 If we assumed comparable fuel has the average
heating value in our data base—11,200 Btu/lb—the
benzene concentration cutpoint would be 1.8%.
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We then considered what cutpoint we
should propose for acrolein. We are
proposing a 2% concentration cutpoint
for acrolein as well because: (1)
Acrolein poses hazards similar to
benzene and there is no basis for being
more or less stringent on the allowable
composite fuel concentrations; and (2) a
2% cutpoint would not control acrolein
in ECF more stringently than it is
controlled in comparable fuel (i.e., ECF
fired at a 25% firing rate as a
supplement to fuel oil and with an
acrolein concentration of 2% would not
result in a composite fuel acrolein
concentration lower than that allowed if
the boiler burned 100% existing
comparable fuel at the maximum
allowable acrolein concentration).
We specifically request comment on
whether ECF firing rate restrictions are
warranted for benzene and acrolein, and
if so, whether the proposed restrictions
are appropriate. Any such comment
must include an appropriate rationale
and supporting information in order for
the Agency to be able to consider it for
final action.
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IV. What Conditions Would Apply to
Storage of ECF?
A. What Are the Proposed Storage
Conditions?
The proposed exclusion for ECF
would also be conditioned on meeting
the storage controls applicable to the
closest analogous raw material/
product—fuel oil—plus a few additional
controls considered appropriate to
minimize the potential for releases to
the environment. The additional
controls would include ‘‘engineered’’
secondary containment and fugitive air
emission controls.
Although we are proposing generally
to apply storage controls applicable to
the closest analogous raw material/
product—fuel oil, the exclusion would
be conditioned on more substantial
‘‘engineered’’ secondary containment
than several of the permissible
secondary containment methods for oil
under the Spill Prevention, Control, and
Countermeasure (SPCC) provisions.
Examples of SPCC secondary
containment provisions applicable to oil
include the use of dikes, berms,
retaining walls, spill diversion ponds
and sorbent materials. We are proposing
to apply a more substantial
‘‘engineered’’ secondary containment
condition, such as double-walled tanks
because we believe it important that
such secondary containment address
potential releases to groundwater.
Today’s proposed controls on air
releases are based on those applicable to
another comparable product, organic
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liquids at the chemical plants which
often generate ECF.
These controls are appropriate
considering that ECF can contain higher
concentrations of certain hazardous,
volatile hydrocarbons and oxygenates
than fuel oil, and so though productlike, is not precisely analogous.
Consequently, ECF has a higher
potential for releases to the environment
and a higher potential for those releases
to cause environmental harm. Therefore,
we are proposing storage and
recordkeeping controls to ensure that
ECF is not managed so as to become
‘‘part of the waste disposal problem’’.
American Mining Congress v. EPA, 907
F. 2d 1179, 1186 (D.C. Cir. 1990).
We are also proposing that ECF be
stored only in tanks (including USTs),
tank cars, and tank trucks. ECF could
not be stored in other containers (e.g.,
portable devices, such as 55 gallon
drums) because: (1) We believe that ECF
would be generated in quantities that
would make storage in portable devices
other than tank cars and tank trucks
impractical; and (2) providing
conditions to ensure adequate
monitoring, inspections and air
emission controls for storage in other
containers would unnecessarily
complicate the rule. Nonetheless, we
request comment on whether ECF
would likely be stored in vessels other
than tanks, tank cars and tank trucks
(e.g., drums positioned to collect
process drippage that is eventually
consolidated with ECF in acceptable
tank, tank car, or tank truck). If so, and
if a final rule were to allow storage in
containers other than tank cars and tank
trucks, we would subject those units to
management conditions similar to those
that apply to hazardous waste
containers under subpart I, Part 265,
control releases.
1. Tank Systems, Tank Cars and Tank
Trucks
a. SPCC Discharge Prevention
Requirements.73 For ECF tank systems,
tank cars, and tank trucks, we are
proposing to condition the exclusion on
meeting certain of the discharge
prevention provisions which apply to
fuel oil, or are adapted therefrom. These
are from the Spill Prevention, Control,
and Countermeasure (SPCC) provisions
under 40 CFR Part 112 that apply to
petroleum oils managed at onshore
facilities. ECF generators and burners
would comply with these conditions, as
adopted under § 261.38(c)(1)(iii), as
73 The SPCC conditions we propose to adopt
would apply to ECF tanks systems that are not
hazardous substance underground storage tanks
subject to § 280.42(b), as well as tank cars and tank
trucks.
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though ECF met the definition of oil
under § 112.2.74 These adopted SPCC
provisions would apply to all owners
and operators of ECF tanks with a
capacity greater than 55 gallons.75
The SPCC requirements under Part
112 include both discharge prevention
requirements and requirements to
ensure effective responses to discharges.
The discharge prevention requirements
for onshore petroleum oil tanks are
implemented under a SPCC Plan and
associated requirements under §§ 112.1
through 112.8, and the discharge
response requirements are implemented
under a Facility Response Plan (FRP)
and associated requirements under
§§ 112.20 and 112.21. We propose to
adopt specific provisions of the
discharge prevention requirements—the
SPCC Plan—under §§ 112.3, 112.5,
112.7, and 112.8 only. We are not
proposing to adopt the FRP and
associated requirements, as discussed
below in Section IV.A.1.c. In lieu of the
FRP requirements, we are proposing to
adopt more appropriate provisions that
apply to hazardous waste tank systems
and that achieve the same objective as
the FRP requirements—specifying
proactive measures to respond to a
release of ECF.
We propose to adopt the following
SPCC Plan requirements under
§ 261.38(c)(1)(iii) to prevent ECF
releases from tank systems:
• Section 112.2, Definitions.76
• Sections 112.3(d) and 112.3(e),
Requirements to Prepare and Implement
an SPCC Plan. Paragraph (d) requires
that a licensed Professional Engineer
must review and certify the Plan, and
paragraph (e) requires that a copy of the
Plan must be maintained at the facility
and be available to the Regional
74 This proposed rule would neither amend nor
otherwise affect the SPCC provisions under 40 CFR
Part 112. Substantive controls from the SPCC rules
would merely be applied to tanks storing ECF as a
condition of those fuels being excluded from RCRA
subtitle C controls.
75 We note that the SPCC requirements under Part
112 do not apply to facilities that have both an
aggregate capacity for completely buried storage of
42,000 gallons or less of oil and an aggregate
capacity for above ground storage of 1,320 gallons
or less of oil. See § 112.1(d)(2). In addition, the
SPCC requirements do not apply to containers with
a storage capacity of less than 55 gallons of oil. We
propose to adopt the 55 gallon capacity criterion for
applicability of the adopted SPCC provisions to ECF
tanks, but propose to apply those SPCC provisions
to tanks with a capacity greater than 55 gallons at
all facilities managing ECF, irrespective of whether
the aggregate tank capacity for oil and ECF is below
the threshold in § 112.1(d)(2). Applying the adopted
SPCC provisions to all ECF tanks with a capacity
greater than 55 gallons, irrespective of aggregate oil
and ECF storage capacity at a facility, is appropriate
because ECF can pose a greater storage hazard than
petroleum oil, as discussed previously.
76 These SPCC definitions would apply only to
the adopted SPCC provisions.
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Administrator for on-site review. We are
not adopting paragraphs (a), (b), (c), (f),
or (g), which pertain to compliance
dates for plan preparation and
implementation and self-certification of
the plan. Because the ECF exclusion is
optional and conditional, we are
proposing that all conditions in § 261.38
must be met before ECF can be managed
under the conditional exclusion being
proposed today. Therefore we are not
adopting any of the compliance dates
provided in the SPCC regulations. Also,
we propose not to allow selfcertification of Plans in lieu of
certification by a Professional Engineer,
as allowed under § 112.6, for those
facilities with an aggregate aboveground
tank capacity of 10,000 gallons or less,
a provision the Agency recently
promulgated.77 We are proposing not to
adopt § 112.6 because of the greater
hazard that a release of ECF may pose.
We do not view certification of the Plan
by a Professional Engineer as an
unreasonable burden, and believe that
the value added to ensure that the Plan
is complete, accurate, and appropriate
to prevent releases is warranted given
the hazards that ECF may pose. A more
important consideration is that we do
not believe that facilities with ECF tanks
would meet the primary eligibility
criterion for self-certification: the
aggregate oil and ECF tank capacity
must be less than 10,000 gallons.
Therefore, this provision would add
complexity and burden for States and
EPA in implementation and
enforcement with little or no off-setting
benefits. Nonetheless, we specifically
request comment on whether there may
be facilities that store ECF in tanks that
could meet the eligibility criterion and
whether self-certification of the SPCC
Plan would be appropriate.
• Sections 112.5(a) and 112.5(b),
Amendment of SPCC Plan by Owners or
Operators. This section requires that the
Plan be amended by the owner or
operator in accordance with the general
requirements in § 112.7 when there is a
change in the facility design,
construction, operation, or maintenance
that materially affects its potential for a
discharge. This section also states that
owners or operators must complete a
review and evaluation of the SPCC Plan
at least once every five years from the
date the facility becomes subject to this
part, and that any technical
amendments to the Plan must be
certified by a Professional Engineer. We
propose to adopt paragraphs (a) and (b),
but not paragraph (c). Paragraph (c)
requires certification of technical
amendments to the Plan and references
77 See
71 FR 77266, December 26, 2006.
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§ 112.6 which allows self-certification in
lieu of certification by a Professional
Engineer. Given that we propose not to
adopt § 112.6 as discussed above, we
propose a condition that would require
technical amendments to be certified by
a Professional Engineer.
• Section 112.7, General
Requirements for Spill Prevention,
Control, and Countermeasure Plans. We
propose to adopt § 112.7, except for
paragraph (c) secondary containment,
paragraph (d) alternative requirements
in lieu of secondary containment, and
paragraph (k) alternative requirements
in lieu of secondary containment for
qualified oil-filled operational
equipment. These paragraphs would not
be applicable because they pertain to
secondary containment which we
propose to require under separate
conditions. See discussion below. The
§ 112.7 conditions we are proposing to
adopt are paragraph (a) which requires
a discussion of the facility’s
conformance with the requirements
included in § 112.7, and development of
the Plan; paragraph (b) which requires
a prediction of the direction, rate of flow
and total quantity of material which
could be discharged when experience
indicates a potential for equipment
failure, overflow, rupture or leakage;
paragraph (e) which addresses
conducting inspections and tests and
keeping records; paragraph (f) which
addresses personnel, training, and
discharge prevention procedures;
paragraph (g) which addresses security
requirements; paragraph (h) which
addresses facility tank car and tank
truck loading/unloading rack
requirements; paragraph (i) which
requires a brittle fracture evaluation 78 if
a tank undergoes a change in service
that might affect the risk of a discharge;
and paragraph (j) which states that the
Plan must include a complete
discussion of conformance with the
requirements in this part, as well as
applicable more stringent State rules,
regulations and guidelines.
• Section 112.8, Spill Prevention,
Control, and Countermeasure Plan
Requirements for Onshore Facilities
(excluding production facilities). We are
proposing to adopt § 112.8, except for:
Paragraph (b), facility drainage;
paragraph (c)(2), secondary containment
for bulk storage containers; paragraph
(c)(9), prevention of releases from
effluent treatment facilities; and
paragraph (c)(11), secondary
containment for mobile and portable
containers. These provisions are not
warranted because we are proposing
78 This requirement only applies to field erected
aboveground storage tanks.
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separate conditions for secondary
containment, as discussed below. The
conditions we are proposing to adopt
from this section are paragraph (a)
which states that the owner or operator
meet the general requirements for the
Plan listed under § 112.7, and the
specific discharge prevention and
containment procedures listed in this
section; paragraph (c)(1) which states
that a tank not be used for storage unless
its material and construction are
appropriate; paragraph (c)(3) which
addresses the drainage of
uncontaminated rainwater or effluent
bypassing the facility treatment system;
paragraph (c)(4) which states that any
completely buried metallic storage tank
installed on or after January 10, 1974 be
protected from corrosion and regularly
leak test such storage tanks;79 paragraph
(c)(5) which states that partially buried
or bunkered metallic tanks not be used
for storage unless you protect the buried
section of the tank from corrosion;
paragraph (c)(6) which states that each
aboveground tank be tested for integrity
on a regular schedule and whenever
material repairs are made and that the
outside of the tanks be inspected
frequently for signs of deterioration,
discharges, or accumulation of ECF
inside diked areas; paragraph (c)(7)
which states that leakage through
defective internal heating coils be
controlled by monitoring the steam
return and exhaust lines for
contamination from internal heating
coils that discharge into an open
watercourse, or pass the steam return or
exhaust lines through a settling tank,
skimmer, or other separation or
retention system; paragraph (c)(8) which
states that the tank system be
engineered or updated in accordance
with good engineering practice to avoid
discharges (e.g., overfill prevention);
paragraph (c)(10) which states that
visible discharges from tanks, tank cars,
and tank trucks be promptly corrected;
and paragraph (d) which addresses
provisions regarding facility transfer
operation, pumping, and facility
process. We are not proposing to adopt
the provision which requires that buried
piping be provided with a protective
wrapping and coating only if the buried
piping is installed or replaced on or
after August 16, 2002. Rather, we
propose to apply this provision to all
buried piping. This is because ECF can
pose a greater hazard than oil, and in
particular, because leaks of the
79 We request comment on whether we should
specify that completely buried metallic storage
tanks installed prior to January 10, 1974 must be
protected from corrosion and regularly leak
checked.
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hazardous organic compounds present
in ECF are more likely than oil to sink
into the ground and surrounding water,
and therefore create a greater hazard.
We are not proposing to adopt § 112.4,
Amendment of Spill Prevention,
Control, and Countermeasure Plan by
Regional Administrator. That section
requires the owner/operator of a facility
that has discharged more than 1000
gallons of oil in a single discharge or
more than 42 gallons of oil in each of
two discharges in any 12 month period
to submit a report to the Regional
Administrator (RA) that provides
information including the corrective
action and countermeasures taken, the
cause of the discharge, and preventive
measures to minimize the possibility of
recurrence. That section also allows the
RA to require the owner/operator to
amend the Plan if the RA determines
that the Plan does not meet the
requirements of Part 112 or amendment
is necessary to prevent and contain
discharges from the facility. Finally, that
section prescribes procedures that the
owner/operator may use to appeal the
RA’s decision to require an amendment
to the Plan. We are not proposing to
adopt § 112.4 because: (1) Given that
ECF tanks would be required to be
equipped with engineered secondary
containment (as discussed below), we
would not expect releases from ECF
tanks of the magnitude that would
trigger a report under § 112.4; (2) the
proposal already contains a provision
that the owner/operator must amend the
Plan upon a finding by the RA that
amendment is necessary to prevent and
contain releases of emission-comparable
fuel (see proposed
§ 2613.8(c)(1)(iii)(B)(3)), and this
provision would not include prescribed
appeal provisions given that the ECF
exclusion is elective 80; and (3) the
proposal already contains a provision
that the owner/operator must submit a
report to the RA within 24 hours of
detection of any release of ECF to the
environment, except de minimis leaks
(i.e., less than or equal to one pound)
that are immediately contained and
cleaned-up (see Section IV.A.1 below,
and proposed § 261.38(c)(1)(v)(C)).
b. Containment and detection of
releases. Preventing the release of
hazardous secondary materials, such as
ECF, to groundwater is one of the
primary exposure routes to be addressed
under RCRA; the SPCC secondary
containment requirements primarily
address the release of oil to surface
80 Even though we are not proposing prescribed
appeal provisions, the owner/operator could
certainly explain and clarify why the Plan already
addresses concerns the RA may express in a
requirement to amend the Plan.
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waters. In addition, because ECF can
have higher concentrations of certain
hazardous hydrocarbons and
oxygenates, it can pose a greater hazard
to human health and the environment
than fossil fuel if released to the
environment. Therefore, we believe that
the secondary containment
requirements in the SPCC rule are not
adequate for ECF. Thus, we are
proposing engineered secondary
containment for the storage of ECF in
tank systems.
Engineered secondary containment
means the use of an external liner, vault,
or double-walled tank. We note that two
states—Florida and Minnesota—require
some form of engineered secondary
containment for fuel oil and do not
allow the ‘‘non-engineered’’ options
allowed by SPCC (e.g., ponds, weirs,
and absorbent materials).81 However,
we have decided to propose the
substantive engineered secondary
containment provisions provided by the
hazardous waste rules for tank systems
under § 264.193(b–f). Although we
recognize they are somewhat more
prescriptive than those required by
Florida and Minnesota, we believe that
persons likely to use this exclusion are
likely to use the same tanks in which
the hazardous secondary material is
currently stored and thus, the facility
would not need to retrofit the design of
these tanks. However, the Agency does
solicit comments on whether an
alternative ‘‘engineered’’ secondary
containment system that may not
provide containment equivalent to an
external liner, vault, or double-walled
tank would also be appropriate.
We propose to adopt the following
requirements:
• Section 264.193(b), which
prescribes general performance
standards for secondary containment
systems;
• Section 264.193(c), which
prescribes minimum requirements for
secondary containment systems;
• Sections 264.193(d)(1–3), which
prescribe permissible secondary
containment devices—external liner,
vault, or double-walled tank. We are not
proposing to adopt § 264.193(d)(4),
which allows approval by the Regional
Administrator of an equivalent device,
because the exclusion is designed to be
self-implementing. Nevertheless, we
request comment on whether the final
rule should allow approval of
equivalent means of secondary
containment to avoid stifling innovation
(and potentially having to revise the
rule to allow alternative means we
81 See Florida Administrative Code at 62-762.501,
and Minn. R. Ch. at 7151.5400.
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33303
believe are appropriate). In providing
comments on this issue, we would ask
that commenters specifically describe
how this provision could work,
considering that the rule is designed to
be a self-implementing regulation;
• Section 264.193(e), which
prescribes design and operating
requirements for the permissible
secondary containment devices; and
• Section 264.193(f), which
prescribes secondary containment
requirements for ancillary equipment.
To comply with the adopted
hazardous waste tank secondary
containment provisions, we propose
that the term ‘‘emission-comparable
fuel’’ be substituted for the term
‘‘waste,’’ and that the term ‘‘document
in the record’’ be substituted for the
term ‘‘demonstrate to the Regional
Administrator.’’ Demonstrations to the
Regional Administrator to obtain a
waiver are allowed for hazardous waste
tank systems in the following situations:
• Section 264.193(c)(3), where the
owner or operator can demonstrate to
the Regional Administrator that the leak
detection system or site conditions will
not allow detection of a release within
24 hours;
• Section 264.193(c)(4), where the
owner or operator can demonstrate to
the Regional Administrator that removal
of released materials or accumulated
precipitation cannot be accomplished
within 24 hours; and
• Section 264.193(e)(3)(iii), where the
owner or operator can demonstrate to
the Regional Administrator that the leak
detection technology for a doublewalled tank or site conditions would not
allow detection of a release within 24
hours.
As mentioned above, site-specific
approval of an alternative provision is
inconsistent with the self-implementing
provisions of a regulatory exclusion.
Consequently, we propose to require the
owner or operator to document in the
record the basis for not being able to
comply with those provisions within 24
hours, as nominally required. This
information will be available for review
by the Regional Administrator.
We are not proposing to adopt
§§ 264.193(g) and 264.193(h) because
those provisions provide procedures to
support and request a variance from
secondary containment. Again,
substantive variance provisions cannot
be implemented under a selfimplementing regulatory exclusion.
Finally, we are not proposing to adopt
§ 264.193(i) which allows for alternative
secondary containment until a facility
can comply with the requirements of
§§ 264.193(b–f). We do not believe that
§ 264.193(i) is appropriate because the
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proposed ECF exclusion is not a
mandated provision; owners and
operators that elect to take advantage of
the exclusion should be in compliance
with all of the requirements necessary to
protect human health and the
environment before managing excluded
ECF.
c. Preparedness and Prevention,
Emergency Procedures, and Response to
Leaks or Spills. We considered whether
to adopt the Facility Response Plan
(FRP) provisions applicable to fuel oil
tanks under §§ 112.20 and 112.21 that
require proactive responses to oil
discharges, but believe that they are not
appropriate for tanks that handle ECF.
The FRP requirements are tailored to oil
discharges and may not be appropriate
for ECF, given that, for example, ECF
may contain high concentrations of
hazardous compounds that behave in
the environment as a dense nonaqueous
phase liquid and therefore do not float
on the water surface. In addition, the
FRP requirements are designed to
respond to discharges of oil to navigable
waters and adjoining shorelines (i.e.,
through the use of sorbents, booms, and
skimmers). In contrast, today’s proposed
rule is designed to equip ECF tanks with
engineered secondary containment (i.e.,
external liner, vault, or double-walled
tank), as discussed above in order to
control and prevent releases to the
environment. Consequently, we believe
it is appropriate to adopt certain
hazardous waste tank provisions that
provide proactive measures to respond
to a release of ECF. We specifically
request comment on our view that the
Part 112 FRP requirements would not
provide effective measures to respond to
releases of ECF, and whether there may
be release response provisions
applicable to other products that may be
more appropriate to adopt for ECF than
the hazardous waste tank provisions
that we discuss below.
We propose to adopt certain
provisions of Subparts C and D of Part
264 and § 264.196 82 to provide
proactive measures to respond to a
release of ECF: preparedness and
prevention; emergency procedures; and
response to leaks or spills. See proposed
§ 261.38(c)(1)(v).
The Part 64, Subpart C and D
provisions are similar to some of the
proactive requirements under the Part
82 As discussed later in the text, the § 264.196
provisions specifically address failures of the types
of engineered secondary containment (i.e., external
liner, vault, or double-walled tank) that we propose
to specify for ECF tanks. Thus, adopting these
provisions in lieu of the Part 112 RFP provisions,
which address discharge countermeasures (e.g.,
absorbents, booms, skimmers, and dispersants)
more appropriate for other types of secondary
containment, is particularly appropriate.
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112 FRP and in some cases are virtually
identical to the FRP provisions. The
specific Subpart C (Preparedness and
Prevention) provisions we propose to
adopt are discussed below. These are
commonsense provisions that should
represent standard operating practice for
facilities that store liquid fuels:
• Section 264.32, Required
Equipment. All provisions of this
section are appropriate for ECF tank
systems: requirements for an internal
communications or alarm system
capable of providing immediate
emergency instruction to facility
personnel; a device such as a telephone
or two-way radio capable of summoning
emergency assistance; portable fire
extinguishers, fire control equipment,
spill control equipment and
decontamination equipment; and water
at adequate volume and pressure, or
foam producing equipment, or
automatic sprinklers, or water spray
systems.
• Section 264.33, Testing and
Maintenance of Equipment. This section
requires that all communications or
alarm systems, fire protection
equipment, spill control equipment, and
decontamination equipment must be
tested and maintained as necessary to
assure its proper operation in case of
emergency.
• Section 264.34, Access to
Communications or Alarm System. We
propose to adopt this section to specify
that, whenever ECF is distributed into
or out of a tank system, all personnel
involved in the operation must have
access to an internal alarm or emergency
communication device, either directly
or through visual or voice contact with
another employee.
• Section 264.37, Arrangements with
Local Authorities. We propose to adopt
this section to specify that the owner or
operator must attempt to make
arrangements with the appropriate local
authorities (fire departments, emergency
response teams, police departments,
hospitals, etc.) to familiarize the
authorities with the layout of the
facility, properties of the ECF being
managed at the facility, possible
evaluation routes, and types of injuries
which could result from fires,
explosions, or releases at the facility. If
State or local authorities decline to enter
into such arrangements, the owner or
operator must document this refusal in
the facility’s record.
The specific Part 264, Subpart D
(Contingency Plan and Emergency
Procedures) provisions we propose to
adopt are: 83
83 We
are not proposing to adopt the Subpart D
contingency plan provisions because the SPCC Plan
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• Section 264.55, Emergency
Coordinator. We propose to adopt this
provision to specify that, at all times,
there must be at least one employee
either on the facility premises or on call
(i.e., available to respond to an
emergency by reaching the facility
within a short period of time) with the
responsibility for coordinating all
emergency response measures. This
emergency coordinator must be
thoroughly familiar with all aspects of
the facility’s Spill Prevention, Control,
and Countermeasures (SPCC) Plan, all
ECF operations and activities at the
facility, the location and characteristics
of ECF handled, the location of all
records within the facility pertaining to
ECF, and the facility layout. In addition,
this person must have the authority to
commit the resources needed to carry
out the SPCC Plan.
• Section 264.56, Emergency
Procedures. We propose to adopt this
provision to specify that: (1) Whenever
there is an imminent or actual
emergency situation relating to the ECF
tank system, the emergency coordinator
must immediately activate internal
facility alarms or communication
systems, where applicable, to notify all
facility personnel and notify appropriate
State or local agencies with designated
response roles if their help is needed;
(2) whenever there is a release, fire, or
explosion relating to the ECF tank
system, the emergency coordinator must
immediately identify the character,
exact source, amount, and aerial extent
of any released materials; (3) the
emergency coordinator must assess
possible hazards to human health or the
environment that may result from the
release, fire, or explosion; (4) if the
emergency coordinator determines that
the facility has had a release, fire, or
explosion associated with the ECF tank
system which could threaten human
health, or the environment outside the
facility, he must report his findings to
the government official designated as
the on-scene coordinator for that
geographical area or the National
Response Center; (5) if the emergency
coordinator’s assessment indicates that
evacuation of local areas may be
advisable, he must immediately notify
appropriate local authorities; (6) during
an emergency, the emergency
coordinator must take all reasonable
measures necessary to ensure that fires,
explosions, and releases do not occur,
recur, or spread to other materials at the
facility; (7) if the ECF tank system stops
operations in response to a fire,
that we propose to specify as a condition of the
exclusion is equivalent to the contingency plan
required for hazardous waste tank facilities.
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explosion, or release, the emergency
coordinator must monitor for leaks,
pressure buildup, gas generation, or
ruptures in valves, pipes, or other
equipment, wherever this is
appropriate; (8) immediately after an
emergency, the emergency coordinator
must provide for treating, storing, or
disposing of recovered ECF,
contaminated soil or surface water, or
any other material that results from a
release, fire, or explosion at the
facility; 84 (9) the emergency coordinator
must ensure that, in the affected area(s)
of the facility, materials that may be
incompatible with the released ECF is
treated, stored, or disposed of until
cleanup procedures are completed and
all emergency equipment listed in the
SPCC Plan is cleaned and fit for its
intended use before operations are
resumed; and (10) the owner or operator
must note in the record the time, date,
and details of any incident that requires
implementing the SPCC Plan for the
ECF tank system and within 15 days
after the incident, the owner or operator
must submit a written report on the
incident to the Regional Administrator.
We propose to adopt the provisions
under § 264.196 (Response to Leaks or
Spills and Disposition of Leaking or
Unfit-for-Use Tank Systems), except for
§§ 264.196(e)(1) and (e)(4), for all ECF
tank systems not subject to the
hazardous substance underground
storage tank requirements of § 280.42(b).
To comply with the adopted provisions
of § 264.196, you would substitute the
term ‘‘emission-comparable fuel’’ for the
terms ‘‘hazardous waste’’ and ‘‘waste,’’
and the term ‘‘record’’ for the term
‘‘operating record.’’ The adopted
provisions would specify that an ECF
tank system or secondary containment
system from which there has been a leak
or spill, or which is unfit for use, must
be removed from service immediately,
and the owner or operator must satisfy
the following conditions: (1) The owner
or operator must immediately stop the
flow of ECF into the tank system or
secondary containment system and
inspect the system to determine the
cause of the release; (2) if the release
was from the tank system, the owner/
operator must, within 24 hours after
detection of the leak or, if the owner/
operator demonstrates that it is not
possible, at the earliest practicable time,
remove as much of the ECF as is
necessary to prevent further release of
ECF to the environment and to allow
inspection and repair of the tank system
to be performed; (3) if the ECF released
84 ECF that is released from the tank system must
generally be managed as hazardous waste. See
proposed § 261.38(b)(15).
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was to a secondary containment system,
all released ECF must be removed
within 24 hours or in as timely a
manner as is possible to prevent harm
to human health and the environment;
(4) the owner/operator must
immediately conduct a visual
inspection of the release and, based
upon that inspection prevent further
migration of the leak or spill to soils or
surface water and remove, and properly
dispose of, any visible contamination of
the soil or surface water; (5) any release
to the environment, except de minimis
leaks (i.e., less than or equal to one
pound) that are immediately contained
and cleaned-up must be reported to the
Regional Administrator within 24 hours
of its detection; (6) within 30 days of
detection of a release to the
environment, a report containing the
following information must be
submitted to the Regional
Administrator—likely route of migration
of the release, characteristics of the
surrounding soil (soil composition,
geology, hydrogeology, climate), results
of any monitoring or sampling
conducted in connection with the
release (if available), proximity to
downgradient drinking water, surface
water, and populated areas, and
description of response actions taken or
planned; (7) the tank system must be
closed unless the cause of the release
was a spill that has not damaged the
integrity of the system and the released
material is removed and repairs, if
necessary, are made, or unless the cause
of the release was a leak from the
primary tank system into the secondary
containment system and the system is
repaired; and (8) if the owner/operator
has repaired a tank system and the
repair has been extensive (e.g.,
installation of an internal liner; repair of
a ruptured primary containment or
secondary containment vessel), the tank
system must not be returned to service
unless the owner/operator has obtained
a certification by a qualified
Professional Engineer that the repaired
system is capable of handling ECF
without release for the intended life of
the system.
We are not proposing to adopt
§ 264.196(e)(1) because that paragraph
would require the tank to be closed
under the § 264.197 provisions for
closure of a hazardous waste tank.
Those provisions are inappropriate for
closure of a tank that stored a product—
ECF. As provided under proposed
§ 261.38(b)(13), when ECF operations
cease, liquid and accumulated solid
residues that remain in a tank system for
more than 90 days after the tank system
ceases to be operated for storage of ECF
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33305
are subject to regulation under Parts 262
through 265, 268, 270, 271, and 124. In
addition, liquid and accumulated solid
residues that are removed from an ECF
tank system after the tank system ceases
to be operated for storage of ECF are
solid wastes subject to regulation as
hazardous waste if the waste exhibits a
characteristic of hazardous waste under
§§ 261.21–261.24 or if the ECF was
derived from a hazardous waste listed
under §§ 261.31–261.33 when the
exclusion was claimed.
Finally, we are not proposing to adopt
§ 264.196(e)(4) because that paragraph
addresses tanks that are not equipped
with secondary containment. We are
proposing that all ECF tanks must be
equipped with secondary containment
prior to managing ECF.
d. Air Emissions. As mentioned
above, ECF can contain higher levels of
certain hazardous, volatile
hydrocarbons and oxygenates than
found in fuel oil. In this regard, ECF is
more analogous to organic liquids
typically present in organic chemical
production operations than they are to
fuel oil. Therefore, we believe it
appropriate to condition the exclusion
on meeting air emission controls which
apply to those organic liquids to prevent
the release of one or more of these
chemicals to the environment. To this
end, we are proposing to adopt virtually
all of the provisions of the National
Emission Standards for Hazardous Air
Pollutants (NESHAP) for Organic
Liquids Distribution (OLD) under
Subpart EEEE, Part 63 as RCRA § 261.38
conditions to control the fugitive air
emissions from ECF tank systems.85
Note that there are no provisions of this
proposed rule that would impose new
or additional CAA Title V obligations on
ECF generators or burners.
ECF would already be subject to the
OLD NESHAP if certain applicability
requirements are met, including: (1) The
facility must be a major source; (2) the
ECF must contain greater than 5% of the
organic HAP listed in Table 1 to Subpart
EEEE; (3) the facility is not subject to
another NESHAP; 86 and (4) certain tank
size and HAP vapor pressure criteria are
met. Thus, we are proposing not to
85 This subpart establishes emission limitations,
operating limits, and work practice standards for
organic hazardous air pollutants (HAP) emitted
from organic liquids distribution (OLD) (nongasoline) operations at major sources of HAP
emissions for facilities that are not subject to
another NESHAP. This subpart also establishes
requirements to demonstrate initial and continuous
compliance with the emission limitations, operating
limits, and work practice standards.
86 The subpart EEEE controls are intended to be
generic, catch-all controls for air emissions from
storage and transfer of organic liquids at facilities
that are not already subject to a specific NESHAP.
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apply the OLD controls—that we are
proposing to adopt under § 261.38 87—to
ECF tanks that are subject to the OLD
controls under § 63.2346, with one
exception. We are proposing to apply
adopted conditions for any ECF tanks
that would not be subject to the controls
provided by item 6 in Table 2 to Subpart
EEEE because the vapor pressure of the
regulated organic HAP does not exceed
76.6 kPa. Specifically, item 6 in Table
2 provides controls for existing and new
tanks with a capacity greater than 5,000
gallons if the organic liquid has an
annual average true vapor pressure of
the organic HAP listed in Table 1 to
Subpart EEEE equal to or greater than
76.6 kilopascals (kPa). However, 16
RCRA oxygenates 88 for which
comparable fuel specifications have
been established in Table 1 to § 261.38
are not listed as CAA hazardous air
pollutants in Table 1 to Subpart EEEE
(reflection CAA section 112(b)(1)).
Further, 11 of these oxygenates have
vapor pressures that could contribute
significantly to the total vapor pressure
of hazardous organics in ECF.89 Thus,
these RCRA oxygenates could
potentially increase the vapor pressure
of the ECF so that it exceeds 76.6 kPa,
the criterion for requiring more stringent
controls under item 6 in Table 2 to
Subpart EEEE. For this reason, we
propose to specify that tanks which are
subject to OLD but that are not subject
to the requirements under item 6 in
Table 2 to Subpart EEEE must consider
the vapor pressure of the 11 RCRA
oxygenates that have vapor pressures
that could significantly contribute to the
total vapor pressure, as well as the
87 As discussed later in the text in this section,
we are proposing to adopt under § 261.38 for ECF
tank systems virtually all of the Subpart EEEE OLD
provisions.
88 These compounds are Allyl alcohol (CAS No.
107–18–6), Bis(2-ethylhexyl)phthalate [Di-2ethylhexyl phthalate] (CAS No.117–81–7), Butyl
benzyl phthalate (CAS No. 85–68–7), Diethyl
phthalate (CAS No. 84–66–2), 2,4-Dimethylphenol
(CAS No. 105–67–9), Dimethyl phthalate (CAS No.
131–11–3), Di-n-octyl phthalate (CAS No. 117–84–
0), Endothall (CAS No. 145–73–3), Ethyl
methacrylate (CAS No. 97–63–2), 2-Ethoxyethanol
[Ethylene glycol monoethyl ether] (CAS No. 110–
80–5), Isobutyl alcohol (CAS No. 78–83–1),
Iosafrole (CAS No. 120–58–1), Methyl ethyl ketone
[2-Butanone] (CAS No. 78–93–3), 1,4Naphthoquinone (CAS No. 130–15–4), Propargyl
alcohol [2-Propyn-1-ol] (CAS No. 107–19–7), and
Safrole (CAS No. 94–59–7).
89 Five oxygenates—butyl benzyl phthalate,
diethyl phthalate, dimethyl phthalate, di-n-octyl
phthalate, and endothall—have vapor pressures in
the range of 0.0000002 to 0.001 kPa at 25 C and
would not likely contribute significantly to
exceeding the 0.7 kPa threshold defining an organic
liquid, or to changing the vapor pressure category
for the organic liquid that could result in more
stringent controls. See USEPA, ‘‘Draft Technical
Support Document for Expansion of the
Comparable Fuel Exclusion,’’ May 2007, Section
2.2.
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organic HAP listed in Table 1 to Subpart
EEEE in determining whether the vapor
pressure would be equal to or exceed
76.6 kPa. See proposed
§ 261.38(c)(1)(ii)(C)(1)(ii). If so, we are
proposing that the tank must comply
with the § 261.38 adopted OLD
requirements for tanks storing organic
liquids with a vapor pressure equal to,
or exceeding, 76.6 kPa. We specifically
request comment on this proposed
condition. In addition, although we
believe that there would be very few
ECF tanks that would be placed in this
circumstance, we specifically request
comment on how to avoid dual CAA
and RCRA regulation of any such
tanks—tanks that are already subject to
OLD as promulgated at Subpart EEEE,
Part 63, but which would also need to
comply with (more stringent) OLD
requirements adopted under RCRA
§ 261.38 as a condition for the ECF
exclusion.
For tanks that are not already subject
to the OLD controls under § 63.2346, we
are proposing to adopt appropriate
Subpart EEEE provisions under § 261.38
as a condition of the ECF exclusion. See
discussion below where we propose to
adopt virtually all of the Subpart EEEE
provisions. These adopted provisions
would in no way affect Subpart EEEE
and would be implemented and
enforced under RCRA authority (e.g.,
controls under the adopted provisions
would not be included in a facility’s
Title V permit, and a facility would not
be required to obtain a Title V permit to
comply with these provisions).90 Our
principles for proposing to adopt the
OLD provisions under § 261.38 include:
(1) Air emissions from ECF tanks should
be controlled to a level comparable to
levels currently required given that air
emissions from storage and handling of
ECF can pose the same hazards as
storage and handling of the hazardous
waste; and (2) the 11 hazardous RCRA
oxygenates that have significant vapor
pressure, as discussed above, should be
considered as well as the organic HAP
in Table 1 to Subpart EEEE in
determining whether ECF meets the
OLD definition of organic liquid and in
determining the level of control
specified by Table 2 to Subpart EEEE.
We discussed above that 11 of the
hazardous RCRA oxygenates for which
the comparable fuel specifications
would no longer apply and that are not
classified as CAA HAP can potentially
contribute significantly to the vapor
pressure of ECF. Given that vapor
pressure of the hazardous organic
90 Moreover, there are no provisions of this
proposed rule that would impose new CAA Title V
obligations.
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constituents is a criterion for
determining whether the ECF meets the
OLD definition of organic liquid (which
we propose to adopt in revised form
under § 261.38(c)(1)(ii)(C) as discussed
below) and the level of emission control
required under § 63.2346 (which we
also propose to adopt), it is appropriate
to require owners and operators to
consider these 11 RCRA oxygenates
when complying with the adopted OLD
provisions.
We also reviewed the OLD provisions
to determine whether the controls
would be comparable to those currently
required for the hazardous waste from
which the ECF will be derived.
Assurance of comparable controls is
warranted given that air emissions from
storage and handling of ECF can pose
the same hazards as storage and
handling of the parent hazardous waste.
We determined that adopting the OLD
provisions would result in air emission
controls comparable to current controls
in most situations, with four exceptions:
(1) ECF tanks at facilities that are area
sources; (2) existing, reconstructed, or
new ECF tanks with a capacity less than
5,000 gallons handling ECF with a
RCRA oxygenate and organic HAP vapor
pressure equal to or greater than 76.6
kPa; (3) existing ECF tanks with a
capacity in the range of 5,000 gallons to
50,000 gallons handling ECF with a
RCRA oxygenate and organic HAP vapor
pressure in the range of 5.2 kPa to 76.6
kPa; and (4) ECF tanks at facilities that
are subject to a NESHAP other than
Subpart EEEE, unless the tanks at these
facilities have comparable air emission
controls.91 We are proposing to adopt
the OLD provisions under § 261.38 in a
manner that addresses these situations
and thus ensures adequate control of air
emissions from ECF tanks. We
specifically request comment on these
proposed conditions:
• The OLD provisions apply only to
major sources.92 Although we do not
believe that many ECF tanks will be
located at area sources given that we
expect the manufacturing sector to
generate and burn the majority of the
ECF, controls should be maintained at
facilities that may be area sources.
Consequently, we propose to apply the
adopted OLD controls to both area and
91 Also, as discussed previously in this section,
we may regulate, in certain instances, tanks that
store or handle ECF that would not be subject to
the controls provided by item 6 in Table 2 to
Subpart EEEE because the vapor pressure of the
regulated organic HAP does not exceed 76.6 kPa.
92 A major source is a facility that emits, facility
wide, more than 10 tons per year of any single HAP
or 25 tons per year of HAP in the aggregate. An
affected source is an area source if it is located at
a facility that is not a major source.
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major sources. See proposed
§ 261.38(c)(1)(ii)(C)(2)(i);
• OLD does not require controls for
the two tank size/vapor pressure
scenarios listed above, while
substantive tank air emission controls
(under § 264.1084) are required for the
hazardous waste from which the ECF is
derived. Consequently, we propose to
apply the adopted OLD controls as
conditions for ECF tanks with those two
tank size/vapor pressure scenarios so
that they comply with the same OLD
controls applicable to tanks with a
capacity greater than 5,000 gallons and
a vapor pressure below 76.6 kPa. See
proposed § 261.38(c)(1)(ii)(C)(2)(vii);
and
• As mentioned above, the OLD
provisions do not apply to storage and
handling of organic liquids at facilities
that are subject to another NESHAP.
This is the case irrespective of whether
the other NESHAP establishes controls
for air emissions from organic liquid
distribution. Consequently, we propose
to apply the adopted OLD controls to
tanks (and associated equipment) at ECF
tanks at a facility subject to another
NESHAP, unless the owner/operator
documents that the controls (on tanks
that store or handle ECF) provided by
the other NESHAP are at least
equivalent to the controls adopted from
OLD for ECF. See proposed
§ 261.38(c)(1)(ii)(C).
In addition, we are proposing
conforming changes to implement the
provisions discussed above, and
specifically request comment on these
proposed provisions. Specifically:
• To implement consideration of the
RCRA oxygenates, substitute the term
‘‘RCRA oxygenates as well as organic
HAP’’ for each occurrence of the term
‘‘organic HAP’’; the term ‘‘RCRA
oxygenates as well as organic HAP
listed in Table 1’’ for each occurrence of
the term ‘‘organic HAP listed in Table
1’’; and the term ‘‘RCRA oxygenates as
well as Table 1 organic HAP’’ for each
occurrence of the term ‘‘Table 1 organic
HAP.’’ See proposed
§ 261.38(c)(1)(ii)(C)(2)(ii).
• To implement consideration of
RCRA oxygenates, we are proposing to
adopt the following definition of organic
liquid—Organic liquid means emissioncomparable fuel that: (1) Contains 5
percent by weight or greater of the
RCRA oxygenates as well as organic
HAP listed in Table 1 to this subpart, as
determined using the procedures
specified in § 63.2354(c); and (2) has an
annual average true vapor pressure of
0.7 kilopascals (0.1 psia) or greater. See
proposed § 261.38(c)(1)(ii)(C)(2)(iv).
• Defining an affected source as the
collection of activities and equipment
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used to distribute emission-comparable
fuel into, out of, or within a facility.
This would simplify the Part 63
definition of affected source for
purposes of the OLD provisions we
propose to adopt under § 261.38. See
proposed § 261.38(c)(1)(ii)(C)(2)(v); and
• Substituting the term ‘‘subject to
§ 261.38(c)(1)(ii)(C)(3) of this chapter’’
for the term ‘‘subject to this subpart’’ to
facilitate implementation of the adopted
OLD provisions. See proposed
§ 261.38(c)(1)(ii)(C)(2)(vi).
Finally, we are proposing that all
notifications, reports, and
communications required to implement
the OLD provisions that we adopt under
§ 261.38 be submitted to the RCRA
regulatory authority rather than the
CAA regulatory authority. This is
because the conditions for air emission
controls are RCRA provisions adopted
from the CAA OLD NESHAP. As such,
they should be implemented (and
enforced) under RCRA authority. We
specifically request comment on this
proposed provision.
As mentioned above, we propose to
adopt virtually all of the provisions of
the OLD NESHAP as RCRA conditions
to control air emissions from storage
and handling of ECF.93 See proposed
§ 261.38(c)(1)(ii)(C)(3). We believe the
implementation requirements (e.g.,
notifications, reports, testing) are
integral to the substantive emission
controls and are necessary for
compliance assurance.
We acknowledge that this attempt to
adopt the provisions of the OLD
NESHAP to cover ECF tanks
substantially complicates the conditions
of the ECF exclusion. This is primarily
because the OLD NESHAP does not
address hazardous RCRA oxygenates
that have significant vapor pressure, and
the OLD NESHAP does not address ECF
tanks that are currently subject to
hazardous waste tank air emission
controls that address hazards that
remain after the ECF exclusion is
claimed. In retrospect, stakeholders may
conclude it is less problematic to simply
comply with the controls provided for
hazardous waste tanks under Subparts
AA, BB, and CC of Part 264 or 265. We
specifically request comment on: (1)
Whether adopting provisions of the OLD
NESHAP as conditions of the ECF
93 Note
that we are not proposing to adopt
§ 63.2343, What Are My Requirements for Emission
Sources Not Requiring Control? This section
establishes notification, recordkeeping, and
reporting requirements for emissions sources not
currently subject to control under Subpart EEE. We
do not believe those controls are necessary given
that ECF burners and generators must comply with
the conditions of the exclusion (and thus the
adopted OLD provisions) when they first manage
ECF in a tank, tank car, or tank truck.
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exclusion is appropriate to address the
hazards posed by fugitive air emissions
from storage and handling of ECF; (2)
whether adopting the OLD NESHAP
provisions in the manner proposed is
appropriate; and (3) whether it would be
equally protective, but less problematic,
to simply comply with the air emission
controls for hazardous waste tanks in
lieu of the adopted OLD NESHAP
provisions. Any such comments must
include an appropriate rationale and
supporting information in order for the
Agency to be able to consider it for final
action.
2. Underground Storage Tank Systems
ECF storage tank systems that are
subject to the requirements under 40
CFR Part 280, Technical Standards and
Corrective Action Requirements for
Owners and Operators of Underground
Storage Tanks would not be subject to
the proposed ECF storage tank
conditions.94 The Part 280 requirements
are self-implementing and apply to
hazardous substances listed in 40 CFR
Part 302.4 which are not hazardous
wastes. All of the hydrocarbons and
oxygenates for which the comparable
fuel specifications would be waived for
ECF are included on this list of
hazardous substances. Thus, the Part
280 requirements would apply to all
ECF storage tank systems that meet the
§ 280.12 definition of underground
storage tank. However, the Agency does
request information on whether ECF is
or would be stored in underground
storage tanks or whether, because of the
size of these tanks or other factors, ECF
would only be stored in above ground
storage tanks, tank cars and tank trucks.
If so, the Agency solicits comment on a
condition that would prohibit the
storage of ECF in underground storage
tanks.
3. Closure of Tank Systems
If an ECF tank system, tank car, or
tank truck ceases to be operated to store
ECF product, but has not been cleaned
by removing all liquids and
accumulated solids within 90 days of
cessation of ECF storage operations, the
tank system, tank car, and tank truck
would become subject to the RCRA
94 We request comment, however, on whether
owners and operators of ECF tanks subject to the
Part 280 requirements for underground storage
tanks should also need to control fugitive air
emissions as proposed as a condition of the ECF
exclusion for storage in other tank systems.
Similarly, we request comment on whether owners
and operators of such tanks should also need to
comply with the preparedness and prevention and
emergency procedures provisions we propose as a
condition of the ECF exclusion for storage in other
tanks.
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Subtitle C regulation.95 96 See proposed
§ 261.38(b)(13). This provision is
modeled on § 261.4(c) which states:
A hazardous waste which is generated in
a product or raw material storage tank, a
product or raw material transport vehicle or
vessel, a product or raw material pipeline, or
in a manufacturing process unit or an
associated non-waste-treatmentmanufacturing unit, is not subject to
regulation under parts 262 through 265, 268,
270, 271 and 124 of this chapter or to the
notification requirements of section 3010 of
RCRA until it exits the unit in which it was
generated, unless the unit is a surface
impoundment, or unless the hazardous waste
remains in the unit more than 90 days after
the unit ceases to be operated for
manufacturing, or for storage or
transportation of product or raw materials.
Thus, like any other product storage
unit which goes out of service, tank
systems, tank cars or tank trucks that
store or transport ECF would not be
required to undergo closure according to
the RCRA hazardous waste regulations
(unless liquids or accumulated solids
were not cleaned from the tank system
within 90 days of cessation of operation
as an ECF storage/transportation unit),
when the unit ceases operation as a
product storage/transportation unit.
However, the Agency expects that the
owner/operators will take commonsense steps to decontaminate and
decommission the ECF storage unit if
and when it goes out of service. We also
encourage the owner/operators in these
situations to consult with the regulatory
authority as to the best way to ensure
that the unit is cleaned properly.
Liquids and accumulated solids
removed from a tank system, tank car,
or tank truck that ceases to be operated
for storage/transport of ECF product are
solid wastes. They are hazardous waste
if they exhibit a characteristic of
hazardous waste or if the ECF were
derived from a listed hazardous waste
because the ECF is no longer meeting
the conditions of the exclusion.
4. Waiver of RCRA Closure for RCRA
Tanks That Become ECF Tanks
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Interim status and permitted storage
units, and generator accumulation units
exempt from permit requirements under
§ 262.34 of this chapter, are currently
subject to the closure requirements in 40
CFR Parts 264 and 265, including the
95 We are also proposing today to clarify that this
provision currently applies to currently excluded
comparable fuel.
96 If the tank is used to actively accumulate
hazardous waste after being taken out of service as
an ECF (or comparable fuel) product tank, the tank
may be eligible for the provisions under § 262.34
that waive the permit requirements for generator
tanks that accumulate hazardous waste for not more
than 90 days.
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requirement to close the unit within 90
days of receiving the final volume of
hazardous waste (see 264.113(a) and
265.113(a)). However, we are proposing
in this rulemaking not to subject these
units to these closure requirements
provided that the storage units have
been used to store only hazardous waste
that is subsequently excluded under the
conditions of § 261.38, and that
afterward will be used only to store fuel
excluded under § 261.38. See proposed
§ 261.38(b)(14).97
This provision is intended to address
situations where units such as tanks that
have been used to store hazardous
wastes, would be required under the
existing regulations to go through RCRA
closure before storage of the excluded
material could commence. In the case of
facilities that would be affected by
today’s proposed rule, this would mean
that, for tanks that have been storing
hazardous waste for which the generator
claims an ECF exclusion, the owner/
operator would need to remove all
waste residues and other contamination
from the tank system in order for the
unit to then commence storing the
identical material under the terms of the
conditional exclusion for ECF. We
believe that requiring closure under
these circumstances would serve little,
if any, environmental purpose, and so
propose to explicitly provide in these
situations that the storage tank system
would not be subject to RCRA closure
requirements. As discussed above,
however, although an ECF tank system
would not be required to undergo
closure according to the RCRA
hazardous waste regulations, the
Agency expects that the owner/
operators will take common-sense steps
to decontaminate and decommission the
tank system if and when it ultimately
ceases to operate as an ECF storage tank
system. We also note that tank cars/
trucks need not meet the definition of
an empty HW container before
managing the same material as ECF (if
that is the only material the container
has managed).
5. Management of Incompatible Waste
Fuels and Other Materials
In today’s proposal, ECF generators
would need to take precautions to
prevent the mixing of ECF and other
materials which could result in
reactions which could: (1) Generate
extreme heat or pressure, fire or
explosions, or violent reactions; (2)
produce uncontrolled hazardous mists,
97 This proposed provision mirrors the parallel
provision for storage units managing zinc-bearing
hazardous wastes where the wastes were
subsequently excluded as zinc fertilizer. See
§ 261.4(a)(20)(v) and 67 FR at 48400 (July 24, 2002).
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fumes, dusts, or gases; (3) produce
uncontrolled flammable fumes or gases;
or (4) damage the structural integrity of
the storage unit or facility. See proposed
§ 261.38(c)(1)(iv). Appropriate
documentation is also proposed to be
kept by ECF generators to document
how they will take precautions to avoid
these situations. This documentation
must be kept on-site for three years.
Tanks, tank cars and tank trucks holding
incompatible materials should be
separated by means of a dike, berm, wall
or other device.
B. What Other Options Did We
Consider?
1. Other Options We Considered To
Establish Storage Conditions for ECF
In evaluating possible storage controls
for ECF, we considered two other
options. One option would impose no
specific new controls, but rather would
rely on currently applicable controls for
commercial products. The other option
would apply full RCRA Subtitle C
provisions until the ECF leaves the
burner storage system—that is, the
waste would remain hazardous until it
was fed into the boiler.
In considering the first option, we
determined that it would be difficult to
assure the safe management of ECF
because it is not clear what, if any,
existing controls would apply to a
hazardous waste that becomes an
excluded product/fuel. There is a
patchwork of Federal and State controls
that apply to various products and fuels,
but no one set of controls that we would
be confident would apply across the
board and ensure that ECF would be
properly managed, particularly given
that ECF can contain higher
concentrations of particular hazardous,
volatile hydrocarbons and oxygenates.
We also believe it would complicate the
implementation of this rule, and
persons who handled ECF would not
necessarily know what conditions must
be followed to assure exclusion of the
ECF. Consequently, we did not consider
this option further.
The other option we considered,
applying RCRA Subtitle C provisions
until the ECF leaves the burner storage
system, would in effect, move the point
of exclusion to the ECF boiler. Storage
and transportation of ECF would be
subject to Subtitle C standards (which
could include permits for burner storage
units and for those generators that
accumulate ECF for more than 90 days).
We believe this option would be
inappropriate because it would
overregulate a material that has
substantial fuel value and is
inconsistent with the idea that ECF is an
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excluded product, rather than a waste
material. See Safe Food and Fertilizer,
350 F. 3d at 1269 (exclusion based on
comparability can extend back to
encompass exclusion of the material
when stored). We believe that our
tailored management conditions
adopted from the SPCC requirements,
and engineered secondary containment,
along with the conditions related to
control of fugitive air emissions, are
more appropriate for ECF because they
reflect requirements to which analogous
commercial products are subject.
2. Consideration of Storage Controls for
Currently Excluded Comparable Fuels
As a separate issue, we considered
whether to propose storage conditions
for the currently excluded comparable
fuel. The existing comparable fuel
exclusion was promulgated in June 1998
and was not conditioned on meeting
any particular storage controls. The
comparable fuel exclusion was based on
the principle that the excluded fuel
would be comparable to fuel oil in
concentration of hazardous constituents
and physical properties that affect
combustion, and thus can pose the same
hazards as fuel oil during storage.
Comparable fuel does not meet the
definition of oil, however, and so is not
subject to the SPCC requirements
applicable to fuel oil. See 40 CFR Part
112. Consequently, we considered
whether to propose to apply the SPCC
requirements to comparable fuel. We do
not believe that applying the SPCC
controls is warranted at this time
because we are not aware of evidence of
improper storage of these comparable
fuels. Nonetheless, we request comment
on whether there is evidence of
improper storage of comparable fuel and
whether the SPCC controls (or other
storage controls) should be included as
a condition for the existing comparable
fuel exclusion.
V. How Would We Assure That the
Conditions Are Being Satisfied?
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A. What Recordkeeping, Notification
and Certificate Conditions Would Apply
to Generators and Burners?
We believe it is appropriate to
propose that ECF generators and burners
satisfy the same recordkeeping,
notification and certification conditions
that apply to existing comparable fuel
generators and burners, as well as
additional conditions that reflect that
ECF is not physically identical to
comparable fuels. In today’s preamble,
we provide a brief description of our
rationale for proposing these provisions
as part of the exclusion. However,
persons should also refer to the
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1. Waste Analysis Plans
We are proposing the same waste
analysis plan conditions for ECF as
existing comparable fuel because ECF
must also meet all of the specifications
for comparable fuel, except the
specifications for particular
hydrocarbons and oxygenates. See
existing § 261.38(c)(7) renumbered as
proposed § 261.38(b)(4). These
conditions require that generators
develop a waste analysis plan prior to
sampling and analysis of their ECF to
determine if the waste fuel meets the
exclusion specifications.
In addition, burners of ECF would
need to address a number of the other
conditions to ensure that the ECF is in
compliance with the exclusion.
Specifically, burners would need to
ensure that the heating value of the fuel,
as-fired, is 8,000 Btu/lb, as well as
whether the concentration of benzene or
acrolein exceeds two percent, the
cutpoint for firing rate restrictions on
the ECF. If the generator does not
provide this information to the burner
for each shipment of ECF, today’s
proposal would require the burner to
develop and implement an ECF waste
analysis plan to obtain the information.
In addition, if a burner blends or treats
ECF to achieve an as-fired heating value
of 8,000 Btu/lb or greater or an as-fired
concentration of benzene or acrolein of
two percent or lower, we are proposing
that the burner must analyze the fuel as
received from the generator and again
after blending or treatment to determine
the heating value, benzene
concentration, or acrolein
concentration, as relevant. See proposed
§ 261.38(b)(5).
The generator (and burners required
to develop a sampling and analysis
plan) also must have documentation of
the: (1) Sampling, analysis, and
statistical analysis protocols that were
employed; (2) sensitivity and bias of the
measurement process; (3) precision of
the analytical results for each batch of
waste/fuel tested; and (4) results of the
statistical analysis. More information on
developing these elements of a waste/
fuel analysis plan is found in the SW–
846 guidance document. These are the
same requirements that exist in the
existing comparable fuels exclusion
waste analysis plans.
hydrocarbons and oxygenates.
Therefore, we are proposing the same
conditions regarding sampling and
analysis for ECF that are part of the
existing comparable fuel exclusion,
except the condition to determine the
concentrations of particular
hydrocarbons and oxygenates.98
The sampling and analysis provisions
allow process knowledge to be used
under certain circumstances to
determine which constituents to test for
in the initial scan and any follow up
testing. Generators of ECF should have
adequate knowledge of this hazardous
secondary material to allow the use of
process knowledge in determining
which constituents may and may not be
present in their waste. The use of
process knowledge may only be used by
the original generator of the hazardous
waste. We are proposing that testing be
required for all constituents, except the
particular hydrocarbons and oxygenates
for which the specifications do not
apply, and those compounds that the
initial generator determines are not
present in the waste. We are also
proposing that the following cannot be
determined to ‘‘not be present’’ in the
waste: (1) A hazardous constituent that
causes it to exhibit the toxicity
characteristic for the waste or hazardous
constituents that were the basis for the
waste code in 40 CFR 268.40; (2) a
hazardous constituent detected in
previous analysis of the waste; (3) a
hazardous constituent introduced into
the process that generates the waste; or
(4) a hazardous constituent that is a
byproduct or side reaction to the
process that generates the waste. This
condition is also in the existing
comparable fuels exclusion.
Furthermore, we are proposing that
the original generator has the
responsibility to document their claim
that specific hazardous constituents
meet the exclusion specifications based
on process knowledge. Regardless of
which method a generator uses, testing
or process knowledge, the generator is
responsible for ensuring that the ECF
meets all constituent specifications at
all times. If at any time the ECF fails to
meet any of the specifications, or other
conditions contained in the proposed
exclusion, any facility that treats
(including burning in a boiler), stores or
disposes of the ECF is in violation of
Subtitle C hazardous waste
requirements.
2. Sampling and Analysis
As discussed above, we are proposing
that ECF must meet all of the
specifications for comparable fuel,
except the specifications for particular
98 Although the specifications for benzene and
acrolein would not apply, the generator (or the
burner) must determine the concentration of these
compounds because we propose ECF firing rate
restrictions for ECF containing more than two
percent of either of these compounds.
proposed rule for comparable fuels (see
61 FR 17358) and the final rule (see 63
FR 33782) for further discussion.
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3. Speculative Accumulation
We are proposing to adopt for ECF the
same speculative accumulation
provisions that apply to existing
comparable fuel and to any recycled
hazardous waste under § 261.2(c)(4). See
proposed § 261.38(b)(7). Generators and
burners must actually put a given
volume of the fuel to its intended use
during a one-year period, namely 75
percent of what is on hand at the
beginning of each calendar year
commencing on January 1. See also the
definition of ‘‘accumulated
speculatively’’ in § 261.1(c)(8).
Prohibiting speculative accumulation is
warranted because over-accumulation of
hazardous waste-derived recyclables has
led to severe hazardous waste damage
incidents. See 50 FR at 658–61 and 634–
37 (January 4, 1985). There is no formal
recordkeeping requirement associated
with the speculative accumulation
provision, but the burden of proof is on
the generator and burner to demonstrate
that the material has not been
speculatively accumulated.99
4. Notifications
We are proposing the same
notification requirements for ECF
generators that comparable fuel
generators must comply. Also, ECF
burners would be subject to the same
notification conditions as comparable
fuel burners, as well as additional
notification conditions.
a. ECF Generator Notification. The
person claiming that a hazardous waste
meets the exclusion criteria for ECF
would be the ECF generator. The ECF
generator need not be the person who
originally generates the hazardous
waste, but can be the first person who
documents and certifies that a specific
hazardous waste meets the exclusion
criteria.
Just as for comparable fuel generators,
we are proposing that an ECF generator
submit a one-time notification to
regulatory officials (i.e., State RCRA and
CAA officials). To be excluded, the
generator must send a notification to the
EPA Regional RCRA and CAA Directors
in States without final RCRA program
authorization, and to the State RCRA
and CAA Directors in authorized States.
Notification of the RCRA and CAA
Directors will provide notification of the
exclusion and appropriate
documentation to both the RCRA and
CAA implementing officials. The
Agency’s intent is for the notification to
be sent to both the RCRA and CAA
99 Consult § 261.2(f) and 50 FR at 636–37 placing
the burden for documenting conformance with
conditions of an exclusion on the person claiming
the exclusion in an enforcement action.
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implementing officials because of the
nature of this exclusion—a RCRA
excluded waste being burned in the
CAA regulated unit. Also, if the ECF is
burned in a State other than the
generating State, then we are proposing
that the ECF generator also provide
notification to that State’s or Region’s
RCRA and CAA Directors.
Since this would be a selfimplementing exclusion, in order to
ensure delivery, we are proposing that
the notification be sent by certified mail,
or other mail service that provides
written confirmation of delivery and
until the notification of exclusion is
received and the ECF generator is
informed of such receipt, the waste is
still a hazardous waste and must be
managed as such. Only after the receipt
of such notification by the regulatory
officials would the hazardous waste be
excluded, provided it was managed in
accordance with the conditions
proposed today for ECF. If an ECF loses
the exclusion, the waste fuel is subject
to regulation as a hazardous waste until
it returns to compliance with the
conditions and a new notification is
provided by the generator or another
subsequent handler.
Just as for the one-time generator
notification in the existing comparable
fuels exclusion, we are proposing that
the notification contain the following
information: (1) The name, address, and
RCRA ID number of the person/facility
claiming the exclusion; (2) the
applicable EPA Hazardous Waste Codes
for the ECF if it were not excluded from
the definition of solid waste; (3) the
name and address of the units, meeting
the requirements of proposed
§ 261.38(c)(2), that will burn the ECF;
and (4) the following statement signed
and submitted by the person claiming
the exclusion or his authorized
representative:
Under penalty of criminal and civil
prosecution for making or submitting false
statements, representations, or omissions, I
certify that the requirements of 40 CFR
261.38 have been met for all emissioncomparable fuel/comparable fuel (specify
which) identified in this notification. Copies
of the records and information required at 40
CFR 261.38(b)(8) are available at the
generator’s facility. Based on my inquiry of
the individuals immediately responsible for
obtaining the information, the information is,
to the best of my knowledge and belief, true,
accurate, and complete. I am aware that there
are significant penalties for submitting false
information, including the possibility of fine
and imprisonment for knowing violations.
b. ECF Burner Notifications. We are
proposing that the ECF Burner would
provide the same public notification as
required for existing comparable fuel
burners, as well as a one-time, initial
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notification to the regulatory authority.
For the public notification, the burner
must submit for publication in a major
newspaper of general circulation local
to the site where the ECF will be
burned, a notice entitled ‘‘Notification
of Burning of Emission Comparable Fuel
Excluded Under the Resource
Conservation and Recovery Act’’
containing the following information:
(1) Name, address, and RCRA ID
number of the generating facility; (2)
name of the unit(s) that will burn the
ECF; (3) a brief, general description of
the manufacturing, treatment, or other
process generating the emission
comparable fuel; (4) an estimate of the
average and maximum monthly and
annual quantity of ECF that will be used
as a fuel in such units; and (5) name and
mailing address of the State or Regional
Directors to whom the notification is
being submitted. This notification must
be published in the newspaper prior to
the use of the ECF, and is only
necessary once for each material. In
addition, to be excluded, we are also
proposing that the ECF burner submit a
one-time initial notification to
regulatory officials (proposed
§ 261.38(c)(4)(i)). The one-time
notification would require that the
burner certify that the excluded fuel
will be stored under the conditions
required by this rule and that the burner
will comply with the design, operating,
notification, reporting and
recordkeeping requirements of this rule.
This initial notification would facilitate
compliance assurance by alerting the
regulatory authority that the burner is
subject to substantive conditions of the
exclusion and by ensuring that the
burner is aware of those conditions.
5. Burner Certification
We are proposing the same burner
certification for ECF burners as exist for
comparable fuel with a few additional
conditions. This burner certification is
intended to protect the generator by
having the ECF burner certify to the
generator that he will comply with all
applicable storage and burning
conditions. Specifically, generators
intending to ship the ECF off site for
burning would obtain a one-time
written, signed statement from the
burner that includes the following: A
certification that the burner will comply
with the storage conditions, burner
conditions, and the notification,
reporting, recordkeeping and other
conditions of the exclusion of ECF
under 40 CFR 261.38; the name and
address of the facility that will use the
ECF as a fuel; and a certification that the
state in which the burner is located is
authorized to exclude wastes as
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excluded fuels under (proposed) 40 CFR
261.38(a)(2). This condition coupled
with the condition to notify the State or
Regional Directors will enable
regulatory officials to take any measure
that may be appropriate to ensure that
excluded fuel is burned in conformance
with the applicable regulations and so
does not become part of the waste
management problem.
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6. Recordkeeping
a. General. We are proposing the same
recordkeeping conditions for ECF
generators that currently apply to
comparable fuel generators. In addition,
we are proposing a condition that ECF
burners keep any records pertaining to
the sampling and analysis of the ECF.100
The Agency believes that because of the
self-implementing nature of this
exclusion, maintenance of proper
information on-site is essential to the
proper implementation of the
conditional exclusion.
More specifically, we are proposing
that ECF generators maintain the
following files (see proposed § 261.38
(b)(8)) at the facility generating the fuel:
(1) All information required to be
submitted to the State RCRA and CAA
Directors as part of the notification of
the claim of exclusion; (2) a brief
description of any process used to
convert the hazardous waste to ECF; (3)
an estimate of the average and
maximum monthly and annual
quantities of each hazardous waste
claimed to be excluded; (4)
documentation for any claim that a
constituent is not present in the
hazardous waste pursuant to
§ 261.38(b)(8)(iv); (5) the results of all
fuel analyses with quantitation limits;
(6) documentation as required for the
treatment or blending of a waste to meet
the exclusion specifications 101; (7) a
certification from the burner if the
excluded fuel is to be shipped off-site;
and (8) the certification signed by the
person claiming the exclusion or his
authorized representative. The ECF
generator would also maintain
documentation of the waste analysis
plan and the results of the sampling and
analysis that includes the following: (1)
100 We are proposing that ECF burners who are
required to sample and analyze ECF to determine
the heating value of the ECF or the concentration
of benzene or acrolein, if the generator has not
provided that information for each shipment, must
keep the same records as ECF generators regarding
the sampling and analysis plan and the results of
sampling and analysis.
101 ECF can be blended in order to meet the
viscosity specification. Records would have to be
kept demonstrating that the ECF met all other
specifications besides viscosity before blending.
ECF can also be treated to meet the specifications.
In that case, records would have to be kept that
demonstrate bona fide treatment has occurred.
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The dates and times waste samples were
obtained, and the dates the samples
were analyzed; (2) the names and
qualifications of the person(s) who
obtained the samples; (3) a description
of the temporal and spatial locations of
the samples; (4) the name and address
of the laboratory facility at which
analyses of the samples were performed;
(5) a description of the analytical
methods used, including any clean-up
and sample preparation methods; (6) all
quantitation limits achieved and all
other quality control results for the
analysis, (including method blanks,
duplicate analyses, matrix spikes, etc.),
laboratory quality assurance data, and a
description of any deviations from
analytical methods written in the plan
or from any other activity written in the
plan which occurred; (7) all laboratory
analytical results demonstrating that the
exclusion specifications have been met
for the ECF; and (8) all laboratory
documentation that support the
analytical results, unless a contract
between the claimant and the laboratory
provides for the documentation to be
maintained by the laboratory for the
period specified in § 261.38(b)(9) and
also provides for the availability of the
documentation to the generator upon
request. These records are to assist with
compliance assurance with the required
operating conditions. These records and
those required for off-site shipments
(discussed below) would have to be
maintained for the period of three years.
A generator (and ECF burner, as
applicable) must maintain a current
waste analysis plan during that three
year period.
b. Off-Site Shipments. We are also
proposing that, for each shipment of
ECF a generator sends off-site for
burning, a record of the shipment must
be kept by the generator and by the
burner. We note that a comparable fuel
generator is currently subject to this
condition, and the condition should
apply to an ECF generator for the same
reasons. The Agency believes that the
generator keeping records of each
shipment would help ensure that ECF is
transported to the designated boiler.
Therefore, we are proposing that ECF
generators keep records of the following
information for each off-site shipment,
as currently required for comparable
fuel generators: (1) The name and
address of the facility receiving the ECF
for burning; (2) the quantity of ECF
delivered; (3) the date of shipment or
delivery; (4) a cross-reference to the
record of ECF analysis or other
information used to make the
determination that it meets the
specifications; and (5) the one-time
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33311
certification by the burner. These
records are to facilitate tracking and to
ensure that ECF is shipped to a
designated burner.
In addition, we believe that an ECF
burner should also keep a record of each
shipment to assist with compliance
assurance given that there are
conditions on burning that relate to the
heating value of the ECF and the
concentration of benzene and acrolein.
Accordingly, we are proposing that ECF
burners keep records of the following
information for each shipment received
from an off-site generator: (1) The name,
address, and RCRA ID number of the
generator shipping the ECF; (2) the
quantity of ECF delivered; and (3) the
date of delivery.
Finally, we are proposing that ECF
generators that ship ECF off-site must
ship directly to the burner. ECF could
not be handled by a broker or
intermediate handler. This would help
ensure that the ECF is received by the
generator’s designated burner and stored
under the prescribed conditions prior to
burning. This is important because ECF
can pose greater hazard when stored
than comparable fuel, and may not have
emissions comparable to fossil fuel if
not burned by the designated burner
under the prescribed conditions. ECF
must be burned under the specified
burner conditions to ensure
conformance with the basic principle of
the exclusion—that emissions are
comparable to those from burning fuel
oil.
7. Transportation
We believe that the Department of
Transportation (DOT) requirements,
which govern the transportation of
hazardous materials, will ensure the
safe transportation of ECF. It should be
noted that DOT requirements are selfimplementing and ECF transporters are
required to comply with all applicable
requirements under the DOT regulations
in 49 CFR parts 171 through 180.
8. Ineligible RCRA Hazardous Waste
Codes
Consistent with the current
comparable fuel exclusion, we are not
proposing to restrict the ECF exclusion
to particular waste codes, except that
wastes listed for the presence of dioxins
or furans would not be eligible for the
ECF exclusion. See § 261.38(b)(11).
However, we do not expect that
corrosive or reactive wastes would be
candidates for ECF because of the
detrimental impacts on the burning unit
that would occur.
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B. What If I Fail To Comply With
Conditions of the Exclusion?
It is the responsibility of the generator
claiming the exclusion to demonstrate
eligibility.102 More specifically, to be
eligible for this exclusion, we are
proposing that the person claiming the
exclusion must meet the ECF
specifications under proposed
§ 261.38(a)(2), as well as the other
conditions of the exclusion: the
provisions for achieving the
specifications under proposed
§§ 261.38(a)(4–7); the implementation
requirements under proposed
§ 261.38(b), and the special
requirements for managing ECF under
proposed § 261.38(c).
After the exclusion for a waste has
become effective, the conditions of the
exclusion must continue to be met in
order to maintain the exclusion.103 If
any person managing ECF fails to meet
one or more of the proposed conditions
of the exclusion under § 261.38, we are
proposing that the ECF must be
managed as a hazardous waste.
Therefore, each person who manages
ECF that loses its exclusion would have
to manage it in accordance with the
hazardous waste management
requirements from the point when the
material was first generated, regardless
of whether the person is the one who
actually causes the loss of the exclusion.
EPA could choose to bring an
enforcement action under RCRA section
3008(a) for all violations of RCRA
subtitle C requirements occurring from
the time the secondary material is
generated through the time that it is
ultimately disposed.
We request comment, however, on
whether the final rule should include a
‘‘reasonable efforts’’ provision that
would provide that the failure of an offsite, unaffiliated burner to meet the
proposed conditions or restrictions of
the exclusion would not mean the
material was considered waste when
handled by the generator, as long as the
generator can adequately demonstrate
that he has made reasonable efforts to
ensure that the material will be
managed by the burner under the
conditions of the exclusion.104 To
102 Consult § 261.2(f) placing the burden for
documenting conformance with conditions of an
exclusion on the person claiming the exclusion in
an enforcement action.
103 Separate and distinct from any requirement or
condition that would be established under this
proposed rule, all generators of a solid waste—
including ECF generators under this exclusion—
have a continuing obligation to conduct proper
hazardous waste determinations, including
notifying the appropriate government official if they
are generating a hazardous waste. 40 CFR 262.11.
104 Although a proposed condition of the ECF
exclusion would require the generator to obtain a
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achieve this benefit, the generator
would have to exercise ‘‘environmental
due diligence’’ in reviewing the
operations of the burner in advance of
transferring the hazardous secondary
materials. We believe that a reasonable
efforts provision might involve
methods, such as audits (including site
visits), that a number of generators of
hazardous secondary materials now use
to maintain their commitment to sound
environmental stewardship, and to
minimize their potential regulatory and
liability exposures. These audits are
frequently performed by third parties.
We also request comment on whether
a reasonable efforts provision should
include criteria that define reasonable
efforts, and what those criteria should
be. For example, a reasonable efforts
provision could prescribe that the
generator must evaluate by site visits,
prior to the first shipment and every six
months thereafter, the ECF storage and
boiler design and operation at off-site
unaffiliated facilities (e.g., an off-site
facility that is not corporately affiliated
with the generator) that they do
business with.
In addition, we request comment on
whether to require the generator to
maintain records at the generating
facility documenting the reasonable
efforts made before transferring ECF to
the burner. Such records would
presumably include copies of audit
reports, and/or other relevant
information that was used as the basis
for the generator’s determination that
the burner will manage the material
under the conditions of the exclusion.
Requiring specific documentation
would help EPA or the authorized state
to determine whether the generator did
make reasonable efforts to ensure that
his ECF was managed appropriately.
We also request comment on whether,
as part of the documentation, the
generator should also be required to
maintain at the generating facility a
certification statement, signed and dated
by an authorized representative of the
generator company, that for each burner
to which the generator transferred ECF,
that the generator made reasonable
efforts to ensure that the ECF was
properly managed. Such certification
statement could, for example, be
worded as follows: ‘‘I hereby certify in
good faith and to the best of my
knowledge that, prior to arranging for
transport of excluded hazardous
certification from the burner that the ECF will be
stored and burned under the conditions of the
exclusion, a ‘‘reasonable efforts’’ provision would
require the generator to take reasonable
independent and proactive measures to ensure that
the burner will manage ECF under the conditions
of the exclusion.
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secondary materials to [insert burner
name], reasonable efforts were made to
ensure that the ECF will be managed
under the conditions of the exclusion
found at 40 CFR 261.38, and that such
efforts were based on current and
accurate information.’’
Finally, we also solicit comment on
whether the frequency of periodic
updates of the ‘‘reasonable efforts’’
should be identified in the regulations,
or whether that question should be left
to individual situations applying an
objectively reasonable belief standard.
Information on industry standards for
facility audits of off-site activities,
including how frequently they are
conducted, would be especially helpful.
Under the reasonable efforts
provision, a generator who met his
reasonable efforts obligations might ship
his ECF to an unaffiliated burner where,
due to circumstances beyond the
generator’s control, the burner failed to
comply with the conditions of the
exclusion. In such situations, and where
the generator’s decision to ship to that
burner is based on an objectively
reasonable evaluation that the burner
would manage the ECF under the
conditions of the exclusion consistent
with this proposed rule, the generator
would not have violated the terms of the
exclusion.
C. How Would Spills and Leaks Be
Managed?
ECF that is spilled or leaked, not
cleaned up immediately and no longer
meets the conditions of the exclusion is
‘‘discarded.’’ Thus, it is a solid waste. In
addition, spilled or leaked ECF is a
hazardous waste if it exhibits a
characteristic of hazardous waste or if
the ECF were derived from a listed
hazardous waste.
Furthermore, the exclusion would not
affect the obligation to promptly
respond to and remediate any releases
of ECF that may occur. Management of
the released material not in compliance
with applicable Federal and State
hazardous waste requirements could
result in an enforcement action. For
example, a person who spilled or
released ECF and failed to immediately
clean it up could potentially be subject
to enforcement for illegal disposal of the
waste. See, for example, 40 CFR
264.1(g)(8). In addition, the release
could potentially be addressed through
enforcement orders, such as orders
under RCRA sections 3013 and 7003.
D. What Would Be the Time-Line for
Meeting the Proposed Conditions?
Because this is an optional and
conditional exclusion, we are proposing
that all conditions in § 261.38 must be
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met before ECF may be managed outside
of the Subtitle C hazardous waste
regulations.
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VI. What Clarifications and Revisions
Are Proposed for the Existing
Conditions for Exclusion of Comparable
Fuel?
We are proposing to clarify the
consequences of failure to maintain
compliance with the conditions of the
exclusion for comparable fuel and the
status of tanks that cease to be operated
as comparable fuel storage tanks.105 We
are also proposing to waive the RCRA
closure requirements for tank systems
that are used only to store hazardous
wastes that are subsequently excluded
as a comparable fuel.
As discussed in Section V in the
context of ECF and for the same reasons,
comparable fuel that has lost its
exclusion because of failure to comply
with one or more conditions of the
exclusion must be managed as
hazardous waste from the point of
generation. See proposed § 261.38(d). As
examples, comparable fuel that is
spilled or leaked and cannot be burned
under the conditions of the exclusion
(i.e., in a burner listed under proposed
§ 261.3(b)(3)(i)), and comparable fuel
that is speculatively accumulated must
be managed as hazardous waste.
In addition, consistent with the
discussion in Section IV.A.3 in the
context of ECF and for the same reasons,
we propose to clarify that, if a
comparable fuel tank system, tank car or
tank truck ceases to be used to store
comparable fuel product, but has not
been cleaned by removing all liquids
and accumulated sludge within 90 days
of cessation of comparable fuel storage
operations, that such systems would
become subject to the RCRA Subtitle C
regulation as a hazardous waste storage
unit.
Finally, we are proposing today that
interim status and permitted storage
units, and generator accumulation units
exempt from permitting under § 262.34,
are not subject to the closure
requirements of 40 CFR Parts 264 and
265 provided that the storage units have
been used to store only hazardous waste
that is subsequently excluded under the
conditions of § 261.38, and that
afterward will be used only to store fuel
105 The proposed rule would also restructure the
current requirements for comparable fuel (and
syngas fuel) to make the regulatory language more
readable given that the regulation must
accommodate the proposed exclusion for ECF. We
regard these language changes as purely technical,
and thus, will accept comment only on whether the
suggested language changes express the current
meaning of the provision. We are not reexamining,
reconsidering or otherwise reopening these
provisions for comment.
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excluded under § 261.38. This is
consistent with the proposed waiver of
RCRA closure requirements for ECF, as
discussed in Section IV.A.4, and is
based on the same rationale. See
proposed § 261.38(b)(14). However, as
we noted in Section IV.A.4, the Agency
expects that the owner/operator take
common-sense steps to decontaminate
and decommission the units and
encourage them to consult with the
regulatory authority as to the best way
to ensure that the tank system is cleaned
properly. See proposed § 261.38(b)(13).
VII. What Are the Responses to Major
Comments of the Peer Review Panel?
In April 2007, EPA assembled two
panels of expert scientists to review the
significant scientific information used to
support the proposed rule. One panel
addressed questions regarding support
for the comparable emissions rationale,
and the other panel addressed questions
regarding support for the procedure we
used to rank the relative hazard of the
37 hydrocarbons and oxygenates for
which specifications have been
established in Table 1 to existing
§ 261.38.
Syracuse Research Corporation, under
contract to USEPA, selected reviewers
for both independence and scientific/
technical expertise. Each panel member
was selected for his/her recognized
technical expertise that bears on the
subject matter under discussion. The
evaluation of real or perceived bias or
conflict of interest is an important
consideration and every effort was made
to avoid conflicts of interest and
significant biases.
The peer review reports, which
contain the resumes of the peer
reviewers, are available in the docket to
the proposed rule (Docket ID No. EPA–
HQ–RCRA–2005–0017):
• Syracuse Research Corporation,
‘‘Rationale for Exclusion of EmissionComparable Fuel,’’ April 2007; and
• Syracuse Research Corporation,
‘‘Application of WMPT to Rank
Comparable Fuels Constituents,’’ April
2007.
In this section of the preamble, we
summarize the major comments by the
peer reviewers and provide responses.
We respond to other comments in
separate documents available in the
docket to the proposed rule:
• USEPA, ‘‘Response to Peer Review
Comments on the Rationale for
Exclusion of Emission-Comparable
Fuel,’’ May 2007; and
• USEPA, ‘‘Response to Peer Review
Comments on the Application of WMPT
to Rank Comparable Fuels Constituents,
May 2007.
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33313
A. What Are the Reponses to Major
Comments Regarding the Comparable
Emissions Rationale?
Comment: One cannot conclude that
ECF boilers would be controlled at least
as stringently as hazardous waste
boilers.
Response: We disagree. As we explain
in Section II.A in Part Two above,106
ECF boilers would be required to: (1)
Continuously monitor carbon monoxide
(CO) to ensure that levels remain below
100 ppmv; and (2) fire the ECF into the
flame zone of the primary fossil fuel,
which must comprise at least 50% of
the boiler’s fuel requirements. These
two conditions ensure good combustion
and a 99.99% destruction and removal
efficiency (DRE) of the hazardous
compounds (i.e., benzene, toluene, and
the listed oxygenates). In addition, these
conditions—CO below 100 ppmv and
ensuring 99.99% DRE—are the principal
controls applicable to hazardous waste
combustors to control non-dioxin/furan
organic HAP. The remaining proposed
ECF boiler conditions (e.g., the boiler
must be of a watertube, nonstoker
design; primary fuel must have a
minimum heating value of 8,000 Btu/lb;
boiler load must be greater than 40%;
the ECF must have low viscosity) help
ensure the good combustion conditions
typical of an oil-fired industrial boiler
and are appropriate given that ECF
would be burned under a conditional
exclusion without a RCRA permit and
without the regulatory oversight typical
for a RCRA hazardous waste combustor.
The reviewer notes that hazardous
waste boilers are subject to operating
requirements in addition to CO
monitoring to control emissions of nondioxin/furan organic HAP. Thus, the
reviewer questions whether ECF boilers
would be controlled as stringently as
hazardous waste boilers. Those
additional operating requirements (e.g.,
minimum combustion chamber
temperature; maximum waste feedrate),
however, are designed to ensure that a
hazardous waste boiler maintains
99.99% DRE. Operating limits on those
parameters are established during the
DRE emissions test. For ECF boilers, the
106 We explain in that discussion, that, of the four
combustion failure modes that EPA has identified—
total ignition failure, partial ignition failure,
combustion air failure, and rapid quench failure—
only a total ignition failure could result in low CO
and poor destruction of organic compounds in the
feed and combustion by-products. Total ignition
failure could potentially occur in a boiler if the fuel
firing gun inadvertently directed the fuel to a
location in the combustion chamber away from the
flame zone—i.e., if the fuel were not fired into the
flame zone. The other combustion failure modes
(i.e., partial ignition failure; combustion air failure;
and rapid quench failure) would result in high CO
and potentially high unburned organics.
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conditions to fire ECF directly into a
stable, primary fuel flame zone and
maintain a CO limit of 100 ppmv or less
ensure 99.99% DRE. Thus, those
additional operating requirements that
are established for hazardous waste
boilers during the DRE emissions test
are not needed to ensure that 99.99%
DRE is maintained for ECF boilers.
Comment: To evaluate whether ECF
boiler emissions are likely to be
substantially higher than oil-fired boiler
emissions, the Agency inappropriately
compared test condition average
emissions for hazardous waste boilers
(as a surrogate for ECF boiler emissions,
given that ECF boilers would be
controlled at least as stringently as
hazardous waste boilers) to the 95th
percentile of run emissions for oil-fired
boilers. The reviewer noted that, to
compare apples-to-apples, hazardous
waste boiler test condition averages
should be compared to oil-fired boiler
test condition averages.
Response: In conducting our initial
analysis, we had not compared
hazardous waste boiler test condition
averages to oil-fired boiler test condition
averages because we have limited oilfired boiler data (test conditions) for
several of the compounds. Given the
general paucity of emissions data and
considering the large number of oil-fired
industrial boilers, we used the oil-fired
boiler runs, rather than test condition
averages, to help represent the range of
values that such boilers may emit.
Nonetheless, in retrospect, we agree
with the reviewer. In fact, we have
substantial oil emissions data
representing many test conditions for
several compounds, such as benzene,
formaldehyde, naphthalene, and
toluene. And, although we have limited
data for several other compounds that
comprise only one to three test
conditions, we also have hazardous
waste boiler data for several compounds
that comprise only a few test conditions.
We have reanalyzed our data base to
compare hazardous waste boiler
emission test condition averages to the
95th percentile oil-fired boiler emission
test condition averages. The results of
that reanalysis support the proposed
rule. See Section I.B.1 in Part Two
above.
The 95th percentile test condition
average benchmark levels for oil-fired
boiler emissions are lower than the 95th
percentile run benchmark levels, as
expected. This results in additional
hazardous waste boiler emissions
exceeding the oil-fired boiler emissions
benchmark.107 However, these
107 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
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additional exceedances do not affect our
view that ECF boiler emissions would
be generally comparable to oil-fired
boiler emissions (e.g., they are directly
comparable or exceedances are not of
consequence because they are de
minimis).
Specifically, there is one additional
exceedance each for benz(a)anthracene
and fluorine, and two additional
exceedances for ethylbenzene. All of
these are de minimis exceedances,
however, with emissions below 1 µg/
dscm.
There is also one additional
exceedance for benzene, but the
exceedance is de minimis given that the
revised oil-fired boiler benchmark is 90
µg/dscm and the additional hazardous
waste boiler exceedance is at an
emission level of 91 µg/dscm.
Finally, there are three additional
exceedances for methylene chloride.
The revised oil emissions benchmark is
40 µg/dscm, rather than the previous
benchmark of 58 µg/dscm based on run
data, but is based on only two test
conditions. Thus, we believe it is not
representative of the range of oil-fired
boiler emissions. The three additional
hazardous waste boiler emissions
exceedances are at 54 µg/dscm, 52 µg/
dscm, and 50 µg/dscm. Test reports for
two of the three boilers indicate that
methylene chloride contamination is
known or suspected. The third test
report is silent on the potential for
contamination, but methylene chloride
is commonly recognized as a sample
and lab contaminant. Thus, we do not
consider the remaining exceedance an
indication that hazardous waste boiler
emissions of methylene chloride are not
comparable to oil emissions,
considering also the limited oil
emissions data and the de minimis
potential (but not likely) increase in
emissions.
Comment: Given that combustion is a
percent destruction process, residual
emissions of organic compounds in the
feed will increase as feedrate increases.
The Agency should ensure that burning
fuels with high concentrations of
hazardous hydrocarbons and oxygenates
will, in fact, result in trace levels of
emissions. An approach would be to
project emission levels for the ECF
compounds assuming 99.99% or
possibly 99.999% DRE (since most DRE
testing has shown this result) to
determine if emissions are within the
range of benchmark levels.
Response: It is reasonable to question
whether emissions of unburned ECF
0017, entitled ‘‘Reanalysis of Comparison of OilFired Boiler Emissions to Hazardous Waste Boiler
Emissions Considering Test Condition Averages for
Oil Emissions Data,’’ dated April 25, 2007.
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compounds could exceed the
benchmark levels given that the ECF
compounds (i.e., benzene, toluene, and
the listed oxygenates) could be fed at
high feedrates. These hazardous
compounds could be present in ECF at
any concentration and ECF could
represent a substantial portion of the
fuel fired to the boiler—25 percent of
the heat input for benzene and acrolein,
and 50 percent of the heat input for the
remaining compounds.108
We believe, however, that the
hazardous waste boiler emissions data
that we use as a surrogate for ECF
emissions 109 are likely to include
emissions that would result from
burning ECF. It is reasonable to assume
that some of the 26 hazardous waste
watertube steam boilers in our data base
are burning waste fuels that are destined
to become ECF.110 As we have
explained above in Part Two, Section
I.B.1, those emissions are comparable to
oil emissions.
Nonetheless, we acknowledge that the
ECF exclusion would allow benzene,
toluene, and the listed oxygenates to be
fed into industrial boilers at much
higher rates than they may be actually
fired in practice. For example, the
maximum concentrations of many of
these compounds in waste fuels that
have been identified as candidate fuels
for exclusion are relatively low: 0.05%
for acrolein; 10% for methyl ethyl
ketone; 15% for isobutyl alcohol and
acetophenone; and 25% for benzene.111
Toluene can be present at much higher
concentrations, however, including
levels up to nearly 100%. (As a practical
matter, although the ECF exclusion
would allow unlimited concentrations,
the concentration of hazardous
108 This is a simplification. The actual condition
would be that the firing rate of ECF containing
benzene and acrolein above the specification levels
in Table 1 to § 261.38 would be restricted to 25%
of the total fuel input to the boiler on a heat or
volume input basis, whichever results in a lower
volume input of ECF, if the concentration of
benzene or acrolein in the ECF exceeds 2 percent
by mass. For the other compounds, the ECF firing
rate would be restricted to 50% of the total fuel
input to the boiler on a heat or volume input basis,
whichever results in a lower volume input of ECF.
109 Hazardous waste boiler emissions are a
reasonable surrogate for ECF boiler emissions
because organic emissions from ECF boilers would
be controlled at least as stringently as emissions
from hazardous waste boilers, as discussed above in
response to Comment 1.
110 This is a reasonable assumption because waste
fuels that would qualify as ECF are premium fuels
that a facility would want to burn, if possible, in
an on-site boiler or in an affiliated facility’s boiler,
rather than contracting with a commercial
hazardous waste combustor to burn the fuel.
111 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
0017, entitled ‘‘Potential Approach to Establish
Firing Rate Restrictions on Emission-Comparable
Fuel,’’ dated May 21, 2007, Table 2.
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compounds will be limited to the levels
actually found in waste fuels.) In
addition, ECF would only represent a
portion of the fuel fed to the boiler since
at least 50% of the fuel must be fossil
fuel. Finally, actual firing rates (and
thus the feedrate of the compound of
concern) will depend on a number of
other factors, including the quantity of
ECF generated by a facility that burns
ECF on-site, and the quantity of ECF in
the vicinity of facilities that burn ECF
from off-site sources.
Notwithstanding current actual
practice regarding the concentrations of
compounds in ECF and ECF firing rates,
it is reasonable to question whether the
exclusion would allow such high
feedrates of the compounds of concern
that ECF emissions may not meet the
criterion of being comparable to the
emissions from burning oil. For
example, if we assumed that a DRE of
only 99.99% were achieved when
feeding ECF with a 90% concentration
of a compound of concern at the
maximum firing rate (i.e., 25% for
benzene and acrolein and 50% for the
other compounds), the residual
emissions of the compound would far
exceed the emissions from burning oil.
Consequently, we request comment
on an approach that would limit the
feedrate of benzene, toluene, and the
listed oxygenates to ensure that ECF
emissions are comparable to the
emissions from burning oil. Under the
approach, we would identify a target
emission level for each of these
hazardous compounds, estimate a
destruction and removal efficiency
(DRE) for the compound, and calculate
a maximum ECF firing rate as a function
of the concentration of the compound in
the ECF.
We would identify the target emission
levels as:
• For each hazardous compound for
which we have emissions data from oilfired industrial boilers, the target level
would be the highest test condition
average (after screening out high
apparent outliers) or a de minimis level,
whichever is higher;
• For each hazardous compound for
which we have only hazardous waste
boiler emissions data, the target level
would be the highest test condition
average (after screening out high
statistical outliers) 112 or a de minimis
level, whichever is higher; and
• For each hazardous compound for
which we have neither oil-fired boiler
nor hazardous waste boiler emissions
112 See USEPA, ‘‘Draft Technical Support
Document for Expansion of the Comparable Fuel
Exclusion,’’ May 2007, Appendix C.
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data, the target level would be a de
minimis level.
The target emission levels for the
three hazardous compounds for which
we have oil emissions data—acrolein,
benzene, and toluene—would range
from a de minimis level of 20 µg/
dscm 113 to 160 µg/dscm.114 The target
emission levels for the seven hazardous
compounds 115 for which we have only
hazardous waste boiler emissions data
would range from a de minimis level of
20 µg/dscm to 130 µg/dscm. And, the
target emission level for hazardous
compounds for which we do not have
emissions data would be a de minimis
level of 20 µg/dscm.
We specifically request comment on
whether these target emission levels are
appropriate.
We believe it is reasonable to estimate
a default DRE (i.e., DRE achievable at
low compound feedrates) of 99.99% for
the hazardous compounds that have a
Thermal Stability 116 ranking of Class I
or Class 2 (i.e., benzene, toluene, and
methyl methacrylate) and a DRE of
99.995% for the other hazardous
compounds. The Thermal Stability
ranking is a principal tool for selecting
difficult to destroy compounds for DRE
testing required to establish operating
requirements for hazardous waste
combustors. We have DRE data for
hazardous waste watertube boilers
indicating that boilers may achieve
DREs below 99.995% for Class I and
Class 2 compounds when they are fed
at low feedrates, while these boilers
achieve greater than 99.995% DRE for
Class 3–7 compounds that are fed at low
feedrates.117
113 It is reasonable to consider 20 µg/dscm a de
minimis emission level because it is comparable to
approximately 0.01 ppmv propane equivalents for
the high molecular weight compounds of concern,
and is 3 orders of magnitude lower than the 10
ppmv total hydrocarbon emission limit the Agency
has established for liquid fuel boilers that burn
hazardous waste. See § 63.1217(a)(5)(ii).
114 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
0017, entitled ‘‘Potential Approach to Establish
Firing Rate Restrictions on Emission-Comparable
Fuel,’’ dated May 21, 2007, Table 1.
115 We have hazardous waste boiler emissions
data for: acetophenone, biz(2-ethylhexyl)phthalate,
diethyl phthalate, di-n-butyl phthalate, di-n-octyl
phthalate, methyl ethyl ketone, and phenol.
116 The Thermal Stability ranking classifies
(generally) hazardous compounds according to their
gas-phase thermal stability under oxygen-starved
conditions. Compounds are ranked according to the
temperature required to destroy 99% of the
compound in 2 seconds under oxygen-starved
conditions. See USEPA, ‘‘Guidance on Setting
Permit Conditions and Reporting Trial Burn
Results, Volume II of the Hazardous Waste
Incineration Guidance Series,’’ January 1989, Table
D–1.
117 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
0017, entitled ‘‘Potential Approach to Establish
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It is also reasonable to conclude that
DRE increases with an increase in
feedrate of the target compound. It is
common knowledge that feedrates of
POHCs must be high enough to avoid
DRE failures attributable to stack
method or analytical method
imprecision and the baseline level of
products of incomplete combustion.118
A recent paper by Brukh, et al, lends
support to this view.119 Moreover, a plot
of hazardous waste boiler DRE run data
versus feedrate MTEC 120 indicates a
general trend toward higher DREs as
feedrates increase for those hazardous
compounds for which we have DRE data
over a range of feedrates.121
It appears that, when MTECs exceed
1.0E+07 µg/dscm, DRE exceeds 99.999%
for all compounds. Additionally, it
appears that, for MTECs in the range of
5.0E+06 to 1.0E+07, DRE exceeds
99.995% for all hazardous compounds.
Consequently, it may be appropriate to
consider this feedrate/DRE relationship
to identify potential ECF firing rate
limits.
We specifically request comment on
our views regarding the relationship
between DRE and compound feedrate.
We also have considered the potential
concentrations of the hazardous
compounds in ECF to calculate
potential ECF firing rate limits
Firing Rate Restrictions on Emission-Comparable
Fuel,’’ dated May 21, 2007.
118 See USEPA, Operational Parameters for
Hazardous Waste Combustion Devices,’’ October
1993. Section 4.3.2.1.
119 See R. Brukh, R. Baret, and S. Mitra, New
Jersey Institute of Technology, ‘‘The Effect of Waste
Concentration on Destruction Efficiency During
Incineration,’’ Environmental Engineering Science,
Vol. 23, No. 2, 2006. The authors conducted
experiments in a small, well-stirred reactor
involving the combustion of methylene chloride
(CH2Cl2) with ethylene (C2H4) as the primary fuel at
residence times of 5–12 ms and temperatures of
1400–1750 K (2050–2700 °F). Experiments were
done at both fuel rich and fuel lean conditions.
CH2Cl2 concentrations were low (2–1350 ppm by
volume in the main feed.). The authors modeled the
combustion of methylene chloride, methyl chloride
(CH3Cl), and benzene. They show limited
experimental data for CH3Cl and C6H6 from
previous work. The authors’ hypothesis is that
higher concentrations of POHC contribute
additional radical fractions and the overall result is
a higher destruction efficiency. This work would
support higher DREs at higher feedrates if the
results can be extrapolated to the higher POHC
concentrations of concern and the higher residence
times for hazardous waste combustors. This paper
is available in the docket to this rulemaking: Docket
ID No. EPA–HQ–RCRA–2005–0017.
120 MTEC means maximum theoretical emission
concentration (µg/dscm) and is an approach to
normalize the feedrate for various size boilers. It is
calculated as the mass feedrate divided by the stack
gas flowrate.
121 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
0017, entitled ‘‘Potential Approach to Establish
Firing Rate Restrictions on Emission-Comparable
Fuel,’’ dated May 21, 2007, Figure 2.
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considering the estimated DREs and
target emission levels discussed above.
As expected, at low concentrations in
the ECF, the ECF firing rate would not
be limited (i.e., other than the limits that
would apply as a basic condition of the
exclusion—25% maximum firing rate if
the benzene or acrolein concentration
exceeds 2%, and 50% maximum firing
rate for all other ECF).122
We noted an anomalous situation for
most hazardous compounds, however,
where the firing rate limit first
decreased as feedrate increased (as
expected), but then at higher feedrates,
the firing rate limit began to increase.
This was caused by our assumption that
DRE increases in a step-wise function
rather than, as likely, in a smooth
progression as feedrate increases. For
example, we estimated DRE at 99.995%
when the MTEC is 9.9E+06, and at
99.999% when the MTEC is 10E+06
(1.0E+07).
Clearly, this is not a realistic
representation of how DRE relates to
MTEC. To address this concern, we
could, for example, consider whether it
is appropriate to use a best-fit curve of
the benzene data to develop a
relationship between DRE and MTEC.
Benzene may be an appropriate
hazardous compound to select to define
the relationship because it ranks the
highest on the thermal stability index of
the compounds for which we have DREs
over a range of feedrates, it has the
highest ranking for the hazardous
compounds, and it is the third highest
ranking compound in the Thermal
Stability index, ranking higher than 341
other compounds.
We specifically request comment on
whether feedrate limits for the
hazardous compounds may be necessary
to ensure that the target emission levels
are not exceeded, and on the approach
described above for potentially
establishing ECF firing rate limits.
Comment: EPA should be sure that all
coal-fired boilers have enough sulfur to
inhibit dioxin/furan formation and thus
justify a waiver from gas temperature
control at the inlet to the electrostatic
precipitator (ESP) or fabric filter (FF).
Response: Although data are limited,
it appears that coal-fired boilers
equipped with an ESP or FF and
burning low sulfur coal will have low
dioxin/furan emissions irrespective of
the gas temperature at the inlet to the
ESP or FF.
We have dioxin/furan data for 17
coal-fired boilers that are equipped with
122 See memorandum from Bob Holloway,
USEPA, to Docket ID No. EPA–HQ–RCRA–2005–
0017, entitled ‘‘Potential Approach to Establish
Firing Rate Restrictions on Emission-Comparable
Fuel,’’ dated May 21, 2007, Table 3.
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an ESP or FF.123 One of the boilers
burns hazardous waste and the
remaining boilers do not burn
hazardous waste. All dioxin/furan
emissions are below 0.35 ng TEQ/dscm,
which is below the 0.40 ng TEQ/dscm
generic MACT dioxin/furan emission
standard for hazardous waste
combustors. See 40 CFR Part 63,
Subpart EEE.
Nine sources operate the ESP or FF
above a (estimated) gas temperature of
400 F, with a range of 401 °F to 500 °F.
All of these boilers have dioxin/furan
emissions below 0.2 ng TEQ/dscm. At
least one of these boilers burns low
sulfur coal.
Nonetheless, given the limited data,
we specifically request comment and
supporting information on the potential
for dioxin/furan formation across the
ESP or FF of a coal-fired boiler when the
APCD is operated above 400 F, and thus
whether a temperature limit is
warranted as a condition of the ECF
exclusion for those boilers burning coal
as the primary fuel.
Comment: If ECF is fired in a separate
firing system at a low firing rate,
potentially high levels of CO from poor
combustion of the ECF may be masked
by the low CO from the primary fuel. In
addition, the method of mixing the ECF
with the other fuel is extremely
important and should be considered
when developing conditions that ensure
good combustion. The location and
design of the ECF injector will also be
critical to ensuring good combustion.
The ECF injector may meet the
proposed conditions, but nonetheless
not provide good combustion.
Response: The proposed conditions
for firing ECF to ensure good
combustion (e.g., atomization
conditions; firing ECF into the flame
zone of the primary, fossil fuel which
must represent at least 50% of the fuel
input to the boiler; the boiler must
operate at >40% load to ensure a stable
flame and well-mixed fuels) are at least
as stringent as those required for
hazardous waste boilers under 40 CFR
266.110, which ensure good combustion
conditions. Moreover, if the ECF is
injected in a manner that may not
ensure good combustion, the 100 ppmv
CO limit could not be achieved.
Nonetheless, we request comment on
whether additional conditions on the
ECF burner design, location, or
operation may be warranted to ensure
good combustion of ECF. Any such
comments must include supporting
123 USEPA, ‘‘Response to Peer Review Comments
on the Rationale for Exclusion of EmissionComparable Fuel,’’ May 2007, Section I, Comment
4.
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information in order for the Agency to
be able to consider it for final action.
Comment: The Agency has few oilfired boiler emissions data to determine
whether ECF boiler emissions (using
hazardous waste boiler emissions as a
surrogate) are likely to be comparable.
Including additional sources in the data
base could increase or decrease the
benchmark emissions levels EPA used
for the comparison.
Response: Our oil-fired emissions
data base was developed under a
comprehensive effort to obtain available
emissions data to develop MACT
standards (i.e., under CAA Section
112(d)) for industrial, commercial, and
institutional boilers that do not burn
hazardous waste. We have emissions
data for 26 compounds for comparison
with hazardous waste boiler emissions,
comprised of more than 500 runs
representing more than 235 test
conditions. Nonetheless, we have few
emissions data for some compounds, as
the reviewer notes—data for only 1 or 2
test conditions that cannot represent the
range of emissions from oil-fired boilers.
We note, however, that if more data
were available, the emissions
benchmark levels would generally
increase rather than decrease as the
range of emission levels is better
represented. Counter-balancing this,
however, is the fact that if we had
additional hazardous waste boiler
emissions data, some data would likely
be higher than those that are currently
in our data base.
Comment: Because most watertube
steam boilers operate at less than 4%
oxygen, requiring that CO be corrected
to 7% oxygen will dilute actual CO
levels. This dilution effect could cause
operators to miss operational problems.
Response: We do not understand how
correcting CO to 7% oxygen rather than
4% oxygen would affect the ability of
operators to detect degradation in
combustion conditions. Nonetheless, we
specifically request comment and
supporting information on whether CO
should be corrected to 4% oxygen,
which more closely reflects actual stack
oxygen concentrations for these types of
boilers. On a 4% oxygen correction
basis, the 100 ppmv CO limit (at 7%
oxygen) would be 120 ppmv.
Comment: A peer reviewer provides
cites for two reports that may provide
additional information on emissions
from coal-fired power plants and one
report that provides emissions estimates
for volatile organic compounds emitted
by the combustion of coal, gas, and oil:
• PCDD/PCDF Emissions from Coal
Fired Power Plants, Riggs, Karen B. et
al., Battelle, Columbus, OH, 15th
International Symposium on
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Chlorinated Dioxins and Related
Compounds, August 21–25, 1995,
Edmonton, Canada, Volume 24, Pages
51–54.
• A Comprehensive Assessment of
Toxic Emissions from Coal-Fired Power
Plants, Phase 1 Results, from the U.S.
Department of Energy Study. Prepared
for Pittsburgh Energy Technology
Center, U.S. Department of Energy.
September 1996.
• The EPA National Air Quality and
Emissions Trends Report, 2003 Special
Study Edition, has Volatile Organic
Compounds Emissions Estimates given
in Table A–5 for coal, gas and oil. Later
reports may be available.
Response: We appreciate the
references and request comment on the
significance and relevance of
information in these reports on the
proposed ECF exclusion. These
documents are in the docket for this
rulemaking: Docket ID No. EPA–HQ–
RCRA–2005–0017.
B. What Are the Reponses to Major
Comments Regarding the Application of
the WMPT to Rank Comparable Fuel
Constituents?
Comment: Because the 37
constituents are found in combustion
(i.e. air) emissions, EPA should use air
half-life data when generating
Persistence scores for this effort, rather
than half-life data from other media.
Response: We disagree. Information
suggests that it’s important to take into
account the risks from indirect
exposures (e.g. ingesting contaminated
soil, food, or water) when considering
the potential risk from combustor
emissions. For example, Fradkin et al.
(1988) 124 linked elevated levels of
chemical pollutants in soils, lake
sediments, and cow’s milk to the
atmospheric transport and deposition of
pollutants from combustion sources.
The current effort is not a full
quantitative risk assessment, but rather
a screening-level ranking of chemicals
based on potential chronic (i.e., longterm) risks to human health and the
environment. As such, we consider it
appropriate to make the protective
assumption, as in the WMPT, of using
the highest half-life data of the relevant
media to derive Persistence scores for
the 37 constituents.
Comment: When deriving a
Persistence score for benzene, it would
be more appropriate to use its half-life
in air, rather than its half-life in
sediment, as in the WMPT.
124 Fradkin, L., R.J.. Bruins, C.H. Cleverly, 1988.
‘‘Assessing the risk of incinerating municipal solid
waste: The development and application of a
methodology’’. Municipal Waste Combustion and
Human Health. CRC Press. Palm Beach, Florida.
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Response: For the reasons stated
above, we consider it appropriate to use
the highest half-life from all relevant
environmental media. We also consider
it appropriate to consistently apply the
WMPT methodology across all 37
constituents whenever possible.
Interestingly, the peer reviewers did
not agree on the implications of using
the air half-life to derive benzene’s
Persistence score: One peer reviewer
thought it would lower the Persistence
score, while another peer reviewer saw
it as grounds for a high Persistence
score. Also, the three peer reviewers do
not agree on the final disposition of
benzene’s ranking. One peer reviewer
recommends moving benzene to
Category C, another peer reviewer
recommends leaving benzene in
category B, while the third peer
reviewer, due to benzene’s toxicity,
recommends elevating it to Category A.
Nevertheless, we recognize that as one
peer reviewer puts it, ‘‘* * * although
the WMPT is a useful screening tool for
evaluating the hazard of particular
compounds, it should not be used
blindly.’’ We thus request public
comment on this issue.
Comment: No toxicity data were
available for five hazardous compounds
(1,4 naphthoquinone, isosafrole,
propargyl alcohol, safrole, dimethyl
phthalate), and therefore complete
scoring was not possible. Therefore, one
of the peer reviewers thought that these
compounds should have been removed
from consideration as emissioncomparable fuel constituents.
Response: While we recognize that no
toxicity data were available for these
five hazardous compounds, and
therefore complete scoring was not
possible, we do not agree that this
should result in these compounds being
removed from consideration as emission
comparable fuel constituents.
Specifically, there were sufficient data
to derive the other two subscores (for
Persistence and Bioaccumulation)
required for final scores. Given their
Persistence and Bioaccumulation scores,
and assuming a worst-case toxicity score
for each, none of the five hazardous
compounds ranked higher than Category
C. Therefore, we believe it appropriate
to include them as emission-comparable
fuel (ECF) constituents.
Comment: Little scientific
justification is provided for grouping the
PAHs and naphthalene into a common
group.
Response: We made the policy
decision to remain consistent with the
pre-reviewed WMPT methodology,
which classified constituents that
scored 8 or 9 as high hazard.
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Naphthalene scored an 8, and thus is
classified as a high hazard compound.
We also remained consistent with the
WMPT methodology and the toxic
release inventory (TRI) by grouping
PAHs together, and classifying them as
high hazard. Most PAHs scored an 8 or
9; benzo(a)anthracene and chrysene,
however, scored 7.125 In addition, we
note that it is an EPA priority to reduce,
whenever possible, the environmental
release of any chemical found on EPA’s
list of Priority Chemicals. PAH’s and
naphthalene are members of EPA’s list
of priority chemicals. Consequently, we
believe it is reasonable to classify PAHs
and naphthalene as high hazard
compounds.
We specifically request comment on
adopting the WMPT (and TRI) policy of
classifying PAHs as a group, and being
consistent with the Agency’s priority to
reduce the environmental release of
chemicals on EPA’s list of priority
chemicals. Any comment suggesting an
alternative approach must include an
appropriate rationale and supporting
information in order for the Agency to
be able to consider it for final action.
Comment: The Agency should
consider the implications of the
combustion process on the composition
of potential emissions components in
terms of the parent constituents, as well
as the combustion by-products.
Response: This comment is not
germane to the scope of this peer
review. We discuss in Part Two,
Sections I and II of the preamble why
we believe that emissions from burning
ECF under the proposed conditions
would be comparable to emissions from
burning oil in an industrial boiler
operating under good combustion
conditions.
Comment: The WMPT model uses
many screening level values (e.g.
ambient water quality criteria (AWQC))
that were developed for purposes other
than that for which they are being used.
Because the Agency used the data that
were contained in the data base, there
was little assessment of the quality of
these data. The use of these values as
‘‘numerical environmental benchmarks’’
is inappropriate and will result in
conservative estimates of risk.
Response: The ambient water quality
criteria were not used to score any of the
ECF constituents. Also, the WMPT
methodology, including its hierarchy of
data sources and data quality assurance
procedures, went through peer and
public review. Therefore, we disagree
with the commenter that there was no
125 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Section 2.4.
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quality control on the data in the data
base. Moreover, commenting on the
basic structure of the WMPT
methodology, beyond its applicability to
the current application, is beyond the
scope of this peer review.
Comment: Very conservative
assumptions are employed in the
assessment process (e.g., the use of
anaerobic sediment degradation halflifes as a measure of the chemicals
environmental persistence).
Response: We believe it is appropriate
to make reasonably conservative
assumptions considering that the ECF
would be burned under a conditional
exclusion absent a RCRA Part B permit
and the regulatory oversight typical for
a RCRA hazardous waste combustor.
Comment: When applying the model
to any particular use or situation,
consideration must be given to exposure
potential and to the data used to
estimate exposure potential.
Response: As we discuss in Part Two,
Section III, of the preamble, our hazard
ranking effort was not a full quantitative
risk assessment, but rather a screeninglevel ranking of hazardous compounds
based on potential chronic (i.e., longterm) risks to human health and the
environment. As such, we consider it
appropriate to apply the WMPT’s use of
a small number of relatively simple
measures (i.e. combination of
bioaccumulation and persistence
factors) to represent the exposure
potential of each chemical.
Comment: No scientific basis is
provided for why ecological toxicity
data were not considered in the
evaluation process. The WMPT requires
information on both human and
ecological toxicity concerns. As
implemented here, only human
concerns were considered.
Response: In developing the WMPT,
the Agency decided to collect the
toxicity data in phases, beginning with
human toxicity. In Phase 2, we would
collect ecological toxicity data only for
those constituents which a high toxicity
score might elevate to a different
category. However, as a result of the
human toxicity data collected in Phase
1, we found that in no instance would
a high ecological toxicity score alter a
chemical’s score sufficiently to elevate
the chemical into a category for which
we recommend action.
Therefore, we disagree with the
opinion that only human toxicity
concerns were considered. As detailed
in the technical support document, 126
some, but not all, of the 37 constituents
are found in the WMPT chemical data
base. We retained the eco-toxicity data
(and scores) for those chemicals already
in the data base. For those chemicals not
already in the WMPT data base, high
eco-toxicity subscores would not have
had a meaningful impact on the final
scores.
Comment: The justification for
acrolein’s ‘‘special characterization’’ is
unclear. Acrolein’s inhalation toxicity
and its proclivity to accumulate in body
tissues (i.e. bioaccumulation score) are
unrelated.
Response: We have clarified our
explanation for assigning acrolein to
hazard Category B—moderate relative
hazard—to explain that our concern is
that acrolein’s human toxicity is based
on the inhalation pathway and that
acrolein has the highest possible WMPT
score (three) for toxicity. See discussion
in Part Two, Section III of the preamble.
Comment: There are several potential
issues with the way different health and
ecotoxicological endpoints are scored.
The authors of the WMPT appear to
have relied on expert judgment to select
consistent levels of concern within a
particular endpoint, but the background
document says little about comparison
or weighting of different endpoints.
Response: As mentioned above, while
the Agency appreciates this comment, it
is beyond the scope of this peer review.
Comment: A basic limitation of the
WMPT approach is the exclusion from
the rankings of any consideration of the
dose likely to be involved in practical
exposure situations.
Response: The WMPT ranking
procedure is not a full quantitative risk
assessment, but rather a screening-level
ranking of hazardous compounds based
on potential chronic (i.e., long-term)
risks to human health and the
environment. As such, we consider it
appropriate to make reasonably
conservative assumptions, as opposed to
the consideration of the dose likely to be
involved in practical exposure
situations.
Comment: There is no explicit
statement that the tables used in this
application have been checked against
the latest iterations of the various
references.
Response: In the technical support
document section titled ‘‘Updating/
Collecting Constituent-Specific Data,’’
we explain that some, but not all the 37
comparable fuel constituents are found
in the WMPT chemical data base.127 For
those constituents found in the data
base, we updated the data and re-
126 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Section 2.4.
127 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007, Section 2.4.
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evaluated each chemical to determine if
their WMPT scores changed with more
up-to-date data.
Comment: The use of an inclusive
category of ‘‘Polycyclic Aromatic
Compounds’’ (PACs) with a single level
of concern to deal with the evaluation
of various carcinogenic polycyclic
aromatic hydrocarbons and related
compounds is appropriate for a
screening tool and protective of public
health, but there is some lack of clarity
as to what compounds are included.
Response: All of the hydrocarbons
listed in Table 1 to § 261.38, except
benzene, naphthalene, and toluene, are
PAHs.
Comment: Placing benzene in the
second tier of concern (i.e., hazard
Category B) is logical given the premise,
with the following exceptions. This
carcinogen is potentially present in
‘‘exemptible’’ fuels at a rather
substantial level, thus offsetting its
lower potency. Also, combustion of
aromatics may under some
circumstances lead to high
concentrations of PAHs in the
emissions. In addition, carcinogenesis is
a severe endpoint and a subject of
greater public concern than most other
health outcomes. Benzene is one of the
relatively few, and thus notorious,
‘‘Known Human Carcinogens’’
according to U.S. EPA and IARC. The
level of concern (and thus, severity of
restriction) should be considered at least
equivalent to naphthalene, and thus
benzene should be in hazard Category
A.
Response: We have clarified our
rationale for assigning benzene to
hazard Category B. See discussion in
Part Two, Section III, of the preamble.
Comment: The ranking of acrolein is
appropriate, but it is odd that this
material is variously described as a fuel
constituent, rather than a combustion
by-product.
Response: The scope of this peer
review pertained to our hazard ranking
procedure for the hydrocarbon and
oxygenate constituents of ECF listed in
Table 1 to § 261.38.
Comment: The use of measured and
predicted data yield an inconsistent
bioaccumulation ranking across PAHs.
It would seem more appropriate to use
the measured data to ensure a consistent
assessment. Nevertheless, the proposed
methodology is relatively robust and
such refinements are not likely to
impact the overall hazard ranking and
resulting conclusions derived from the
present analysis.
Response: The agency acknowledges
the reviewer’s comment. We consider it
appropriate to consistently apply the
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WMPT methodology across all 37
constituents.
Part Three: State Authority
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I. Applicability of the Rule in
Authorized States
EPA would strongly encourage states
to adopt the regulations being proposed
today. Under section 3006 of RCRA,
EPA may authorize qualified states to
administer their own hazardous waste
programs in lieu of the federal program
within the state. When EPA authorizes
a state to implement the RCRA
hazardous waste program, EPA
determines whether the state program is
consistent with the federal program, and
whether it is no less stringent. This
process, codified in 40 CFR 271, ensures
national consistency and minimum
standards, while providing flexibility to
states in implementing rules. Following
authorization, EPA retains enforcement
authority under sections 3008, 3013,
and 7003 of RCRA, although authorized
states have primary enforcement
responsibility. In making this
determination, EPA evaluates the state
requirements to ensure they are no less
stringent than the federal requirements.
Prior to enactment of the Hazardous
and Solid Waste Amendments of 1984
(HSWA), a State with final RCRA
authorization administered its
hazardous waste program entirely in
lieu of EPA administering the federal
program in that state. The federal
requirements no longer applied in the
authorized state, and EPA could not
issue permits for any facilities in that
state, since only the state was
authorized to issue RCRA permits.
When new, more stringent federal
requirements were promulgated, the
state was obligated to enact equivalent
authorities within specified time frames.
However, the new federal requirements
did not take effect in an authorized state
until the state adopted the federal
requirements as state law.
In contrast, under RCRA section
3006(g) (42 U.S.C. 6926(g)), which was
added by HSWA, new requirements and
prohibitions imposed under HSWA
authority take effect in authorized states
at the same time that they take effect in
unauthorized states. EPA is directed by
the statute to implement these
requirements and prohibitions in
authorized states, including the
issuance of permits, until the state is
granted authorization to do so. While
states must still adopt HSWA related
provisions as state law to retain final
authorization, EPA implements the
HSWA provisions in authorized states
until the states do so.
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RCRA section 3009 allows the states
to impose standards more stringent than
those in the federal program (see also 40
CFR 271.1). Therefore, authorized states
are required to modify their programs
only when EPA enacts federal
requirements that are more stringent or
broader in scope than existing federal
requirements. Authorized states may,
but are not required to, adopt federal
regulations that are considered less
stringent than previous federal
regulations. Because today’s rule would
eliminate specific requirements for
materials that are currently managed as
hazardous waste, state programs would
no longer need to include those specific
requirements in order to be consistent
with EPA’s regulations, when and if
today’s rule is finalized.
II. Effect on State Authorization
Today’s notice proposes regulations
that would not be promulgated under
the authority of HSWA. Thus, the
standards proposed today would be
applicable on the effective date only in
those States that do not have final RCRA
authorization. Moreover, authorized
States are required to modify their
program only when EPA promulgates
Federal regulations that are more
stringent or broader in scope than the
authorized State regulations. For those
changes that are less stringent or reduce
the scope of the Federal program, States
are not required to modify their
program. This is a result of section 3009
of RCRA, which allows States to impose
more stringent regulations than the
Federal program. Today’s proposal is
considered to be less stringent than the
current standards. Therefore, authorized
States would not be required to modify
their programs to adopt regulations
consistent with and equivalent to
today’s proposed standards, although
EPA would encourage States to do so.
Some states incorporate the federal
regulations by reference or have specific
state statutory requirements that their
state program can be no more stringent
than the federal regulations. In those
cases, EPA anticipates that the
exclusions in today’s proposal, when
and if finalized, would be adopted by
these states, consistent with state laws
and state administrative procedures,
unless they take explicit action as
specified by their respective state laws
to decline the proposed revisions.
Part Four: Costs and Benefits of the
Proposed Rule
33319
generates. The Agency’s economic
assessment conducted in support of
today’s proposed action evaluates costs,
cost savings (benefits), waste quantities
affected, and other impacts, such as
environmental justice, children’s health,
unfunded mandates, regulatory takings,
and small entity impacts. To conduct
this analysis, we prepared a baseline
characterization for ECF, developed and
implemented a methodology for
examining impacts, and followed
appropriate guidelines and procedures
for examining equity considerations,
children’s health, and other impacts.
Because EPA’s data were limited, the
estimated findings from these analyses
should be viewed as national, not sitespecific impacts.
II. Baseline Specification
Proper baseline specification is vital
to the accurate assessment of
incremental costs, benefits, and other
economic impacts associated with a rule
that would expand the exclusion for
waste fuels. The baseline essentially
describes the world absent any
expanded exclusion. The incremental
impacts of today’s action are evaluated
by predicting post-rule responses with
respect to baseline conditions and
actions. The baseline, as applied in this
analysis, is assumed to be the point at
which the proposal is published. A full
discussion of baseline specification is
presented in the Assessment 128
document completed for this action.
III. Analytical Methodology, Primary
Data Sources, and Key Assumptions
We developed a simplified four-step
approach for assessing the cost and
economic impacts associated with this
action. First, we identified all
potentially eligible waste streams
currently generated in the U.S. We next
determined the tonnage of waste that is
likely to qualify for the proposed
exclusion. An economic threshold
analysis was next applied to the likely
eligible waste to determine which
facilities could be expected to benefit
from the exclusion. For example, for a
generator with an eligible nonhazardous
boiler on-site, the model assumes that
the facility will use the exclusion if the
total benefits (cost savings) realized by
the generator are projected to exceed the
total costs incurred to take advantage of
the exclusion. Finally, we aggregated all
facilities that are likely to use the
exclusion to derive estimates for total
I. Introduction
The value of any regulatory action is
traditionally measured by the net
change in social welfare that it
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128 Assessment of the Potential Costs, Benefits,
and Other Impacts of the Expansion of the RCRA
Comparable Fuel Exclusion-Proposed Rule, June
2007.
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costs, cost savings, and economic
impacts (waste quantities affected).
The analytical model for this analysis
derives both cost savings and costs
associated with the exclusion. Cost
savings include: Fuel cost savings (net
of baseline fuel recovery), avoided
hazardous waste management costs,
transportation cost savings, tracking cost
savings, and storage cost savings. These
factors may be considered economic
benefits of the proposed action. The
model also assesses relevant costs of the
exclusion. These are: Burner storage
costs, boiler retrofit costs, waste stream
analytical costs, raw materials
replacement cost (related to waste that
is recycled in the baseline),
recordkeeping costs, and transport costs.
The net social benefits are calculated
as the difference between the social
benefits (cost savings) and social costs.
The total net social benefits of the
proposed rule are then calculated by
aggregating the net social impacts
associated with each facility expected to
use the exclusion. Impacts to human
health and the environment are
assumed to be unchanged and are
therefore not included in our monetized
assessment.
The primary data sources used in this
analysis are the 2003 Biennial Report
(2003 BR) 129, the 1996 National
Hazardous Waste Constituent Survey
(NHWCS),130 the 2002 National
Emissions Inventory (NEI),131 ACC
Survey data,132 and information
provided in the engineering analysis
developed by EERGC. The 2003 BR data
were used to derive the potentially
eligible waste streams currently
generated in the U.S. This is the only
national database available for this use
that has been reviewed by the Agency
to ensure data quality. The 1996
NHWCS reflects dated information, but
was the only quality controlled data
source available that provided the
necessary waste constituent information
on a nationwide basis, across all
industries. The NEI data were used to
make a determination of whether an
eligible boiler is located at each facility.
129 U.S. EPA, 2003 National Biennial Report,
database and supporting documentation available
for download at https://www.epa.gov/epaoswer/
hazwaste/data/biennialreport/.
130 U.S. EPA, National Hazardous Waste
Constituent Survey, database and supporting
documentation available for download at https://
www.epa.gov/epaoswer/hazwaste/id/hwirwste/
economic.html.
131 U.S. EPA, 2002 National Emissions Inventory,
databases and supporting documentation available
for download at https://www.epa.gov/ttn/chief/net/
2002inventory.html.
132 American Chemistry Council (ACC) voluntary
membership survey of waste generation and
management.
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The EERGC engineering analysis
provided all necessary engineering cost
information.133
Data limitations have required us to
apply several assumptions in our
analysis. The most critical assumptions
are:
• The ECF is assumed to be burned in
nonhazardous waste boilers that meet
the conditions of the exclusion.
• The ECF is assumed to have an
average heating value of 12,200 Btu/lb.
This is based on our assessment of the
National Hazardous Waste Constituent
Survey.
• That a facility that can use the
exclusion, and has a nonhazardous
waste boiler on-site that could burn
ECF, would burn the fuel on-site rather
than sending it off-site.
• The number of facilities purchasing
ECF is assumed to equal the number of
generating facilities expected to send
their ECF off-site.
• That all ECF generated in a
particular state would be shipped the
same distance. Average shipment
distances for each state are derived from
hazardous waste shipped off-site, as
reported in the 2003 BRS.
IV. Key Analytical Limitations
Our primary analytical limitations are
associated with our estimate of the
availability of on-site boilers, and our
estimate of ECF qualifying for the
exclusion. Nationwide data were not
available to indicate whether each
affected generating facility has a boiler
on-site that can burn ECF. Using the
National Emissions Inventory (NEI)
data, we made a determination of
whether an eligible boiler is located at
each facility. This determination may
misrepresent which boilers could burn
ECF and which boilers could not. To
estimate how much waste qualifies as
ECF, we used the ACC survey data, and
data derived from the NHWCS. The data
presented in the NHWCS are the most
comprehensive nationwide data
available. However, these data are from
1993, and may not fully reflect the
characteristics of today’s waste streams.
V. Findings
This rule, as proposed, is projected to
result in a benefit to society in the form
of net cost savings to the private sector,
on a nationwide basis, thereby allowing
for the more efficient use of limited
resources elsewhere in the market. This
is accomplished without compromising
protection of human health and the
environment by ensuring comparable
133 USEPA, ‘‘Draft Technical Support Document
for Expansion of the Comparable Fuel Exclusion,’’
May 2007.
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emissions from the burning of high Btu
value waste.
The total net social benefits projected
as a result of this rule, as proposed, are
estimated at approximately $23 million
per year. Avoided management and fuel
costs represent the vast majority of all
benefits (cost savings). Transportation,
boiler retrofits, and analytical costs
represent the majority of the costs. This
estimate assumes all States adopt the
rule, and incorporates all cost savings to
affected generators, less all associated
costs. Nearly 183,000 tons (U.S.) of
waste are expected to initially qualify
for the exclusion with approximately
107,000 tons/year actually excluded. Of
this total, we estimate that
approximately 34,000 tons are not
currently burned for energy recovery.
We also analyzed various scenarios
under the two primary regulatory
options for the storage of ECF
considered by the Agency. Annual net
social benefits under the first option
were found to be $603,000 to $1,396,000
greater than the net benefits of our
proposed approach. The additional cost
savings reflect reduced storage
requirements. In addition, this scenario
assumes that the specification for
naphthalene and PAHs would not
apply, which would increase the
percentage of waste qualifying for the
exclusion. Under the second option,
annual net social benefits were found to
range from $15 million to $20 million
per year. These reduced savings largely
reflect additional RCRA Subtitle C
storage and tracking requirements.
Furthermore, this option assumes that
generating facilities would not send any
of their ECF offsite. This assumption
results in a significant reduction in
annual fuel cost savings and avoided
management costs.
We believe that it is important to not
only understand the change in
economic efficiency, as presented
above, but to also understand the
primary distributional effects associated
with this change. Hazardous waste
commercial incinerators and cement
kilns are projected to experience
negative distributional impacts
associated with this action. These
effects include revenue losses for both
groups, plus fuel replacement costs for
commercial kilns. Revenue losses to
commercial incinerators are estimated at
$3 million/year, while commercial kilns
may experience combined revenue and
fuel replacement losses of
approximately $13.5 million per year.
These impacts represent between one
and 1.7 percent of the total estimated
annual gross revenues for these sectors.
Although impacts to these groups may
be considered a cost in accounting
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terms, they do not represent a real
resource cost of the proposed rule. The
actual net benefits of this proposal
reflect the impacts to these groups to the
extent that there are real resource
impacts, but do not include transfers
from one facility to another.
The findings presented here reflect
numerous analytical assumptions and
limitations. Furthermore, we have
analyzed additional scenarios and
sensitivity analyses that are not
presented in this Preamble. The reader
is strongly encouraged to read the
Assessment document prepared in
support of this proposal to gain a full
understanding of all findings, analytical
assumptions, limitations, and how the
adjustment of selected key parameters
may influence the findings.
Part Five: Statutory and Executive
Order Reviews
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I. Executive Order 12866: Regulatory
Planning and Review
Under Executive Order (EO) 12866
(58 FR 51735, October 4, 1993), this
action is a ‘‘significant regulatory
action.’’ This action may raise novel
legal or policy issues [3(f)(4)] due to our
determination of Emission-Comparable
Fuel (ECF), as applied in this proposed
rulemaking. Accordingly, EPA
submitted this action to the Office of
Management and Budget (OMB) for
review under EO 12866. Any changes
made in response to OMB
recommendations have been
documented in the docket for this
action.
This rule, as proposed, is projected to
result in benefits to society in the form
of cost savings. The total net cost
savings are estimated at $23 million per
year. This figure is significantly below
the $100 million threshold 134
established under part 3(f)(1) of the
Order. Thus, this proposal is not
considered to be an economically
significant action. However, in an effort
to comply with the spirit of the Order,
we have prepared an economic
assessment in support of today’s
proposal. This document is entitled:
Assessment of the Potential Costs,
Benefits, and Other Impacts of the
Expansion of the RCRA Comparable
Fuel Exclusion-Proposed Rule, June
2007. The RCRA docket established for
today’s rulemaking maintains a copy of
this Assessment for public review.
Interested persons are encouraged to
read and comment on this document.
134 This $100 million threshold applies to both
costs, and cost savings.
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II. Paperwork Reduction Act
The information collection
requirements in this proposed rule have
been submitted for approval to the
Office of Management and Budget
(OMB) under the Paperwork Reduction
Act, 44 U.S.C. 3501 et seq. The
Information Collection Request (ICR)
document prepared by EPA has been
assigned EPA ICR number 1361.11.
Today’s proposed rule is deregulatory.
The respondents generating and burning
excluded emission-comparable fuel
would be subject to an annual public
reporting and recordkeeping burden for
the collection of information required
under this proposed rule of 75,284
hours, and a cost of $4,071,341.
However, because the excluded fuel
would no longer be considered
hazardous waste, the generator would
not be required to comply with the
paperwork, reporting, and
recordkeeping requirements for
hazardous wastes under RCRA.
Therefore, the reporting and
recordkeeping burden reduction
associated with the reduced
requirements for emission-comparable
fuel would result in a net annual burden
reduction of 21,206 hours and savings of
$3,186,590 in capital and operation and
maintenance costs.
Burden means the total time, effort, or
financial resources expended by persons
to generate, maintain, retain, disclose or
provide information to or for a Federal
agency. This includes the time needed
to review instructions; develop, acquire,
install, and utilize technology and
systems for the purposes of collecting,
validating, verifying, processing,
maintaining, disclosing and providing
information; adjust existing ways to
comply with any previously applicable
instructions and requirements; train
personnel to be able to respond to a
collection of information; search data
sources; complete and review the
collection of information; and transmit
or otherwise disclose the information.
An agency may not conduct or
sponsor, and a person is not required to
respond to a collection of information,
unless it displays a currently valid OMB
control number. The OMB control
numbers for EPA’s regulations in 40
CFR are listed in 40 CFR Part 9.
To comment on the Agency’s need for
this information, the accuracy of the
provided burden estimates, and any
suggested methods for minimizing
respondent burden, including the use of
automated collection techniques, EPA
has established a public docket for this
proposed rule, which includes this ICR,
under Docket ID number EPA–HQ–
RCRA–2005–0017. Submit any
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33321
comments related to the ICR for this
proposed rule to EPA and OMB. See
ADDRESSES section at the beginning of
this notice for where to submit
comments to EPA. Send comments to
OMB at the Office of Information and
Regulatory Affairs, Office of
Management and Budget, 725 17th
Street, NW., Washington, DC 20503,
Attention: Desk Office for EPA. Since
OMB is required to make a decision
concerning the ICR between 30 and 60
days after June 15, 2007, a comment to
OMB is best assured of having its full
effect if OMB receives it by July 16,
2007. The Agency will respond to any
public comments on the information
collection requirements contained in
this proposal in the final rule.
III. Regulatory Flexibility Act
The Regulatory Flexibility Act (RFA)
as amended by the Small Business
Regulatory Enforcement Fairness Act of
1996 (SBREFA), 5 U.S.C. 601 et seq.,
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act, or any
other statute. This analysis must be
completed unless the agency is able to
certify that the rule will not have a
significant economic impact on a
substantial number of small entities.
Small entities include small businesses,
small not-for-profit enterprises, and
small governmental jurisdictions.
The RFA provides default definitions
for each type of small entity. Small
entities are defined as: (1) A small
business as defined by the Small
Business Administration’s (SBA)
regulations at 13 CFR 121.201; (2) a
small governmental jurisdiction that is a
government of a city, county, town,
school district or special district with a
population of less than 50,000; and (3)
a small organization that is any not-forprofit enterprise which is independently
owned and operated and is not
dominant in its field.
After considering the economic
impacts of today’s proposal on small
entities, I certify that this action will not
have a significant economic impact on
a substantial number of small entities.
In determining whether a rule has a
significant economic impact on a
substantial number of small entities, the
impact of concern is any significant
adverse economic impact on small
entities, since the primary purpose of
the regulatory flexibility analyses is to
identify and address regulatory
alternatives ‘‘which minimize any
significant economic impact of the rule
on small entities.’’ 5 U.S.C. 603 and 604.
Thus, an agency may certify that a rule
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will not have a significant economic
impact on a substantial number of small
entities if the rule relieves regulatory
burden, or otherwise has a positive
economic effect on all of the small
entities subject to the rule. We have
determined that the affected ECF
generators are not owned by small
governmental jurisdictions or nonprofit
organizations. Therefore, only small
businesses were analyzed for small
entity impacts. For the purposes of the
impact analyses, small entity is defined
either by the number of employees or by
the dollar amount of sales. The level at
which a business is considered small is
determined for each North American
Industrial Classification System
(NAICS) code by the Small Business
Administration.
This rule, as proposed, is projected to
result in benefits in the form of cost
savings to facilities that use the
exclusion. As a result, the rule would
not result in adverse impacts for any
small businesses that generate ECF. The
reader is encouraged to review our
regulatory flexibility screening analysis
prepared in support of this
determination. This analysis is
incorporated in the Assessment
document, which is available in the
docket to today’s proposal. We continue
to be interested in the potential impacts
of the proposed rule on small entities
and welcome comments on issues
related to such impacts.
IV. Unfunded Mandates Reform Act of
1995
Title II of the Unfunded Mandates
Reform Act of 1995 (UMRA), Public
Law 104–4, establishes requirements for
Federal agencies to assess the effects of
their regulatory actions on State, local,
and tribal governments and the private
sector. Under section 202 of the UMRA,
EPA generally must prepare a written
statement, including a cost-benefit
analysis, for proposed and final rules
with ‘‘Federal mandates’’ that may
result in expenditures to State, local,
and tribal governments, in the aggregate,
or to the private sector, of $100 million
or more in any one year. Before
promulgating an EPA rule for which a
written statement is needed, section 205
of the UMRA generally requires EPA to
identify and consider a reasonable
number of regulatory alternatives and
adopt the least costly, most costeffective or least burdensome alternative
that achieves the objectives of the rule.
The provisions of section 205 do not
apply when they are inconsistent with
applicable law. Moreover, section 205
allows EPA to adopt an alternative other
than the least costly, most cost-effective
or least burdensome alternative if the
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Administrator publishes with the final
rule an explanation why that alternative
was not adopted. In addition, before
EPA establishes any regulatory
requirements that may significantly or
uniquely affect small governments,
including tribal governments, it must
have developed under section 203 of the
UMRA a small government agency plan.
The plan must provide for notifying
potentially affected small governments,
enabling officials of affected small
governments to have meaningful and
timely input in the development of EPA
regulatory proposals with significant
Federal intergovernmental mandates,
and informing, educating, and advising
small governments on compliance with
the regulatory requirements.
Today’s proposal contains no Federal
mandates (under the regulatory
provisions of Title II of the UMRA) for
State, local, or tribal governments or the
private sector. The UMRA generally
excludes from the definition of ‘‘Federal
intergovernmental mandate’’ duties that
arise from participation in a voluntary
federal program. This rule, as proposed,
may be considered a voluntary program
because the States are not required to
adopt these requirements.
In any event, EPA has determined that
this rule, as proposed, does not contain
a Federal mandate that may result in
expenditures of $100 million or more
for State, local, and tribal governments,
in the aggregate, or the private sector in
any one year. The total net benefits (cost
savings) of this action are estimated to
be $23 million per year.
EPA has determined that this rule
contains no regulatory requirements that
might significantly or uniquely affect
small governments. Small governments
are not affected by this action, as
proposed.
V. Executive Order 13132: Federalism
Executive Order 13132, entitled
‘‘Federalism’’ (64 FR 43255, August 10,
1999), requires EPA to develop an
accountable process to ensure
‘‘meaningful and timely input by State
and local officials in the development of
regulatory policies that have federalism
implications.’’ ‘‘Policies that have
federalism implications’’ is defined in
the Executive Order to include
regulations that have ‘‘substantial direct
effects on the States, on the relationship
between the national government and
the States, or on the distribution of
power and responsibilities among the
various levels of government.’’
This proposed rule does not have
federalism implications. It will not have
substantial direct effects on the States,
on the relationship between the national
government and the States, or on the
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distribution of power and
responsibilities among the various
levels of government, as specified in
Executive Order 13132. The proposed
rule focuses on modified requirements
for facilities generating ECF, without
affecting the relationships between
Federal and State governments. Thus,
Executive Order 13132 does not apply
to this rule.
Although section 6 of Executive Order
13132 does not apply to this proposed
rule, EPA did consult with
representatives of state governments in
developing it. Representatives from the
States of North Carolina, Georgia,
Missouri, Louisiana, and Oregon
provided valuable input and review.
In the spirit of Executive Order 13132,
and consistent with EPA policy to
promote communications between EPA
and State and local governments, EPA
specifically solicits comment on this
proposed rule from State and local
officials.
VI. Executive Order 13175:
Consultation and Coordination With
Indian Tribal Governments
Executive Order 13175, entitled
‘‘Consultation and Coordination with
Indian Tribal Governments’’ (65 FR
67249, November 9, 2000), requires EPA
to develop an accountable process to
ensure ‘‘meaningful and timely input by
tribal officials in the development of
regulatory policies that have tribal
implications.’’ This proposed rule does
not have tribal implications, as specified
in Executive Order 13175. No Tribal
governments are known to own or
operate hazardous waste generating
facilities that generate ECF subject to
this proposal. Thus, Executive Order
13175 does not apply to this proposed
rule.
VII. EO 13045 ‘‘Protection of Children
From Environmental Health Risks and
Safety Risks’’
EO 13045 ‘‘Protection of Children
from Environmental Health Risks and
Safety Risks’’ (62 FR 19885, April 23,
1997) applies to any rule that: (1) Is
determined to be ‘‘economically
significant’’ as defined under EO 12866,
and (2) concerns an environmental
health or safety risk that EPA has reason
to believe may have a disproportionate
effect on children. If the regulatory
action meets both criteria, the Agency
must evaluate the environmental health
or safety effects of the planned rule on
children, and explain why the planned
regulation is preferable to other
potentially effective and reasonably
feasible alternatives considered by the
Agency.
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This final rule is not subject to the
Executive Order because it is not
economically significant as defined in
Executive Order 12866, and because the
Agency does not have reason to believe
the environmental health or safety risks
addressed by this action present a
disproportionate risk to children.
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VIII. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
This rule is not a ‘‘significant energy
action’’ as defined in Executive Order
13211, ‘‘Actions Concerning Regulations
That Significantly Affect Energy Supply,
Distribution, or Use’’ (66 FR 28355 (May
22, 2001)) because it is not likely to
have a significant adverse effect on the
supply, distribution, or use of energy.
This rule, as proposed, will not
seriously disrupt energy supply,
distribution patterns, prices, imports or
exports. Furthermore, this proposed rule
is designed to improve economic
efficiency by expanding the use of ECF.
IX. National Technology Transfer
Advancement Act
Section 12(d) of the National
Technology Transfer and Advancement
Act of 1995 (‘‘NTTAA’’), Public Law
104–113, 12(d) (15 U.S.C. 272 note)
directs EPA to use voluntary consensus
standards in its regulatory activities
unless to do so would be inconsistent
with applicable law or otherwise
impractical. Voluntary consensus
standards are technical standards (e.g.,
materials specifications, test methods,
sampling procedures, and business
practices) that are developed or adopted
by voluntary consensus standards
bodies. The NTTAA directs EPA to
provide Congress, through OMB,
explanations when the Agency decides
not to use available and applicable
voluntary consensus standards.
This proposed rulemaking involves
environmental monitoring or
measurement. Consistent with the
Agency’s Performance Based
Measurement System (‘‘PBMS’’), EPA
proposes not to require the use of
specific, prescribed analytic methods.
Rather, the Agency plans to allow the
use of any method that meets the
prescribed performance criteria. The
PBMS approach is intended to be more
flexible and cost-effective for the
regulated community; it is also intended
to encourage innovation in analytical
technology and improved data quality.
EPA is not precluding the use of any
method, whether it constitutes a
voluntary consensus standard or not, as
long as it meets the performance criteria
specified.
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EPA welcomes comments on this
aspect of the proposed rulemaking and,
specifically, invites the public to
identify potentially-applicable
voluntary consensus standards and to
explain why such standards should be
used in this regulation.
X. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order (EO) 12898 (59 FR
7629 (Feb. 16, 1994)) establishes federal
executive policy on environmental
justice. Its main provision directs
federal agencies, to the greatest extent
practicable and permitted by law, to
make environmental justice part of their
mission by identifying and addressing,
as appropriate, disproportionately high
and adverse human health or
environmental effects of their programs,
policies, and activities on minority
populations and low-income
populations in the United States.
EPA has determined that this
proposed rule will not have
disproportionately high and adverse
human health or environmental effects
on minority or low-income populations
because it does not affect the level of
protection provided to human health or
the environment. This proposal is
designed to allow for the use of waste
as fuel under emission comparable
standards, resulting in no increased risk
to human health and the environment,
when compared to the burning of fossil
fuels.
List of Subjects in 40 CFR Part 261
Hazardous waste, Recycling,
Reporting and recordkeeping
requirements.
Dated: May 31, 2007.
Stephen L. Johnson,
Administrator.
For the reasons set out in the
preamble, title 40, chapter I, of the Code
of Federal Regulations is proposed to be
amended as follows:
PART 261—IDENTIFICATION AND
LISTING OF HAZARDOUS WASTE
1. The authority citation for part 261
continues to read as follows:
Authority: 42 U.S.C. 6905, 6912(a), 6921,
6922, and 6938.
2. Section 261.4 is amended by
revising paragraph (a)(16) to read as
follows:
§ 261.4
Exclusions.
(a) * * *
(16) Comparable fuels, emissioncomparable fuels, or comparable syngas
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fuels that meet the requirements of
§ 261.38.
*
*
*
*
*
3. Section 261.38 is revised to read as
follows:
§ 261.38 Exclusion of comparable fuel,
emission-comparable fuel, and syngas fuel.
(a) Specifications for excluded fuels.
Wastes that meet the specifications for
comparable fuel, emission-comparable
fuel, or syngas fuel under paragraphs
(a)(1), (a)(2), or (a)(3) of this section,
respectively, and the other requirements
of this section, are not solid wastes.
(1) Comparable fuel specifications.—
(i) Physical specifications.—(A) Heating
value. The heating value must exceed
5,000 BTU/lbs. (11,500 J/g).
(B) Viscosity. The viscosity must not
exceed: 50 cs, as-fired.
(ii) Constituent specifications. For
compounds listed in Table 1 to this
section the specification levels and,
where non-detect is the specification,
minimum required detection limits are:
(see Table 1 of this section).
(2) Emission-comparable fuel
specifications—(i) Physical
specifications.—(A) Heating value. The
heating value must exceed 5,000 BTU/
lbs (11,500 J/g).
(B) Viscosity. The viscosity must not
exceed 50 cSt, as-fired.
(ii) Constituent specifications—(A)
Except as provided by paragraph
(a)(2)(ii)(B) of this section, for
compounds listed in Table 1 of this
section the specification levels and,
where nondetect is the specification,
minimum required detection limits are:
(see Table 1).
(B) Waived specifications. The
specification levels in Table 1 to this
section do not apply for the following
hydrocarbons and oxygenates under the
special conditions provided under this
section for emission-comparable fuel:
(1) Benzene (CAS No. 71–43–2).
(2) Toluene (CAS No. 108–88–3).
(3) Acetophenone (CAS No. 98–86–2).
(4) Acrolein (CAS No. 107–02–8).
(5) Allyl alcohol (CAS No. 107–18–6).
(6) Bis(2-ethylhexyl)phthalate [Di-2ethylhexyl phthalate] (CAS No. 117–81–
7).
(7) Butyl benzyl phthalate (CAS No.
85–68–7).
(8) o-Cresol [2-Methyl phenol] (CAS
No. 95–48–7).
(9) m-Cresol [3-Methyl phenol] (CAS
No. 108–39–4).
(10) p-Cresol [4-Methyl phenol] (CAS
No. 106–44–5).
(11) Di-n-butyl phthalate (CAS No.
84–74–2).
(12) Diethyl phthalate (CAS No. 84–
66–2).
(13) 2,4-Dimethylphenol (CAS No.
105–67–9).
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(14) Dimethyl phthalate (CAS No.
131–11–3).
(15) Di-n-octyl phthalate (CAS No.
117–84–0).
(16) Endothall (CAS No. 145–73–3).
(17) Ethyl methacrylate (CAS No. 97–
63–2).
(18) 2-Ethoxyethanol [Ethylene glycol
monoethyl ether] (CAS No. 110–80–5).
(19) Isobutyl alcohol (CAS No. 78–83–
1).
(20) Isosafrole (CAS No. 120–58–1).
(21) Methyl ethyl ketone [2-Butanone]
(CAS No. 78–93–3).
(22) Methyl methacrylate (CAS No.
80–62–6).
(23) 1,4-Naphthoquinone (CAS No.
130–15–4).
(24) Phenol (CAS No. 108–95–2).
(25) Propargyl alcohol [2-Propyn-1-ol]
(CAS No. 107–19–7).
(26) Safrole (CAS No. 94–59–7); or
(3) Synthesis gas fuel specifications.—
Synthesis gas fuel (i.e., syngas fuel) that
is generated from hazardous waste must:
(i) Have a minimum Btu value of 100
Btu/Scf;
(ii) Contain less than 1 ppmv of total
halogen;
(iii) Contain less than 300 ppmv of
total nitrogen other than diatomic
nitrogen (N2);
(iv) Contain less than 200 ppmv of
hydrogen sulfide; and
(v) Contain less than 1 ppmv of each
hazardous constituent in the target list
of appendix VIII constituents of this
part.
(4) Blending to meet the specifications
for comparable fuel or emissioncomparable fuel. Hazardous waste shall
not be blended to meet the specification
under paragraphs (a)(1) or (a)(2) of this
section, except as follows:
(i) Blending to meet the viscosity
specification. A hazardous waste
blended to meet the viscosity
specification for comparable fuel or
emission-comparable fuel shall:
(A) As generated and prior to any
blending, manipulation, or processing,
meet the constituent and heating value
specifications of paragraphs (a)(1)(i)(A)
and (a)(1)(ii) of this section for
comparable fuel, and, for emissioncomparable fuel, the specifications of
paragraphs (a)(2)(i)(A) and (a)(2)(ii) of
this section;
(B) Be blended at a facility that is
subject to the applicable requirements of
parts 264 and 265, or § 262.34 of this
chapter; and
(C) Not violate the dilution
prohibition of paragraph (a)(7) of this
section.
(ii) Blending emission-comparable
fuel to meet the 8,000 Btu/lb, as-fired
condition. Emission-comparable fuel
may be blended with other fuels to meet
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the 8,000 Btu/lb, as-fired, condition of
paragraph (c)(2)(ii)(B) of this section.
(5) Treatment to meet the comparable
fuel or emission-comparable fuel
specifications. (i) A hazardous waste
may be treated to meet the
specifications of paragraphs (a)(1) or
(a)(2) of this section provided the
treatment:
(A) Destroys or removes the
constituent listed in the specification or
raises the heating value by removing or
destroying hazardous constituents or
materials;
(B) Is performed at a facility that is
subject to the applicable requirements of
parts 264 and 265, or § 262.34 of this
chapter; and
(C) Does not violate the dilution
prohibition of paragraph (a)(7) of this
section.
(ii) Residuals resulting from the
treatment of a hazardous waste listed in
subpart D of this part to generate a
comparable fuel remain a hazardous
waste.
(6) Generation of a syngas fuel. (i) A
syngas fuel can be generated from the
processing of hazardous wastes to meet
the exclusion specifications of
paragraph (a)(3) of this section provided
the processing:
(A) Destroys or removes the
constituent listed in the specification or
raises the heating value by removing or
destroying constituents or materials;
(B) Is performed at a facility that is
subject to the applicable requirements of
parts 264 and 265, or § 262.34 of this
chapter or is an exempt recycling unit
pursuant to § 261.6(c); and
(C) Does not violate the dilution
prohibition of paragraph (a)(7) of this
section.
(ii) Residuals resulting from the
treatment of a hazardous waste listed in
subpart D of this part to generate a
syngas fuel remain a hazardous waste.
(7) Dilution prohibition for
comparable fuel, emission-comparable
fuel, and syngas fuel. No generator,
transporter, handler, or owner or
operator of a treatment, storage, or
disposal facility shall in any way dilute
a hazardous waste to meet the
specifications of paragraphs (a)(1)(i)(A)
or (a)(1)(ii) of this section for
comparable fuel, or (a)(2)(i)(A) and
(a)(2)(ii) of this section for emissioncomparable fuel, or (a)(3) of this section
for syngas.
(b) Implementation—(1) General. (i)
Wastes that meet the specifications
provided by paragraph (a) of this section
for comparable fuel, emissioncomparable fuel, or syngas fuel are
excluded from the definition of solid
waste provided that the conditions
under this section are met. For purposes
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of this section, such wastes are called
excluded fuel, and the person claiming
and qualifying for the exclusion is
called the excluded fuel generator and
the person burning the excluded fuel is
called the excluded fuel burner.
(ii) The person who generates the
excluded fuel must claim the exclusion
by compliance with the conditions of
this section and keep records necessary
to document compliance with those
conditions.
(2) Notices—(i) Notices to state RCRA
and CAA Directors in authorized states
or regional RCRA and CAA Directors in
unauthorized states. The generator must
submit a one-time notice to the Regional
or State RCRA and CAA Directors, in
whose jurisdiction the exclusion is
being claimed and where the excluded
fuel will be burned, certifying
compliance with the conditions of the
exclusion and providing the following
documentation:
(A) The name, address, and RCRA ID
number of the person/facility claiming
the exclusion;
(B) The applicable EPA Hazardous
Waste Codes for the hazardous waste;
(C) The name and address of the units
meeting the requirements of paragraphs
(b)(3) and (c) of this section, that will
burn the excluded fuel;
(D) An estimate of the average and
maximum monthly and annual quantity
of waste for which an exclusion would
be claimed; and
(E) The following statement, which
shall be signed and submitted by the
person claiming the exclusion or his
authorized representative:
Under penalty of criminal and civil
prosecution for making or submitting false
statements, representations, or omissions, I
certify that the requirements of 40 CFR
261.38 have been met for all emissioncomparable fuel/comparable fuel (specify
which) identified in this notification. Copies
of the records and information required at 40
CFR 261.38 are available at the generator’s
facility. Based on my inquiry of the
individuals immediately responsible for
obtaining the information, the information is,
to the best of my knowledge and belief, true,
accurate, and complete. I am aware that there
are significant penalties for submitting false
information, including the possibility of fine
and imprisonment for knowing violations.
(ii) Public notice. Prior to burning an
excluded fuel, the burner must publish
in a major newspaper of general
circulation local to the site where the
fuel will be burned, a notice entitled
‘‘Notification of Burning a Fuel
Excluded Under the Resource
Conservation and Recovery Act’’ and
containing the following information:
(A) Name, address, and RCRA ID
number of the generating facility(ies);
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(B) Name and address of the burner
and identification of the unit(s) that will
burn the excluded fuel;
(C) A brief, general description of the
manufacturing, treatment, or other
process generating the excluded fuel;
(D) An estimate of the average and
maximum monthly and annual quantity
of the excluded waste to be burned; and
(E) Name and mailing address of the
Regional or State Directors to whom the
generator submitted a claim for
exclusion.
(3) Burning—(i) Comparable fuel and
syngas fuel. The exclusion for fuels
meeting the specifications under
paragraphs (a)(1) or (a)(3) of this section
applies only if the fuel is burned in the
following units that also shall be subject
to Federal/State/local air emission
requirements, including all applicable
CAA MACT requirements:
(A) Industrial furnaces as defined in
§ 260.10 of this chapter;
(B) Boilers, as defined in § 260.10 of
this chapter, that are further defined as
follows:
(1) Industrial boilers located on the
site of a facility engaged in a
manufacturing process where
substances are transformed into new
products, including the component
parts of products, by mechanical or
chemical processes; or
(2) Utility boilers used to produce
electric power, steam, heated or cooled
air, or other gases or fluids for sale;
(C) Hazardous waste incinerators
subject to regulation under subpart O of
parts 264 or 265 of this chapter or
applicable CAA MACT standards.
(D) Gas turbines used to produce
electric power, steam, heated or cooled
air, or other gases or fluids for sale.
(ii) Emission-comparable fuel. The
exclusion for fuel meeting the
specifications under paragraph (a)(2) of
this section applies only if the fuel is
burned under the conditions provided
by paragraph (c) of this section.
(4) Waste analysis plan for generators.
The generator of an excluded fuel shall
develop and follow a written waste
analysis plan which describes the
procedures for sampling and analysis of
the hazardous waste to be excluded. The
plan shall be followed and retained at
the facility excluding the waste.
(i) At a minimum, the plan must
specify:
(A) The parameters for which each
hazardous waste will be analyzed and
the rationale for the selection of those
parameters;
(B) The test methods which will be
used to test for these parameters;
(C) The sampling method which will
be used to obtain a representative
sample of the waste to be analyzed;
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(D) The frequency with which the
initial analysis of the waste will be
reviewed or repeated to ensure that the
analysis is accurate and up to date; and
(E) If process knowledge is used in the
waste determination, any information
prepared by the generator in making
such determination.
(ii) For each analysis, the generator
shall document the following:
(A) The dates and times that samples
were obtained, and the dates the
samples were analyzed;
(B) The names and qualifications of
the person(s) who obtained the samples;
(C) A description of the temporal and
spatial locations of the samples;
(D) The name and address of the
laboratory facility at which analyses of
the samples were performed;
(E) A description of the analytical
methods used, including any clean-up
and sample preparation methods;
(F) All quantitation limits achieved
and all other quality control results for
the analysis (including method blanks,
duplicate analyses, matrix spikes, etc.),
laboratory quality assurance data, and
the description of any deviations from
analytical methods written in the plan
or from any other activity written in the
plan which occurred;
(G) All laboratory results
demonstrating whether the exclusion
specifications have been met for the
waste; and
(H) All laboratory documentation that
support the analytical results, unless a
contract between the claimant and the
laboratory provides for the
documentation to be maintained by the
laboratory for the period specified in
paragraph (b)(7) of this section and also
provides for the availability of the
documentation to the claimant upon
request.
(iii) Syngas fuel generators shall
submit for approval, prior to performing
sampling, analysis, or any management
of a syngas fuel as an excluded waste,
a waste analysis plan containing the
elements of paragraph (b)(3)(i) of this
section to the appropriate regulatory
authority. The approval of waste
analysis plans must be stated in writing
and received by the facility prior to
sampling and analysis to demonstrate
the exclusion of a syngas. The approval
of the waste analysis plan may contain
such provisions and conditions as the
regulatory authority deems appropriate.
(5) Analysis plans for burners of
emission-comparable fuel. An emissioncomparable fuel burner is subject to the
waste analysis plan requirements under
paragraph (b)(4) of this section to
determine the heating value of the fuel
and the benzene and acrolein
concentration of the fuel if:
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33325
(i) The burner has not received
information from the generator for each
shipment documenting the heating
value of the fuel and the concentration
of benzene and acrolein;
(ii) The burner blends or otherwise
treats emission-comparable fuel to
achieve the 8,000 Btu/lb, as-fired
criterion under paragraph (c)(2)(ii)(B) of
this section; or
(iii) The burner blends or otherwise
treats emission-comparable fuel to
achieve a concentration of benzene or
acrolein of two percent or less, as-fired,
to avoid the emission-comparable fuel
firing rate restrictions of paragraph
(c)(2)(ii)(I) of this section.
(6) Excluded fuel sampling and
analysis—(i) General. For each waste
(and syngas) for which an exclusion is
claimed under the specifications
provided by paragraphs (a)(1), (a)(2), or
(a)(3) of this section, the generator of the
hazardous waste/syngas must test for all
the constituents in appendix VIII to this
part, except those that the generator
determines, based on testing or
knowledge, should not be present in the
waste/syngas, and, for emissioncomparable fuel, except for the
compounds listed in paragraph
(a)(2)(ii)(B) of this section. The generator
is required to document the basis of
each determination that a constituent
with an applicable specification should
not be present. The generator may not
determine that any of the following
categories of constituents with an
applicable specification should not be
present:
(A) A constituent that triggered the
toxicity characteristic for the waste
constituents that were the basis of the
listing of the waste stream, or
constituents for which there is a
treatment standard for the waste code in
40 CFR 268.40;
(B) A constituent detected in previous
analysis of the waste/syngas;
(C) Constituents introduced into the
process that generates the waste/syngas;
or
(D) Constituents that are byproducts
or side reactions to the process that
generates the waste/syngas.
Note to paragraph (b)(6)(i): Any claim
under this section must be valid and
accurate for all hazardous constituents;
a determination not to test for a
hazardous constituent will not shield a
generator from liability should that
constituent later be found in the waste/
syngas above the exclusion
specifications.
(ii) For each waste for which the
exclusion is claimed where the
generator of the excluded fuel is not the
original generator of the hazardous
waste, the generator of the excluded fuel
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may not use process knowledge
pursuant to paragraph (b)(6)(i) of this
section and must test to determine that
all of the constituent specifications of
paragraphs (a)(1) and (a)(2) of this
section, as applicable, have been met.
(iii) The excluded fuel generator may
use any reliable analytical method to
demonstrate that no constituent of
concern is present at concentrations
above the specification levels. It is the
responsibility of the generator to ensure
that the sampling and analysis are
unbiased, precise, and representative of
the waste/syngas. For the waste/syngas
to be eligible for exclusion, a generator
must demonstrate that:
(A) The 95% upper confidence limit
of the mean concentration for each
constituent of concern is not above the
specification level; and
(B) The analyses could have detected
the presence of the constituent at or
below the specification level.
(iv) Nothing in this paragraph
preempts, overrides or otherwise
negates the provision in § 262.11 of this
chapter, which requires any person who
generates a solid waste to determine if
that waste is a hazardous waste.
(v) In an enforcement action, the
burden of proof to establish
conformance with the exclusion
specification shall be on the generator
claiming the exclusion.
(vi) The generator must conduct
sampling and analysis in accordance
with the waste analysis plan developed
under paragraph (b)(4) of this section.
(vii) Excluded fuel that has not been
blended to meet the kinematic viscosity
specification shall be analyzed as
generated.
(viii) If hazardous waste is blended to
meet the kinematic viscosity
specification, the generator shall:
(A) Analyze the waste as generated to
ensure that it meets the constituent and
heating value specifications, except that
emission comparable fuel need not meet
the 8,000 Btu/lb, as-fired heating value
criterion of paragraph (a)(2)(i)(A) of this
section; and
(B) After blending, analyze the fuel
again to ensure that the blended fuel
continues to meet all excluded fuel
specifications.
(ix) Excluded fuel must be re-tested,
at a minimum, annually and must be
retested after a process change that
could change the chemical or physical
properties of the waste.
(x) If an emission-comparable fuel
burner has not received information
from the generator for each shipment
documenting the heating value of the
fuel and the concentration of benzene
and acrolein, the burner must sample
and analyze the fuel to determine the
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heating value and the concentration of
benzene and acrolein.
(xi) If a burner blends or treats
emission-comparable fuel to achieve an
as-fired heating value of 8,000 Btu/lb or
greater or an as-fired concentration of
benzene or acrolein of two percent or
lower, the burner shall determine the
heating value, benzene concentration, or
acrolein concentration, as relevant, by
analysis or information from the
generator prior to blending and must
analyze the fuel after blending or
treatment to determine the heating
value, benzene concentration, or
acrolein concentration, as relevant.
(7) Speculative accumulation.
Excluded fuel must not be accumulated
speculatively, as defined in
§ 261.1(c)(8).
(8) Records. The generator must
maintain records of the following
information on-site:
(i) All information required to be
submitted to the implementing
authority as part of the notification of
the claim:
(A) The owner/operator name,
address, and RCRA facility ID number of
the person claiming the exclusion;
(B) The applicable EPA Hazardous
Waste Codes for each hazardous waste
excluded as a fuel; and
(C) The certification signed by the
person claiming the exclusion or his
authorized representative.
(ii) A brief description of the process
that generated the hazardous waste and
process that generated the excluded
fuel, if not the same;
(iii) The monthly and annual
quantities of each waste claimed to be
excluded;
(iv) Documentation for any claim that
a constituent is not present in the
hazardous waste as required under
paragraph (b)(6) of this section;
(v) The results of all analyses and all
detection limits achieved as required
under paragraph (b)(4) of this section;
(vi) If the excluded waste was
generated through treatment or
blending, documentation of compliance
with the applicable provisions of
paragraphs (a)(4) and (a)(5) of this
section;
(vii) If the waste is to be shipped offsite, a certification from the burner as
required under paragraph (b)(10) of this
section;
(viii) The waste analysis plan and
documentation of all sampling and
analysis results as required by
paragraph (b)(4) of this section; and
(ix) If the generator ships excluded
fuel off-site for burning, the generator
must retain for each shipment the
following information on-site:
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(A) The name and address of the
facility receiving the excluded fuel for
burning;
(B) The quantity of excluded fuel
shipped and delivered;
(C) The date of shipment or delivery;
(D) A cross-reference to the record of
excluded fuel analysis or other
information used to make the
determination that the excluded fuel
meets the specifications as required
under paragraph (b)(4) of this section;
and
(E) A one-time certification by the
burner as required under paragraph
(b)(10) of this section.
(9) Records retention. Records must
be maintained for a period of three
years.
(10) Burner certification—(i)
Comparable fuel and syngas fuel. Prior
to submitting a notification to the State
and Regional Directors, a generator of
comparable fuel or syngas fuel excluded
under paragraphs (a)(1) or (a)(3) of this
section who intends to ship the
excluded fuel off-site for burning must
obtain a one-time written, signed
statement from the burner:
(A) Certifying that the excluded fuel
will only be burned in an industrial
furnace, industrial boiler, utility boiler,
or hazardous waste incinerator, as
required under paragraph (b)(3) of this
section;
(B) Identifying the name and address
of the facility that will burn the
excluded fuel; and
(C) Certifying that the state in which
the burner is located is authorized to
exclude wastes as excluded fuel under
the provisions of this section.
(ii) Emission-comparable fuel. Prior to
submitting a notification to the State
and Regional Directors, a generator of
emission-comparable fuel who intends
to ship the excluded fuel off-site for
burning must obtain a one-time written,
signed statement from the burner:
(A) Certifying that the excluded fuel
will be stored under the conditions of
paragraph (c)(1) of this section and
burned in a boiler under the conditions
of paragraph (c)(2) of this section, and
that the burner will comply with the
notification, reporting, and
recordkeeping conditions of paragraph
(c)(4) of this section;
(B) Identifying the name and address
of the facility that will burn the
excluded fuel; and
(C) Certifying that the state in which
the burner is located is authorized to
exclude wastes as excluded fuel under
the provisions of this section.
(11) Ineligible waste codes. Wastes
that are listed because of presence of
dioxins or furans, as set out in
Appendix VII of this part, are not
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eligible for this exclusion, and any fuel
produced from or otherwise containing
these wastes remains a hazardous waste
subject to full RCRA hazardous waste
management requirements.
(12) Regulatory status of boiler
residues. Burning excluded fuel that
was derived from a hazardous waste
listed under §§ 261.31 through 261.33
does not subject boiler residues,
including bottom ash and emission
control residues, to regulation as
derived-from hazardous waste.
(13) Residues in containers and tank
systems upon cessation of operations. (i)
Liquid and accumulated solid residues
that remain in a container or tank
system for more than 90 days after the
container or tank system ceases to be
operated for storage or transport of
excluded fuel product are subject to
regulation under parts 262 through 265,
268, 270, 271, and 124 of this chapter.
(ii) Liquid and accumulated solid
residues that are removed from a
container or tank system after the
container or tank system ceases to be
operated for storage or transport of
excluded fuel product are solid wastes
subject to regulation as hazardous waste
if the waste exhibits a characteristic of
hazardous waste under §§ 261.21
through 261.24 or if the emissioncomparable fuel was derived from a
hazardous waste listed under §§ 261.31
through 261.33 when the exclusion was
claimed.
(14) Waiver of RCRA Closure
Requirements. Interim status and
permitted storage units, and generator
storage units exempt from the permit
requirements under § 262.34 of this
chapter, are not subject to the closure
requirements of 40 CFR Parts 264 and
265 provided that the storage units have
been used to store only hazardous waste
that is subsequently excluded under the
conditions of this section, and that
afterward will be used only to store fuel
excluded under this section.
(15) Spills and leaks. Excluded fuel
that is spilled or leaked and that
therefore no longer meets the conditions
of the exclusion is discarded and must
be managed as a hazardous waste if it
exhibits a characteristic of hazardous
waste under §§ 261.21 through 261.24 or
if it was derived from a hazardous waste
listed in §§ 261.31 through 261.33 when
the exclusion was claimed.
(16) Nothing in this section preempts,
overrides, or otherwise negates the
provisions in CERCLA Section 103,
which establish reporting obligations for
releases of hazardous substances, or the
Department of Transportation
requirements for hazardous materials in
49 CFR parts 171 through 180.
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(c) Special conditions for emissioncomparable fuel. The following
additional conditions apply to emissioncomparable fuel—fuel that meets the
specifications under paragraph (a)(2) of
this section.
(1) Storage—(i) General. Emissioncomparable fuel may be stored in a tank,
tank car, or tank truck only.
(ii) Applicability. Emissioncomparable fuel tank systems that are
not subject to the hazardous substance
underground storage tank requirements
under § 280.42(b) of this chapter are
subject to the conditions of this
paragraph.
(iii) Spill prevention, control, and
countermeasures (SPCC) requirements.
Emission-comparable fuel tank systems
with a capacity greater than 55 gallons
and that are not subject to 40 CFR Part
280 (Standards for Underground Storage
Tanks) are subject to the following SPCC
requirements adopted from 40 CFR Part
112. You must comply with the adopted
conditions by substituting the term
‘‘emission-comparable fuel’’ for the term
‘‘oil,’’ and by substituting the term
‘‘release of emission-comparable fuel to
the environment’’ for the term
‘‘discharge as described in § 112.1(b).’’
(A) Section 112.2, Definitions. These
definitions apply to the adopted SPCC
requirements under paragraph
(c)(1)(iii)(B) through (c)(1)(iii)(D) of this
section.
(B) Sections 112.3(d) and 112.3(e) of
this chapter, Requirement to Prepare
and Implement a Spill Prevention,
Control, and Countermeasure Plan.
(1) You must prepare a Spill
Prevention, Control, and
Countermeasure Plan in writing, and in
accordance with the adopted provisions
of §§ 112.7 and 112.8 of this chapter;
(2) The SPCC Plan must be reviewed
and certified according to the provisions
of § 112.3(d) of this chapter and must be
made available to the Regional
Administrator according to the
provisions of § 112.3(e) of this chapter;
(3) You must amend your SPCC Plan
as directed by the Regional
Administrator upon a finding that
amendment is necessary to prevent and
contain releases of emission-comparable
fuel from your facility. You must
implement the amended SPCC Plan as
soon as possible, but not later than six
months after you amend your SPCC
Plan, unless the Regional Administrator
specifies another date;
(C) Sections 112.5(a) and 112.5(b) of
this chapter, Amendment of Spill
Prevention, Control, and
Countermeasures Plan by Owners or
Operators.
(1) You must comply with the
provisions of §§ 112.5(a) and 112.5(b) of
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this chapter by substituting the term
‘‘release of emission-comparable fuel to
the environment’’ for the term
‘‘discharge as described in § 112.1(b);’’
(2) You must have a Professional
Engineer certify any technical
amendment to your Plan in accordance
with § 112.3(d) of this chapter.
(D) Section 112.7 of this chapter,
General Requirements for Spill
Prevention, Control, and
Countermeasure Plans.
(1) You must comply with the
requirements of this section, except for
paragraphs (a)(2), (c), (d), and (k) of this
section.
(2) Your Plan may deviate from the
requirements §§ 112.7(g), (h)(2), (h)(3)
and (i), and the adopted provisions of
§ 112.8, where applicable to a specific
facility, if you provide equivalent
protection by some other means of spill
prevention, control, or countermeasure.
Where your Plan does not conform to
the applicable requirements in
§§ 112.7(g), (h)(2), (h)(3) and (i) and the
adopted provisions of § 112.8 of this
chapter, you must state the reasons for
nonconformance in your Plan and
describe in detail alternate methods and
how you will achieve equivalent
environmental protection. If the
Regional Administrator determines that
the measures described in your Plan do
not provide equivalent environmental
protection, he may require that you
amend your Plan.
(E) Section 112.8 of this chapter, Spill
Prevention, Control, and
Countermeasure Plan Requirements for
Onshore Facilities, except for paragraph
(b) of this section (facility drainage),
paragraph (c)(2) of this section
(secondary containment for bulk storage
containers), and paragraph (c)(11) of this
section (secondary containment for
mobile containers). In addition,
§ 112.8(d)(1) of this chapter applies to
all buried piping irrespective of the
installation or replacement date.
(iv) Containment and detection of
releases—To prevent the release of
emission comparable fuel or hazardous
constituents to the environment, you
must provide secondary containment for
emission-comparable fuel tank systems
as prescribed by the following
requirements adopted from § 264.193 of
this chapter. You must comply with the
adopted conditions by substituting the
term ‘‘emission-comparable fuel’’ for the
term ‘‘waste,’’ and by substituting the
term ‘‘document in the record’’ for the
term ‘‘demonstrate to the Regional
Administrator.’’
(A) Section 264.193(b) of this chapter,
which prescribes general performance
standards for secondary containment
systems;
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(B) Section 264.193(c) of this chapter,
which prescribes minimum
requirements for secondary containment
systems;
(C) Section 264.193(d)(1) through (3),
which prescribe permissible secondary
containment devices;
(D) Section 264.193(e) of this chapter,
which prescribes design and operating
requirements for the permissible
secondary containment devices; and
(E) Section 264.193(f) of this chapter,
which prescribes secondary
containment requirements for ancillary
equipment.
(v) Preparedness and prevention,
emergency procedures and response to
releases—(A) Preparedness and
prevention—(1) Required equipment.
Your facility must be equipped with the
equipment required under § 264.32(a)
through (d) of this chapter in a manner
that it can be used in emergencies
associated with storing and handling
emission-comparable fuel.
(2) Testing and maintenance of
equipment. You must test and maintain
as necessary to assure proper operation
in times of emergency all
communications or alarm systems, fire
protection equipment, spill control
equipment, and decontamination
equipment required for your emissioncomparable fuel tank system.
(3) Access to communications or
alarm system. Whenever emissioncomparable fuel is distributed into or
out of the tank system, all personnel
involved in the operation must have
immediate access to an internal alarm or
emergency communication device,
either directly or through visual or voice
contact with another employee.
(4) Arrangements with local
authorities. You must comply with
§ 264.37(a) of this chapter. If State or
local authorities decline to enter into
the arrangements prescribed by
§ 264.37(a) of this chapter, you must
keep a record documenting the refusal.
(B) Emergency procedures—(1)
Emergency coordinator. At all times,
there must be at least one employee
either on the facility premises or on call
(i.e., available to respond to an
emergency by reaching the facility
within a short period of time) with the
responsibility for coordinating all
emergency response measures. This
emergency coordinator must be
thoroughly familiar with all aspects of
the facility’s Spill Prevention, Control,
and Countermeasures (SPCC) Plan
required under paragraph (c)(1)(iii) of
this section, all emission-comparable
fuel operations and activities at the
facility, the location and characteristics
of emission-comparable fuel handled,
the location of all records within the
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facility pertaining to emissioncomparable fuel, and the facility layout.
In addition, this person must have the
authority to commit the resources
needed to carry out the SPCC Plan.
(2) Emergency procedures. (i)
Whenever there is an imminent or
actual emergency situation relating to
the emission-comparable fuel tank
system, the emergency coordinator (or
his designee when the emergency
coordinator is on call) must
immediately activate internal facility
alarms or communication systems,
where applicable, to notify all facility
personnel and notify appropriate State
or local agencies with designated
response roles if their help is needed.
(ii) Whenever there is a release, fire,
or explosion relating to the emissioncomparable fuel tank system, the
emergency coordinator must
immediately identify the character,
exact source, amount, and aerial extent
of any released materials. He may do
this by observation or review of facility
records, and, if necessary, by chemical
analysis.
(iii) Concurrently, the emergency
coordinator must assess possible
hazards to human health or the
environment that may result from the
release, fire, or explosion. This
assessment must consider both direct
and indirect effects of the release, fire,
or explosion (e.g., the effects of any
toxic, irritating, or asphyxiating gases
that are generated, or the effects of any
hazardous surface water run-off from
water or chemical agents used to control
fire and heat-induced explosions).
(iv) If the emergency coordinator
determines that the facility has had a
release, fire, or explosion associated
with the emission-comparable fuel tank
system which could threaten human
health, or the environment outside the
facility, he must report his findings as
provided by paragraph (c)(1)(v)(B)(2)(v)
of this section.
(v) If the emergency coordinator’s
assessment indicates that evacuation of
local areas may be advisable, he must
immediately notify appropriate local
authorities. He must be available to help
appropriate officials decide whether
local areas should be evacuated, and he
must immediately notify either the
government official designated as the
on-scene coordinator for that
geographical area, (in the applicable
regional contingency plan under part
1510 of this title) or the National
Response Center (using their 24-hour
toll free number 800/424–8802). The
report must include: the name and
telephone number of the reporter; the
name and address of the facility; the
time and type of incident (e.g., release,
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fire); the name and quantity of
material(s) involved, to the extent
known; the extent of injuries, if any; and
the possible hazards to human health, or
the environment, outside the facility.
(vi) During an emergency, the
emergency coordinator must take all
reasonable measures necessary to ensure
that fires, explosions, and releases do
not occur, recur, or spread to other
materials at the facility. These measures
must include, where applicable,
stopping processes and operations and
collecting and containing released
emission-comparable fuel.
(vii) If the emission-comparable fuel
tank system stops operations in
response to a fire, explosion, or release,
the emergency coordinator must
monitor for leaks, pressure buildup, gas
generation, or ruptures in valves, pipes,
or other equipment, wherever this is
appropriate.
(viii) Immediately after an emergency,
the emergency coordinator must provide
for treating, storing, or disposing of
recovered emission-comparable fuel,
contaminated soil or surface water, or
any other material that results from a
release, fire, or explosion at the facility.
(ix) The emergency coordinator must
ensure that, in the affected area(s) of the
facility: materials that may be
incompatible with the released
emission-comparable fuel is treated,
stored, or disposed of until cleanup
procedures are completed; and all
emergency equipment listed in the
SPCC Plan is cleaned and fit for its
intended use before operations are
resumed.
(x) You must note in the record the
time, date, and details of any incident
that requires implementing the SPCC
Plan for the emission-comparable fuel
tank system. Within 15 days after the
incident, you must submit a written
report on the incident to the Regional
Administrator. The report must include:
the name, address, and telephone
number of the owner or operator; the
name, address, and telephone number of
the facility; the date, time, and type of
incident (e.g., fire, explosion); the name
and quantity of material(s) involved; the
extent of injuries, if any; an assessment
of actual or potential hazards to human
health or the environment, where this is
applicable; and the estimated quantity
and disposition of recovered material
that resulted from the incident.
(C) Response to leaks or spills and
disposition of leaking or unfit-for-use
tank systems. (1) You must comply with
the provisions of § 264.196 of this
chapter, except for §§ 264.196(e)(1) and
(e)(4) of this chapter.
(2) To comply with the adopted
provisions of § 264.196, you must
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substitute the term ‘‘emissioncomparable fuel’’ for the terms
‘‘hazardous waste’’ and ‘‘waste;’’ and
the term ‘‘record’’ for the term
‘‘operating record,’’ and
(3) Unless you satisfy the
requirements of §§ 264.196(e)(2) and (3)
of this chapter, you must close the
emission-comparable fuel tank system.
(vi) Air emissions—(A) Applicability.
(1) If your emission-comparable fuel
storage tank or transfer rack is not
subject to the controls provided by
§ 63.2346 of this chapter, you must
comply with the provisions of
paragraphs (c)(1)(vi)(B) and (C) of this
section:
(2) If your emission-comparable fuel
storage tank is subject to the controls
provided by § 63.2346 of this chapter
other than those prescribed by item 6 in
Table 2 to subpart EEEE, part 63 of this
chapter (i.e., requirements for organic
liquids with an annual average true
vapor pressure of the total listed organic
HAP >=76.6 kilopascals (11.1 psia)), you
must determine whether the tank would
be subject to the controls prescribed by
item 6 after considering the vapor
pressure of the RCRA oxygenates listed
in paragraph (c)(1)(vi)(B)(3) of this
section as well as the organic HAP listed
in Table 1 to subpart EEEE, part 63 of
this chapter. If the annual average true
vapor pressure of the total RCRA
oxygenates and Table 1 organic HAP in
the emission-comparable fuel is >=76.6
kilopascals (11.1 psia), you are subject
to the requirements of paragraphs
(c)(1)(vi)(B) through (C) of this section.
(B) Conditions of applicability. When
complying with the conditions under
paragraph (c)(1)(vi)(C) of this section,
you must:
(1) Comply with the conditions
irrespective of whether your facility is
an area source as defined by § 63.2 of
this chapter.
(2) Comply with the conditions by
substituting the term ‘‘RCRA oxygenates
as well as organic HAP’’ for each
occurrence of the term ‘‘organic HAP;’’
the term ‘‘RCRA oxygenates as well as
organic HAP listed in Table 1’’ for each
occurrence of the term ‘‘organic HAP
listed in Table 1;’’ and the term ‘‘RCRA
oxygenates as well as Table 1 organic
HAP’’ for each occurrence of the term
‘‘Table 1 organic HAP.’’
(3) Comply with the conditions using
the following definition of RCRA
oxygenates: The term ‘‘RCRA
oxygenates’’ means the following
organic compounds:
(i) Allyl alcohol (CAS No. 107–18–6);
(ii) Bis(2-ethylhexyl)phthalate [Di-2ethylhexyl phthalate] (CAS No. 117–81–
7);
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(iii) 2,4-Dimethylphenol (CAS No.
105–67–9);
(iv) Ethyl methacrylate (CAS No. 97–
63–2);
(v) 2-Ethoxyethanol [Ethylene glycol
monoethyl ether] (CAS No. 110–80–5);
(vi) Isobutyl alcohol (CAS No. 78–83–
1);
(vii) Isosafrole (CAS No. 120–58–1);
(viii) Methyl ethyl ketone [2Butanone] (CAS No. 78–93–3);
(ix) 1,4-Naphthoquinone (CAS No.
130–15–4);
(x) Propargyl alcohol [2-Propyn-1-ol]
(CAS No. 107–19–7); and
(xi) Safrole (CAS No. 94–59–7).
(4) Comply with the conditions using
the following definition of organic
liquid. Organic liquid means emission
comparable fuel that:
(i) Contains 5 percent by weight or
greater of the RCRA oxygenates as well
as organic HAP listed in Table 1 to this
subpart, as determined using the
procedures specified in § 63.2354(c) of
this chapter; and
(ii) Has an annual average true vapor
pressure of 0.7 kilopascals (0.1 psia) or
greater.
(5) Comply with the conditions using
the following definition of affected
source. Affected source means the
collection of activities and equipment
used to distribute emission-comparable
fuel into, out of, or within a facility.
(6) Comply with the conditions by
substituting the term ‘‘subject to
§ 261.38(c)(1)(vi)(C)of this chapter’’ for
the term ‘‘subject to this subpart.’’
(7) Comply with the storage tank
controls in Table 2 to subpart EEEE, part
63 of this chapter as follows:
(i) If your tank has a capacity less than
18.9 cubic meters (5,000 gallons) and
the annual average true vapor pressure
of the total RCRA oxygenates and Table
1 organic HAP in the stored organic
liquid is >=76.6 kilopascals (11.1 psia),
you must comply with the requirements
under item 1 of Table 2 to subpart EEEE,
part 63 of this chapter, for existing
sources or item 3 of that table for
reconstructed or new sources; and
(ii) If your existing source tank has a
capacity identified in item 1 of Table 2
to subpart EEEE, part 63 of this chapter,
you must comply with the requirements
of item 1.a.i or 1.a.ii of that table if the
annual average true vapor pressure of
the total RCRA oxygenates and Table 1
organic HAP in the stored organic liquid
is >=5.2 kilopascals (0.75 psia) and
<76.6 kilopascals (11.1 psia);
(8) Comply with the conditions if:
(i) Your tank or transfer rack is
exempt from subpart EEEE, part 63 of
this chapter, under the provisions of
§ 63.228(c)(1) of this chapter, which
exempts tanks at facilities subject to a
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NESHAP other than subpart EEEE, part
63; and
(ii) The requirements applicable to the
tank or transfer rank under the other
NESHAP are not equivalent to, at a
minimum, the conditions under
paragraph (c)(1)(vi)(C) of this section.
You must document and record your
determination whether the requirements
under the other NESHAP are less
stringent than the conditions under
paragraph (c)(1)(vi)(C) of this section.
You may contact the RCRA regulatory
authority to assist with this
determination.
(9) Submit all notifications, reports,
and other communications to the RCRA
regulatory authority rather than the
CAA regulatory authority.
(C) Conditions to control air
emissions. (1) The affected source is the
equipment identified under
§ 63.2338(b)(1) through (5) of this
chapter, except for equipment identified
in § 63.2338(c)(2) through (3) of this
chapter.
(2) Definitions of new, reconstructed,
and existing affected sources are
provided under § 63.2338(d) through (f)
of this chapter.
(3) You must comply with the
emission limitations, operating limits,
and work practice standards under
§ 63.2346 of this chapter.
(4) You must comply with the general
requirements under § 63.2350 of this
chapter. The startup, shutdown, and
malfunction plan required by
§ 63.2350(c) of this chapter need not
address equipment not subject to
paragraph (c)(1)(vi)(C) of this section.
(5) You must comply with the
performance tests, design evaluation,
and performance evaluations
requirements under § 63.2354 of this
chapter. When complying with
§ 63.2354(c) of this chapter, however,
you must determine the content of
RCRA oxygenates as well as organic
HAP in the emission-comparable fuel.
(6) You must conduct performance
tests and other initial compliance
demonstrations by the dates specified in
§ 63.2358 of this chapter.
(7) You must conduct subsequent
performance tests by the dates specified
in § 63.2362 of this chapter.
(8) You must comply with the
monitoring, installation, operation, and
maintenance requirements under
§ 63.2366 of this chapter.
(9) You must demonstrate initial
compliance with the emission
limitations, operating limits, and work
practice standards as required under
§ 63.2370 of this chapter.
(10) You must monitor and collect
data to demonstrate continuous
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compliance and use the collected data
as required by § 63.2374 of this chapter.
(11) You must demonstrate
continuous compliance with the
emission limitations, operating limits,
and work practice standards as required
by § 63.2378 of this chapter.
(12) You must submit the
notifications and on the schedule
required by § 63.2382 of this chapter.
Notifications must be submitted to the
RCRA regulatory authority.
(13) You must submit the reports and
on the schedule required by § 63.2386 of
this chapter. Reports must be submitted
to the RCRA regulatory authority.
(14) You must keep the records
required by § 63.2390 of this chapter.
(15) You must keep records in the
form, and for the duration, required by
§ 63.2394 of this chapter.
(16) The parts of the General
Provisions that apply to you are
provided by § 63.2398 of this chapter.
(17) The definitions that apply to the
conditions under paragraph (c)(1)(vi)(C)
of this section are provided by § 63.2406
of this chapter, and paragraphs
(c)(1)(vi)(B)(3) through (5) of this
section.
(18) You are subject to the
requirements in Tables 1–12 to subpart
EEEE, part 63 of this chapter.
(vii) Underground storage tank
systems. Underground storage tank
systems are subject to the applicable
requirements under 40 CFR Part 280.
(viii) Management of incompatible
waste fuels and other materials. (A) The
generator must document in the waste
analysis plan under paragraph (b)(4) of
this section how (e.g., using trial tests,
analytical results, scientific literature, or
process knowledge) precautions will be
taken to prevent mixing of waste fuels
and other materials which could result
in reactions which:
(1) Generate extreme heat or pressure,
fire or explosions, or violent reactions;
(2) Produce uncontrolled toxic mists,
fumes, dusts, or gases;
(3) Produce uncontrolled flammable
fumes or gases; or
(4) Damage the structural integrity of
the storage unit or facility.
(B) Incompatible materials must not
be placed in the same tank.
(2) Burning—(i) General. Emissioncomparable fuel must be burned in an
industrial or utility boiler as defined in
paragraph (b)(3) of this section but that
is further restricted by being a watertube
type steam boiler that does not feed fuel
using a stoker or stoker-type
mechanism.
(ii) Operating conditions—(A) Fossil
fuel as primary fuel. A minimum of 50
percent of fuel fired to the device shall
be fossil fuel, fuels derived from fossil
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fuel, or tall oil. Such fuels are termed
‘‘primary fuel’’ for purposes of this
section. (Tall oil is a fuel derived from
vegetable and rosin fatty acids.) The 50
percent primary fuel firing rate shall be
determined on a total heat or volume
input basis, whichever results in the
greater volume feedrate of primary fuel
fired;
(B) Fuel heating value. Primary fuels
and emission-comparable fuel shall
have a minimum as-fired heating value
of 8,000 Btu/lb, and each material fired
in a firing nozzle where hazardous
waste is fired must have a heating value
of at least 8,000 Btu/lb, as-fired;
(C) CO CEMS. When burning
emission-comparable fuel, carbon
monoxide emissions must not exceed
100 parts per million by volume, over
an hourly rolling average (monitored
with a continuous emissions monitoring
system (CEMS)), dry basis and corrected
to 7 percent oxygen. You must use an
oxygen CEMS to continuously correct
the carbon monoxide level to 7 percent
oxygen. You must install, calibrate,
maintain, and continuously operate the
CEMS in compliance with the quality
assurance procedures provided in the
appendix to subpart EEE of part 63 of
this chapter (Quality Assurance
Procedures for Continuous Emissions
Monitors Used for Hazardous Waste
Combustors) and Performance
Specification 4B (carbon monoxide and
oxygen) in appendix B, part 60 of this
chapter.
(D) Dioxin/furan control. (1) If the
boiler is equipped with a dry particulate
matter control device and the primary
fuel is not coal, you must monitor the
combustion gas temperature at the inlet
to the dry particulate matter control
device, and the gas temperature must
not exceed 400 °F on an hourly rolling
average.
(2) Calibration of thermocouples. The
calibration of thermocouples must be
verified at a frequency and in a manner
consistent with manufacturer
specifications, but no less frequently
than once per year.
(E) Calculation of rolling averages—
(1) Calculation of rolling averages upon
intermittent operations. You must
ignore periods of time when one-minute
values are not available for calculating
the hourly rolling average. When oneminute values become available again,
the first one-minute value is added to
the previous 59 values to calculate the
hourly rolling average.
(2) Calculation of rolling averages
when the emission-comparable fuel feed
is cutoff. You must continue monitoring
carbon monoxide and combustion gas
temperature at the inlet to the dry
particulate matter emission control
PO 00000
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device when the emission-comparable
fuel feed is cutoff, but the source
continues operating on other fuels. You
must not resume feeding emissioncomparable fuel if the emission levels
exceed the limits provided in
paragraphs (c)(2)(ii)(C) and (D) of this
section.
(F) Automatic fuel cutoff system—(1)
General. You must operate the boiler
with a functioning system that
immediately and automatically cuts off
the emission-comparable fuel feed,
except as provided by paragraph
(c)(2)(ii)(F)(7) of this section:
(i) When the hourly rolling average
carbon monoxide level exceeds 100
ppmv or the combustion gas
temperature at the inlet to the initial dry
particulate matter control device
exceeds 400 °F on an hourly rolling
average.
(ii) When the span value of the
combustion gas temperature detector is
exceeded;
(iii) Upon malfunction of the carbon
monoxide CEMS or the gas temperature
detector; or
(iv) When any component of the
automatic waste feed cutoff system fails.
(2) Failure of the automatic fuel cutoff
system. If the automatic emissioncomparable fuel cutoff system fails to
automatically and immediately cut off
the flow of emission-comparable fuel
upon exceedance of the carbon
monoxide or gas temperature limits, you
have failed to comply with the
emission-comparable fuel cutoff
requirements of this section. If an
equipment failure prevents immediate
and automatic cutoff of the emissioncomparable fuel feed, however, you
must cease feeding emissioncomparable fuel as quickly as possible.
(3) Corrective measures. If, after any
automatic emission-comparable fuel
feed cutoff, the carbon monoxide or gas
temperature limit was exceeded while
emission-comparable fuel remained in
the combustion chamber, you must
investigate the cause of the automatic
emission-comparable fuel feed cutoff,
take appropriate corrective measures to
minimize future automatic cutoffs, and
record the findings and corrective
measures in the operating record.
(4) Excessive exceedance reporting. (i)
For each set of 10 exceedances of the
carbon monoxide emission limit or the
limit on the gas temperature at the inlet
to the dry particulate matter control
device while emission-comparable fuel
remains in the combustion chamber
(i.e., when the emission-comparable fuel
residence time has not transpired since
the emission-comparable fuel feed was
cut off) during a 60-day block period,
you must submit to the Administrator a
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Federal Register / Vol. 72, No. 115 / Friday, June 15, 2007 / Proposed Rules
written report within 5 calendar days of
the 10th exceedance documenting the
exceedances and results of the
investigation and corrective measures
taken.
(ii) On a case-by-case basis, the
Administrator may require excessive
exceedance reporting when fewer than
10 exceedances occur during a 60-day
block period.
(5) Testing. The automatic emissioncomparable fuel feed cutoff system and
associated alarms must be tested at least
weekly to verify operability, unless you
document in the operating record that
weekly inspections will unduly restrict
or upset operations and that less
frequent inspection will be adequate. At
a minimum, you must conduct
operability testing at least monthly. You
must document and record in the
operating record automatic emissioncomparable fuel feed cutoff system
operability test procedures and results.
(6) Ramping down emissioncomparable fuel feed. You may ramp
down the emission-comparable fuel
feedrate over a period not to exceed one
minute. If you elect to ramp down the
emission-comparable fuel feed, you
must document ramp down procedures
in the operating record. The procedures
must specify that the ramp down begins
immediately upon initiation of
automatic emission-comparable fuel
feed cutoff and the procedures must
prescribe a bona fide ramping down. If
the limit on carbon monoxide emissions
or gas temperature at the inlet to the dry
particulate matter control device is
exceeded during the ramp down, you
have failed to comply with those limits.
(G) Boiler load. Boiler load shall not
be less than 40 percent. Boiler load is
the ratio at any time of the total heat
input to the maximum design heat
input.
(H) Fuel atomization. The emissioncomparable fuel shall be fired directly
into the primary fuel flame zone of the
combustion chamber with an air or
steam atomization firing system,
mechanical atomization system, or a
rotary cup atomization system under the
following conditions:
(1) Particle size. The emissioncomparable fuel must pass through a
200 mesh (74 micron) screen, or
equivalent;
(2) Mechanical atomization systems.
Fuel pressure within a mechanical
atomization system and fuel flow rate
shall be maintained within the design
range taking into account the viscosity
and volatility of the fuel;
(3) Rotary cup atomization systems.
Fuel flow rate through a rotary cup
atomization system must be maintained
within the design range taking into
account the viscosity and volatility of
the fuel.
(I) Restrictions on benzene and
acrolein. If the as-fired concentration of
benzene or acrolein in the emissioncomparable fuel exceeds 2 percent by
mass, the firing rate of emissioncomparable fuel cannot exceed 25% of
the total fuel input to the boiler on a
heat or volume input basis, whichever
results in a lower volume input of
emission-comparable fuel.
(3) Intermediate handlers. ECF may
not be managed by any entity other than
the generator, transporter, and
designated burner.
(4) EPA Identification Number. A
burner that receives emissioncomparable fuel from an offsite
generator must obtain an EPA
identification number from the
Administrator. A burner who has not
received an EPA identification number
may obtain one by applying to the
Administrator using EPA form 8700–12.
Upon receiving the request, the
Administrator will assign an EPA
identification number to the burner.
(5) Notification, reporting, and
recordkeeping—(i) Initial Notification.
A burner that receives emissioncomparable fuel from an offsite
generator must submit an initial
notification to the Regional or State
RCRA and CAA Directors prior to
receiving the first shipment:
(A) Providing the name, address, and
EPA identification number of the burner
(B) Certifying that the excluded fuel
will be stored under the conditions of
paragraph (c)(1) of this section and
burned in a boiler under the conditions
of paragraph (c)(2) of this section, and
that the burner will comply with the
notification, reporting, and
recordkeeping conditions of paragraph
(c)(3) of this section;
(C) Identifying the specific units that
will burn the excluded fuel; and
(D) Certifying that the state in which
the burner is located is authorized to
exclude wastes as excluded fuel under
the provisions of this section.
(ii) Reporting. The burner must
submit to the Administrator excessive
CO exceedance reports required under
paragraph (c)(2)(ii)(F)(5) of this section.
(iii) Recordkeeping—(A) Records of
shipments. If the burner receives a
shipment of emission-comparable fuel
from an offsite generator, the burner
must retain for each shipment the
following information on-site:
(1) The name, address, and RCRA ID
number of the generator shipping the
excluded fuel;
(2) The quantity of excluded fuel
delivered; and
(3) The date of delivery;
(B) Boiler operating data. The burner
must retain records of information
required to comply with the operating
requirements of paragraph (c)(2) of this
section.
(C) Records retention. The burner
must retain records at the facility for
three years.
(d) Failure to comply with the
conditions of the exclusion. An
excluded fuel loses its exclusion if any
person managing the fuel fails to
comply with the conditions of the
exclusion under this section, and the
material must be managed as hazardous
waste from the point of generation. In
such situations, EPA or an authorized
state agency may take enforcement
action under RCRA section 3008(a).
TABLE 1 TO § 261.38.—DETECTION AND DETECTION LIMIT VALUES FOR COMPARABLE FUEL SPECIFICATION
rwilkins on PROD1PC63 with PROPOSALS2
Chemical name
Total Nitrogen as N ...................................................................................................
Total Halogens as Cl .................................................................................................
Total Organic Halogens as Cl ...................................................................................
Polychlorinated biphenyls, total [Aroclors, total] ........................................................
Cyanide, total .............................................................................................................
Metals:
Antimony, total ....................................................................................................
Arsenic, total .......................................................................................................
Barium, total .......................................................................................................
Beryllium, total ....................................................................................................
Cadmium, total ...................................................................................................
VerDate Aug<31>2005
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Jkt 211001
PO 00000
Concentration limit
(mg/kg at 10,000
Btu/lb)
Minimum required
detection limit
(mg/kg)
NA
NA
NA
1336–36–3
57–12–5
4900
540
(1)
ND
ND
..............................
..............................
7440–36–0
7440–38–2
7440–39–3
7440–41–7
7440–43–9
12
0.23
23
1.2
ND
..............................
..............................
..............................
..............................
1.2
CAS No.
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1.4
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Federal Register / Vol. 72, No. 115 / Friday, June 15, 2007 / Proposed Rules
TABLE 1 TO § 261.38.—DETECTION AND DETECTION LIMIT VALUES FOR COMPARABLE FUEL SPECIFICATION—Continued
rwilkins on PROD1PC63 with PROPOSALS2
Chemical name
Chromium, total ..................................................................................................
Cobalt .................................................................................................................
Lead, total ...........................................................................................................
Manganese .........................................................................................................
Mercury, total ......................................................................................................
Nickel, total .........................................................................................................
Selenium, total ....................................................................................................
Silver, total ..........................................................................................................
Thallium, total .....................................................................................................
Hydrocarbons:
Benzo[a]anthracene ............................................................................................
Benzene ..............................................................................................................
Benzo[b]fluoranthene ..........................................................................................
Benzo[k]fluoranthene ..........................................................................................
Benzo[a]pyrene ...................................................................................................
Chrysene ............................................................................................................
Dibenzo[a,h]anthracene ......................................................................................
7,12-Dimethylbenz[a]anthracene ........................................................................
Fluoranthene .......................................................................................................
Indeno(1,2,3-cd)pyrene ......................................................................................
3-Methylcholanthrene .........................................................................................
Naphthalene .......................................................................................................
Toluene ...............................................................................................................
Oxygenates:
Acetophenone .....................................................................................................
Acrolein ...............................................................................................................
Allyl alcohol .........................................................................................................
Bis(2-ethylhexyl)phthalate [Di-2-ethylhexyl phthalate] .......................................
Butyl benzyl phthalate ........................................................................................
o-Cresol [2-Methyl phenol] .................................................................................
m-Cresol [3-Methyl phenol] ................................................................................
p-Cresol [4-Methyl phenol] .................................................................................
Di-n-butyl phthalate ............................................................................................
Diethyl phthalate .................................................................................................
2,4-Dimethylphenol .............................................................................................
Dimethyl phthalate ..............................................................................................
Di-n-octyl phthalate .............................................................................................
Endothall .............................................................................................................
Ethyl methacrylate ..............................................................................................
2-Ethoxyethanol [Ethylene glycol monoethyl ether] ...........................................
Isobutyl alcohol ...................................................................................................
Isosafrole ............................................................................................................
Methyl ethyl ketone [2-Butanone] .......................................................................
Methyl methacrylate ...........................................................................................
1,4-Naphthoquinone ...........................................................................................
Phenol .................................................................................................................
Propargyl alcohol [2-Propyn-1-ol] .......................................................................
Safrole ................................................................................................................
Sulfonated Organics:
Carbon disulfide ..................................................................................................
Disulfoton ............................................................................................................
Ethyl methanesulfonate ......................................................................................
Methyl methanesulfonate ...................................................................................
Phorate ...............................................................................................................
1,3-Propane sultone ...........................................................................................
Tetraethyldithiopyrophosphate [Sulfotepp] .........................................................
Thiophenol [Benzenethiol] ..................................................................................
O,O,O-Triethyl phosphorothioate .......................................................................
Nitrogenated Organics:
Acetonitrile [Methyl cyanide] ...............................................................................
2-Acetylaminofluorene [2–AAF] ..........................................................................
Acrylonitrile .........................................................................................................
4-Aminobiphenyl .................................................................................................
4-Aminopyridine ..................................................................................................
Aniline .................................................................................................................
Benzidine ............................................................................................................
Dibenz[a,j]acridine ..............................................................................................
O,O-Diethyl O-pyrazinyl phosphorothioate [Thionazin] ......................................
Dimethoate .........................................................................................................
p-(Dimethylamino) azobenzene [4-Dime thylaminoazobenzene] .......................
VerDate Aug<31>2005
20:28 Jun 14, 2007
Jkt 211001
PO 00000
Concentration limit
(mg/kg at 10,000
Btu/lb)
Minimum required
detection limit
(mg/kg)
7440–47–3
7440–48–4
7439–92–1
7439–96–5
7439–97–6
7440–02–0
7782–49–2
7440–22–4
7440–28–0
2.3
4.6
31
1.2
0.25
58
0.23
2.3
23
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
56–55–3
71–43–2
205–99–2
207–08–9
50–32–8
218–01–9
52–70–3
57–97–6
206–44–0
193–39–5
56–49–5
91–20–3
108–88–3
2400
4100
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
36000
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
98–86–1
107–02–8
107–18–6
117–81–7
85–68–7
95–48–7
108–39–4
106–44–5
84–74–2
84–66–2
105–67–9
131–11–3
117–84–0
145–73–3
97–63–2
110–80–5
78–83–1
120–58–1
78–93–3
80–62–6
130–15–4
108–95–2
107–19–7
94–59–7
2400
39
30
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
100
39
100
39
2400
39
39
2400
2400
30
2400
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
..............................
75–15–0
298–04–4
62–50–0
66–27–3
298–02–2
1120–71–4
3689–24–5
108–98–5
126–68–1
ND
ND
ND
ND
ND
ND
ND
ND
ND
39
2400
2400
2400
2400
100
2400
30
2400
75–05–8
53–96–3
107–13–1
92–67–1
504–24–5
62–53–3
92–87–5
224–42–0
297–97–2
60–51–5
60–11–7
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
39
2400
39
2400
100
2400
2400
2400
2400
2400
2400
CAS No.
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33333
TABLE 1 TO § 261.38.—DETECTION AND DETECTION LIMIT VALUES FOR COMPARABLE FUEL SPECIFICATION—Continued
rwilkins on PROD1PC63 with PROPOSALS2
Chemical name
3,3[prime]-Dimethylbenzidine .............................................................................
a,a-Dimethylphenethylamine ..............................................................................
3,3[prime]-Dimethoxybenzidine ..........................................................................
1,3-Dinitrobenzene [m-Dinitrobenzene] ..............................................................
4,6-Dinitro-o-cresol .............................................................................................
2,4-Dinitrophenol ................................................................................................
2,4-Dinitrotoluene ...............................................................................................
2,6-Dinitrotoluene ...............................................................................................
Dinoseb [2-sec-Butyl-4,6-dinitrophenol] .............................................................
Diphenylamine ....................................................................................................
Ethyl carbamate [Urethane] ................................................................................
Ethylenethiourea (2-Imidazolidinethione) ...........................................................
Famphur .............................................................................................................
Methacrylonitrile ..................................................................................................
Methapyrilene .....................................................................................................
Methomyl ............................................................................................................
2-Methyllactonitrile [Acetone cyanohydrin] .........................................................
Methyl parathion .................................................................................................
MNNG (N-Metyl-N-nitroso-N[prime]-nitroguanidine) ..........................................
1-Naphthylamine [a-Naphthylamine] ..................................................................
2-Naphthylamine [(b-Naphthylamine] .................................................................
Nicotine ...............................................................................................................
4-Nitroaniline, [p-Nitroaniline] .............................................................................
Nitrobenzene ......................................................................................................
p-Nitrophenol, [p-Nitrophenol] ............................................................................
5-Nitro-o-toluidine ...............................................................................................
N-Nitrosodi-n-butylamine ....................................................................................
N-Nitrosodiethylamine ........................................................................................
N-Nitrosodiphenylamine [Diphenylnitrosamine] ..................................................
N-Nitroso-N-methylethylamine ............................................................................
N-Nitrosomorpholine ...........................................................................................
N-Nitrosopiperidine .............................................................................................
N-Nitrosopyrrolidine ............................................................................................
2-Nitropropane ....................................................................................................
Parathion ............................................................................................................
Phenacetin ..........................................................................................................
1,4-Phenylene diamine [p-Phenylenediamine] ...................................................
N-Phenylthiourea ................................................................................................
2-Picoline [alpha-Picoline] ..................................................................................
Propylthioracil [6-Propyl-2-thiouracil] ..................................................................
Pyridine ...............................................................................................................
Strychnine ...........................................................................................................
Thioacetamide ....................................................................................................
Thiofanox ............................................................................................................
Thiourea ..............................................................................................................
Toluene-2,4-diamine [2,4-Diaminotoluene] ........................................................
Toluene-2,6-diamine [2,6-Diaminotoluene] ........................................................
o-Toluidine ..........................................................................................................
p-Toluidine ..........................................................................................................
1,3,5-Trinitrobenzene [sym-Trinitobenzene] .......................................................
Halogenated Organics:
Allyl chloride .......................................................................................................
Aramite ...............................................................................................................
Benzal chloride [Dichloromethyl benzene] .........................................................
Benzyl chloride ...................................................................................................
bis(2-Chloroethyl)ether [Dichoroethyl ether] .......................................................
Bromoform [Tribromomethane] ..........................................................................
Bromomethane [Methyl bromide] .......................................................................
4-Bromophenyl phenyl ether [p-Bromo diphenyl ether] .....................................
Carbon tetrachloride ...........................................................................................
Chlordane ...........................................................................................................
p-Chloroaniline ....................................................................................................
Chlorobenzene ...................................................................................................
Chlorobenzilate ...................................................................................................
p-Chloro-m-cresol ...............................................................................................
2-Chloroethyl vinyl ether .....................................................................................
Chloroform ..........................................................................................................
Chloromethane [Methyl chloride] ........................................................................
2-Chloronaphthalene [beta-Chloronaphthalene] ................................................
2-Chlorophenol [o-Chlorophenol] .......................................................................
VerDate Aug<31>2005
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PO 00000
Concentration limit
(mg/kg at 10,000
Btu/lb)
Minimum required
detection limit
(mg/kg)
119–93–7
122–09–8
119–90–4
99–65–0
534–52–1
51–28–5
121–14–2
606–20–2
88–85–7
122–39–4
51–79–6
96–45–7
52–85–7
126–98–7
91–80–5
16752–77–5
75–86–5
298–00–0
707–25–7
134–32–7
91–59–8
54–11–5
100–01–6
98–96–3
100–02–7
99–55–8
924–16–3
55–18–5
86–30–6
10595–95–6
59–89–2
100–75–4
930–55–2
79–46–9
56–38–2
62–44–2
106–50–3
103–85–5
109–06–8
51–52–5
110–86–1
57–24–9
62–55–5
39196–18–4
62–56–6
95–80–7
823–40–5
95–53–4
106–49–0
99–35–4
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
2400
2400
100
2400
2400
2400
2400
2400
2400
2400
100
110
2400
39
2400
57
100
2400
110
2400
2400
100
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
2400
57
2400
100
2400
100
57
100
57
57
57
2400
100
2400
107–05–1
140–57–8
98–87–3
100–44–77
111–44–4
75–25–2
74–83–9
101–55–3
56–23–5
57–74–9
106–47–8
108–90–7
510–15–6
59–50–7
110–75–8
67–66–3
74–87–3
91–58–7
95–57–8
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
39
2400
100
100
2400
39
39
2400
39
14
2400
39
2400
2400
39
39
39
2400
2400
CAS No.
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33334
Federal Register / Vol. 72, No. 115 / Friday, June 15, 2007 / Proposed Rules
TABLE 1 TO § 261.38.—DETECTION AND DETECTION LIMIT VALUES FOR COMPARABLE FUEL SPECIFICATION—Continued
Chemical name
CAS No.
rwilkins on PROD1PC63 with PROPOSALS2
Chloroprene [2-Chloro-1,3-butadiene] ................................................................
2,4-D [2,4-Dichlorophenoxyacetic acid] ..............................................................
Diallate ................................................................................................................
1,2-Dibromo-3-chloropropane .............................................................................
1,2-Dichlorobenzene [o-Dichlorobenzene] .........................................................
1,3-Dichlorobenzene [m-Dichlorobenzene] ........................................................
1,4-Dichlorobenzene [p-Dichlorobenzene] .........................................................
3,3[prime]-Dichlorobenzidine ..............................................................................
Dichlorodifluoromethane [CFC–12] ....................................................................
1,2-Dichloroethane [Ethylene dichloride] ............................................................
1,1-Dichloroethylene [Vinylidene chloride] .........................................................
Dichloromethoxy ethane [Bis(2-chloroethoxy)methane] .....................................
2,4-Dichlorophenol ..............................................................................................
2,6-Dichlorophenol ..............................................................................................
1,2-Dichloropropane [Propylene dichloride] .......................................................
cis-1,3-Dichloropropylene ...................................................................................
trans-1,3-Dichloropropylene ...............................................................................
1,3-Dichloro-2-propanol ......................................................................................
Endosulfan I ........................................................................................................
Endosulfan II .......................................................................................................
Endrin .................................................................................................................
Endrin aldehyde ..................................................................................................
Endrin Ketone .....................................................................................................
Epichlorohydrin [1-Chloro-2,3-epoxy propane] ...................................................
Ethylidene dichloride [1,1-Dichloroethane] .........................................................
2-Fluoroacetamide ..............................................................................................
Heptachlor ..........................................................................................................
Heptachlor epoxide .............................................................................................
Hexachlorobenzene ............................................................................................
Hexachloro-1,3-butadiene [Hexachlorobutadiene] .............................................
Hexachlorocyclopentadiene ................................................................................
Hexachloroethane ...............................................................................................
Hexachlorophene ................................................................................................
Hexachloropropene [Hexachloropropylene] .......................................................
Isodrin .................................................................................................................
Kepone [Chlordecone] ........................................................................................
Lindane [gamma-BHC] [gamma-Hexachlorocyclohexane] ................................
Methylene chloride [Dichloromethane] ...............................................................
4,4[prime]-Methylene-bis(2-chloroaniline) ..........................................................
Methyl iodide [Iodomethane] ..............................................................................
Pentachlorobenzene ...........................................................................................
Pentachloroethane ..............................................................................................
Pentachloronitrobenzene [PCNB] [Quintobenzene] [Quintozene] .....................
Pentachlorophenol ..............................................................................................
Pronamide ..........................................................................................................
Silvex [2,4,5-Trichlorophenoxypropionic acid] ....................................................
2,3,7,8-Tetrachlorodibenzo-p-dioxin [2,3,7,8-TCDD] ..........................................
1,2,4,5-Tetrachlorobenzene ................................................................................
1,1,2,2-Tetrachloroethane ..................................................................................
Tetrachloroethylene [Perchloroethylene] ............................................................
2,3,4,6-Tetrachlorophenol ...................................................................................
1,2,4-Trichlorobenzene .......................................................................................
1,1,1-Trichloroethane [Methyl chloroform] ..........................................................
1,1,2-Trichloroethane [Vinyl trichloride] ..............................................................
Trichloroethylene ................................................................................................
Trichlorofluoromethane [Trichlormonofluoromethane] ........................................
2,4,5-Trichlorophenol ..........................................................................................
2,4,6-Trichlorophenol ..........................................................................................
1,2,3-Trichloropropane .......................................................................................
Vinyl Chloride .....................................................................................................
Concentration limit
(mg/kg at 10,000
Btu/lb)
Minimum required
detection limit
(mg/kg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
39
7
3400
39
2400
2400
2400
2400
39
39
39
2400
2400
2400
39
39
39
30
1.4
1.4
1.4
1.4
1.4
30
39
100
1.4
2.8
2400
2400
2400
2400
59000
2400
2400
4700
1.4
39
100
39
2400
39
2400
2400
2400
7
30
2400
39
39
2400
2400
39
39
39
39
2400
2400
39
39
1126–99–8
94–75–7
2303–16–4
96–12–8
95–50–1
541–73–1
106–46–7
91–94–1
75–71–8
107–06–2
75–35–4
111–91–1
120–83–2
87–65–0
78–87–5
10061–01–5
10061–02–6
96–23–1
959–98–8
33213–65–9
72–20–8
7421–93–4
53494–70–5
106–89–8
75–34–3
640–19–7
76–44–8
1024–57–3
118–74–1
87–68–3
77–47–4
67–72–1
70–30–4
1888–71–7
465–73–6
143–50–0
58–89–9
75–09–2
101–14–4
74–88–4
608–93–5
76–01–7
82–68–8
87–88–5
23950–58–5
93–72–1
1746–01–6
95–94–3
79–35–4
127–18–4
58–90–2
120–82–1
71–56–6
79–00–5
79–01–6
75–69–4
95–95–4
88–06–2
96–18–4
75–01–4
Notes: NA—Not Applicable. ND—Nondetect.
or individual halogenated organics listed below.
1 25
[FR Doc. E7–11130 Filed 6–14–07; 8:45 am]
BILLING CODE 6560–50–P
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Agencies
[Federal Register Volume 72, Number 115 (Friday, June 15, 2007)]
[Proposed Rules]
[Pages 33284-33334]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: E7-11130]
[[Page 33283]]
-----------------------------------------------------------------------
Part II
Environmental Protection Agency
-----------------------------------------------------------------------
40 CFR Part 261
Expansion of RCRA Comparable Fuel Exclusion; Proposed Rule
Federal Register / Vol. 72, No. 115 / Friday, June 15, 2007 /
Proposed Rules
[[Page 33284]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 261
[EPA-HQ-RCRA-2005-0017; FRL-8324-2]
RIN 2050-AG24
Expansion of RCRA Comparable Fuel Exclusion
AGENCY: Environmental Protection Agency (EPA).
ACTION: Proposed rule.
-----------------------------------------------------------------------
SUMMARY: EPA is proposing to expand the comparable fuel exclusion under
the rules implementing subtitle C of the Resource Conservation and
Recovery Act (RCRA) for fuels that are produced from hazardous waste
but which generate emissions that are comparable to emissions from
burning fuel oil when such fuels are burned in an industrial boiler.
Such excluded fuel would be called emission-comparable fuel (ECF). ECF
would be subject to the same specifications that currently apply to
comparable fuels, except that the specifications for certain
hydrocarbons and oxygenates would not apply. The ECF exclusion would be
conditioned on requirements including: Design and operating conditions
for the ECF boiler to ensure that the ECF is burned under the good
combustion conditions typical for oil-fired industrial boilers; and
conditions for tanks storing ECF which conditions are typical of those
for storage of commercial fuels, and are tailored for the hazards that
ECF may pose.
DATES: Comments must be received on or before August 14, 2007. Under
the Paperwork Reduction Act, comments on the information collection
provisions must be received by OMB on or before July 16, 2007.
ADDRESSES: Submit your comments, identified by Docket ID No. EPA-HQ-
RCRA-2005-0017, by one of the following methods:
https://www.regulations.gov: Follow the on-line
instructions for submitting comments.
E-mail: rcra-docket@epa.gov.
Fax: 202-566-9744.
Mail: RCRA Docket, Environmental Protection Agency,
Mailcode: 2822T, 1200 Pennsylvania Ave., NW., Washington, DC 20460.
Please include a total of two copies. We request that you also send a
separate copy of your comments to the contact person listed below (see
FOR FURTHER INFORMATION CONTACT). In addition, please mail a copy of
your comments on the information collection provisions to the Office of
Information and Regulatory Affairs, Office of Management and Budget
(OMB), Attn: Desk Officer for EPA, 725 17th St., NW., Washington, DC
20503.
Hand Delivery: RCRA Docket, EPA Docket Center (2822T), EPA
West, Room 3334, 1301 Constitution Ave., NW., Washington, DC. Such
deliveries are only accepted during the Docket's normal hours of
operation, and special arrangements should be made for deliveries of
boxed information. Please include a total of two copies. We request
that you also send a separate copy of each comment to the contact
person listed below (see FOR FURTHER INFORMATION CONTACT).
Instructions: Direct your comments to Docket ID No. EPA-HQ-RCRA-
2005-0017. EPA's policy is that all comments received will be included
in the public docket without change and may be made available online at
https://www.regulations.gov, including any personal information
provided, unless the comments include information claimed to be
Confidential Business Information (CBI) or other information the
disclosure of which is restricted by statute. Do not submit information
that you consider to be CBI or otherwise protected through https://
www.regulations.gov or e-mail. Send or deliver information identified
as CBI to the following address: Ms. LaShan Haynes, RCRA Document
Control Officer, EPA (Mail Code 5305P), Attention Docket ID No. EPA-HQ-
RCRA-2005-0017, 1200 Pennsylvania Avenue, NW., Washington, DC 20460.
Clearly mark the part or all of the information that you claim to be
CBI. The https://www.regulations.gov Web site is an ``anonymous access''
system, which means EPA will not know your identity or contact
information unless you provide it in the body of your comment. If you
send an e-mail comment directly to EPA without going through https://
www.regulations.gov, your e-mail address will be automatically captured
and included as part of the comment that is placed in the public docket
and made available on the Internet. If you submit an electronic
comment, EPA recommends that you include your name and other contact
information in the body of your comment and with any disk or CD-ROM you
submit. If EPA cannot read your comment due to technical difficulties
and cannot contact you for clarification, EPA may not be able to
consider your comment. Electronic files should avoid the use of special
characters, any form of encryption, and be free of any defects or
viruses. For additional information about EPA's public docket, visit
the EPA Docket Center homepage at https://www.epa.gov/epahome/
dockets.htm. We also request that interested parties who would like
information they previously submitted to EPA to be considered as part
of this action identify the relevant information by docket entry
numbers and page numbers.
Docket: All documents in the docket are listed in the https://
www.regulations.gov index. Although listed in the index, some
information is not publicly available, e.g., CBI or other information
whose disclosure is restricted by statute. Certain other material, such
as copyrighted material, will be publicly available only in hard copy.
Publicly available docket materials are available either electronically
in https://www.regulations.gov or in hard copy at the RCRA Docket, EPA/
DC, EPA West, Room 3334, 1301 Constitution Ave., NW., Washington, DC.
The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday
through Friday, excluding legal holidays. The telephone number for the
Public Reading Room is (202) 566-1744, and the telephone number for the
RCRA Docket is (202) 566-0270.
FOR FURTHER INFORMATION CONTACT: Mary Jackson, Hazardous Waste
Minimization and Management Division, Office of Solid Waste, Mailcode:
5302P, Environmental Protection Agency, 1200 Pennsylvania Ave., NW.,
Washington, DC 20460; telephone number: (703) 308-8453; fax number:
(703) 308-8433; e-mail address: jackson.mary@epa.gov.
SUPPLEMENTARY INFORMATION:
General Information
A. Does This Action Apply to Me?
Categories and entities potentially affected by this action
include:
--------------------------------------------------------------------------------------------------------------------------------------------------------
Category NAICS code SIC code Examples of potentially regulated entities
--------------------------------------------------------------------------------------------------------------------------------------------------------
Any industry that generates or combusts 562 49 Waste Management and Remediation Services.
hazardous waste as defined in the proposed
rule.
327 32 Non-metallic Mineral Products Manufacturing.
[[Page 33285]]
325 28 Chemical Manufacturing.
324 29 Petroleum and Coal Products Manufacturing.
331 33 Primary Metals Manufacturing.
333 38 Machinery Manufacturing.
326 306 Plastic and Rubber Products Manufacturing.
488, 561 49 Administration and Support Services.
421 50 Scrap and waste materials.
422 51 Wholesale Trade, Non-durable Goods, N.E.C.
512, 541, 812 73 Business Services, N.E.C.
512, 514, 541, 711 89 Services, N.E.C.
924 95 Air, Water and Solid Waste Management.
336 37 Transportation Equipment Manufacturing.
928 97 National Security.
334 35 Computer and Electronic Products Manufacturing.
339 38 Miscellaneous Manufacturing.
--------------------------------------------------------------------------------------------------------------------------------------------------------
This table is not intended to be exhaustive, but rather provides a
guide for readers regarding entities likely to be impacted by this
action. This table lists examples of the types of entities EPA is now
aware could potentially be regulated by this action. Other types of
entities not listed could also be affected. To determine whether your
facility, company, business, organization, etc., is affected by this
action, you should examine the applicability criteria in this proposed
rule. If you have any questions regarding the applicability of this
action to a particular entity, consult the person listed in the
preceding FOR FURTHER INFORMATION CONTACT section.
B. What Should I Consider as I Prepare My Comments for EPA?
1. Submitting CBI. Do not submit this information to EPA through
https://www.regulations.gov or e-mail. Clearly mark the part or all of
the information that you claim to be CBI. For CBI information in a disk
or CD ROM that you mail to EPA, mark the outside of the disk or CD ROM
as CBI and then identify electronically within the disk or CD ROM the
specific information that is claimed as CBI. In addition to one
complete version of the comment that includes information claimed as
CBI, a copy of the comment that does not contain the information
claimed as CBI must be submitted for inclusion in the public docket.
Information so marked will not be disclosed except in accordance with
procedures set forth in 40 CFR part 2.
2. Tips for Preparing Your Comments. When submitting comments,
remember to:
Identify the rulemaking by docket number and other
identifying information (subject heading, Federal Register date and
page number).
Follow directions--The agency may ask you to respond to
specific questions or organize comments by referencing a Code of
Federal Regulations (CFR) part or section number.
Explain why you agree or disagree; suggest alternatives
and substitute language for your requested changes.
Describe any assumptions and provide any technical
information and/or data that you used.
If you estimate potential costs or burdens, explain how
you arrived at your estimate in sufficient detail to allow for it to be
reproduced.
Provide specific examples to illustrate your concerns, and
suggest alternatives.
Explain your views as clearly as possible, avoiding the
use of profanity or personal threats.
Make sure to submit your comments by the comment period
deadline identified.
3. Docket Copying Costs:
You may copy a maximum of 100 pages from any regulatory docket at
no charge. Additional copies are 15 cents/page.
4. How Do I Obtain a Copy of This Document and Other Related
Information?
In addition to being available in the docket, an electronic copy of
today's proposed rule will also be available on the Worldwide Web
(WWW). Following the Administrator's signature, a copy of this document
will be posted on the WWW at https://www.epa.gov/hwcmact. This Web site
also provides other information related to the NESHAP for hazardous
waste combustors.
5. Index of Contents
The information presented in this preamble is organized as follows:
Part One: Background and Summary
I. Statutory Authority
II. Background
A. What Is the Intent of This Proposed Rule?
B. Who Would Be Affected by This Proposed Rule?
C. What Is the Relationship Between the Proposed Rule and the
Existing Exclusion for Comparable Fuel?
1. What Modifications to the Comparable Fuel Exclusion May Be
Warranted?
2. How Has EPA Involved Stakeholders in Discussions Regarding
Potential Revisions to the Comparable Fuel Exclusion?
III. Summary of the Proposed Rule
A. What Are the Conditions for Exclusion of Emission-Comparable
Fuel (ECF)?
B. What Changes Is EPA Proposing to the Conditions for Existing
Comparable Fuel?
Part Two: Rationale for the Proposed Rule
I. What Is the Rationale for Excluding Emission-Comparable Fuel
From the Definition of Solid Waste?
A. Why Would the Specifications Be Waived Only for Hydrocarbons
and Oxygenates?
B. Do Available Data and Information Support a Comparable
Emissions Finding?
1. Evaluation of Organic Emissions Data for Hazardous Waste
Boilers
2. Evaluation of RCRA Risk Assessments
3. Comparative Risk Assessment for Dioxin/Furan
II. What Conditions Would Apply to Burners of Emission-
Comparable Fuel?
A. Why Isn't a DRE Performance Test a Critical Requirement To
Ensure Good Combustion Conditions?
B. What Is the Rationale for the Proposed Burner Conditions?
1. ECF Must Be Burned in a Watertube Steam Industrial or Utility
Boiler That Is Not Stoker-Fired
2. CO Monitoring
3. The Boiler Must Fire at Least 50% Primary Fuel
4. The Boiler Load Must Be 40% or Greater
5. The ECF Must Have an As-Fired Heating Value of 8,000 Btu/lb
or Greater
6. ECF Must Be Fired Into the Primary Fuel Flame Zone
[[Page 33286]]
7. The ECF Firing System Must Provide Proper Atomization
8. Dioxin/Furan Controls for Boilers Equipped With an ESP or FF
III. What Restrictions Would Apply to Particular Hydrocarbons
and Oxygenates?
A. What Is the Rationale for the Relative Hazard
Characterization Scheme?
B. What Are the Results of the Relative Hazard Ranking?
C. What Firing Rate Restrictions Would Apply to Benzene and
Acrolein?
IV. What Conditions Would Apply to Storage of ECF?
A. What Are the Proposed Storage Conditions?
1. Tank Systems, Tank Cars and Tank Trucks
2. Underground Storage Tank Systems
3. Closure of Tank Systems
4. Waiver of RCRA Closure for RCRA Tanks That Become ECF Tanks
5. Management of Incompatible Waste Fuels and Other Materials
B. What Other Options Did We Consider?
1. Other Options We Considered to Establish Storage Conditions
for ECF
2. Consideration of Storage Controls for Currently Excluded
Comparable Fuels
V. How Would We Assure That The Conditions Are Being Satisfied?
A. What Recordkeeping, Notification and Certificate Conditions
Would Apply to Generators and Burners?
1. Waste Analysis Plans
2. Sampling and Analysis
3. Speculative Accumulation
4. Notifications
5. Burner Certification
6. Recordkeeping
7. Transportation
8. Ineligible RCRA Hazardous Waste Codes
B. What If I Fail To Comply With Conditions of the Exclusion?
C. How Would Spills and Leaks Be Managed?
D. What Would Be the Time-Line for Meeting the Proposed
Conditions?
VI. What Clarifications and Revisions Are Proposed for the
Existing Conditions for Exclusion of Comparable Fuel?
VII. What Are the Responses to Major Comments of the Peer Review
Panel?
A. What Are the Reponses to Major Comments Regarding the
Comparable Emissions Rationale?
B. What Are the Reponses to Major Comments Regarding the
Application of the WMPT To Rank Comparable Fuel Constituents?
Part Three: State Authority
I. Applicability of the Rule in Authorized States
II. Effect on State Authorization
Part Four: Costs and Benefits of the Proposed Rule
I. Introduction
II. Baseline Specification
III. Analytical Methodology, Primary Data Sources, and Key
Assumptions
IV. Key Analytical Limitations
V. Findings
Part Five: Statutory and Executive Order Reviews
I. Executive Order 12866: Regulatory Planning and Review
II. Paperwork Reduction Act
III. Regulatory Flexibility Act
IV. Unfunded Mandates Reform Act of 1995
V. Executive Order 13132: Federalism
VI. Executive Order 13175: Consultation and Coordination With
Indian Tribal Governments
VII. EO 13045 ``Protection of Children From Environmental Health
Risks and Safety Risks''
VIII. Executive Order 13211: Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use
IX. National Technology Transfer Advancement Act
X. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
Part One: Background and Summary
I. Statutory Authority
These regulations are proposed under the authority of sections
2002, 3001, 3002, 3003, and 3004 of the Solid Waste Disposal Act of
1970, as amended by the Resource Conservation and Recovery Act of 1976
(RCRA), as amended by the Hazardous and Solid Waste Amendments of 1984
(HSWA), 42 U.S.C. 6921, 6922, 6923, and 6924.
II. Background
A. What Is the Intent of This Proposed Rule?
Section 40 CFR 261.38 states that secondary materials (i.e.,
materials that otherwise would be hazardous wastes) which have fuel
value and whose hazardous constituent levels are comparable to those
found in the fossil fuels which would be burned in their place are not
solid wastes, and hence not hazardous wastes. We are proposing to amend
the comparable fuel exclusion by expanding the exclusion to include
fuels that are produced from a hazardous waste but which generate
emissions when burned in an industrial boiler that are comparable to
emissions from burning fuel oil. In other words, the fuels would be
comparable from an emissions standpoint but not a physical standpoint.
The revised rule would establish a new category of excluded waste-
derived fuel called emission-comparable fuel (ECF).
The quantity of waste fuels excluded under this approach would
increase substantially the amount of hazardous waste fuels that would
eligible for exclusion from the RCRA hazardous waste regulations.
Specifically, we estimate that approximately 13,000 tons per year of
waste fuels are currently excluded under the existing comparable fuel
exclusion, while we project that up to an additional 107,000 tons per
year may be excluded under the exclusion being proposed today.
These additional hazardous secondary materials could be burned for
energy recovery without imposing unnecessary regulatory costs on
generators, primarily the manufacturing sector. However, the expanded
comparable fuel exclusion may not substantially increase the amount of
hazardous waste burned for energy recovery because high Btu wastes,
even though not currently excluded from RCRA, are currently burned in
industrial furnaces and incinerators for their fuel value. Nonetheless,
continuing to regulate these waste-derived fuels as hazardous wastes
would treat a potentially valuable fuel commodity (especially
considering the increasing value of fuels) as a waste without a
compelling basis.
B. Who Would Be Affected by This Proposed Rule?
Entities that generate, burn, and store ECF are potentially
affected by this proposal. The basic structure of the proposal is that
ECF is no longer a solid (and hazardous) waste, and hence that each of
these entities would not be subject to subtitle C regulation when
managing ECF. Thus, generators of hazardous waste fuels that meet the
conditions of the ECF exclusion could manage these fuels without being
subject to subtitle C regulation assuming that the management
conditions are satisfied. Burners, which are limited to certain
industrial boilers (including utility boilers), could burn ECF provided
the boilers meet the design and operating conditions in the proposed
rule, as discussed in Part II, Section II. Generators would benefit
from lower operating costs because of lower (or eliminated) waste
management fees and because these fuels would substitute for fuels
which would otherwise be purchased. In addition, entities storing ECF
would not be subject to subtitle C standards provided they satisfy the
management conditions tailored to ECF, as discussed in Part Two,
Section IV.
Commercial hazardous waste combustors that are currently managing
waste fuels that qualify as ECF, on the other hand, might find
themselves unable to continue to charge hazardous waste management fees
for the excluded waste fuels. Consequently, commercial hazardous waste
combustors might lose the waste management revenues for those diverted
fuels and may need to meet their heat input requirements by using other
waste fuels or fossil fuels.
[[Page 33287]]
C. What Is the Relationship Between the Proposed Rule and the Existing
Exclusion for Comparable Fuel?
On June 19, 1998 (63 FR 33782 and Sec. 261.38), EPA promulgated
standards to exclude from the regulatory definition of solid waste
certain hazardous waste-derived fuels that meet specification levels
for hazardous constituents and physical properties that affect burning
which are comparable to the same levels in fossil fuels. EPA's goal was
to develop a comparable fuel specification which is useable by the
regulated community, but assures that an excluded waste-derived fuel is
similar in composition to commercially available fuel and therefore
poses no greater risk than burning fossil fuel.
During the eight years that the comparable fuel exclusion has been
part of the hazardous waste regulations, several stakeholders have
pointed out that many hazardous wastes with fuel value do not satisfy
the terms of the exclusion. Independently, in 2003, EPA began examining
the effectiveness of the current comparable fuel program as part of an
effort to promote the energy conservation component of the Resource
Conservation Challenge \1\ to determine whether other hazardous wastes
could be appropriately excluded as comparable fuel.
---------------------------------------------------------------------------
\1\ See https://www.epa.gov/epaoswer/osw/conserve/strat-plan/
strat-plan.htm#rccplan.
---------------------------------------------------------------------------
As part of this effort, we contacted the American Chemistry Council
(ACC) in early 2003 to determine how much waste is currently excluded
as comparable fuel and whether there were additional quantities of
other high Btu wastes that could potentially be considered comparable
fuel. ACC conducted a survey of its members and provided results to EPA
in late 2003 indicating that approximately 13,000 tons per year of
waste fuels are currently excluded, but that approximately 190,000 tons
per year of additional waste fuels could potentially be excluded under
revisions to the exclusion.\2\
---------------------------------------------------------------------------
\2\ Letter from American Chemistry Council (Carter Lee Kelly,
Leader, Waste Issues Team, and Robert A. Elam, Director, Regulatory
Affairs, Waste Issues Team) to Robert Springer and Matt Hale, USEPA,
dated November 24, 2003.
---------------------------------------------------------------------------
Therefore, ACC recommended that EPA consider approaches to address
the following barriers perceived as excluding additional quantities of
waste fuels:
Analytic Issues: High analysis cost and matrix
interferences hamper meeting the detection limit requirements for
nondetected analytes in many waste fuel matrices.
Over-Rigid Specifications: Wastes containing
nonhalogenated organics and oxygenates do not result in emissions
greater than burning waste fuel meeting the specification if the
combustor operates under good combustion conditions.
Blending: The current exclusion bans blending to meet
hazard constituent specifications. Flexibility is needed on blending of
streams containing low levels of constituents, such as chromium and
manganese attributable to corrosion from stainless steel vessels and
pipes.
1. What Modifications to the Comparable Fuel Exclusion May Be
Warranted?
We are proposing in this action to expand the exclusion for
comparable fuel to establish a new category of excluded fuel--emission-
comparable fuel (ECF). This proposal would exclude waste fuels that
generate emissions, when burned in an industrial boiler, which are
comparable to emissions from burning fuel oil. ECF would be subject to
the same hazardous constituent and other specifications in Table 1 to
Sec. 261.38 that currently apply to comparable fuels, except that the
specifications for certain hydrocarbons and oxygenates would not apply.
The exclusion would be based on the rationale that ECF has substantial
fuel value, that the hydrocarbon and oxygenate constituents no longer
subject to a specification add fuel value, and that emissions from
burning ECF in an industrial boiler operating under good combustion
conditions are likely not to differ from emissions from burning fossil
fuels under those same conditions. As a result, the current
specifications limiting the hydrocarbons and oxygenates appear to be
unnecessary.
The exclusion would be conditioned on the ECF being burned and
stored under certain conditions, including: (1) Design and operating
conditions for the ECF boiler that ensure that the ECF is burned under
the good combustion conditions typical for oil-fired industrial
boilers; and (2) conditions for storage in tanks which are comparable
to those for storage of fuels and organic liquids and which are
tailored for the hazards that ECF may pose given that ECF can have
higher concentrations of certain hydrocarbons and oxygenates than fuel
oil and gasoline.
We are not proposing revisions to the comparable fuel exclusion to
address the analytical and blending recommendations raised by ACC.
a. Why Are We Not Proposing Revisions To Address Analytic Concerns?
The specifications in Table 1 to Sec. 261.38 for volatile organic
compounds that were not detected in fuel oil or gasoline were based on
the low levels of detection achievable for fuel oil rather than the
much higher levels of detection achievable for gasoline. Given that
only benzene, toluene, and naphthalene were detected, EPA used this
approach for most of the volatile organic compounds. EPA acknowledged
this deviation from establishing the specification for nondetected
compounds as the highest level of detection in a benchmark fuel and
explained that the levels of detection for volatile compounds in
gasoline were inflated because of matrix effects. ACC suggested that
EPA consider the fact that many waste fuels may pose the same matrix
effects as gasoline, such that the fuel oil-based specifications would
not be reasonably achievable.
We believe that it would not be appropriate to consider increasing
the specifications for all volatile organic compounds and base them on
the higher levels of detection in gasoline rather than fuel oil levels
of detection because most of the compounds would simply not be expected
to be found in fuel oil or gasoline. Rather, only certain hydrocarbons
would be expected to be in these fuels. We could potentially also
consider oxygenates, however, because they are within a class of
compounds that are added to fuels to enhance combustion. It appeared,
however, that this revision would not likely result in additional
hazardous waste fuel being conditionally excluded. There were very few,
if any, waste fuels that meet the specifications for all volatile
compounds, except for the enumerated hydrocarbons and oxygenates, and
that also could meet revised, higher specifications for the
hydrocarbons and oxygenates based on the levels of detection in
gasoline. Consequently, we are not pursuing this approach further but,
nonetheless, solicit comment on such an approach.
b. Why Are We Not Proposing Revisions To Address Blending Concerns?
A condition of the existing comparable fuel exclusion is that blending
to meet the specification (except for viscosity) is prohibited to
preclude dilution to avoid treatment.\3\ ACC noted that waste fuels
often contain incidental contamination of metals, such as chromium and
manganese from corrosion of stainless steel vessels and pipes, and that
blending to meet the specifications for
[[Page 33288]]
low levels of metals appears reasonable. We believe that blending to
meet the specifications for metals is explicitly prohibited because it
would be inconsistent with the section 3004(m) hazardous waste
treatment provisions (which, although not directly applicable,
articulate important overall statutory objectives) which require
hazardous constituents to be removed or destroyed by treatment, not
diluted. See 63 FR at 33795.
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\3\ See 63 FR at 33795, and existing Sec. 261.38(c)(3-4).
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We believe, however, that blending to meet the specification for
organic compounds that may be present in fuel oil or gasoline--
hydrocarbons--or that are within a class of compounds that are added to
fuels to enhance combustion--oxygenates--could be considered. These
compounds would not be diluted to avoid treatment; they would still be
treated by combustion. However, it appears that there were very few, if
any, additional waste fuels that would be excluded under such a
blending provision. Nonetheless, we solicit comment on such an approach
and its applicability to additional waste fuels.
2. How Has EPA Involved Stakeholders in Discussions Regarding Potential
Revisions to the Comparable Fuel Exclusion?
On December 15, 2005, EPA convened a public meeting of stakeholders
to discuss potential revisions to the comparable fuel exclusion under
40 CFR 261.38.\4\ Meeting notes are available in the docket for this
rulemaking.\5\ Participants in the stakeholder meeting raised several
issues during the meeting and our responses are included in the meeting
notes. In addition, several participants submitted written comments
after the meeting. These comments and our responses are available in
the docket to today's proposal.\6\
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\4\ See e-mail from Jim Berlow, USEPA, to Jim Pew, Earthjustice;
Melvin Keener, Coalition for Responsible Waste Incineration; David
Case, Environmental Technology Council; Michael Benoit, Cement Kiln
Recycling Coalition; Barbara Simcoe, Association of State and
Territorial Solid Waste Management Officials; and Robert Elam,
American Chemistry Council, dated November 23, 2005.
\5\ See memorandum from Bob Holloway, USEPA, to Docket Number
RCRA 2005-0017, entitled ``Meeting Notes--Comparable Fuel
Stakeholder Meeting on Dec. 15, 2005,'' dated January 4, 2006.
\6\ USEPA, ``Response to Comments on the December 15, 2005
Stakeholder Meeting Regarding Expanding the Comparable Fuel
Exclusion,'' May 2007.
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III. Summary of the Proposed Rule
Today's proposed rule would expand the comparable fuel exclusion by
conditionally waiving the specifications for certain hydrocarbons and
oxygenates listed in Table 1 to Sec. 261.38. This excluded waste fuel
would be called emission-comparable fuel. We are also proposing to
clarify the regulatory status of existing comparable fuel that no
longer meets the conditions of the exclusion.
A. What Are the Conditions for Exclusion of Emission-Comparable Fuel
(ECF)?
ECF is a fuel derived from hazardous waste but which would be
excluded from the RCRA hazardous waste regulations if it meets
prescribed specifications and management conditions. The ECF
specifications would be the same as those that are applicable to
comparable fuel, except the specifications for particular hydrocarbons
and oxygenates would not apply. See proposed Sec. 261.38(a)(2). The
exclusion would apply from the point that ECF meets the specifications.
Special conditions of the exclusion specific to ECF would include
the following design and operating conditions for the ECF burner: (1)
The burner must be a watertube steam boiler other than a stoker-fired
boiler; (2) carbon monoxide (CO) must be monitored continuously, must
be linked to an automatic ECF feed cutoff system, and must not exceed
100 ppmv on an hourly rolling average (corrected to 7% oxygen); (3) the
boiler must fire at least 50% primary fuel on a heating value or volume
basis, whichever results in a higher volume of primary fuel, and the
primary fuel must be fossil fuel or tall oil with a heating value not
less than 8,000 Btu/lb; (4) the boiler load must be 40% or greater; (5)
the ECF must have an as-fired heating value of 8,000 Btu/lb or greater;
(6) ECF must be fired into the primary fuel flame zone; (7) the ECF
firing system must provide proper atomization; and (8) if the boiler is
equipped with an electrostatic precipitator (ESP) or fabric filter (FF)
and does not fire coal as the primary fuel, the combustion gas
temperature at the inlet to the ESP or FF must be continuously
monitored, must be linked to the automatic ECF feed cutoff system, and
must not exceed 400 [deg]F on an hourly rolling average. See proposed
Sec. 261.38(c)(2). (Please note that we specifically request comment
on these proposed conditions, as discussed later.) The principal
conditions that would apply to ECF boilers--waterwall steam boiler, low
CO, burning high Btu primary fuel that is properly atomized, operating
at boiler loads above 40%--reflect design and operating conditions
typical for oil-fired industrial boilers that operate under good
combustion conditions.
In addition, ECF must be stored in tanks, tank cars, or tank
trucks. See proposed Sec. 261.38(c)(1). These tank systems, tank cars,
and tank trucks would be excluded from regulation if they meet
conditions similar to those which apply to fuel oil (the product most
analogous to ECF), along with additional conditions necessary to
minimize the potential for releases to the environment accounting for
the differences between ECF and fuel oil. These include: (1) Certain
provisions of the Spill Prevention, Control, and Countermeasures (SPCC)
requirements applicable to oil under Sec. Sec. 112.2, 112.5, 112.7,
and 112.8; (2) secondary containment and leak detection requirements
for tank systems, including use of liners, vaults, or double-walled
tanks; (3) preparedness and prevention, emergency procedures, and
response to release provisions adopted from requirements applicable to
tank systems that store hazardous waste, and (4) fugitive air emission
technical controls adopted from Subpart EEEE, Part 63, for organic
liquids distribution (which would apply not only to any hazardous air
pollutants among the oxygenates and hydrocarbons, but also would apply
to the 11 oxygenates for which there would be no specification in this
proposed rule and which are hazardous constituents under RCRA having
significant vapor pressure but which are not hazardous air pollutants
under the CAA). Underground tanks storing ECF are subject to the
applicable requirements of 40 CFR Part 280. A further condition of the
exclusion is that the generator must document in the waste analysis
plan how precautions will be taken to prevent mixing of ECF and other
materials which could result in adverse consequences from incompatible
materials. In addition, to be excluded, ECF would need to meet all of
the conditions applicable to existing comparable fuel, including: (1)
The specifications under Table 1 to 261.38, except for the
specifications for certain hydrocarbons and oxygenates; (2) prohibition
on blending to meet the specifications, except for viscosity; \7\ (3)
notifications to state RCRA and Clean Air Act (CAA) Directors and
public notification; (4) waste analysis plans; (5) sampling and
analysis conditions; (6) prohibition on speculative accumulation; (7)
recordkeeping; (8)
[[Page 33289]]
burner certification to the generator; and (9) ineligible waste codes.
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\7\ ECF must have a heating value of 5,000 Btu/lb or greater as-
generated (or after bona fide treatment), but must have a heating
value of 8,000 Btu/lb, as fired. Thus, ECF with an as-generated
heating value below 8,000 Btu/lb may be blended with other fuels to
achieve a heating value of 8,000 Btu/lb.
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ECF that has lost its exclusion because of failure to satisfy a
condition of the exclusion must be managed as a hazardous waste from
the point of ECF generation.\8\ In addition, ECF that is spilled or
leaked and cannot be burned under the conditions of the exclusion is a
waste (it is a hazardous waste if it exhibits a characteristic of
hazardous waste or if the ECF were derived from a listed hazardous
waste) and must be managed in accordance with existing federal and
state regulations. Furthermore, if an ECF tank system ceases to be
operated to store ECF product, but has not been cleaned by removing all
liquids and accumulated solids within 90 days of cessation of ECF
storage operations, the tank system would become subject to the RCRA
subtitle C hazardous waste regulations.\9\ (This is the same principle
that applies to any product storage unit when it goes out of service.
See Sec. 261.4(c).) Liquids and accumulated solids removed from a tank
system that ceases to be operated for storage of ECF product are waste
(they are hazardous wastes if they exhibit a characteristic of
hazardous waste or if the ECF were derived from a listed hazardous
waste).
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\8\ Please note that we request comment on whether the final
rule should include a ``reasonable efforts'' provision that would
provide that the failure of an off-site, unaffiliated burner to meet
the proposed conditions or restrictions of the exclusion would not
mean the material was considered waste when handled by the
generator, as long as the generator can adequately demonstrate that
he has made reasonable efforts to ensure that the material will be
managed by the burner under the conditions of the exclusion. See
discussion in Part Two, Section V.B of the preamble.
\9\ If the tank is used to actively accumulate hazardous waste
after being taken out of service as an ECF product tank, the tank
may be eligible for the provisions under Sec. 262.34 that waive the
permit requirements for generator tanks that accumulate hazardous
waste for not more than 90 days.
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B. What Changes Is EPA Proposing to the Conditions for Existing
Comparable Fuel?
The proposed rule would restructure the current conditions for
comparable fuel (and syngas fuel) to make the regulatory language more
readable given that the regulation must accommodate the proposed
exclusion for ECF. Consequently, we are redrafting the entire section
for clarity. In addition, we are making technical corrections to
several provisions of the rule.\10\ We regard these language changes as
purely technical, and thus will accept comment only on whether the
suggested language change expresses the current meaning of the
provision. We are not reexamining, reconsidering, or otherwise
reopening these provisions for comment.
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\10\ See memorandum from Bob Holloway, USEPA, to Docket ID No.
EPA-HQ-RCRA-2005-0017, dated January 10, 2007.
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We are, however, proposing to amend several provisions that apply
to comparable fuel for the same reasons that we are proposing to apply
the amended provisions to ECF. We specifically request comment on
whether these clarifications and conforming amendments are appropriate:
We are proposing to clarify the consequences of failure to
satisfy the conditions of the existing comparable fuel exclusion. The
material must be managed as hazardous waste from the point of
generation. In addition, we are proposing to clarify that excluded fuel
that is spilled or leaked and that no longer meets the conditions of
the exclusion must be managed as a hazardous waste if it exhibits a
characteristic of hazardous waste or if it was derived from a listed
hazardous waste when the exclusion was claimed. See proposed Sec.
261.38(d).
We are proposing to clarify the status of tanks that cease
to be operated as comparable fuel storage tanks. The tank system
becomes subject to the RCRA hazardous waste facility standards if not
cleaned of liquids and accumulated solids within 90 days of ceasing
operations as a comparable fuel tank. In addition, we are proposing to
clarify that liquids and accumulated solids removed from the tank after
the tank ceases to be operated as a comparable fuel product tank must
be managed as hazardous waste if they exhibit a characteristic of
hazardous waste or if they were derived from a listed hazardous waste
when the exclusion was claimed. See proposed Sec. 261.38(b)(13).
We are proposing to waive the RCRA closure requirements
for tank systems that are used only to store hazardous wastes that are
subsequently excluded as comparable fuel. See proposed Sec.
261.38(b)(14).
We are proposing to clarify the regulatory status of
boiler residues, including bottom ash and emission control residue.
Burning excluded fuel that was derived from a listed hazardous waste
does not subject boiler residues to regulation as derived-from
hazardous waste. See Sec. 261.38(b)(12).
We are proposing that the one-time notice by the generator
to regulatory officials include an estimate of the average and maximum
monthly and annual quantity of waste for which an exclusion would be
claimed.\11\ See proposed Sec. 261.38(b)(2)(i)(D).
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\11\ Providing an estimate of excluded quantities would help
regulatory officials establish inspection and monitoring priorities.
This requirement was an oversight when the exclusion was initially
promulgated. We required the burner to issue a public notice that
included this information (see existing Sec. 261.38(c)(1)(ii)(D)),
but we inadvertently did not require the generator who claims the
exclusion to provide this information in his notice to regulatory
officials.
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Part Two: Rationale for the Proposed Rule
I. What Is the Rationale for Excluding Emission-Comparable Fuel From
the Definition of Solid Waste?
Emission-comparable fuel (ECF) is a fuel derived from hazardous
waste, but which would be excluded from RCRA hazardous waste regulation
if it meets prescribed specifications and management conditions. The
ECF specifications would be the same as those that currently apply to
existing comparable fuel, except the specifications for particular
hydrocarbons and oxygenates would not apply. See proposed Sec.
261.38(a)(2).\12\
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\12\ Table 1 to Sec. 261.38 provides specifications for 37
hydrocarbons and oxygenates. For ECF, the specifications would not
apply for those compounds, except for PAHs and naphthalene, as
discussed in Part Two, Section III, of the text. In addition, there
would be firing rate restrictions for ECF that contained more than
2% benzene or acrolein.
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The exclusion would be based on the rationale that ECF has fuel
value, that the hydrocarbon and oxygenate constituents no longer
subject to a specification themselves have fuel value, and that
emissions from burning ECF in an industrial boiler operating under good
combustion conditions are likely not to differ from emissions from
burning fossil fuels under those same conditions. Emissions from
burning ECF in an industrial boiler operating under good combustion
conditions would be comparable to emissions from burning fuel oil in an
industrial boiler operating under the same good combustion conditions
because operating a boiler under good combustion conditions, evidenced
by carbon monoxide (CO) emissions below 100 ppmv (on an hourly rolling
average), assures the destruction of organic compounds generally to
trace levels, irrespective of the type or concentration of the organic
compound in the feed.\13\ As
[[Page 33290]]
hydrocarbons are oxidized during combustion, eventually (ideally) to
carbon dioxide and water, CO is formed just prior to complete oxidation
to carbon dioxide. Because CO is difficult to oxidize, it is the rate-
limiting step in the oxidation process. Thus, low CO levels indicate
good combustion and low levels of organic compounds.
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\13\ This assumes that fuels are fired into the flame zone, thus
avoiding total ignition failure. If a waste fuel were inadvertently
fired out of the flame zone, the fuel may not even partially
combust. If this were to happen, CO levels could be low even though
organic emissions could be high. ECF boilers would be required to
fire ECF into the primary fuel flame zone. Also see USEPA, ``Draft
Technical Support Document for Expansion of the Comparable Fuel
Exclusion,'' May 2007, Section 5.
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EPA has discretion to classify such material as a fuel product, and
not as a waste. See generally Safe Foods and Fertilizer v. EPA, 350 F.
3d 1263, 1269-71 (D.C. Cir. 2004) (secondary materials physically
comparable to virgin products which would be used in their place, or
which pose similar or otherwise low risks when used in the same manner
as the virgin product, need not be considered ``discarded'' and hence
need not be classified as solid wastes). Given that ECF (including the
hydrocarbon and oxygenate portion) would have legitimate energy value
and that emissions from burning ECF are comparable to fuel oil when
burned in an industrial boiler under the good combustion conditions
typical of such boilers, classifying such material as a fuel product
and not as a waste promotes RCRA's resource recovery goals without
creating a risk from burning greater than those posed by fossil fuel.
Under these circumstances, EPA can permissibly classify ECF as a non-
waste.
The conditional exclusion would be an exclusion only from the RCRA
subtitle C regulations, and not from the emergency, remediation and
information-gathering sections of the RCRA statute [sections 3007,
3013, and 7003]. This is consistent with the principle already codified
for other excluded hazardous secondary materials--that the exclusion is
only from the RCRA regulatory provisions, and not from these statutory
authorities. See Sec. 261.1(b). We are restating this principle here
in the interest of clarity, not to reopen the issue. The legal basis
for the distinction of the Agency's authority under these provisions is
that they use the broader statutory definition of solid waste (and
hazardous waste, as well) and so need not (and should not) be read as
being limited by the regulatory definition. See, for example, 50 FR at
627. See also Connecticut Coastal Fishermen's Assn. v. Remington Arms,
989 F. 2d 1305, 1313-15 (2d Cir. 1993) (EPA may permissibly ascribe
different definitions to the term ''solid waste'' for regulatory and
statutory purposes).
Although ECF could have higher concentrations of particular
hydrocarbons and oxygenates than the benchmark fossil fuels--fuel oil
and gasoline--that EPA used to establish the specifications in Table 1
to Sec. 261.38, higher levels of hydrocarbons and oxygenates in ECF do
not imply that burning ECF for energy recovery constitutes waste
management because: (1) Hydrocarbons naturally occur in virgin fuels
\14\ and oxygenates are a class of compounds that are added to virgin
fuels to enhance combustion; \15\ (2) the hydrocarbons and oxygenates
have a heating value of 10,000 Btu/lb to 18,500 Btu/lb,\16\ which is
comparable to the range for virgin fuels (e.g., coal and fuel oil); and
(3) the hydrocarbons and oxygenates produce emissions comparable to
virgin fuels when burned under conditions typical of those under which
virgin fuels are burned.
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\14\ We explained in the final comparable fuel rule that it is
reasonable to assume that the Table 1 hydrocarbons that we did not
detect in fuel oil or gasoline could in fact be present at levels up
to the detection limit. See 63 FR at 33791.
\15\ Examples of fuel oxygenates are: Ethanol; methyl tert-butyl
ether (MTBE), tert-amyl methyl ether (TAME); diisopropyl ether
(DIPE); ethyl tert-butyl ether (ETBE); tert-amyl alcohol (TAA); and
tert-butyl alcohol (TBA). For further discussion, see USEPA, ``Draft
Technical Support Document for Expansion of the Comparable Fuel
Exclusion,'' May 2007, Section 3.1.
\16\ USEPA, ``Draft Technical Support Document for Expansion of
the Comparable Fuel Exclusion,'' May 2007, Section 2.2.
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We note, however, that ECF can pose a greater hazard during storage
than fuel oil given that ECF can contain higher concentrations of
certain hazardous, volatile hydrocarbons and oxygenates. We are
consequently proposing to condition the exclusion on certain storage
conditions similar to those applicable to commercial products and
commodities analogous to ECF, namely fuel oil and other commercial
organic liquids. See discussion below in Part Two, Section IV.
In addition, we are proposing to condition the exclusion on
requirements for the design and operation of the ECF burner to ensure
that ECF is burned under the good combustion conditions typical of most
fossil fuel boilers. See discussion below in Part Two, Section II.
These conditions should ensure that emissions from burning ECF remain
comparable to emissions from burning fossil fuels.
A. Why Would the Specifications Be Waived Only for Hydrocarbons and
Oxygenates?
We are proposing not to apply the specifications for certain
hydrocarbons and oxygenates, but are proposing to retain the
specifications for metals and the other categories of organic compounds
for which specifications are provided under Sec. 261.38. We would not
apply the specifications for these hydrocarbons \17\ because: (1) It is
reasonable to assume that these compounds may be present in fossil
fuels (see 63 FR at 33791); and (2) when they are burned under the good
combustion conditions typical for fossil fuel-fired boilers, emissions
from burning these compounds would be comparable to emissions from
burning fuel oil.
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\17\ Please note, however, that we are proposing to retain the
specifications for certain hydrocarbons: PAHs (polycyclic aromatic
hydrocarbons) and naphthalene. See discussion in the text in Part
Two, Section III.
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We also would not apply the specifications for the listed
oxygenates because they are a class of organic compounds that are added
to fuels to enhance combustion.\18\ These compounds would burn cleanly
under the good combustion conditions typical of a fuel oil-fired
industrial boiler and would generate only trace or comparable levels of
emissions.
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\18\ We acknowledge that oxygenates are added to fuels burned in
internal combustion engines rather than fuels burned in industrial
boilers. However, oxygenates burn cleanly--they do not contain
halogens, sulfur, or nitrogen that would result in emissions of
halogen acids and sulfur and nitrogen oxides.
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It is appropriate to retain the specifications for metals since
they do not contribute energy and are not destroyed during the
combustion process. Given that the metal specifications in Table 1 to
Sec. 261.38 reflect levels that can be present in fuel oil, excess,
noncontributing metals are ``along for the ride,'' suggesting
discarding. Moreover, metals emissions would necessarily be higher than
emissions from fuel oil if the metals specifications do not apply
because oil-fired boilers typically lack optimized particulate control
due to low metal content of commercially available fuel oils.
Also, it is appropriate to retain the specifications for the other
categories of organic compounds listed under Table 1 to Sec. 261.38--
sulfonated organics, nitrogenated organics, and halogenated organic
compounds. These organic compounds, for the most part, are not likely
to be found in the benchmark fuels--fuel oil and gasoline--we used to
establish the specifications. And, unlike oxygenates, these organic
compounds are not within a class of compounds that are added to fossil
fuels to enhance combustion. These hazardous compounds also would
appear to be along for the ride when present at concentrations higher
than benchmark
[[Page 33291]]
fuels, and consequently their destruction via combustion can be viewed
as waste management.
B. Do Available Data and Information Support a Comparable Emissions
Finding?
We investigated whether emissions from burning ECF in an industrial
boiler operating under prescribed good combustion conditions would be
comparable to emissions from burning fuel oil in an industrial boiler
operating under good combustion conditions. We evaluated organic
emissions data from watertube steam boilers (other than stoker-fired
boilers) burning hazardous waste and compared those emissions against
emissions from oil-fired industrial boilers. In addition, we conducted
two qualitative analyses of the risk that ECF emissions may pose: (1)
Evaluation of RCRA risk assessments for watertube steam boilers burning
hazardous waste to determine if organic emissions had been found to
pose a hazard to human health and the environment; and (2) a limited
comparative risk assessment for dioxin/furan emissions.
As discussed below, we believe that available data and information
indicate that emissions from burning ECF under the proposed, prescribed
conditions would be comparable to emissions from an oil-fired
industrial watertube steam boiler operating under good combustion
conditions.
1. Evaluation of Organic Emissions Data for Hazardous Waste Boilers
In the absence of emissions data from boilers burning ECF, we
evaluated organic emissions data from watertube steam boilers burning
hazardous waste and compared those emissions against emissions from
oil-fired industrial boilers. Using hazardous waste boiler emissions as
a surrogate for ECF boiler emissions is a reasonable worst-case because
the exclusion would be conditioned on the ECF boiler operating under
conditions relating to assuring good combustion conditions that are at
least as stringent as those required of boilers burning hazardous
waste.\19\
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\19\ See discussion in Part Two, Section II, of the text
describing the ECF boiler conditions. The CO controls for ECF
boilers plus the requirement to fire ECF into the primary fuel flame
zone are equivalent to the controls on organic emissions for
hazardous waste boilers--CO controls and compliance with the 99.99%
destruction and removal efficiency (DRE) standard. The other ECF
boiler controls are more restrictive than controls that apply to
hazardous waste boilers, but are appropriate to help assure that an
ECF boiler operates under good combustion conditions given that ECF
would be burned under a conditional exclusion absent a RCRA permit
and the regulatory oversight typical for a RCRA hazardous waste
combustor, and absent the extensive operating limits (e.g.,
combustion chamber temperature, maximum load) that are established
subsequent to emissions testing to demonstrate compliance with a
destruction and removal efficiency (DRE) standard.
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We obtained organic emissions data for 26 hazardous waste watertube
steam boilers which data were generated during risk-burn testing
required under RCRA omnibus authority codified at Sec. 270.32(b)(2).
EPA requires this testing as necessary on a site-specific basis to
ensure that emissions are protective of human health and the
environment. We have data for 28 test conditions for the 26 boilers
that provide 175 detected measurements of organic compounds, where a
measurement is a three-run set.\20\ We also have data for hazardous
organic compounds emitted from oil-fired industrial boilers. Those data
were compiled in support of the NESHAP for Industrial, Commercial, and
Institutional Boilers and Process Heaters promulgated under Part 63,
Subpart DDDDD. See 69 FR 55218 (Sept. 13, 2004). We use oil-fired
industrial boiler emissions data for comparison because fuel oil is the
closest analogous fuel to ECF, and ECF could be burned only in
industrial or utility boilers. See discussion below in Section II.B.1.
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\20\ A test condition is normally comprised of three test runs
conducted under identical (controllable) operating conditions.
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We have emissions data for both hazardous waste boilers and oil-
fired industrial boilers for 26 hazardous organic compounds. We also
have hazardous waste boiler emissions data for another 33 hazardous
organic compounds for which we do not have oil-fired boiler emissions
data for comparison. We discuss our investigation of these data below.
a. Hazardous Organic Compounds for Which We Have Both Hazardous
Waste Boiler and Fuel Oil Boiler Emissions Data. We have both hazardous
waste boiler and fuel-oil boiler emissions data for 26 hazardous
organic compounds. The great majority of the hazardous waste boiler
test condition averages for these compounds (150, or greater than 85%)
were unequivocally comparable to fuel oil emissions--the hazardous
waste emissions were below the oil emissions 95th percentile level.
There were 24 test condition averages, however, that exceeded the oil
emissions 95th percentile level for 10 compounds.\21\ Nonetheless, we
do not believe that these exceedances indicate that ECF emissions would
be higher than oil-fired boiler emissions, as discussed below.
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\21\ Please note that we have reanalyzed the oil-fired boiler
emissions data to identify the 95th percentile benchmarks based on
test condition averages, rather than test runs, based on comments
submitted by one of the peer reviewers. As discussed in Part Two,
Section VII, although the reanalysis resulted in several additional
exceedances of the oil emissions benchmarks, our conclusion remains
unchanged. It is reasonable to conclude that ECF emissions will be
either generally comparable to oil emissions or at de minimis
levels.
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For 12 of the 24 exceedances, laboratory contamination of the
sample was known or suspected. Specifically, for nine exceedances--six
for dichloromethane, two for benzene, and one for toluene--the
constituent being measured was found in the blank, while there were
three additional exceedances for dichloromethane, a common lab
contaminant that is frequently found in laboratory samples and in the
environment. For one of these test conditions, the report indicated
that dichloromethane is a common laboratory contaminant, implying that
the data may be suspect. For the other two test conditions, laboratory
contamination was not discussed in the test reports. Even if laboratory
contamination were not an issue for these two tests, however, we note
that these hazardous waste boilers were not operating under the
conditions that are proposed for an ECF boiler. Both boilers were
burning waste fuels with a heating value below the 8,000 Btu/lb minimum
heating value that is proposed for ECF. In addition, it is unclear if
one boiler was burning vent gas or natural gas as the primary fuel. ECF
must be burned with at least 50% primary fuel that is fossil fuel.
Operating under conditions less stringent than proposed for ECF boilers
could result in higher emissions of organic compounds.
For seven exceedances, hazardous waste boiler emissions were at
trace levels \22\--there was a de minimis increase in emissions. Test
condition averages were below 8 [mu]g/dscm for the exceedances for
anthracene, benzo[a]pyrene, ethylbenzene, fluorine, 2-
methlynaphthalene, and phenanthrene.
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\22\ Emissions of 8 [mu]g/dscm for high molecular weight
compounds such as these are equivalent to approximately 0.005 ppmv
expressed as propane equivalents. Thus, these are de minimis
concentrations considering that the hydrocarbon emission limit for
boilers burning hazardous waste is 10 ppmv, expressed as propane
equivalents. See Sec. 63.1217(a)(5)(ii).
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In addition, an exceedance for acetaldehyde was at an emissions
level of 100 [mu]g/dscm, while oil emission levels for acetaldehyde are
virtually comparable at 70 [mu]g/dscm. However, the hazardous waste
boiler emissions for acetaldehyde were well below the 95th percentile
emissions for natural gas boilers, 635 [mu]g/dscm. This is relevant
because ECF may be burned with natural gas as the primary fuel.
Further,
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we note that the hazardous waste boiler was operating under conditions
less stringent than proposed for ECF boilers--it was burning only 20%
natural gas as the primary fuel, while it is proposed that ECF boilers
fire at least 50% primary fuel. Thus, acetaldehyde emissions may be
higher than they would have been if the boiler had the hot, stable
flame that burning 50% natural gas (or fuel oil) would provide.
Finally, there were four exceedances for benzene that we
nonetheless believe are comparable to fuel oil emissions. Three of the
exceedances were below the highest fuel oil emission test run level of
200 [mu]g/dscm, while the fourth exceedance was at a level of 260
[mu]g/dscm, just somewhat higher. More importantly, for all four
exceedances, the hazardous waste boiler was not operating under the
conditions proposed for an ECF boiler. For all four exceedances, the