Regulation of Fuels and Fuel Additives: 2011 Renewable Fuel Standards, 42238-42268 [2010-17281]
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42238
Federal Register / Vol. 75, No. 138 / Tuesday, July 20, 2010 / Proposed Rules
40 CFR Part 80
[EPA–HQ–OAR–2010–0133; FRL–9175–8]
RIN 2060–AQ16
Regulation of Fuels and Fuel
Additives: 2011 Renewable Fuel
Standards
AGENCY: Environmental Protection
Agency (EPA).
ACTION: Notice of proposed rulemaking.
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SUMMARY: Under the Clean Air Act
Section 211(o), as amended by the
Energy Independence and Security Act
of 2007 (EISA), the Environmental
Protection Agency is required to set the
renewable fuel standards each
November for the following year based
on gasoline and diesel projections from
EIA. Additionally, EPA is required to set
the cellulosic biofuel standard each year
based on the volume projected to be
available during the following year,
using EIA projections and assessments
of production capability from industry.
This regulatory action proposes these
annual standards for cellulosic biofuel,
biomass-based diesel, advanced biofuel,
and renewable fuels that apply to all
gasoline and diesel produced or
imported in year 2011. This action also
presents two proposed changes to the
RFS2 regulations. The first would create
a temporary and limited means for
certain renewable fuel producers to
generate delayed RINs after they have
produced and sold renewable fuel. This
proposed provision would apply only to
those producers who use canola oil,
grain sorghum, pulpwood, or palm oil to
produce renewable fuel. The second
proposed regulatory provision would
establish criteria for foreign countries to
adopt an aggregate approach to
compliance with the renewable biomass
provision akin to that applicable to the
U.S.
DATES: Comments must be received on
or before August 19, 2010.
Hearing: We do not expect to hold a
public hearing. However, if we receive
such a request we will publish
information related to the timing and
location of the hearing and the timing of
a new deadline for public comments.
NAICS 1 codes
Category
Industry
Industry
Industry
Industry
Industry
Industry
.............
.............
.............
.............
.............
.............
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SIC 2 codes
324110
325193
325199
424690
424710
424720
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Submit your comments,
identified by Docket ID No. EPA–HQ–
OAR–2010–0133, by one of the
following methods:
• https://www.regulations.gov: Follow
the online instructions for submitting
comments.
• E-mail: asdinfo@epa.gov.
• Mail: Air and Radiation Docket and
Information Center, Environmental
Protection Agency, Mailcode: 2822T,
1200 Pennsylvania Ave., NW.,
Washington, DC 20460.
• Hand Delivery: EPA Docket Center,
EPA West Building, Room 3334, 1301
Constitution Ave., NW., Washington,
DC 20460. Such deliveries are only
accepted during the Docket’s normal
hours of operation, and special
arrangements should be made for
deliveries of boxed information.
Instructions: Direct your comments to
Docket ID No. EPA–HQ–OAR–2010–
0133. EPA’s policy is that all comments
received will be included in the public
docket without change and may be
made available online at https://
www.regulations.gov, including any
personal information provided, unless
the comment includes information
claimed to be Confidential Business
Information (CBI) or other information
whose disclosure is restricted by statute.
Do not submit information that you
consider to be CBI or otherwise
protected through https://
www.regulations.gov or e-mail. The
https://www.regulations.gov Web site is
an ‘‘anonymous access’’ system, which
means 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
ADDRESSES:
ENVIRONMENTAL PROTECTION
AGENCY
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2869
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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.
For additional instructions on
submitting comments, go to Section I.B
of the SUPPLEMENTARY INFORMATION
section of this document.
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 Air and Radiation Docket and
Information Center, 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 Air Docket is (202) 566–
1742.
FOR FURTHER INFORMATION CONTACT: Julia
MacAllister, Office of Transportation
and Air Quality, Assessment and
Standards Division, Environmental
Protection Agency, 2000 Traverwood
Drive, Ann Arbor, MI 48105; Telephone
number: 734–214–4131; Fax number:
734–214–4816; E-mail address:
macallister.julia@epa.gov, or
Assessment and Standards Division
Hotline; telephone number 734–214–
4636; E-mail address asdinfo@epa.gov.
SUPPLEMENTARY INFORMATION:
I. General Information
A. Does this action apply to me?
Entities potentially affected by this
proposed rule are those involved with
the production, distribution, and sale of
transportation fuels, including gasoline
and diesel fuel or renewable fuels such
as ethanol and biodiesel. Potentially
regulated categories include:
Examples of potentially regulated entities
Petroleum Refineries.
Ethyl alcohol manufacturing.
Other basic organic chemical manufacturing.
Chemical and allied products merchant wholesalers.
Petroleum bulk stations and terminals.
Petroleum and petroleum products merchant wholesalers.
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Federal Register / Vol. 75, No. 138 / Tuesday, July 20, 2010 / Proposed Rules
NAICS 1 codes
Category
Industry .............
1 North
SIC 2 codes
454319
5989
42239
Examples of potentially regulated entities
Other fuel dealers.
American Industry Classification System (NAICS).
Industrial Classification (SIC) system code.
2 Standard
This table is not intended to be
exhaustive, but rather provides a guide
for readers regarding entities likely to be
regulated by this proposed action. This
table lists the types of entities that EPA
is now aware could potentially be
regulated by this proposed action. Other
types of entities not listed in the table
could also be regulated. To determine
whether your activities would be
regulated by this proposed action, you
should carefully examine the
applicability criteria in 40 CFR part 80.
If you have any questions regarding the
applicability of this proposed action to
a particular entity, consult the person
listed in the preceding 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.
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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
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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.
Outline of This Preamble
I. Executive Summary
A. Statutory Requirements for Cellulosic
Biofuel
B. Assessment of 2011 Cellulosic Biofuel
Volume
C. Advanced Biofuel and Total Renewable
Fuel
D. Proposed Percentage Standards
II. Volume Production and Import Potential
for 2011
A. Cellulosic Biofuel
1. Domestic Cellulosic Ethanol
2. Domestic Cellulosic Diesel
3. Other Domestic Cellulosic Biofuels
4. Imports of Cellulosic Biofuel
5. Summary of Volume Projections
B. Potential Limitations
C. Advanced Biofuel and Total Renewable
Fuel
D. Biomass-Based Diesel
III. Proposed Percentage Standards for 2011
A. Background
B. Calculation of Standards
1. How are the standards calculated?
2. Small Refineries and Small Refiners
IV. Cellulosic Biofuel Technology
Assessment
A. What pathways are valid for the
production of cellulosic biofuel?
B. Cellulosic Feedstocks
C. Emerging Technologies
1. Biochemical
a. Feedstock Handling
b. Biomass Pretreatment
c. Hydrolysis
i. Acid Hydrolysis
ii. Enzymatic Hydrolysis
d. Fuel Production
e. Fuel Separation
f. Process Variations
g. Current Status of Biochemical
Conversion Technology
h. Major Hurdles to Commercialization
2. Thermochemical
a. Ethanol Based on a Thermochemical
Platform
b. Diesel and Naphtha Production Based on
a Thermochemical Platform
3. Hybrid Thermochemical/Biochemical
Processes
4. Pyrolysis and Depolymerization
a. Pyrolysis Diesel Fuel and Gasoline
b. Catalytic Depolymerization
5. Catalytic Reforming of Sugars to
Gasoline
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V. Proposed Changes to RFS2 Regulations
A. Delayed RIN Generation for New
Pathways
B. Criteria and Process for Adoption of
Aggregate Approach to Renewable
Biomass for Foreign Countries
1. Criterion and Considerations
2. Data Sources
3. Petition Submission
4. Petition Process
VI. Public Participation
A. How do I submit comments?
B. How should I submit CBI to the agency?
VII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory
Planning and Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
I. National Technology Transfer
Advancement Act
J. Executive Order 12898: Federal Actions
to Address Environmental Justice in
Minority Populations and Low-Income
Populations
VIII. Statutory Authority
I. Executive Summary
The Renewable Fuel Standard (RFS)
program began in 2007 following the
requirements in Clean Air Act (CAA)
section 211(o) which were implemented
through the Energy Policy Act of 2005
(EPAct). The statutory requirements for
the RFS program were subsequently
modified through the Energy
Independence and Security Act of 2007
(EISA), resulting in the release of
revised regulatory requirements on
March 26, 2010 1. In general, the
transition from the RFS1 requirements
of EPAct to the RFS2 requirements of
EISA will occur on July 1, 2010.
EPA is required to determine and
publish the applicable annual
percentage standards for each
compliance year by November 30 of the
previous year. The determination of the
applicable standards under RFS2
requires the EPA to conduct an in-depth
evaluation of the volume of qualifying
cellulosic biofuel that can be supplied
in the following year. If the projected
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volume of cellulosic biofuel production
is less than the required volume
specified in the statute, EPA must lower
the required volume used to set the
annual cellulosic biofuel percentage
standard to the projected volume of
production. We must also determine
whether the advanced biofuel and/or
total renewable fuel volumes should be
reduced by the same or a lesser amount.
Since these evaluations will be based on
evolving information about emerging
segments of the biofuels industry, and
may result in the required volumes
differing from those in the statute, we
believe that a notice-and-comment
rulemaking process is appropriate.
Today’s notice provides our evaluation
of the projected production of cellulosic
biofuel for 2011, and proposed
percentage standards for compliance
year 2011. We will complete our
evaluation based on comments received
in response to this proposal, the
Production Outlook Reports due to the
Agency on September 1, 2010, the
estimate of projected biofuel volumes
that the EIA is required to provide to
EPA by October 31, and other
information that becomes available, and
will finalize the standards for 2011 by
November 30, 2010.
Today’s proposed rule does not
include an assessment of the
environmental impacts of the standards
we are proposing for 2011. All of the
impacts of the RFS2 program were
addressed in the RFS2 final rule
published on March 26, 2010, including
impacts of the biofuel standards
specified in the statute. Today’s
rulemaking simply proposes the
standards for 2011 whose impacts were
already analyzed previously.
Today’s notice also presents two
proposed changes to the RFS2
regulations. The first would create a
temporary and limited means for certain
renewable fuel producers to generate
RINs after they have produced and sold
renewable fuel. This proposed provision
for ‘‘Delayed RINs’’ would apply only to
those producers who use canola oil,
grain sorghum, pulpwood, or palm oil to
produce renewable fuel, and only if EPA
determines that fuel pathways utilizing
these feedstocks provide appropriate
greenhouse gas reductions as compared
to baseline fuels to enable EPA to list
the pathways in Table 1 to § 80.1426.
We are proposing that the provision for
Delayed RINs would apply only to these
four feedstocks because we would have
included them in the final RFS2 rule if
the lifecycle analyses had been
completed in time. The greenhouse gas
(GHG) lifecycle impacts of these four
feedstocks are currently being analyzed
as a supplement to the RFS2 final rule
and are expected to be completed in
2010. The second proposed regulatory
provision would establish criteria for
EPA to use in determining whether to
authorize renewable fuel producers
using foreign-grown feedstocks to use an
aggregate approach to compliance with
the renewable biomass verification
provisions, akin to that applicable to
producers using crops and crop residue
grown in the United States. Further
discussion of both of these proposed
provisions can be found in Section V.
Finally, we note that in the RFS2 final
rule we also stated our intent to make
two announcements each year:
• Set the price for cellulosic biofuel
waiver credits that will be made
available to obligated parties in the
event that we reduce the volume of
cellulosic biofuel below the volume
required by EISA.
• Announce the results of our
assessment of the aggregate compliance
approach for verifying renewable
biomass requirements for U.S. crops and
crop residue, and our conclusion
regarding whether the aggregate
compliance provision will continue to
apply.
For both of these determinations EPA
will use specific sources of data and a
methodology laid out in the RFS2 final
rule. We intend to present the results of
both of these determinations in the final
rule following today’s proposal.
A. Statutory Requirements for Cellulosic
Biofuel
The volumes of renewable fuel that
must be used under the RFS2 program
each year (absent an adjustment or
waiver by EPA) are specified in CAA
211(o)(2). These volumes for 2011 are
shown in Table I.A–1.
TABLE I.A–1—REQUIRED VOLUMES IN THE CLEAN AIR ACT FOR 2011
[Bill gal]
Actual
volume
Cellulosic biofuel ..........................................................................................................................................................
Biomass-based diesel ..................................................................................................................................................
Advanced biofuel .........................................................................................................................................................
Renewable fuel ............................................................................................................................................................
0.25
0.80
1.35
13.95
Ethanol
equivalent
volume
a 0.25
1.20
1.35
13.95
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a This value assumes that all cellulosic biofuel would be ethanol. If any portion of the renewable fuel used to meet the cellulosic biofuel volume
mandate has a volumetric energy content greater than that for ethanol, this value will be higher.
By November 30 of each year, the EPA
is required under CAA 211(o) to
determine and publish in the Federal
Register the renewable fuel standards
for the following year. These standards
are to be based in part on transportation
fuel volumes estimated by the Energy
Information Administration (EIA) for
the following year. The calculation of
the percentage standards is based on the
formulas in § 80.1405(c) which express
the required volumes of renewable fuel
as a volume percentage of gasoline and
diesel sold or introduced into commerce
in the 48 contiguous states plus Hawaii.
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The statute requires the EPA to
determine whether the projected
volume of cellulosic biofuel production
for the following year is less than the
minimum applicable volume shown in
Table I.A–1. If this is the case, then the
standard for cellulosic biofuel must be
based upon the volume projected to be
available rather than the applicable
volume in the statute. In addition, if
EPA reduces the required volume of
cellulosic biofuel below the level
specified in the statute, the Act also
indicates that we may reduce the
applicable volume of advanced biofuels
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and total renewable fuel by the same or
a lesser volume.
As described in the final rule for the
RFS2 program, we intend to examine
EIA’s projected volumes and other
available data including the Production
Outlook Reports required under
§ 80.1449 in making the determination
of the appropriate volumes to require for
2011. Since the first set of Production
Outlook Reports are not due until
September 1, 2010, they were not
available for today’s proposal but will
be considered for development of the
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final rule to be released by November
30, 2010.
B. Assessment of 2011 Cellulosic Biofuel
Volume
To estimate the volume of cellulosic
biofuel that could be made available in
the U.S. in 2011, we researched all
potential production sources by
company and facility. This included
sources that were still in the planning
stages, those that were under
construction, and those that are already
producing some volume of cellulosic
ethanol, cellulosic diesel, or some other
type of cellulosic biofuel. We
considered all pilot and demonstration
plants as well as commercial plants.
From this universe of potential
cellulosic biofuel sources we identified
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the technology and contracts for
feedstocks, and progress towards
construction and production goals. A
complete list of all the factors we expect
to consider in this process is provided
in Section II.A.5.
In our assessment we evaluated both
domestic and foreign sources of
cellulosic biofuel. Of the domestic
sources, we estimated that seven
facilities have the potential to make
volumes of cellulosic biofuel available
for transportation use in the U.S. in
2011. We also determined that one
facility in Canada has the potential to
export some cellulosic biofuel to the
U.S. These facilities are listed in Table
I.B–1 along with our estimate of the
maximum potentially available volume.
the subset that had a possibility of
producing some volume of qualifying
cellulosic biofuel for use as
transportation fuel in 2011. We then
conducted a rigorous process of
contacting all of these producers to
determine which ones were actually in
a position to produce and make
available any commercial volumes of
cellulosic biofuel in 2011. Based on
information gathered in this process, we
estimated the maximum potentially
available 2011 volumes. For the final
rule, we will specify the projected
available volume for 2011 that will be
the basis for the percentage standard for
cellulosic biofuel. To determine the
projected available volume, we will
consider factors such as the current and
expected state of funding, the status of
TABLE I.B–1—MAXIMUM POTENTIALLY AVAILABLE CELLULOSIC BIOFUEL PLANT VOLUMES FOR 2011
Maximum potentially
available volume (million
ethanol-equivalent
gallons)
Location
Fuel type
AE Advanced Fuels Keyes ..............................
Agresti Biofuels ................................................
Bell Bio-Energy ................................................
Cello Energy ....................................................
DuPont Dansico ...............................................
Fiberight ...........................................................
Iogen Corporation ............................................
KL Energy Corp/WBE ......................................
Keyes, CA ..................................
Pike County, KY .........................
Atlanta, GA .................................
Bay Minette, AL ..........................
Vonore, TN .................................
Blairstown, IA .............................
Ottawa, Ont ................................
Upton, WY ..................................
Ethanol .......................................
Ethanol .......................................
Diesel feedstock .........................
Diesel ..........................................
Ethanol .......................................
Ethanol .......................................
Ethanol .......................................
Ethanol .......................................
0.5
1
11.9
8.5
0.15
2.8
0.25
0.4
Total ..........................................................
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Company
.....................................................
.....................................................
25.5
The volumes in Table I.B–1 for each
facility represent the volume that would
be produced in 2011 based upon the
owner’s expected month of startup and
an assumed period of production
rampup for testing and process
validation. However, none of the
facilities we evaluated are currently
producing cellulosic biofuel at the rates
they project for 2011. Moreover, there
are other uncertainties associated with
each facility’s projected volume that
could result in less production volume
in 2011 than the maximum potentially
available values shown in Table I.B–1.
These uncertainties include outstanding
issues in areas such as technology,
funding, and construction. Historical
successes in meeting various past
milestones also play a role in assessing
the likelihood of meeting future
milestones. A detailed discussion of
these uncertainties is presented in
Section II.A. Finally, the volumes that
should be considered for setting the
2011 standard are those that result from
valid cellulosic biofuel pathways in
Table 1 to § 80.1426. As described more
fully in Section IV.A, some of the
facilities in Table I.B–1 may use
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feedstocks that have not yet been
subjected to lifecycle analyses to
determine if the pathway meets the
applicable GHG thresholds.
Based on our preliminary assessment
for this NPRM, we believe that we could
justify a 2011 cellulosic biofuel volume
requirement of at least 6.5 million
ethanol-equivalent gallons, and
potentially as high as 25.5 million
gallons. For the final rule we will use
additional information that becomes
available after publication of this
proposal and a more precise assessment
of the uncertainties associated with each
facility to determine the projected
available volume on which to base the
cellulosic biofuel percentage standard
for 2011.
C. Advanced Biofuel and Total
Renewable Fuel
As described in Section I.A above, the
statute indicates that we may reduce the
applicable volume of advanced biofuel
and total renewable fuel if we determine
that the projected volume of cellulosic
biofuel production for 2011 falls short of
the statutory volume of 250 million
gallons. As shown in Table I.B–1, we are
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proposing a determination that this is
the case. Therefore, we also needed to
evaluate the need to lower the required
volumes for advanced biofuel and total
renewable fuel.
We first considered whether it
appears likely that the required
biomass-based diesel volume of 0.8
billion gallons can be met with existing
biodiesel production capacity in 2011.
As discussed in Section II.D, we believe
that the 0.8 billion gallon standard can
indeed be met. Since biodiesel has an
Equivalence Value of 1.5, 0.8 billion
physical gallons of biodiesel would
provide 1.20 billion ethanol-equivalent
gallons that can be counted towards the
advanced biofuel standard of 1.35
billion gallons. Of the remaining 0.15
bill gallons, up to 0.026 bill gallons
would be met with the proposed volume
of cellulosic biofuel. Based on our
analysis as described in Section II.C,
there may be sufficient volumes of other
advanced biofuels, such as imported
sugarcane ethanol, additional biodiesel,
or renewable diesel, such that the
standard for advanced biofuel could
remain at the statutory level of 1.35
billion gallons. However, uncertainty in
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the potential volumes of these other
advanced biofuels coupled with the
range of potential production volumes
of cellulosic biofuel could provide a
rationale for lowering the advanced
biofuel standard. If we do not
simultaneously lower the required
volume for total renewable fuel, the
result would be that additional volumes
of conventional renewable fuel, such as
corn-starch ethanol, would be produced,
effectively replacing some advanced
biofuels. In today’s NPRM we are
proposing that neither the required 2011
volumes for advanced biofuel nor total
renewable fuel be lowered below the
statutory volumes. However, we request
comment on whether the advanced
biofuel and/or total renewable fuel
volume requirements should be lowered
if, as we propose, EPA lowers the
required cellulosic biofuel volume from
that specified in the Act.
D. Proposed Percentage Standards
The renewable fuel standards are
expressed as a volume percentage, and
are used by each refiner, blender or
importer to determine their renewable
fuel volume obligations. The applicable
percentages are set so that if each
regulated party meets the percentages,
and if EIA projections of gasoline and
diesel use are accurate, then the amount
of renewable fuel, cellulosic biofuel,
biomass-based diesel, and advanced
biofuel used will meet the volumes
required on a nationwide basis. To
calculate the percentage standard for
cellulosic biofuel for 2011, we have
used a potential volume range of 6.5–
25.5 million ethanol-equivalent gallons
(representing 5–17.1 million physical
gallons). For the final rule, EPA intends
to pick a single value from within this
range to represent the projected
available volume on which the 2011
percentage standard for cellulosic
biofuel will be based. We are also
proposing that the applicable volumes
for biomass-based diesel, advanced
biofuel, and total renewable fuel for
2011 will be those specified in the
statute. These volumes are shown in
Table I.D–1.
TABLE I.D–1—PROPOSED VOLUMES FOR 2011
Ethanol equivalent
volume
Actual volume
Cellulosic biofuel ...................................................................
Biomass-based diesel ...........................................................
Advanced biofuel ..................................................................
Renewable fuel .....................................................................
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Four separate standards are required
under the RFS2 program, corresponding
to the four separate volume
requirements shown in Table I.D–1. The
specific formulas we use to calculate the
renewable fuel percentage standards are
contained in the regulations at § 80.1405
and repeated in Section III.B.1. The
percentage standards represent the ratio
of renewable fuel volume to nonrenewable gasoline and diesel volume.
The projected volumes of gasoline and
renewable fuels used to calculate the
standards are provided by EIA’s ShortTerm Energy Outlook (STEO) 2. The
projected volume of transportation
diesel used to calculate the standards is
provided by EIA’s 2010 Annual Energy
Outlook (early release version).3
Because small refiners and small
refineries are also regulated parties
beginning in 2011 4, there is no small
2 The March 2010 issue of STEO was used for
today’s proposal. We intend to use the October 2010
version for the final rule.
3 EIA has recommended the use of the Annual
Energy Outlook (AEO) rather than the Short Term
Energy Outlook as a better representation of the
estimated transportation sector diesel fuel use. We
will use the most recent version of AEO in the final
values of the standards.
4 The Department of Energy concluded that there
is no reason to believe that any small refinery
would be disproportionately harmed by inclusion
in the proposed RFS2 program for 2011 and
beyond. See DOE report ‘‘EPACT 2005 Section 1501
Small Refineries Exemption Study’’, (January 2009).
We will revisit extensions to the exemption for
small refiners and refineries if DOE revises their
study and provides a different conclusion, or an
individual small refinery is able to demonstrate that
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5–17.1 mill gal ......................................................................
0.80 bill gal ...........................................................................
1.35 bill gal ...........................................................................
13.95 bill gal .........................................................................
6.5–25.5 mill gal.
1.20 bill gal.
1.35 bill gal.
13.95 bill gal.
this section do not represent the
projected available volume of cellulosic
biofuel that will be used to finalize the
cellulosic biofuel percentage standard
for 2011. Rather, for today’s NPRM we
have assessed the maximum potentially
available volume for 2011, which is
intended to represent an upper bound of
the volume of fuel that may be produced
and made available. The production of
cellulosic biofuel remains highly
TABLE I.D–2—PROPOSED
uncertain, and EPA expects that the
PERCENTAGE STANDARDS FOR 2011 volume of cellulosic biofuel used to set
the 2011 percentage standard will be a
Percent
lesser volume than this maximum
potentially available volume. Section III
Cellulosic biofuel ...................
0.004–0.015
describes the conversion of our
Biomass-based diesel ..........
0.68
Advanced biofuel ..................
0.77 maximum potentially available volumes
Renewable fuel .....................
7.95 for cellulosic biofuel into a range of
percentage standards.
II. Volume Production and Import
While the 2011 volume projections in
Potential for 2011
today’s proposal were based on our own
assessment of the cellulosic biofuel
In order to project production
volumes of cellulosic biofuel in 2011 for industry, by the time we announce the
final 2011 volumes and percentage
use in setting the percentage standards,
standards we will have additional
we collected information on individual
information. First, in addition to
facilities that have the potential to
comments in response to today’s
produce qualifying volumes for
proposal, we will have updated and
consumption as transportation fuel,
more detailed information about how
heating oil, or jet fuel in the U.S. in
the industry is progressing in 2010.
2011. This section describes the
potential volumes that we believe could Second, by September 1 all registered
be produced or imported in 2011 as well producers and importers of renewable
fuel must submit Production Outlook
as the uncertainties associated with
Reports describing their expectations for
those volumes. The volumes listed in
new or expanded biofuel supply for the
next five years, according to § 80.1449.
it will suffer a disproportionate economic hardship
under the RFS program.
Finally, by October 2010 the Energy
refiner/refinery volume adjustment to
the 2011 standard as there was for the
2010 standard. Thus, the increase in the
percentage standards relative to 2010
appears smaller than would otherwise
be the case, since more obligated parties
will be participating in the program.
The proposed standards for 2011 are
shown in Table I.D–2. Detailed
calculations can be found in Section III.
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Information Administration (EIA) is
required by statute to provide EPA with
an estimate of the volumes of
transportation fuel, biomass-based
diesel, and cellulosic biofuel projected
to be sold or introduced into commerce
in the U.S. in 2011.
A. Cellulosic Biofuel
The task of projecting the volume of
cellulosic biofuels that will be produced
in 2011 is a difficult one. Currently
there are no facilities consistently
producing cellulosic biofuels for
commercial sale. Announcements of
new projects, changes in project plans,
project delays, and cancellations occur
with great regularity. Biofuel producers
face not only the challenge of the scale
up of innovative, first-of-a-kind
technology, but also the challenge of
securing funding in a difficult economy.
In order to project cellulosic biofuel
production in 2011, EPA has tracked the
progress of over 100 biofuel production
facilities. From this list of facilities we
used publicly available information, as
well as information provided by DOE
and USDA, to determine which facilities
were the most likely candidates to
produce cellulosic biofuel and make it
commercially available in 2011. Each of
these companies was contacted by EPA
in order to determine the current status
of their facilities and discuss their
commercialization plans for the coming
years. Our estimate of the maximum
potentially available cellulosic biofuel
production in 2011 is based on the
information we received in
conversations with these companies as
well as our own assessment of the
likelihood of these facilities successfully
producing cellulosic biofuel in the
volumes indicated.
A brief description of each of the
companies we believe may produce
cellulosic biofuel and make it
commercially available can be found
below. These companies have been
grouped according to the type of biofuel
they produce. For the purpose of setting
the cellulosic biofuel standard for 2011
this is a convenient grouping, as the
number of RINs generated per gallon of
fuel produced is dependent on the type
of fuel. A more in depth discussion of
the technologies used to produce
cellulosic biofuels can be found in
Section IV.
In today’s NPRM EPA is proposing a
range, rather than a single value, for the
required 2011 cellulosic biofuel volume.
At a minimum, we believe that a
volume of 6.5 million gallons could be
justified based on currently available
information. This is the cellulosic
biofuel volume that was required in
2010, and absent a waiver for some
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portion of this volume, producers will
be aiming to meet it. Therefore, it is
reasonable to project that this same
volume could, at minimum, also be
produced in 2011.
For a maximum potentially available
cellulosic biofuel volume for 2011, we
are proposing 25.5 million ethanol
equivalent gallons, representing the
highest volume of fuel that can
reasonably be expected to be produced
and made available based on current
information. In order for this volume of
cellulosic biofuel to be produced in
2011, each of the companies discussed
below would have to achieve their
production targets in their projected
timeframes. However, historical trends
among cellulosic biofuel producers
suggests that this is unlikely to be the
case, as there are many factors which
have the potential to result in
production delays. For instance, several
of the companies we considered when
setting the 2010 cellulosic biofuel
standard have yet to sell cellulosic
biofuel in the United States and appear
unlikely to do so by the end of 2010.
This fact demonstrates the uncertainty
of cellulosic biofuel production
estimates, and is one of many factors
EPA will consider when setting the
cellulosic biofuel standard for 2011.
The rest of this section describes the
analyses that were used as the basis for
this maximum value. We will continue
to gather more information to help
inform our decision on the final
cellulosic biofuel standard for 2011, and
we will specify a single volume in the
final rule that will be the basis for the
cellulosic biofuel percentage standard
for 2011.
1. Domestic Cellulosic Ethanol
Based on our assessment of the
cellulosic biofuel industry we believe
that there are five companies in the
United States with the potential to
produce cellulosic ethanol and make it
commercially available in 2011. These
companies are AE Biofuels, Agresti
Biofuels, DuPont Danisco Cellulosic
Ethanol, Fiberight, and KL Energy
Corporation. This section will provide a
brief description of each of these
companies and our assessment of their
potential fuel production in 2011. This
section also provides a brief update on
companies from whom we do not expect
any commercial sales of transportation
fuel in 2011 in the U.S. but were
included in prior assessments.
AE Biofuels is a company that plans
to convert corn cobs and corn stover to
ethanol using an enzymatic hydrolysis.
They plan to use an integrated process
that converts both starch and cellulose
to ethanol. In August 2008 they opened
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a demonstration plant in Butte, Montana
to test their technology and gather
information for their first commercial
scale plant. AE Biofuels has reached a
lease agreement with Cilion to operate
Cilion’s 55 MGY corn ethanol plant in
Keyes, CA under the name AE
Advanced Fuels Keyes. This facility has
been idled since April 2009 and will
require repairs before being operational.
AE Biofuels plans to start up production
with a starch feedstock in late-2010 and
then begin to transition some
production to cellulosic feedstock in
mid-2011. AE Biofuels plans to
eventually use up to 25% cellulosic
feedstock for ethanol production in this
facility. EPA projects that up to 0.5
million gallons of ethanol may be
produced by this facility in 2011.
Agresti Biofuels plans to produce
ethanol from separated municipal solid
waste (separated MSW) at a facility in
Pike County, Kentucky. Their process
uses a gravity pressure vessel licensed
from GeneSyst to crack the lignin in
their feedstock and then a combination
of weak bases and acids to convert the
cellulose and hemicellulose into simple
sugars for later fermentation into
ethanol. Agresti plans to begin
construction on their first production
facility in Pike County sometime in the
summer of 2010 and hope to be
producing ethanol by the end of 2011.
The full production capacity of this
facility will be 20 million gallons of
ethanol per year. Due to the fact that
construction on this facility has not yet
begun and production is not expected
until late in 2011 EPA expects no more
than 1 million gallons of cellulosic
ethanol to be produced by Agresti
Biofuels in 2011.
DuPont Danisco Cellulosic Ethanol
(DDCE) began start up operations at a
small demonstration facility in Vonore,
Tennessee in early 2010. This facility
has a maximum production capacity of
250,000 gallons of ethanol per year and
uses an enzymatic hydrolysis process to
convert corn cobs into ethanol. The
main purpose of this facility is not to
produce ethanol to be sold
commercially, but rather to provide
information for the future construction
and optimization of larger, commercial
scale cellulosic ethanol production
facilities. DDCE have indicated that they
do not intend to produce more than
150,000 gallons of ethanol in 2011 from
the Vonore facility.
Fiberight is another company
planning to convert MSW to ethanol.
Fiberight purchased a small corn
ethanol plant in Blairstown, IA and has
converted it to produce cellulosic
ethanol. They use an enzymatic
hydrolysis process, with enzymes
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provided by Novozymes, to convert the
cellulosic waste materials to simple
sugars and eventually to ethanol.
Fiberight has a unique enzyme recycle
and recovery process that allows them
to affordably use high concentrations of
enzymes to increase the speed and
conversion rate of the cellulose to
simple sugars. Fiberight plans to begin
ethanol production in the summer of
2010 and ramp up to full production
capacity of 5.7 million gallons of
ethanol per year by late 2011. Based on
company estimates, EPA projects
Fiberight could produce as much as 2.8
million gallons of cellulosic ethanol in
2011.
The fifth company that EPA is aware
of with the potential to produce
cellulosic ethanol in 2011 is KL Energy
Corporation. KL Energy has a small
facility in Upton, Wyoming that uses an
enzymatic hydrolysis process to convert
wood chips and wood waste to ethanol.
This facility has a maximum annual
production volume of 1.5 million
gallons and has been operational since
the fall of 2007. Since KL Energy
completed construction on this facility
they have been slowly ramping up
production and gathering information to
optimize this and future ethanol
production facilities. KL has informed
EPA that they intend to produce
400,000 gallons of cellulosic ethanol
from their Upton, WY facility in 2011.
In addition to the five companies
mentioned above, EPA is also tracking
the progress of more than 70 ethanol
production facilities in various stages
ranging from construction to planning
stages. Several of these companies,
including Abengoa, BlueFire Ethanol,
Coskata, Fulcrum, POET, and Vercipia
all intend to begin the production and
commercial sale of cellulosic ethanol in
2012. These facilities range in maximum
production capacity from 10 to 100
million gallons of ethanol. EPA
anticipates a significant increase in the
production and sale of cellulosic
ethanol in 2012, and strong continued
growth in the following years. In
addition, if any of these or other
companies accelerates their production
plans to make cellulosic biofuel
available for commercial sale in 2011,
we will take those volumes into account
in our final rule.
2. Domestic Cellulosic Diesel
EPA is also aware of two companies
in the United States with the potential
of producing cellulosic diesel fuel in
2011. The first of these companies is
Cello Energy. Cello Energy plans to use
a catalytic depolymerization process to
produce diesel fuel from wood chips
and hay. Cello currently has a
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structurally complete facility in Bay
Minette, Alabama with an annual
production capacity of 20 million
gallons of diesel per year. While having
a structurally complete facility puts
Cello ahead of many other potential
biofuel producers they have yet to be
able to produce biofuel at anywhere
near the production capacity. They are
currently assessing feedstock
preparation and handling issues that
must be resolved before they are able to
again attempt start up and production at
this facility. If these issues are
successfully addressed EPA believes
that Cello could, at most, produce up to
5 million gallons (8.5 million ethanol
equivalent gallons) of cellulosic diesel
fuel in 2011.
Another potential producer of
cellulosic biofuel in 2011 is Bell BioEnergy. Bell Bio-Energy uses proprietary
organisms to convert waste materials to
liquid fuels and compost in a single
step. The company currently has an
agreement in place for the sale of the
compost they produce and are searching
for a location for their first plant and a
partner to supply the waste materials
they intend to use as feedstock. The
liquid fuel they produce is not a
finished transportation fuel, but could
be upgraded to jet or diesel fuel. Bell
Bio-Energy is currently working with a
refining company to analyze the fuel
they produce and determine the extent
of upgrading necessary for the fuel to
qualify as transportation fuel. They plan
to begin construction on their first
facility, which will have an annual fuel
production capacity of 14.4 million
gallons per year, as soon as a suitable
site and partner are found. The
simplicity and low capital costs of Bell
Bio-Energy’s single step production
process allow them to construct plants
very rapidly, in as little as six weeks.
This would make it possible for Bell
Bio-Energy to produce cellulosic biofuel
in 2011 despite the fact that they have
not yet begun construction on their first
commercial scale facility. It is unclear
when fuel will be produced at this
facility, and whether it would qualify
under the RFS2 program. If Bell BioEnergy is successful in producing and
upgrading their fuel EPA estimates the
maximum volume of fuel they could
produce in 2011 would be 7 million
gallons (11.9 million ethanol equivalent
gallons) of jet or diesel fuel.
EPA is also tracking the progress of 17
other facilities that plan to produce
cellulosic diesel. Flambeau Rivers
Biofuels, New Page, and Terrabon are
planning on opening commercial scale
cellulosic diesel facilities in 2012. Both
Bell Bio-Energy and Cello have plans to
build additional facilities if their initial
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projects are successful. As with
cellulosic ethanol, cellulosic diesel
production has the potential for rapid
growth in 2012 and the following years.
3. Other Domestic Cellulosic Biofuels
We are currently unaware of any
companies in the United States
planning on producing cellulosic
biofuel other than ethanol and diesel
and making it commercially available.
EPA is currently tracking the efforts of
10 companies that plan to produce fuels
such as gasoline, jet fuel, dimethyl ether
(DME), and others. Many of these
companies have reported that they are
still developing their technologies and
waiting for funding, and that they are
not expecting to make any cellulosic
fuel commercially available until 2012
at the earliest. There are several
companies, such as Gevo and Virent,
with small demonstration facilities who
intend to produce other fuels from
cellulosic feedstocks, but are currently
optimizing their technology with sugar
or starch feedstocks. EPA anticipates
that in the future this may be a
significant source of cellulosic biofuel,
however we are only expecting
cellulosic ethanol and diesel to be
produced in 2011.
4. Imports of Cellulosic Biofuel
In addition to the companies located
in the United States, EPA is also aware
of two Canadian companies with the
potential for cellulosic biofuel
production in 2011. If this fuel was
imported into the United States, these
companies would be eligible to
participate in the RFS2 program.
Counting on cellulosic biofuel produced
internationally in setting the 2011
standard brings with it the additional
uncertainty associated with the fact that
the fuel may be used locally rather than
imported into the United States.
Iogen uses a steam explosion pretreatment process followed by
enzymatic hydrolysis to produce
cellulosic ethanol from wheat, oat, and
barley straw. They have a demonstration
facility with an annual production
capacity of 500,000 gallons of ethanol
located in Ontario, Canada. This facility
has been operational and producing
small volumes of ethanol since 2004. So
far all of the ethanol produced by this
facility has been used locally and in
racing and other promotional events.
Iogen, however, is exploring the
possibility of participating in the RFS2
program. If they do decide to import
ethanol to the United States, EPA
projects that they could provide as
much as 250,000 gallons of cellulosic
ethanol in 2011 based on production
volumes from previous years.
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Another Canadian company with the
potential to produce cellulosic ethanol
in 2011 is Enerkem. Enerkem plans to
use a thermo-chemical process to gasify
separated MSW and other waste
products and then use a catalyst to
convert the synthesis (syn) gas into
ethanol. Enerkem is currently finishing
construction on a 1.3 million gallon per
year facility in Westbury, Quebec and
plans to begin producing ethanol in the
summer of 2010. They are also planning
a 10 million gallon per year facility in
Edmonton, Alberta, however production
from this facility is not expected until
2012. Enerkem has informed EPA that
they plan to market ethanol they
produce locally, and have no intentions
to import cellulosic ethanol into the
United States. We are therefore not
projecting any available cellulosic fuel
from Enerkem in 2011.
While Canada may be the most likely
source of imported cellulosic biofuels
due to its close proximity, it is possible
that cellulosic biofuels produced in
other countries may be imported into
the United States as well. Another
potential source of cellulosic biofuel
imports is Brazil, due to its established
ethanol industry and history of
importing ethanol into the United
States. EPA is aware of several
companies exploring the possibility of
cellulosic biofuel production in Brazil;
however none of these companies are
likely to make cellulosic biofuels
commercially available in the United
States in 2011. With the exception of
Iogen, as mentioned above, EPA has not
projected imports of cellulosic biofuels
from outside the United States in 2011.
5. Summary of Volume Projections
The information EPA has gathered on
the potential cellulosic biofuel
producers in 2011, summarized in
Section II.A above, allows us to project
a maximum potentially available biofuel
volume for each facility in 2011. After
the appropriate ethanol equivalence
value has been applied to the volumes
of those facilities producing diesel fuel,
the overall maximum potentially
available volume of cellulosic biofuels
for 2011 can be calculated by summing
the maximum potential of each facility.
EPA is not proposing to set the 2011
cellulosic biofuel standard at this
maximum potentially available volume,
rather this is intended to serve as an
upper bound. This information is
summarized in Table II.A.5–1 below.
TABLE II.A.5–1—CELLULOSIC BIOFUEL MAXIMUM 2011 POTENTIALLY AVAILABLE VOLUME
Capacity
(MGY)
Earliest
production
Maximum
2011 potentially available
volume
(MG)
Ethanol
equivalent
gallons
(MG)
Company name
Location
Feedstock
Fuel
AE Advanced
Fuels Keyes.
Agresti Biofuels ..
Bell Bio-Energy ..
Keyes, CA .........
Corn, then stover
Ethanol ..............
20
June 2011 ....
0.5
0.5
Pike County, KY
Atlanta, GA ........
Ethanol ..............
Diesel Feedstock
20
14.4
Oct. 2011 .....
June 2011 ....
1
7
1
11.9
Cello Energy ......
DuPont Danisco a
Bay Minette, AL
Vonore, TN ........
Diesel ................
Ethanol ..............
20
0.25
Online ...........
Online ...........
5
0.15
8.5
0.15
Fiberight a ...........
Iogen ..................
Blairstown, IA ....
Ottawa, Ontario
Ethanol ..............
Ethanol ..............
6
0.5
April 2010 .....
Online ...........
2.8
0.25
2.8
0.25
KL Energy a ........
Upton, WY .........
MSW ..................
MSW or other
cellulosic biomass.
Wood, hay .........
Corn cobs, then
switchgrass.
MSW ..................
Wheat, oat &
barley straw.
Wood .................
Ethanol ..............
1.5
Online ...........
0.4
0.4
Total ............
............................
............................
............................
........................
......................
17.1
25.5
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a Maximum
Production/Import Potential represents company estimate.
It is important to note that this
maximum potentially available volume
of 17.1 million gallons of cellulosic
biofuel, or 25.5 million ethanol
equivalent gallons, is not the volume on
which the final 2011 cellulosic biofuel
standard will be based. This number
represents the maximum amount of fuel
EPA believes could reasonably be
expected to be produced or imported
and made available for use as
transportation fuel, heating oil, or jet
fuel in 2011. It incorporates some
reductions from the annual production
capacity of each facility based on when
the facilities anticipate fuel production
will begin and assumptions regarding a
ramp up period to full production.
However, as stated earlier, in order for
this volume of cellulosic biofuel to be
produced in 2011, each of the
companies listed in Table II.A.5–1
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would have to achieve their production
targets in their projected timeframes.
The history of the cellulosic biofuels
industry has many examples of delays
in achieving full production capacity in
new facilities. Also, there are many
other factors that increase the
uncertainty of fuel production facilities
being able to achieve their maximum
potential production. These factors may
include:
• Difficulty/delays in securing
necessary funding.
• Delays in permitting and/or
construction.
• Difficulty in scale up, especially for
1st of their kind technologies.
• Volumes from pilot and
demonstration plants may not be sold
commercially.
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• Not all feedstocks may qualify to
produce cellulosic RINs; some still
awaiting evaluation of lifecycle impacts.
• Likelihood that fuels produced
internationally will be exported to the
United States rather than consumed
locally.
Each of the facilities listed in Table
II.A.5–1 may experience some of the
difficulties listed above, and as a result
may produce a volume of fuel less than
that listed as their maximum 2011
potentially available volume. Despite
this uncertainty, EPA believes that the
volume of cellulosic biofuel produced
in 2011 will, at minimum, be able to
meet or exceed the 2010 standard of 6.5
million ethanol equivalent gallons.
However, we will have more detailed
and accurate information for the final
rule, including the first round of
Production Outlook Reports, due on
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September 1, 2010 5 which will provide
information from each producer or
importer on the type or types of fuel
they plan to make available, the volume
of fuel, and the number of RINs they
plan to generate for the next five
calendar years.6 Therefore, in today’s
NPRM we are proposing a range of
values, from a minimum of 6.5 million
ethanol equivalent gallons to a
maximum of 25.5 million ethanol
equivalent gallons for the 2011
cellulosic biofuel standard. As time
progresses and we are able to track
whether or not the cellulosic biofuels
producers are able to meet the
construction and ramp up schedules
they have presented, we will have a
better idea of the appropriate volume of
fuel that we can reasonably expect to be
produced and made commercially
available in 2011. Additionally, each
year by October 31 EIA is required to
provide an estimate of the volume of
cellulosic biofuel they expect to be sold
or introduced into commerce in the
United States in the following year. EPA
will consider this information as well
when finalizing a single volume for use
in setting the 2011 cellulosic biofuel
standard.
Although we are currently projecting
that the potentially available volume of
cellulosic biofuel in 2011 will be in the
range of 6.5 to 25.5 million ethanolequivalent gallons, we expect that
volumes of cellulosic biofuel will
increase rapidly in the years following
2011. As stated before, we are aware of
more than 100 companies that are
actively investigating or making plans to
produce cellulosic biofuel in the near
future. Many of these companies intend
to begin construction in 2011 or 2012.
We will be monitoring these companies
carefully as we project the potential
volumes of cellulosic biofuel for years
2012 and beyond.
B. Potential Limitations
In addition to production capacity, a
variety of other factors have the
potential to limit the amount of
cellulosic biofuel that can be produced
and used in the U.S. For instance, there
may be limitations in the availability of
qualifying cellulosic feedstocks at
reasonable prices. Most of the cellulosic
biofuel producers that we project will
produce commercial volumes in 2011
have indicated that they will use some
type of cellulosic waste, such as
5 In future years, Production Outlook Reports will
be due on March 1. As a result, they may be
considered during development of the NPRM in
year 2011 and beyond.
6 For more information on the annual production
outlook reports see § 80.1449 of the RFS2
regulations.
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separated municipal solid waste, wastes
from the forestry industry, and
agricultural residues. Based on the
analyses of cellulosic feedstock
availability in the RFS2 final rule, we
believe that there will be significantly
more than enough sources of these
feedstocks for 2011. For producers that
intend to use dedicated energy crops,
we do not believe that the availability of
existing cropland will limit production
in 2011. We plan to continue to evaluate
the availability of valid feedstocks in
future years as the required volumes of
cellulosic biofuel increase.
Another factor that has the potential
to limit the amount of renewable fuel
that can be produced and used in the
U.S. is distribution and storage capacity.
In the longer term, most biofuels are
expected to be produced in the
heartland of the country and then be
shipped towards the coasts, flowing
roughly in the opposite direction of
petroleum-based fuels. The physical and
chemical nature of many of these
biofuels may limit the extent to which
they can be shipped and/or stored
fungibly with petroleum-based fuels. As
a result, new and expanded rail, barge
and tank truck transport will need to be
put in place. Dedicated biofuels
pipelines are also being investigated.
For instance, a short gasoline pipeline
in Florida is currently shipping batches
of ethanol.7 Evaluations are also
currently underway regarding the
feasibility of constructing a new
dedicated ethanol pipeline from the
Midwest to the East coast.8 However, for
2011 the volumes of cellulosic biofuel
are small enough that long-distance
transport will be unnecessary; with the
exception of foreign-produced biofuels,
much of the cellulosic biofuel volumes
can be consumed in regions close to
their production facilities. We also
expect existing distribution and storage
capacity to be sufficient to
accommodate the small increase in
cellulosic biofuel volumes in 2011.
C. Advanced Biofuel and Total
Renewable Fuel
Under CAA 211(o)(7)(D)(i), EPA has
the flexibility to reduce the applicable
volume of the advanced biofuel and
total renewable fuel requirements in the
event that the projected volume of
cellulosic biofuel is determined to be
7 Kinder Morgan announcement that their Central
Florida Pipeline from Tampa to Orlando ships
batches of ethanol along with batches of gasoline.
https://www.kindermorgan.com/business/
products_pipelines/.
8 ‘‘POET Joins Magellan Midstream Partners to
Assess Dedicated Ethanol Pipeline’’, March 2009,
https://www.poet.com/news/
showRelease.asp?id=155.
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below the volume specified in the
statute. As described in Section II.A
above, even the largest potential
volumes of cellulosic biofuel supply for
2011 are significantly below the
statutory volume of 250 million gallons.
Therefore, we must consider whether
and to what degree to lower the
advanced biofuel and total renewable
fuel standards for 2011.
As described in the RFS2 final rule,
we believe it may be appropriate to
allow excess advanced biofuels to make
up some or all of the shortfall in
cellulosic biofuel. This could include
excess biomass-based diesel, sugarcane
ethanol, or other biofuels categorized as
advanced biofuel. We believe that
Congress wanted to encourage the
development of advanced renewable
fuels and allow in appropriate
circumstances for the use of additional
volumes of those fuels in the event that
the projected volume of cellulosic
biofuel falls below the statutory
mandate.
If we were to maintain the advanced
biofuel and total renewable fuel volume
requirements at the levels specified in
the statute, we estimate that 125–144
million ethanol-equivalent gallons of
additional advanced biofuels would be
needed, depending on the standard we
set for cellulosic biofuel. See Table II.C–
1.
TABLE II.C–1—PROJECTED IMPACT OF
CELLULOSIC VOLUME ON USE OF
OTHER BIOFUELS IN 2011
[Mill gallons]
Ethanolequivalent
volume
Total renewable
fuel ................
Conventional renewable fuel a
Total advanced
biofuel ............
Cellulosic biofuel
Biomass-based
diesel .............
Other advanced
biofuel b .........
Physical
volume
13,950
13,500–
13,549
12,600
12,600
1,350
6.5–25.5
900–949
5–17.1
1200
800
125–144
83 c–144 d
a Predominantly
b Rounded
corn-starch ethanol.
to nearest million gallons for sim-
plicity.
c Lowest volume of other advanced biofuel
assumes cellulosic biofuel standard is based
on 25.5 mill gallons and only excess biodiesel
(with an equivalence value (EV) of 1.5) is
used to fill the need for other advanced
biofuel.
d Highest volume of other advanced biofuel
assumes cellulosic biofuel standard is based
on 6.5 mill gallons and only imported sugarcane ethanol (with an EV of 1.0) is used to fill
the need for other advanced biofuel.
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To determine if there are likely to be
sufficient volumes of imported
sugarcane ethanol and/or excess
biodiesel to meet the need for 125–144
million gallons of other advanced
biofuel, we examined historical data on
ethanol imports and EIA projections for
2011. For instance, as shown in Table
II.C–2 below, recent annual import
volumes of ethanol were higher than
what would be needed in 2011.
TABLE II.C–2—HISTORICAL IMPORTS
OF ETHANOL
[Mill gallons] 9
2007 ..................................................
2008 ..................................................
2009 ..................................................
439
530
194
Brazilian imports have made up a
sizeable portion of total ethanol
imported into the U.S. However, as
shown above, these import volumes
decreased significantly in 2009. Part of
the reason for this decline in imports is
the cessation of the duty drawback that
became effective on October 1, 2008, but
also changes in world sugar prices.10
However, Brazil produces the most
ethanol in the world, reaching about 9
billion gallons in 2008.11 Thus if there
were a demand in the U.S. in 2011 for
125–144 million gallons of advanced
biofuel, it may be economical for Brazil
to export at least this volume of
sugarcane ethanol to the U.S.
EIA’s projections for 2011 suggest that
there may be sufficient volumes of
imported sugarcane ethanol and excess
biodiesel production to make up for our
proposed reduction in the required
volume of cellulosic biofuel. See Table
II.C–3.
TABLE II.C–3—EIA PROJECTED IMPORTED ETHANOL AND BIODIESEL
AVAILABILITY IN 2011
[Mill gallons] 12
Imported ethanol ...............................
Total domestic biodiesel production
Biodiesel needed to meet biomassbased diesel standard ...................
Excess biodiesel ...............................
202
860
800
60
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Further discussion of the potential
availability of biomass-based diesel in
9 ‘‘Monthly U.S. Imports of Fuel Ethanol,’’ EIA,
released 4/8/2010.
10 Lundell, Drake, ‘‘Brazilian Ethanol Export
Surge to End; U.S. Customs Loophole Closed Oct.
1,’’ Ethanol and Biodiesel News, Issue 45, November
4, 2008.
11 Renewable Fuels Association (RFA), ‘‘2008
World Fuel Ethanol Production,’’ https://
www.ethanolrfa.org/industry/statistics/#E, March
31, 2009.
12 EIA STEO, June 2010, Table 8.
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15:29 Jul 19, 2010
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2011 can be found in the next Section
II.D below.
Based on these projections, there
would be a total of 60 million gallons
of excess biodiesel production (90
million gallons ethanol-equivalent),
plus another 202 million gallons of
imported sugarcane ethanol. The total
would therefore be 292 million gallons
ethanol-equivalent. Since we are
projecting that the need for other
advanced biofuel would be in the range
of 125–144 million gallons depending
on the cellulosic biofuel standard that
we set, 292 million gallons would likely
be sufficient. Moreover, the projections
in Table II.C–3 do not account for other
potential sources of advanced biofuels.
For instance, California’s Low Carbon
Fuel Standard goes into effect in 2011,
and may compel some refiners to import
additional volumes of sugarcane ethanol
from Brazil into California. These same
volumes could count towards the
Federal RFS2 program as well. There
may also be other types of advanced
biofuel not included in the EIA
projections that could help meet our
projected shortfall. These other
advanced biofuels include, for instance,
renewable fuels made from separated
yard and food waste such as waste
cooking oil or restaurant grease used as
a diesel fuel additive. Finally,
additional market demand for imported
sugarcane ethanol and biodiesel would
likely be created if we chose not to
lower the advanced biofuel standard for
2011. Given these factors, we believe
that there are likely to be sufficient
volumes of other advanced biofuels
such that the advanced biofuel standard
need not be lowered below 1.35 billion
gallons. Thus, we are proposing to leave
the required volume of advanced biofuel
for 2011 at 1.35 billion gallons.
Nevertheless, we request comment on
whether we should lower the advanced
biofuel standard. If we do lower the
advanced biofuel standard, we request
comment on the degree to which we
should take into account other potential
sources of advanced biofuel as
discussed above.
If we lower the cellulosic biofuel
standard, we would also need to
determine if the total renewable
standard should be lowered. Lowering
both the advanced biofuel standard and
the total renewable fuel standard by the
same amount would mean that the
expected amount of conventional
renewable fuel use, such as cornethanol, would remained unchanged at
12,600 million gallons ethanol
equivalent, the same as shown in Table
II.C–1.
If instead we were to lower the
advanced biofuel standard but retain the
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42247
total renewable fuel standard at 13,950
million gallons, then we would expect
the use of conventional renewable fuels
such as corn ethanol to increase. For
instance, if we were to lower the
advanced biofuel standard by 144
million gallons to 1,206 million gallons,
we would expect the amount of cornethanol used would increase by 144
million gallons in order to satisfy the
total renewable fuel standard of 13,950
million gallons. According to EIA,
projected volumes of corn-ethanol are
indeed expected to be higher than
12,600 million gallons in 2011,
producing an excess of 1050 million
gallons. See Table II.C–4.
TABLE II.C–4—PROJECTED EXCESS
CORN ETHANOL IN 2011
[Mill gallons]
Total domestic corn ethanol production 13 .............................................
Corn ethanol needed to meet total
renewable fuel standard ...............
Excess corn ethanol .........................
13 EIA
13,650
12,600
1050
STEO, June 2010, Table 8.
However, the market potential for
ethanol in the U.S. is also a function of
the ethanol blender’s tax credit, set to
expire at the end of 2010. If this tax
credit is not renewed, the excess ethanol
volume shown in Table II.C–4 may be
smaller. Thus, while we are proposing
that the required volume of total
renewable fuel for 2011 be set at the
statutory level of 13.95 billion gallons,
we request comment on whether the
total renewable fuel standard should be
lowered.
D. Biomass-Based Diesel
While the statutory requirement that
we project volumes of cellulosic biofuel
for next year does not explicitly apply
to biomass-based diesel as well, there
are two other statutory requirements
that compel us to investigate current
and potential future volumes of
biomass-based diesel. First, the Clean
Air Act provides limited waiver
authority specific to biomass-based
diesel under 211(o)(7)(E) if a significant
renewable feedstock disruption or other
market circumstance would make the
price of biomass-based diesel fuel
increase significantly. Second, as
described more fully in Section II.C
above, we must determine whether the
required volumes of advanced biofuel
and/or total renewable fuel should be
reduced at the same time that we reduce
the required volume of cellulosic
biofuel. The amount of biomass-based
diesel that we project can be available
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in the U.S. was estimated at 2.2 billion
gallons per year across approximately
137 facilities.14 Biodiesel production for
calendar year 2009, according to the
most recently available information, was
540 million gallons, with an estimated
351 mill gallons (or 65%) being used
domestically. Domestic production rates
in the second half of 2009 increased
above production rates in the first half
as economic conditions improved, to an
annualized rate of around 646 mill gal
per year. Meanwhile, exports appeared
to stabilize at an annualized rate of
about 242 mill gal per year, after
recovering from changes in European
import regulations early in the year.
These trends for 2009 are shown
inFigure II.D–1.
In the early part of 2010, industry
reports of monthly biodiesel production
indicated that production rates have
dropped below the 2009 average. The
most likely cause is the expiration of the
biodiesel tax credit. However, EIA’s
Short-Term Energy Outlook projects
that, for the year as a whole, average
monthly biodiesel production rates in
2010 will actually exceed those in 2009.
The projected increase in monthly
biodiesel production rates later in 2010
is consistent with the fact that obligated
parties are not required to demonstrate
compliance with the 2010 biomassbased diesel volume requirement of 1.15
billion gallons until February 28, 2011.
For development of our final rule setting
the standards for 2011, we will have
more complete data with which to
evaluate the progress of the biodiesel
industry in meeting the 2010 volume
mandate and thus its preparedness for
2011.
In order to meet a 2011 biomass-based
diesel volume requirement of 0.8 billion
gallons to be consumed in the United
States, the biodiesel industry will need
to produce approximately 725 million
gal of fuel. This value accounts for the
production of 75 million gallons of
renewable diesel at one renewable
diesel facility in Geismar, Louisiana, set
to begin operations later this year.16
Assuming imports and exports continue
at a rate equivalent to that in the second
half of 2009, biodiesel production in the
U.S. would need to total approximately
900 million gal in 2011. While this
production rate would be about 10%
higher than the production rate
projected by EIA for the second half of
2010, it would be significantly lower
than the current 2.2 billion gallon
biodiesel production capacity of the
industry. Indications from the biodiesel
industry are that these idled facilities
can be brought back into production
with a relatively short leadtime, and can
thus meet the 2011 requirements for
biomass-based diesel. Moreover, as
shown in Table II.C–3, EIA is projecting
that biodiesel availability will in fact
exceed the minimum volume needed to
meet the biomass-based diesel standard
in 2011.
Finally, we believe that there will be
sufficient sources of qualifying
renewable biomass to meet the needs of
the biodiesel industry in 2011. The
largest sources of feedstock for biodiesel
in 2011 are expected to be soy oil,
rendered fats, and potentially some corn
14 Figures taken from National Biodiesel Board
list of operating plants as of April 5, 2010.
15 Data taken from Energy Information
Administration Monthly Energy Review, Table 10.4,
March 2010.
16 Project status updates are available via the
Syntroleum Web site, https://dynamicfuelsllc.com/
wp-news/.
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will directly affect our consideration of
adjustments to the volumetric
requirements for advanced biofuel and
total renewable fuel.
To project biodiesel production
volumes for 2011, we examined both
production capacity of the industry as
well as actual recent production rates.
As of April 2010, the aggregate
production capacity of biodiesel plants
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Federal Register / Vol. 75, No. 138 / Tuesday, July 20, 2010 / Proposed Rules
oil extracted during production of fuel
ethanol, as this technology continues to
proliferate. Moreover, comments we
received from a large rendering
company after the May 2009 RFS2
proposed rule suggest that there will be
adequate fats and greases feedstocks to
supply biofuels production as well as
other historical uses.17
III. Proposed Percentage Standards for
2011
A. Background
The renewable fuel standards are
expressed as a volume percentage, and
are used by each refiner, blender or
importer to determine their renewable
volume obligations (RVO). Since there
are four separate standards under the
RFS2 program, there are likewise four
separate RVOs applicable to each
obligated party. Each standard applies
to the sum of all gasoline and diesel
produced or imported. The applicable
percentage standards are set so that if
each regulated party meets the
percentages, then the amount of
renewable fuel, cellulosic biofuel,
biomass-based diesel, and advanced
biofuel used will meet the volumes
required on a nationwide basis.
As discussed in Section II.A.5, we are
proposing a required volume of
cellulosic biofuel for 2011 in the range
of 5–17.1 million gallons (6.5–25.5
million ethanol equivalent gallons). The
single volume we select for the final
rule will be used as the basis for setting
the percentage standard for cellulosic
biofuel for 2011. We are also proposing
that the advanced biofuel and total
renewable fuel volumes would not be
reduced below the statutory
requirements. The proposed 2011
volumes used to determine the four
percentage standards are shown in
Table III.A–1.
TABLE III.A–1—PROPOSED VOLUMES FOR 2011
Ethanol equivalent
volume
Actual volume
Cellulosic biofuel ...................................................................
Biomass-based diesel ...........................................................
Advanced biofuel ..................................................................
Renewable fuel .....................................................................
The formulas used in deriving the
annual renewable fuel standards are
based in part on an estimate of
combined gasoline and diesel volumes,
for both highway and nonroad uses, for
the year in which the standards will
apply. Producers of other transportation
fuels, such as natural gas, propane, and
electricity from fossil fuels, are not
StdBBD,i = 100% ×
StdAB,i = 100% ×
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StdRF,i = 100% ×
subject to the standards. Since the
standards apply to producers and
importers of gasoline and diesel, these
are the transportation fuels used to set
the standards, and then again to
determine the annual volume
obligations of an individual producer or
importer.
B. Calculation of Standards
1. How are the standards calculated?
The following formulas are used to
calculate the four percentage standards
applicable to producers and importers
of gasoline and diesel (see § 80.1405):
RFVCB,i
( Gi − RGi ) + ( GSi − RGSi ) − GEi + ( Di − RDi ) + ( DSi − RDSi ) − DEi
RFVBBD,i × 1.5
( Gi − RGi ) + ( GSi − RGSi ) − GEi + ( Di − RDi ) + ( DSi − RDSi ) − DEi
RFVAB,i
( Gi − RGi ) + ( GSi − RGSi ) − GEi + ( Di − RDi ) + ( DSi − RDSi ) − DEi
RFVRF,i
( Gi − RGi ) + ( GSi − RGSi ) − GEi + ( Di − RDi ) + ( DSi − RDSi ) − DEi
Where
StdCB,i = The cellulosic biofuel standard for
year i, in percent.
StdBBD,i = The biomass-based diesel standard
(ethanol-equivalent basis) for year i, in
percent.
StdAB,i = The advanced biofuel standard for
year i, in percent.
StdRF,i = The renewable fuel standard for year
i, in percent.
RFVCB,i = Annual volume of cellulosic
biofuel required by section 211(o) of the
Clean Air Act for year i, in gallons.
RFVBBD,i = Annual volume of biomass-based
diesel required by section 211(o) of the
Clean Air Act for year i, in gallons.
RFVAB,i = Annual volume of advanced
biofuel required by section 211(o) of the
Clean Air Act for year i, in gallons.
RFVRF,i = Annual volume of renewable fuel
required by section 211(o) of the Clean
Air Act for year i, in gallons.
Gi = Amount of gasoline projected to be used
in the 48 contiguous states and Hawaii,
in year i, in gallons.
Di = Amount of diesel projected to be used
in the 48 contiguous states and Hawaii,
in year i, in gallons.
RGi = Amount of renewable fuel blended into
gasoline that is projected to be consumed
in the 48 contiguous states and Hawaii,
in year i, in gallons.
RDi = Amount of renewable fuel blended into
diesel that is projected to be consumed
17 See Federal Register v.74 n.99 p.24903.
Comments are available in docket EPA–HQ–OAR–
2005–0161.
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6.5–25.5 mill gal.
1.20 bill gal.
1.35 bill gal.
13.95 bill gal.
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StdCB,i = 100% ×
5–17.1 mill gal ......................................................................
0.80 bill gal ...........................................................................
1.35 bill gal ...........................................................................
13.95 bill gal .........................................................................
42250
Federal Register / Vol. 75, No. 138 / Tuesday, July 20, 2010 / Proposed Rules
in the 48 contiguous states and Hawaii,
in year i, in gallons.
GSi = Amount of gasoline projected to be
used in Alaska or a U.S. territory in year
i if the state or territory opts-in, in
gallons.
RGSi = Amount of renewable fuel blended
into gasoline that is projected to be
consumed in Alaska or a U.S. territory in
year i if the state or territory opts-in, in
gallons.
DSi = Amount of diesel projected to be used
in Alaska or a U.S. territory in year i if
the state or territory opts-in, in gallons.
RDSi = Amount of renewable fuel blended
into diesel that is projected to be
consumed in Alaska or a U.S. territory in
year i if the state or territory opts-in, in
gallons.
GEi = The amount of gasoline projected to be
produced by exempt small refineries and
small refiners in year i, in gallons, in any
year they are exempt per §§ 80.1441 and
80.1442, respectively. For 2011, this
value is zero. See further discussion in
Section III.B.2 below.
DEi = The amount of diesel projected to be
produced by exempt small refineries and
small refiners in year i, in gallons, in any
year they are exempt per §§ 80.1441 and
80.1442, respectively. For 2011, this
value is zero. See further discussion in
Section III.B.2 below.
The four separate renewable fuel
standards for 2011 are based on the 49state gasoline and diesel consumption
volumes projected by EIA. The Act
requires EPA to base the standards on
an EIA estimate of the amount of
gasoline and diesel that will be sold or
introduced into commerce for that year.
The projected volume of gasoline used
to calculate the final percentage
standards will continue to be provided
by the October issue of EIA’s ShortTerm Energy Outlook (STEO). For the
purposes of this proposal, we have used
the March 2010 issue of STEO. The
projected volume of transportation
diesel used to calculate the final
percentage standards will be provided
by the most recent Annual Energy
Outlook (AEO). For the purposes of this
proposal, we have used the Early
Release version of AEO2010. Gasoline
and diesel volumes are adjusted to
account for renewable fuel contained in
the EIA projections. Beginning in 2011,
gasoline and diesel volumes produced
by small refineries and small refiners
are not exempt, and thus there is no
adjustment to the gasoline and diesel
volumes in today’s proposal to account
for such an exemption, as there has been
in past years. However, as discussed
more fully in Section III.B.2 below,
depending upon the results of a
Congressionally-mandated DOE study, it
is possible that the exemption for
gasoline and diesel volumes produced
by small refineries and small refiners
may be extended. In addition, EPA may
extend the exemption for individual
small refineries on a case-by-case basis
if they demonstrate disproportionate
economic hardship.
As finalized in the March 26, 2010
RFS2 rule, the standards are expressed
in terms of energy-equivalent gallons of
renewable fuel, with the cellulosic
biofuel, advanced biofuel, and total
renewable fuel standards based on
ethanol equivalence and the biomassbased diesel standard based on biodiesel
equivalence. However, all RIN
generation is based on ethanolequivalence. More specifically, the
RFS2 regulations provide that
production or import of a gallon of
biodiesel will lead to the generation of
1.5 RINs. In order to ensure that demand
for 0.8 billion physical gallons of
biomass-based diesel will be created in
2011, the calculation of the biomassbased diesel standard provides that the
required volume be multiplied by 1.5.
The net result is a biomass-based diesel
gallon being worth 1.0 gallons toward
the biomass-based diesel standard, but
worth 1.5 gallons toward the other
standards.
The levels of the percentage standards
would be reduced if Alaska or a U.S.
territory chooses to participate in the
RFS2 program, as gasoline and diesel
produced in or imported into that state
or territory would then be subject to the
standard. Neither Alaska nor any U.S.
territory has chosen to participate in the
RFS2 program at this time, and thus the
value of the related terms in the
calculation of the standards is zero.
Note that the terms for projected
volumes of gasoline and diesel use
include gasoline and diesel that has
been blended with renewable fuel.
Because the gasoline and diesel volumes
described above include renewable fuel
use, we must subtract the total
renewable fuel volume from the total
gasoline and diesel volume to get total
non-renewable gasoline and diesel
volumes. The values of the variables
described above are shown in Table
III.B.1–1. Terms not included in this
table have a value of zero.
TABLE III.B.1–1—VALUES FOR TERMS
IN CALCULATION OF THE STANDARDS
[Bill gallons]
Term
RFVCB,2011 .............
RFVBBD,2011 ..........
RFVAB,2011 ............
RFVRF,2011 .............
G2011 .....................
D2011 ......................
RG2011 ...................
RD2011 ...................
Value
0.0065–0.0255
0.80
1.35
13.95
139.66
50.01
13.38
0.74
Using the volumes shown in Table
III.B.1–1, we have calculated the
proposed percentage standards for 2011
as shown in Table III.B.1–2.
TABLE III.B.1–2—PROPOSED PERCENTAGE STANDARDS FOR 2011
Cellulosic biofuel ..............................................................................................................................................................................
Biomass-based diesel ......................................................................................................................................................................
Advanced biofuel .............................................................................................................................................................................
Renewable fuel ................................................................................................................................................................................
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2. Small Refineries and Small Refiners
In CAA section 211(o)(9), enacted as
part of EPAct, Congress provided a
temporary exemption to small refineries
(those refineries with a crude
throughput of no more than 75,000
barrels of crude per day) through
December 31, 2010. In RFS1, we
exercised our discretion under section
211(o)(3)(B) and extended this
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temporary exemption to the few
remaining small refiners that met the
Small Business Administration’s (SBA)
definition of a small business (1,500
employees or less company-wide) but
did not meet the statutory small refinery
definition as noted above. Because EISA
did not alter the small refinery
exemption in any way, the RFS2
program regulations exempt gasoline
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0.004–0.015%
0.68%
0.77%
7.95%
and diesel produced by small refineries
and small refiners in 2010 from the
renewable fuels standard (unless the
exemption was waived), see 40 CFR
§ 80.1141.
Under the RFS program, Congress has
provided two ways that small refineries
can receive a temporary extension of the
exemption beyond 2010. One is based
on the results of a study conducted by
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Federal Register / Vol. 75, No. 138 / Tuesday, July 20, 2010 / Proposed Rules
the Department of Energy (DOE) to
determine if small refineries would face
a disproportionate economic hardship
under the RFS program. The other is
based on EPA determination of
disproportionate economic hardship on
a case-by-case basis in response to
refiner petitions.
In January 2009, DOE issued a Small
Refineries Exemption Study which did
not find that small refineries would face
a disproportionate economic hardship
under the RFS program. The
conclusions were based in part on the
expected robust availability of RINs and
EPA’s ability to grant relief on a case-bycase basis. Subsequently, Congress
directed DOE to complete a
reassessment and issue a revised report
by June 30, 2010. DOE had not revised
its study at the time of the RFS2 final
rulemaking nor at the time of this
writing. Additionally, we have not
received any requests for relief on a
case-by-case basis from any small
refinery. If DOE prepares a revised
study, and the results of that study show
a disproportionate economic hardship
for any small refineries under the RFS
program, we will take appropriate
42251
action to extend the exemption.
However, until and unless a DOE study
supporting an extension to the
temporary exemption for small
refineries beyond 2010 is used, or any
petitions to EPA from individual small
refineries claiming disproportionate
economic hardship are approved, we are
not proposing to change the required
inclusion of small refineries and small
refiners in the RFS2 program beginning
with the 2011 compliance period.
actively preparing for production. This
smaller group of companies formed the
basis for our projection of potential 2011
volumes of cellulosic biofuel.
This section discusses the full range
of cellulosic biofuel technologies being
considered among producers, with
reference to those individual companies
that are focusing on each technology
and those we project will be most likely
to use those technologies to produce
cellulosic biofuel in 2011.
IV. Cellulosic Biofuel Technology
Assessment
A. What pathways are valid for the
production of cellulosic biofuel?
In projecting the volumes of cellulosic
biofuel for 2011, we conducted a
technical assessment of the production
technologies that are under
consideration by the broad universe of
companies we investigated. Many of
these companies are still in the research
phase, resolving outstanding issues with
specific technologies, and/or in the
design phase to implement those
technologies for the production of
commercial-scale volumes of cellulosic
biofuel. A subset of the companies we
investigated have moved beyond the
research and design phase and are
In determining the appropriate
volume of cellulosic biofuel on which to
base the percentage standard for 2011,
we must ensure that the production
facilities we use as the basis for this
volume are using fuel pathways that are
valid for the production of cellulosic
biofuel. In general this means that each
facility’s pathway (combination of
feedstock, production process, and fuel
type) must be included in Table 1 to
§ 80.1426 and be assigned a D code of
either 3 or 7. As of this writing, there
are three valid pathways available as
shown in Table IV.A–1 below.
TABLE IV.A–1—CELLULOSIC BIOFUEL PATHWAYS FOR USE IN GENERATING RINS
Fuel type
Feedstock
Production process requirements
Ethanol ................................
Cellulosic Biomass from agricultural residues, slash, forest thinnings and forest product residues, annual
covercrops; switchgrass, and miscanthus; cellulosic
components of separated yard wastes; cellulosic
components of separated food wastes; and cellulosic
components of separated MSW.
Cellulosic Biomass from agricultural residues, slash, forest thinnings and forest product residues, annual
covercrops, switchgrass, and miscanthus; cellulosic
components of separated yard wastes; cellulosic
components of separated food wastes; and cellulosic
components of separated MSW.
Cellulosic Biomass from agricultural residues, slash, forest thinnings and forest product residues, annual
covercrops, switchgrass, and miscanthus; cellulosic
components of separated yard wastes; cellulosic
components of separated food wastes; and cellulosic
components of separated MSW.
Any ......................................
3 (cellulosic biofuel).
Any ......................................
7 (cellulosic diesel).
Fischer-Tropsch process ....
3 (cellulosic biofuel).
Cellulosic Diesel, Jet Fuel
and Heating Oil.
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Cellulosic Naphtha ..............
Of the eight facilities that we
currently believe could contribute to the
volume of commercially available
cellulosic biofuel in 2011, six would
produce ethanol from cellulosic biomass
and two would produce diesel from
cellulosic biomass. None of the facilities
we have evaluated would produce
cellulosic naphtha through a FischerTropsch process.
Two of the facilities shown in Table
II.A.5–1, Cello Energy and KL Energy,
intend to use wood as the primary
feedstock. The only types of wood that
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are currently allowed as a valid
feedstock are those derived from various
types of waste. If either of these two
companies choose to use trees from a
tree plantation instead of qualifying
waste wood, its pathway would not fall
into the any of the pathways currently
listed in Table 1 to § 80.1426. However,
as described more fully in Section V.A,
we are currently evaluating the lifecycle
GHG impacts of biofuel made from
pulpwood, including wood from tree
plantations. If such a pathway is
determined to meet the 60% GHG
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D–Code
threshold required for cellulosic biofuel,
we expect that it will be added to Table
1 to § 80.1426 in time to apply to fuel
produced in 2011. For the purposes of
this proposal, we have chosen to retain
the volumes from these two companies
in our projections of 2011 cellulosic
biofuel volume, but we will revisit this
issue for the final rule.
B. Cellulosic Feedstocks
Cellulosic biofuel technologies are
different from other biofuel technologies
because they convert the cellulose and
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other very difficult to convert
compounds into biofuels. Unlike grain
feedstocks where the major
carbohydrate is starch (very simply
combined sugars), lignocellulosic
biomass is composed mainly of
cellulose (40–60%) and hemicellulose
(20–40%).18 Cellulose and
hemicellulose are made up of sugars
linked together in long chains called
polysaccharides. Once hydrolyzed, they
can be fermented into ethanol. Most all
the remainder of cellulosic feedstocks
consists of lignin, a complex polymer
which serves as a stiffening and
hydrophobic (water-repelling) agent in
cell walls. Currently, lignin cannot be
fermented into ethanol, but could be
burned as a by-product to generate
electricity. Thermochemical, pyrolysis
and depolymerization processing,
however, can convert some or even most
of the lignin, in addition to the
cellulosic and hemicellulose, into
biofuels.
C. Emerging Technologies
When evaluating the array of biofuel
technologies which could produce one
or more fuels from cellulose that could
qualify under RFS2, we found that it is
helpful to organize them into fuel
technology categories. Organizing them
into categories eases the task of
understanding the technologies, and
also simplifies our understanding of the
costs and lifecycle impacts of these
technologies because similar
technologies likely have similar cost
and lifecycle impacts. The simplest
organization is by the fuel produced.
However, we frequently found that
additional subdivisions were also
helpful. Table IV.C–1 provides a list of
technologies, the cellulosic fuels
produced and a list of many of the
companies which we learned are
pursuing the technology (or something
very similar to the technology listed in
the category).
TABLE IV.C–1—LIST OF TECHNOLOGY CATEGORIES, THE FUELS PRODUCED THROUGH EACH TYPE OF TECHNOLOGY, AND
THE COMPANIES PURSUING THEM
Technology category
Technology
Fuels produced
Companies
Biochemical ..............................
Enzymatic Hydrolysis .........................
Ethanol ...................................
Acid Hydrolysis ...................................
Ethanol ...................................
Dilute Acid, Steam Explosion of Cellulose.
Consolidated Bioprocessing (one step
hydrolysis and fermentation) of Cellulose.
Conversion of Cellulose via carboxylic
acid.
One step Conversion of Cellulose to
distillate.
Thermochemical/Fischer Tropsch ......
Ethanol ...................................
Abengoa, AE Fuels, DuPont Danisco,
Florida Crystals, Gevo, Poet, ICM,
Iogen, BPI, Energy, Fiberight, KL
Energy.
Agresti, Arkenol, Blue Fire, Pencor,
Pangen, Raven Biofuels.
Verenium, BP, Central Minnesota
Ethanol Coop.
Mascoma, Qteros.
Thermochemical/Fischer Tropsch ......
Thermochemical/Catalytic conversion
of syngas to alcohols.
DME .......................................
Ethanol ...................................
Thermochemical w/Biochemical catalyst.
Acid Hydrolysis of cellulose to intermediate;
hydrogenation
using
Thermochemical syngas from noncellulose fraction.
Catalytic Depolymerization of Cellulose.
Pyrolysis of Cellulose .........................
Thermochemical .......................
Hybrid .......................................
Depolymerization ......................
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Other .........................................
Catalytic Reforming of Sugars from
Cellulose.
Of the technologies listed above,
many of them are considered to be
‘‘second generation’’ biofuels or new
biofuel technologies capable of meeting
either the advanced biofuel or cellulosic
biofuel RFS standard. The following
sections describe specific companies
and the new biofuel technologies which
the companies have developed or are
Ethanol ...................................
Ethanol, Gasoline, Jet Fuel,
Diesel Fuel.
Diesel, Jet Fuel or Naphtha ...
Terrabon, Swift Fuels.
Diesel Fuel and Naphtha .......
Ethanol ...................................
Choren, Flambeau River Biofuels,
Baard, Clearfuels, Gulf Coast Energy, Rentech, TRI.
Chemrec, New Page.
Range Fuels, Pearson Technologies,
Fulcrum Bioenergy, Enerkem, and
Gulf Coast Energy.
Coskata, INEOS Bio.
Ethanol, Other alcohols ..........
Zeachem.
Diesel, Jet Fuel or Naphtha ...
Cello Energy.
Diesel, Jet Fuel, or Gasoline
Envergent (UOP/Ensyn), Dynamotive,
Petrobras, Univ. of Mass, KIOR.
Virent.
Gasoline. ................................
developing. This summary is not meant
to be an unabridged list of new biofuel
technologies, but rather a description of
some of the more prominent of the new
biofuel technologies that serve to
provide a sense of the technology
categories listed above. The process
technology summaries are based on
information provided by the respective
Bell Bioenergy, LS9.
companies. EPA has not been able to
confirm all of the information,
statements, process conditions, and the
process flow steps necessary for any of
these processes and companies.
1. Biochemical
Biochemical conversion refers to a
broad grouping of processes that use
18 DOE. ‘‘Biomass Program: ABC’s of Biofuels’’.
Accessed at: https://www1.eere.energy.govbiomass/
abcs_biofuels.html#content.
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particle size of the incoming feedstock
and removes any contaminants that may
negatively impact the rest of the
process. In the pretreatment step the
structure of the lignin and
hemicellulose is disrupted, usually
using some combination of heat,
pressure, acid, or base, to allow for a
more effective hydrolysis of the
cellulosic material to simple sugars. In
the hydrolysis stage the cellulose and
any remaining hemicellulose is
converted into simple sugars, usually
using an enzyme or strong acid. In the
fermentation or fuel conversion step, the
simple sugars are converted to the
desired fuel by a biological organism. In
the final step the fuel that is produced
is separated from the water and other
byproducts by distillation or some other
means. A basic diagram of the
biochemical conversion process can be
found in Figure IV.C.1–1 below.
While this diagram shows the
production of ethanol from cellulosic
biomass, it is possible to use the same
process to produce other fuels or
specialty chemicals using different
biological organisms.
The following sections will discuss
each of these steps in greater detail,
discuss some of the variations to this
general process, and discuss some of the
advantages and disadvantages of the
biochemical process of producing
biofuel from cellulosic materials as
compared to other fuel production
processes.
Seven of the eight companies that
EPA believes may produce cellulosic
biofuel in 2011 plan to use a
biochemical process to produce
biofuels. Five of these companies, AE
Biofuels, Dupont Danisco Cellulosic
Ethanol, Fiberight, Iogen, and KL
energy, all plan to use an enzymatic
hydrolysis, while Agresti Biofuels and
Bell Bio-Energy are pursuing gravity
pressure vessel and single step process
technologies, respectively. The main
reason for the dominance of
biochemical technologies in 2011 is the
relatively low capital costs of these
projects compared to other cellulosic
biofuel facilities. Biochemical projects
also benefit less from economies of
scale, making smaller and less capital
intensive commercial facilities more
feasible. The following sections, as well
as a technical memorandum that has
been added to the docket 20, provide
more information on the biochemical
processes being pursued by majority of
the companies we expect to produce
cellulosic biofuels and make them
commercially available in 2011, as well
as many other companies planning to
begin production in later years.
reduce the size of the material they
receive as needed for their process. In
coming years, as the market for
cellulosic materials expands,
purchasing feedstock that has already
been ground or chipped may be possible
and cost effective, as these processes
increase the density of this material and
may reduce transportation costs.
In addition to size reduction, steps
must also be taken to remove any
material from the feedstock that might
be detrimental to the fuel production
process. Contaminants in the feedstock,
such as dirt, rocks, plastics, metals, and
other non-biogenic materials, would at
best travel through the fuel production
process unchanged, resulting in reduced
fuel production capacity. Depending on
the type of contaminant they may also
be converted to undesired byproducts
that must be separated from the fuel.
They could also be toxic to the
biological organisms being used to
convert the sugars to fuel, necessitating
a shut down and restart of the plant.
Any of these scenarios would result in
a significant cost to the fuel producer.
Feedstocks such as agricultural
residues, wood chips, or herbaceous or
woody energy crops are likely to contain
far fewer contaminants than more
heterogeneous feedstocks such as
municipal solid waste (MSW).
19 Image
From: https://www.afdc.energy.gov/afdc/
ethanol/production_cellulosic.html.
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a. Feedstock Handling
The first step of the biochemical
conversion process is to insure that the
biomass stream can be utilized by the
rest of the conversion process. This
most often takes the form of size
reduction, either by grinding or
chipping as appropriate for the type of
biomass. While this is a relatively
simple process it is essential to allow
the following steps of the process to
function as designed. It is also a
potentially energy intensive process. It
may be possible for biofuel producers to
purchase cellulosic material that is
already of the appropriate size, however
we believe that in the near term this is
unlikely and most biofuel producers
will have to invest in equipment to
20 Wyborny, Lester. ‘‘In-Depth Assessment of
Advanced Biofuels Technologies.’’ Memo to the
docket, May 2010.
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biological organisms to convert
cellulosic feedstocks into biofuels.
While no two processes are identical,
many of these processes follow a similar
basic pathway to convert cellulosic
materials to biofuel. The general process
of most biochemical cellulosic biofuel
processes consists of five main steps:
feedstock handling, pretreatment,
hydrolysis, fermentation/fuel
conversion, and distillation/separation.
The feedstock handling step reduces the
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b. Biomass Pretreatment
The purpose of the biomass
pretreatment stage is to disrupt the
structure of the cellulosic biomass to
allow for the hydrolysis of the cellulose
and hemicellulose into simple sugars.
The ideal pretreatment stage would
allow for a high conversion of the
cellulose and hemicellulose to simple
sugars, minimize the degradation of
these sugars to undesired forms that
reduce fuel yields and inhibit
fermentation, not require especially
large or expensive reaction vessels, and
be a relatively robust and simple
process. No single biomass pretreatment
method has yet been discovered that
meets all of these goals, but rather a
variety of options are being used by
various cellulosic fuel producers, each
with their own strengths and
weaknesses. Dilute acid pretreatment
and alkaline pretreatment are two
methods currently being used that
attack the hemicellulose and lignin
portions of the cellulosic biomass
respectively. Other methods, such as
steam explosion and ammonia fiber
expansion, seek to use high temperature
and pressure, followed by rapid
decompression to disrupt the structure
of the cellulosic biomass and allow for
a more efficient hydrolysis of the
cellulose and hemicellulose to simple
sugars. Each of these methods is
discussed in more detail in a technical
memo that has been added to the
docket.21 The cost and characteristics of
the cellulosic feedstock being processed
is likely to have a significant impact on
the pretreatment process that is used.
c. Hydrolysis
In the hydrolysis step the cellulose
and any remaining hemicellulose are
converted to simple sugars. There are
two main methods of hydrolysis, acid
hydrolysis and enzymatic hydrolysis.
Acid hydrolysis is the oldest technology
for the conversion of cellulosic
feedstock to ethanol and can only be
used following an acid pretreatment
process. An alternative method is to use
a combination of enzymes to perform
the hydrolysis after the biomass has
been pretreated. This process is
potentially more effective at
hydrolyzing pretreated biomass but in
the past has not been economically
feasible due to the prohibitively high
cost of the enzymes. The falling cost of
these enzymes in recent years has made
the production of cellulosic biofuels
using enzymatic hydrolysis possible.
The lignin is largely unaffected by the
21 Wyborny, Lester. ‘‘In-Depth Assessment of
Advanced Biofuels Technologies.’’ Memo to the
docket, May 2010.
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hydrolysis and fuel production steps but
is carried through these processes until
it is separated out in the fuel separation
step and burned for process energy or
sold as a co-product.
i. Acid Hydrolysis
Acid hydrolysis is a technique that
has been used for over 100 years to
convert cellulosic feedstocks into fuels.
In the acid hydrolysis process the lignin
and cellulose portions of the feedstock
that remain after the hemicellulose has
been dissolved, hydrolyzed, and
separated during the dilute acid
pretreatment process is treated with a
second acid stream. This second acid
treatment uses a less concentrated acid
than the pretreatment stage but at a
higher temperature, as high as 215° C.
This treatment hydrolyzes the cellulose
into glucose and other 6 carbon sugars
that are then fed to biological organisms
to produce the desired fuel. It is
necessary to hydrolyze the
hemicellulose and cellulose in two
separate steps to prevent the conversion
of the pentose sugars that result from
the hydrolysis of the hemicellulose from
being further converted into furfural and
other chemicals. This would not only
reduce the total production of sugars
from the cellulosic feedstock, but also
inhibit the production of fuel from the
sugars in later stages of the process.
The acidic solution containing the
sugars produced as a result of the
hydrolysis reaction must also be treated
so that this stream can be fed to the
biological organisms that will convert
these sugars into fuel. In order to
operate an acid hydrolysis process cost
effectively the acid must be recovered,
not simply neutralized. Methods
currently being used to recover this acid
include membrane separation and
continuous ion exchange. The
advantages of using an acid hydrolysis
are that this process is well understood
and capable of producing high sugar
yields from a wide variety of feedstocks.
Capital costs are high however, as
materials compatible with the acidic
streams must be extensively utilized.
The high temperatures necessary for
acid hydrolysis also result in
considerable energy costs, and
profitability is highly dependent on the
ability to effectively recover and reuse
the acid.
ii. Enzymatic Hydrolysis
The enzymatic hydrolysis process
uses enzymes, rather than acids, to
hydrolyze the cellulose and any
remaining hemicellulose from the
pretreatment process. This process is
much more versatile than the acid
hydrolysis and can be used in
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combination with any of the
pretreatment processes described above,
provided that the structure of the
lignocellulosic feedstock has been
disrupted enough to allow the enzymes
to easily access the hemicellulose and
cellulose. After the feedstock has gone
through pretreatment a cocktail of
cellulose enzymes is added. These
enzymes can be produced by the
cellulosic biofuel producer or purchased
from enzyme producers such as
Novozymes, Genencor, and others. The
exact mixture of enzymes used in the
enzymatic hydrolysis stage can vary
greatly depending on which of the
pretreatment stages is used as well as
the composition of the feedstock.
The main advantages of the enzymatic
hydrolysis process are a result of the
mild operating conditions. Because no
acid is used special materials are not
required for the reaction vessels.
Enzymatic hydrolysis is carried out at
relatively low temperatures, usually
around 50° C, and atmospheric pressure
and therefore has low energy
requirements. These conditions also
result in less undesired reactions that
would reduce the production of sugars
and potentially inhibit fuel production.
Enzymatic hydrolysis works best with a
uniform feedstock, such as agricultural
residues or energy crops, where the
concentration and combination of
enzymes can be optimized for maximum
sugar production. If the composition of
the feedstock varies daily, as can be the
case with fuel producers utilizing MSW
or other waste streams, or even
seasonally, it would make it more
difficult to ensure that the correct
enzyme cocktail is being used to carry
out the hydrolysis as efficiently as
possible. The main hurdle to using an
enzymatic hydrolysis has been and
continues to be the costs of the
enzymes. Recent advances by
companies that produce enzymes for the
hydrolysis of cellulosic materials have
resulted in a drastic cost reduction of
these enzymes. If, as many researchers
and cellulosic biofuel producers expect,
the cost of these enzymes continues to
fall it is likely that enzymatic hydrolysis
will be a lower cost option than acid
hydrolysis, especially for cellulosic
biofuel producers utilizing uniform
feedstocks.
d. Fuel Production
After the cellulosic biomass has been
hydrolyzed to simple sugars this sugar
solution is converted to fuel by
biological organisms. In some
biochemical fuel production processes
the sugars produced from the
fermentation of the hemicellulose,
which are mainly five carbon sugars, are
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converted to fuel in a separate reactor
and with a different set of organisms
than the sugars produced from the
cellulose hydrolysis, which are mainly
six carbon sugars. Others processes,
however, produce fuel from the five and
six carbon sugars in the same reaction
vessel.
A wide range of biological organisms
can be used to convert the simple sugars
into fuel. These include yeasts, bacteria,
and other microbes, some of which are
naturally occurring and others that have
been genetically modified. The ideal
biological organism converts both five
and six carbon sugars to fuel with a high
efficiency, is able to tolerate a range of
conditions, and is adaptable to process
sugar streams of varying compositions
that may result from variations in
feedstock. Many cellulosic biofuel
producers have their own proprietary
organism or organisms optimized to
produce the desired fuel from their
unique combination of feedstock,
pretreatment and hydrolysis processes,
and fuel conversion conditions. Other
cellulosic fuel producers license these
organisms from biotechnology
companies who specialize in their
discovery and production.
The many different biological
organisms being considered for
cellulosic biofuel production are
capable of producing many different
types of fuels. Many cellulosic biofuel
producers are working with organisms
that produce ethanol. In many ways this
is the most simple fuel to produce from
lignocellulosic biomass as the
production of ethanol from simple
sugars is a well understood process.
Others intend to produce butanol or
other alcohols that have higher energy
content. Butanol may be able to be
blended into gasoline in greater
proportion to ethanol and therefore has
a potentially greater market as well as
value due to its higher energy content.
Yields for butanol, however, are
currently significantly lower per ton of
feedstock than ethanol. Some of the fuel
producers who plan to produce alcohols
are considering purchasing and
modifying already existing grain ethanol
plants. This would potentially have
significant capital cost savings as many
of the units used in a grain ethanol
process are very similar to those
required by the biochemical fuel
production process and could be used
with minimal modification.
Other cellulosic biofuel producers
intend to produce hydrocarbon fuels
very similar to gasoline, diesel, and jet
fuel. These fuels command a higher
price than alcohols, have a greater
energy density, and are potentially drop
in fuels that could be used in any
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conventional vehicles without strict
blending limits. They could also be
transported by existing pipelines and
utilize the same infrastructure as the
petroleum industry. Some of the
processes being researched by fuel
producers produce a single compound,
such as iso-octane, that would need to
be blended into petroleum gasoline in
order to be used while others produce
a range of hydrocarbons very similar to
those found in gasoline or diesel fuel
refined from petroleum and could
potentially be used in conventional
vehicles without blending. While the
prospect of producing hydrocarbon
fuels from cellulosic feedstock is
promising, the current yields of fuel
produced by these organisms are
significantly lower than those that are
producing ethanol and other alcohols.
Improvement in the yields of these
organisms will have to be realized in
order for cellulosic hydrocarbon fuels
produced via a biochemical process to
compete with cellulosic ethanol, and
ultimately petroleum based fuels.
e. Fuel Separation
In the fuel separation stage the fuel
produced is separated from the water,
lignin, any un-reacted hemicellulose
and cellulose, and any other compounds
remaining after the fuel production
stage. The complexity of this stage is
highly dependent on the type of fuel
produced. For processes producing
hydrocarbon fuels this stage can be as
simple as a settling tank, where the
hydrocarbons are allowed to float to the
top and removed. Recovering the
ethanol is a much more difficult task. To
recover the ethanol a distillation
process, nearly identical to that used in
the grain ethanol industry, is used. The
ethanol solution is first separated from
the solids before being sent to a
distillation column called a beer
column. The overheads of the beer
column are fed to a second distillation
column, called a rectifier for further
separation. The rectifier produces a
stream with an ethanol of approximately
96%. A molecular sieve unit is then
used to dehydrate this stream to
produce fuel grade ethanol with purity
greater than 99.5%. Gasoline is added to
the fuel ethanol as a denaturant before
the fuel is stored. The distillation of
ethanol is a very energy intensive
process and new technologies, such as
membrane separation, are being
developed that could potentially reduce
the energy intensity, and thus the cost,
of the ethanol dehydration process.
After the fuel has been recovered the
remaining lignin and solids are dried
and either burned on site to provide
process heat and electricity or sold as a
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byproduct of the fuel production
process. The waste water is either
recycled or sent to a water treatment
facility.
f. Process Variations
While the process described above
outlines the general biochemical process
used by many cellulosic biofuel
producers, there are several prominent
variations being pursued by prospective
biofuel producers. These variations
usually seek to simplify the biochemical
fuel production process by combining
several steps into a single step or using
other means to reduce the capital or
operating costs of the process.
Simultaneous Saccharification and
Fermentation (SSF), Simultaneous
Saccharification and Co-Fermentation
(SSCF), Consolidated Bio-Processing
(CBP), and Single Step Fuel Production
are all production methods being
developed by various biofuel
production companies to combine two
or more of the steps outlined above.
These process variations are discussed
in more detail in a technical memo that
can be found in the docket.22 These
modifications are usually enabled by a
proprietary technology or biological
organism that makes these changes
possible.
g. Current Status of Biochemical
Conversion Technology
The biochemical cellulosic fuel
production industry is currently
transitioning from an industry
consisting mostly of small scale research
and optimization focused facilities to
one capable of producing fuel at a
commercial scale. Companies such as
Iogen, DuPont Danisco Cellulosic
Ethanol, and KL Energy are just
beginning to market the fuel they are
producing at their first small scale
commercial fuel production facilities.
By 2011 we expect several other
cellulosic fuel production facilities
using biochemical processes to come
online, including the first commercial
scale facilities of AE Advanced Fuels,
Agresti Biofuels, Bell Bio-Energy, and
Fiberight. Many other facilities,
including some large scale facilities
capable of producing tens of millions of
gallons of fuel are planned to come
online starting in 2012 and in the
following years.
There are many factors that are likely
to continue to drive the expansion of the
cellulosic biofuel industry. The high
price of petroleum fuels and the
mandates put into place by the RFS2
22 Wyborny, Lester. ‘‘In-Depth Assessment of
Advanced Biofuels Technologies.’’ Memo to the
docket, May 2010.
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program have created a large demand
for cellulosic biofuels. The biochemical
production process also has several
advantages over other methods of
producing fuel from cellulosic
feedstocks including relatively low
capital costs, highly selective fuel
production, flexibility in the type of fuel
produced, and the promise of future
production cost reductions.
While the poor worldwide economy
and tight credit markets has had a
negative impact on the biofuel industry
as a whole the cellulosic biofuel
producers utilizing biochemical
processes have not been as hard hit as
many others in the industry. This is
partially due to the relatively low
capital costs of biochemical production
plants as a result of the relative
simplicity and mild operating
conditions of these plants. Several
companies have been able to purchase
distressed grain ethanol plants and are
in the process of modifying them to
produce cellulosic ethanol, further
reducing the capital costs of their initial
facilities. Once biochemical fuel
production facilities have been
constructed another advantage they
have over other fuel production
processes is that their high selectivity in
the fuels they produce. Unlike chemical
catalysts, which often produce a range
of products and byproducts, biological
organisms often produce a single type of
fuel, which leads to very high fuel
production rates per unit sugar. Finally,
there is a large potential to further
decrease the production costs of
cellulosic biofuels using the
biochemical processes. Unlike other
production methods such as gasification
which are relatively mature
technologies, biochemical production of
fuels is a young technology. One of the
major costs of the biochemical fuel
production processes currently are the
enzymes. Great strides have been made
recently in reducing the cost of these
enzymes, and as the price of enzymes
continues to fall so will the operating
costs of biochemical fuel production
processes.
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h. Major Hurdles to Commercialization
Despite the many promising qualities
of the biochemical fuel production
process several significant hurdles
remain. Improvements must be made to
the pretreatment processes of the
cellulosic materials to maximize the
conversion of cellulose and
hemicellulose to simple sugars and to
minimize the production of other
undesired compounds, especially those
that may inhibit the fuel production
process. The ability of the biological
fuel production organisms to process a
wide range of both five and six carbon
sugars must also continue to be
improved. Both these improvements
will increase the fuel yield per ton of
cellulosic feedstock, reducing the
operating costs of the process. The cost
of enzymes must continue to decrease to
allow the fuel produced by biochemical
processes to be cost competitive with
petroleum and other cellulosic biofuels.
Another significant hurdle that must
be overcome is the profitable utilization
of the lignin portion of the cellulosic
feedstock. Unlike some of the other
cellulosic biofuel production processes,
the biochemical process does not
convert the lignin to fuel. Cellulosic
feedstock can contain up to 40% lignin,
depending on the type of feedstock
used, so the effective utilization of this
lignin is an important piece of the
profitability of the biochemical process.
One option for the use of the lignin is
to burn it to provide process heat and
electricity, as well as excess electricity
to the grid. While this would provide
good value for the lignin, it would
require fairly expensive boilers and
turbines that increases the capital cost
of the facility. If the lignin cannot be
used as part of the fuel production
process it may be able to be marketed
as a solid fuel with high energy density
and low carbon intensity.
2. Thermochemical
Thermochemical conversion involves
biomass being broken down into syngas
using heat and upgraded to fuels using
a combination of heat and pressure in
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the presence of catalysts.23 For
generating the syngas, thermochemical
processes partially oxidize biomass in
the presence of a gasifying agent,
usually air, oxygen, and/or steam. It is
important to note that these processing
steps are also applicable to other
feedstocks (e.g., coal or natural gas); the
only difference is that a renewable
feedstock is used (i.e., biomass) to
produce cellulosic biofuel. The
cellulosic biofuel produced can be
mixed alcohols, but optimizing the
process to produce ethanol, or it could
be diesel fuel and naphtha. A
thermochemical unit can also
complement a biochemical processing
plant to enhance the economics of an
integrated biorefinery by converting
lignin-rich, non-fermentable material
left over from high-starch or cellulosic
feedstocks conversion.24 Compared to
corn ethanol or biochemical cellulosic
ethanol plants, the use of biomass
gasification may allow for greater
flexibility to utilize different biomass
feedstocks at a specific plant. Mixed
biomass feedstocks may be used, based
on availability of long-term suppliers,
seasonal availability, harvest cycle, and
costs.
The general steps of the gasification
thermochemical process include:
feedstock handling, gasification, gas
cleanup and conditioning, fuel
synthesis, and separation. Refer to
Figure IV.C.2–1 for a schematic of the
thermochemical cellulosic ethanol
production process through gasification.
For greater detail on the
thermochemical mixed-alcohols route
refer to NREL technical
documentation.25
23 U.S. DOE. Technologies: Processing and
Conversion. Accessed at: https://
www1.eere.energy.gov/biomass/
processing_conversion.html on October 28, 2008.
24 EERE, DOE, Thermochemical Conversion, &
Biochemical Conversion, Biomass Program
Thermochemical R&D. https://
www1.eere.energy.gov/biomass/
thermochemical_conversion.html https://
www1.eere.energy.gov/biomass/
biochemical_conversion.html.
25 Aden, Andy, Mixed Alcohols from Woody
Biomass—2010, 2015, 2022, National Renewable
Energy Laboratory (NREL), September 23, 2009.
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which produces diesel fuel and naphtha
through a thermochemical process.
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Figure IV.C.2–2 is a block diagram of
a biomass to liquids (BTL) process
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The first step in a thermochemical
plant is feedstock size reduction. The
particle size requirement for a
thermochemical process is around 10mm to 100-mm in diameter.26 Once the
feed is ground to the proper size, flue
gases from the char combustor and tar
reformer catalyst regenerator dry the
feed from the as received moisture level
of around 30% to 50% moisture to the
level required by the gasifier.
The dried, ground feedstock is fed to
a gasification reactor for producing
syngas. There are two general classes of
gasifiers, partial oxidation (POx) and
indirect gasifiers. Partial oxidation
gasifiers (directly-heated gasifiers) use
the exothermic reaction between oxygen
and organics to provide the heat
necessary to devolatilize biomass and to
convert residual carbon-rich chars.
Indirect gasifiers use steam to
accomplish gasification through heat
transfer from a hot solid or through a
heat transfer surface. Either the
byproduct char and/or a portion of the
product gas can be combusted with air
(external to the gasifier itself) to provide
the energy required for gasification. The
raw syngas produced from either type of
gasifier has a low to medium energy
content which consists mainly of CO,
H2, CO2, H2O, N2, and hydrocarbons.
Once the biomass is gasified and
converted to syngas, the syngas must be
cleaned and conditioned, as minor
components of tars, sulfur, nitrogen
oxides, alkali metals, and particulates
have the potential to negatively affect
the syngas conversion steps. Therefore,
unwanted impurities are removed in a
gas cleanup step and the gas
composition is further modified during
gas conditioning. Because this step is a
necessary part of the thermochemical
process, thermochemical plants are
good candidates for processing
municipal solid waste (MSW) which
may contain a significant amount of
toxic material. Gas conditioning steps
include sulfur polishing to remove trace
levels of H2S and water-gas shift to
adjust the final H2/CO ratio for
optimized fuel synthesis.
After cleanup and conditioning, the
‘‘clean’’ syngas is comprised of
essentially CO and H2. The syngas is
then converted into a liquid fuel by a
catalytic process. The fuel producer has
26 Lin Wei, Graduate Research Assistant, Lester O.
Pordesimo, Assistant Professor Willam D.
Batchelor, Professor, Department of Agricultural
and Biological Engineering, Mississippi State
University, MS 39762, USA, Ethanol Production
from Wood: Comparison of Hydrolysis
Fermentation and Gasification Biosynthesis, Paper
Number: 076036, Written for presentation at the
2007 ASABE Annual International Meeting.
Minneapolis Convention Center, Minneapolis, MN,
17-20 June 2007.
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the choice of producing diesel fuel or
alcohols from syngas by optimizing the
type of catalyst used and the H2/CO
ratio. Diesel fuel has historically been
the primary focus of such processes by
using a Fischer Tropsch reactor, as it
produces a high quality distillate
product. However, with a $1.01 per
gallon cellulosic biofuel tax deduction
which favors the less energy dense
ethanol, it may be economically
advantageous for fuel producers to
convert syngas to ethanol instead of to
diesel fuel.
A carefully integrated conventional
steam cycle produces process heat and
electricity (excess electricity is
exported). Pre-heaters, steam generators,
and super-heaters generate steam that
drives turbines on compressors and
electrical generators. The heat balance
around a thermochemical unit or
thermochemical combined unit must be
carefully designed and tuned in order to
avoid unnecessary heat losses.27 These
facilities greatly increase the thermal
efficiency of these plants, but they add
to the very high capital costs of these
technologies.
a. Ethanol Based on a Thermochemical
Platform
Conceptual designs and technoeconomic models have been developed
for ethanol production via mixed
alcohol synthesis using catalytic
processes. The proposed mixed alcohol
process produces a mixture of ethanol
along with higher normal alcohols (e.g.,
n-propanol, n-butanol, and n-pentanol).
The by-product higher normal alcohols
have value as commodity chemicals and
fuel additives.
The liquid rundown from the lowpressure separator is dehydrated in
vapor-phase molecular sieves,
producing the dehydrated mixed
alcohol feed into a methanol/ethanol
overhead stream and a mixed, higher
molecular weight alcohol bottom
stream. The overhead stream is further
separated into a methanol stream and an
ethanol stream.
Two companies which are pursuing
ethanol based on a thermochemical
route are Range Fuels and Enerkem.
Range has operated a pilot plant for over
7 years using over 20 different nonfood
feedstocks. Range broke ground building
its first commercial plant late in late
2008 and is expected to be operational
in 2010. This plant will be located in
27 S. Phillips, A. Aden, J. Jechura, and D. Dayton,
National Renewable Energy Laboratory, Golden,
Colorado 80401–3393, T. Eggeman, Neoterics
International, Inc., Thermochemical Ethanol via
Indirect Gasification and Mixed Alcohol Synthesis
of Lignocellulosic Biomass, Technical Report,
NREL/TP–510–41168, April 2007.
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Soperton, Georgia and is partially
funded from proceeds of a DOE grant.
The plant will use wood, grasses, and
corn stover as feedstocks. In its initial
phase, the Range plant is expected to
produce 4 million gallons per year of
methanol. After the company is
confident in its operations, Range will
begin efforts to expand the plant and
add additional reaction capacity to
convert the methanol to ethanol.
Enerkem is pursuing cellulosic
ethanol production via the
thermochemical route. The Canadianbased company was recently announced
as a recipient of a $50 million grant
from DOE to build a 10 MGY woody
biomass-to-ethanol plant in Pontotoc,
MS. The U.S. plant is not scheduled to
come online until 2012, but Enerkem is
currently building a 1.3 MGY
demonstration plant in Westbury,
Quebec. According to the company,
plant construction in Westbury started
in October 2007 and the facility is
currently scheduled to come online
around the middle of 2010. While it’s
unclear at this time whether the
cellulosic ethanol produced will be
exported to the United States, Enerkem
has expressed interest in selling its fuel
commercially. If Enerkem does export
some of its cellulosic biofuel to the U.S.,
it could help to enable refiners meet the
2011 cellulosic biofuel standard.
b. Diesel and Naphtha Production Based
on a Thermochemical Platform
The cleaned and water-shifted syngas
is sent to the Fischer Tropsch (FT)
reactor where the carbon monoxide and
hydrogen are reacted over a FT catalyst.
Current FT catalysts include iron-based
catalysts, and cobalt-based catalysts.
The FT reactor creates a syncrude,
which is a variety of hydrocarbons that
boil over a wide distillation range (a mix
of heavy and light hydrocarbons) which
are separated into various components
based on their vapor pressure, mainly
liquid petroleum gas (LPG), naphtha,
distillate and wax fractions. The heavier
compounds are hydrocracked to
maximize the production of diesel fuel.
Conversely, the naphtha material is very
low in octane thus, it would either have
to be upgraded, or blended down with
high octane blendstocks (i.e., ethanol),
or be upgraded to a higher octane
blendstock to have much value for use
in gasoline.
Choren is an European company
which is pursuing a thermochemical
technology for producing diesel fuel and
naphtha. The principal aspect of
Choren’s process is their patented three
stage gasification reactor. The threestage gasification reactor includes low
temperature gasification, high
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temperature gasification and
endothermic entrained bed gasification.
Choren designed its gasification reactor
with three stages to more fully convert
the feedstock to syngas. Choren will be
building a commercial Plant in Freiberg/
Saxony Germany that is expected to be
operational in 2011 or 2012. Initially,
the plant will use biomass from nearby
forests, the wood-processing industry
and straw from farmland. Although any
fuel produced in 2011 by its Freiberg/
Saxony plant and marketed
commercially would most likely be used
in Europe, it is possible that some of
that fuel could be exported to the U.S.
Choren is also planning to build a
commercial thermochemical/biomassto-liquids (BTL) plant in the U.S. after
their Freiberg/Saxony plant is
operational in Germany.
Baard Energy is a U.S. company
which plans on utilizing a
thermochemical technology for
producing diesel fuel and naphtha.
Baard, however, plans on primarily
combusting coal and cofiring biomass
with the coal. Cofiring the biomass with
the coal will make their first plant more
like the coal-to-liquids plants which are
operating today, which may help to
convince investors that this technology
is already tested. Baard’s coal and
biomass-to-liquids plant is not expected
to be operational until at least 2012.
Probably the largest
commercialization hurdle for the
companies pursing the thermochemical
route is the very high capital costs
associated with these technologies.
Because of the economic hardships
associated with recent global recession,
banks are less willing to make loans to
fund new technologies which are likely
to be considered riskier investments.
The capital costs are very high because
there are two significant reactors
required for each plant—the gasification
reactor and the syngas to fuel reactor.
Additionally, the syngas must be
cleaned to protect the catalysts used in
the downstream syngas to fuel reactor
which requires additional capital costs.
Because the syngas would be cleaned
anyways, this technology is a very good
candidate for processing MSW which
may contain toxic compounds. When
considering the cost savings for not
having to pay the tipping fees at
municipal dumping grounds, MSW
feedstocks may avoid almost all the
purchase costs for MSW feedstocks
which would significantly help offset
the high capital costs.
3. Hybrid Thermochemical/Biochemical
Processes
Hybrid technologies include process
elements involving both the gasification
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stage of a typical thermochemical
process, as well as the fermentation
stage of a typical biochemical process
and therefore cannot be placed easily
into either category. For more specific
information regarding either
biochemical processes or
thermochemical, please see Sections
IV.C.1 and IV.C.2 respectively.
Currently, there are several strategies for
the production of ethanol through
hybrid processes; these strategies are
differentiated by the order in which the
thermochemical and biochemical steps
take place within the process, as well as
how the intermediate products from
each step are used.
While we do not expect significant
commercial production from hybrid
processes in 2011, there are several
companies pursing this approach for the
future. Examples of the first process
strategy, described in the paragraph
below, include both INEOS Bio and
Coskata. INEOS Bio (along with partner
New Planet Energy) has recently been
selected for a $50MM DOE grant for the
construction of an 8 MGPY plant in
River County, Florida; predicted to
finish construction in late 2011. Coskata
is currently running a 40,000 gallon per
year pilot plant that became operational
in 2009 in Madison, Pennsylvania.
Coskata is targeting to design and build
a 50 MGPY commercial plant that it
expects to be operational in 2012. A
company currently pursing the second
process strategy, described in the
following third paragraph, is Zeachem
Inc. Zeachem is currently constructing a
250 KGPY demonstration plant in
Boardman, Oregon. They have received
a $25MM DOE grant and expect to have
a full commercial production facility
operational in 2013.
One strategy involves the gasification
of all feedstock material to syngas before
being processed into ethanol using a
biochemical fermenter. Further
information regarding gasification can
also be found in Section IV.C.2. After
gasification, the syngas stream is cooled
and bubbled into a fermenter containing
modified microorganisms, usually
bacteria or yeast. This fermenter
replaces the typical catalysts found after
gasification in a traditional
thermochemical process. Further
information regarding fermentation can
be found in Section IV.C.1. Unlike
traditional fermentation (which break
down C5 and C6 sugars), these
microorganisms are engineered to
convert the carbon monoxide and
hydrogen contained in the syngas
stream directly into ethanol. After
fermentation, the effluent water/ethanol
stream from the fermenter is separated
similarly to a biochemical process;
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usually using a combination of
distillation and molecular sieves. The
separated water can then be recycled
back into the fermentation stage of the
process. Typical yields of ethanol are
predicted in the 100–120 gallon per ton
range.
Since gasification converts all
carbonaceous feedstock material to a
uniform syngas before fermentation,
there is a higher flexibility of feedstock
choices than if these materials were to
be fermented directly; including
agricultural residues, switchgrass, farmgrown trees, sorted MSW, or any
combination of such. In addition,
processing incoming feedstock with
gasification does not require the
addition of enzymes or acid hydrolysis
necessary in a biochemical process to
aid in the breakdown of cellulosic
materials. Fermenting syngas also
captures all available carbon contained
in the feedstock, including lignin that
would not be processed in a typical
biochemical fermentation. However,
more energy is lost as waste heat as well
as secondary carbon dioxide production
in the gasification process than would
be lost for biochemical feedstock
preparation. Using a fermenter in a
hybrid process replaces the catalyst
needed in a typical thermochemical
process. These microorganisms allow
for a higher variation of the incoming
syngas stream properties, avoid the
necessity of a water-shift reaction
preceding traditional catalytic
conversion, and are able to operate at
lower temperatures and pressures than
those required for a catalytic conversion
to ethanol. Microorganisms, unlike a
catalyst, are also self-sustaining and do
not require periodic replacement. They
are, however, susceptible to bacterial
and viral infections which requires
periodic cleaning of the fermentation
reactors.
Another hybrid production strategy
involves gasification of the typically
unfermentable feedstock fraction
(lignin) concurrently with a typical
fermentation step for the cellulose and
hemicellulose fraction. These steps are
subsequently combined in a
hydrogenation reaction of the produced
syngas with the product of the
fermented stream. Feedstock first
undergoes acid hydrolysis to break
down contained cellulose and
hemicellulose. Before fermentation, the
unfermentable portion of feedstock
(lignin, ash and other residue) is
fractioned and sent to a gasifier.
Concurrently, the remaining fraction of
hydrolyzed feedstock is fermented using
an acetogen microorganism. These
acetogens occur naturally, and therefore
do not have to be modified for this
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however, a significant amount of
gasoline would likely be produced as
well. There are two main reaction
pathways currently being explored: A
two step pyrolysis pathway, and a one
step pyrolysis pathway.
The simplest technology used for the
two-step pyrolysis approach is called
fast pyrolysis. The fast pyrolysis
technology uses sand in a fluidized bed
to transform bio-fuels into a product
named bio-oil. This is purely a thermal
process, where the sand’s (or other
solid) role is to transport heat to the
biomass. Fast pyrolysis technology has
two problems to be solved. First, fast
pyrolysis oil is unstable, acidic, viscous
and may separate itself into two phases
so it must be immediately upgraded or
it will begin to degrade and
repolymerize. The second issue is that
pyrolysis bio-oil must be upgraded
before it can be used as a transportation
fuel.
Another approach to Fast Pyrolysis
4. Pyrolysis and Depolymerization
being pursued by several companies
would be to substitute a catalyst in
Pyrolysis and depolymerization is a
group of technologies which are capable place of sand and the catalyst would be
able to stabilize the resulting bio-oil in
of creating biofuels from cellulose by
addition to helping depolymerize the
either thermally or catalytically
biomass to liquids. Although the
breaking them down into molecules
resulting bio-oil is stable, it still has to
which fall within the boiling range of
be upgraded into a transportation fuel,
transportation fuels. Pyrolysis
since it would still have a high level of
technologies are usually thought of
oxygenated compounds.
being primarily a thermal technology,
The National Renewable Energy
however, newer pyrolysis technologies
Laboratory (NREL) is working on a ‘‘hot
are being developed which are
filtration’’ technology that apparently is
attempting to integrate some catalysts
able to stabilize bio-oil created using the
into the technology. These are all
fast pyrolysis process for a very long
unique processes, typically with single
period of time (years). This would allow
companies developing the technologies,
the bio-oil to be stored and transported
so they are discussed separately.
to an upgrading facility without
significant degradation.
a. Pyrolysis Diesel Fuel and Gasoline
It is possible to use a sophisticated
Pyrolysis oils, or bio-oils, are
catalyst (instead of sand) in a single step
produced by decomposing cellulosic
pyrolysis reaction to create pyrolysis
biomass at lower temperatures than the
oils that exhibit much improved bio-oil
gasification process, thus producing a
properties. The catalysts would not only
liquid bio oil instead of a synthesis
be able to help depolymerize cellulosic
gas.28 The reaction can occur either with
feedstocks, but they produce a bio-oil
or without the use of catalysts, but it
which could possibly be used directly
occurs without any additional oxygen
as transportation fuel. Thus, a second
being present. The resulting oil which is
upgrading step may not be necessary.
produced must have particulates and
The difficulty encountered by this
ash removed in filtration to create a
technology is that catalysts which have
homogenous ‘‘dirty’’ crude oil type of
been used in the one step process are
product. This dirty crude oil must be
relatively expensive and they degrade
further upgraded to hydrocarbon fuels
quickly due to the metals which are
via hydrotreating and hydrocracking
present in the biomass. Development
processing, which reduces its total
work on the two-step and one-step
oxygen content and cracks the heaviest
pyrolysis processes is ongoing.
of the hydrocarbon compounds. One of
Dynamotive Energy Systems
the finished fuels produced by the
Corporation is a Canadian company
pyrolysis process is diesel fuel,
which has developed a pyrolysis
technology that uses medium
28 DOE EERE Biomass Program. ‘‘Thermochemical
temperatures and oxygen free reactions
Conversion Processes: Pyrolysis’’ https://
to convert dry waste biomass and energy
www1.eere.energy.gov/biomass/
thermochemical_processes.html, November 6, 2008. crops into different products. The liquid
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process. These acetogen convert both C6
and C5 portions of the hydrolized
feedstock to acetic acid. This reaction
creates no carbon dioxide, unlike
traditional fermentation using yeast,
preserving the maximum amount of
carbon for the finished fuel. The acetic
acid stream then undergoes
esterification to create ethyl acetate.
Meanwhile, the syngas stream from the
gasification of lignin and other residue
is separated into its carbon monoxide
and hydrogen components. The carbon
monoxide stream can be further
combusted to provide process heat or
energy. The hydrogen stream is
combined with the ethyl acetate in a
hydrolysis reaction to form ethanol.
Acetic acid and ethyl acetate also form
the precursors to many other chemical
compounds and therefore may also be
sold in addition to ethanol. Typical
yields for this technology are predicted
in the 130–150 gallon per ton range.
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product produced by the Dynamotive
process is called BioOil. The BioOil
contains up to 25% water, though the
water is intimately mixed and does not
easily separate into another phase with
time. Since the BioOil contains
significant amounts of water, it is not
directly useable as fuel in conventional
vehicles and would have to be
converted via another catalytic
conversion processing step. The
additional catalytic step envisioned by
Dynamotive to upgrade the BioOil into
a transportation fuel would combust the
material into a synthesis gas which
would then be converted into diesel fuel
or bio-methanol via a catalytic reaction
(the BTL process). The diesel fuel
produced is expected to be compatible
with existing petroleum diesel fuels.
The poor quality BioOil, though, could
be used in the No. 2 industrial heating
oil market at industrial facilities.
However, because of its high acidity
level, users would need to change
equipment metallurgy to stainless steel
for pipes, pumps, tanks, nozzles etc.
Dynamotive has two small
demonstration plants. One
demonstration plant is located in
Guelph, Ontario, Canada and its
capacity is 66,000 dry tons of biomass
a year with an energy output equivalent
to 130,000 barrels of oil. The other of its
demonstration plants is located in West
Lorne Ontario, Canada. Dynamotive
continues to work on a technology for
converting its BioOil to transportation
fuels, although they have not
announced plans for building such a
facility due to funding limits. While
Dynamotive is expected to continue to
sell its fuel into the chemicals market,
it could find a fuel oil user in the U.S.
to use its fuel under the RFS2 program
that refiners could use to comply with
the 2011 cellulosic biofuel standard.
Envergent is a company formed
through a joint venture between
Honeywell’s UOP and the Ensyn
Corporation. Although Ensyn has been
using fast pyrolysis for more than a
decade to produce specialty chemicals,
UOP is relying on its decades of
experience developing refining
technologies to convert the pyrolysis
oils into transportation fuels. Envergent
is also working with Federal
laboratories to further their technology.
Based on their current technology and
depending on the feedstock processed,
about 70% of the feedstock is converted
into liquid products. The gasoline range
products produced are high in octane,
while the diesel fuel products are low
in cetane. Envergen estimates that if it
was able to procure cellulosic
feedstocks at 70 per ton, that their
technology would be competitive with
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#2 fuel oil produced from crude oil
priced at about $40 per barrel.
Envergent is licensing this technology as
well as working with a U.S. oil company
to test out this technology in a
commercial setting here in the U.S.
Petrobras is a Brazilian oil company
also working to develop a pyrolysis
technology. Because of Petrobas’ work
in this area (and other areas on
biofuels), a Memorandum of
Understanding was signed by United
States’ Secretary of State and Brazil’s
External Relations Minister on March 9,
2007 to advance the cooperation on
biofuels. A second Memorandum of
Understanding was signed by
PETROBRAS and NREL on September
2008 aiming at collaborating to
maximize the benefit of their respective
institutional interests in second
generation biofuels. Petrobras is
negotiating a Cooperation Agreement
with NREL to develop a two step
pyrolysis route to produce biofuels from
agricultural wastes such as sugar cane
bagasse, wood chips or corn stover.
Petrobras is optimistic that a catalytic
pyrolysis technology can be developed
that will produce a stable bio-oil
(pyrolysis oil). Petrobras is hopeful that
a one-step pyrolysis technology can be
developed to convert biomass directly to
transportation fuels, although in the end
Petrobras believes that the two step
process may be more economically
attractive.
b. Catalytic Depolymerization
Two companies that are pursuing
catalytic depolymerization are Green
Power Inc. and Cello Energy.
The Green Power process catalytically
depolymerizes cellulosic feedstocks at
moderate temperatures into liquid
hydrocarbon fuels. The proposed
feedstock is municipal solid waste
(MSW) or other waste material such as
animal waste, plastics, agriculture
residue, woody biomass and sewage
waste. The feedstock is first ground to
a size finer than 5 mm. The feedstock
is placed along with a catalyst, some
lime, which serves as a neutralizing
agent, and some fuel which provides a
liquid medium, into a reactor and
heated to around 350 degrees Celsius.
As described, this technology may fit
the description for catalyzed pyrolysis
reactions described above, but because
we are not certain of the reaction
kinetics, we have categorized this as a
separate catalytic depolymerization
technology. In the reactor, the feedstock
is catalytically converted to liquid fuels
which primarily fall within the gasoline
and diesel fuel boiling ranges, although
these fuels may need further upgrading.
The liquid fuels are separated from
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some solids which are present and are
distilled into typical fuel streams
including naphtha, diesel fuel, kerosene
and fuel oil. According to the literature
writing about this technology, the
process reportedly produces 120 gallons
per ton of feedstock inputted into the
process. A light hydrocarbon gas, which
is mostly methane, is also produced, but
this gas is expected to be burned in a
turbine to generate electricity and the
waste heat is used for heating the
process. Apparently, some carbon
dioxide is also formed and is released
from the process.
Greenpower completed construction
on a demonstration plant located in
Fife, Washington about March of 2008.
Greenpower is working on obtaining
additional funding and to obtain an air
permit through the State of Washington
Environmental Office. While we don’t
believe that Greenpower will have its
plant operational in 2011 due to
financial and other issues the company
faces, those issues could be resolved to
allow this company to produce fuel that
could help refiners comply with the
cellulosic biofuel volume standard for
2011.
The Cello-Energy process is also a
catalytic depolymerization technology.
At moderate pressure and temperature,
the Cello-Energy process catalytically
removes the oxygen and minerals from
the hydrocarbons that comprise finely
ground cellulose. This results in a
mixture of short chain (3, 6 and 9
carbon) hydrocarbon compounds. These
short chain hydrocarbon compounds are
polymerized to form compounds that
boil in the diesel boiling range, though
the process can also be adjusted to
produce gasoline or jet fuel. The
resulting diesel fuel meets the ASTM
standards, is in the range of 50 cetane
to 55 cetane and typically contains 3
ppm of sulfur.
The Cello process is reported to be on
the order of 82% efficient at converting
the feedstock energy content into the
energy content of the product, which is
very high compared to most of today’s
biochemical and thermochemical
processes which are on the order of 50%
efficient, or less. Because of the
simplicity of the process, the capital
costs are very low. A 50 million gallon
per year plant is claimed to only incur
a total cost of $45 million. Because of
its high efficiency in converting
feedstocks into liquid fuel, the
production and operating costs are
estimated to be very low.
In December 2008, Cello completed
construction on a 20 million gallon per
year commercial demonstration plant.
However, at the present they are still
working to resolve process issues that
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have arisen upon scaleup from their
pilot plant. We expect that Cello will be
able to produce some volume of
cellulosic biofuel in 2011.
5. Catalytic Reforming of Sugars to
Gasoline
Virent Biorefining is pursuing a
process called ‘‘Bioforming’’ which
functions similarly as the gasoline
reforming process used in the refining
industry. Hence, this is a very different
technology to any of those other
cellulosic biofuel technologies
discussed above. While refinery-based
catalytic reforming technologies raise
natural gasoline’s octane value and
produces aromatic compounds,
Bioforming reforms biomass-derived
sugars into hydrocarbons for blending
into gasoline and diesel fuel. The
process operates at moderate
temperatures and pressures. In March of
2010, Virent announced that they had
begun operating a larger pilot plant
capable of about 30 gallons per day.
Commercialization of the Virent process
will happen sometime after 2011.
For this technology to become a
cellulosic biofuel technology, it will be
necessary to link this reforming
technology with a technology which
breaks cellulose down into starch or
sugars. In parallel with its Bioreforming
work, Virent is working on a technology
to break down cellulose into sugars
upstream of its technology which
reforms sugars to gasoline.
V. Proposed Changes to RFS2
Regulations
Following publication of the final
RFS2 program regulations ,29 EPA
identified two program areas that could
benefit from the addition of new
regulatory provisions. The first would
provide for the generation of RINs for
fuel produced between July 1, 2010 and
December 31, 2010 representing certain
fuel pathways that are not currently in
Table 1 to § 80.1426, but which could
possibly be added later this year if they
are determined to meet the applicable
GHG thresholds. Under this proposal
RINs could be generated only if the
pathways are indeed approved, and
only for quantities reflecting fuel
produced between the effective date of
the RFS2 regulations and the effective
date of a new pathway added to Table
1 to § 80.1426. The second program
addition would establish procedures for
petitions requesting EPA authorization
of an aggregate compliance approach to
renewable biomass verification for
feedstocks grown in foreign countries,
akin to that applicable to crops and crop
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residue grown within the U.S. We are
proposing to make amendments to the
RFS regulations in Subpart M to
implement both of these provisions.
A. Delayed RIN Generation for New
Pathways
As described in the RFS2 final rule,
we did not have sufficient time to
complete the necessary lifecycle GHG
impact assessment for certain fuel
pathways. We indicated that we would
model and evaluate several additional
pathways after the final rule (see
Section V.C of the RFS2 final rule, 75
FR 14796). EPA anticipates modeling
and publishing the lifecycle GHG
analyses for the following four pathways
later this year:
• Grain sorghum ethanol.
• Pulpwood biofuel.
• Palm oil biodiesel.
• Canola oil biodiesel.
Depending on how these lifecycle GHG
results compare with the required GHG
thresholds for cellulosic biofuel,
biomass-based diesel, advanced biofuel,
and conventional renewable fuel, we
may add one or more of these pathways
to Table 1 to § 80.1426. Once a new
pathway is approved, producers using
that pathway could generate RINs with
the specified D code.
We consider the four new fuel
pathways currently being analyzed to be
an extension of the RFS2 final rule. Had
we been able to complete these analyses
for the RFS2 final rule and verified that
the GHG thresholds had been met, D
codes to represent these pathways
would have been included in Table 1 to
§ 80.1426 promulgated on March 26,
2010, and renewable fuel producers
could have begun using those pathways
to generate RINs beginning on July 1,
2010. Indeed, we are aware of a number
of producers who intend to produce
biofuel using one of the four pathways
listed above despite the fact that a
determination regarding their lifecycle
GHG impact has not yet been made.
Based on the fact that we may have
included the four pathways listed above
in the RFS2 final rule if the lifecycle
modeling had been completed in time,
we believe that it would be appropriate
to allow renewable fuel producers using
any of these four pathways that are
ultimately approved for inclusion in
Table 1 to § 80.1426 to generate RINs for
all fuel they produce and sell on and
after July 1, 2010. However, while EPA
is expeditiously working to complete its
GHG assessments for these four fuel
pathways in 2010, the determination of
whether any of the four pathways will
meet the 20%, 50%, or 60% GHG
thresholds may not occur until after July
1, 2010. Therefore, RINs representing
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fuel produced between July 1, 2010 and
any EPA approval of a new fuel
pathway could only be generated after
the renewable fuel in question had been
produced and sold, after the time when
EPA announces the results of the
lifecycle analyses and specifies the
applicable D code in Table 1 to
§ 80.1426. Thus we are proposing a new
regulatory provision for the generation
of ‘‘Delayed RINs’’ that would allow
RINs with newly specified D codes to be
generated for eligible fuel produced
between July 1, 2010 and the date any
new D code is approved for one of the
four fuel pathways listed above. This
Delayed RINs provision would only be
applicable for any of the four pathways
described above that are determined to
meet the applicable GHG thresholds. We
are also proposing that this provision
would apply only for renewable fuel
produced in 2010, since the lifecycle
GHG assessments for the four pathways
listed above is expected to be completed
in 2010. Our proposed regulatory
provision for Delayed RIN generation
would be inserted into § 80.1426 as new
paragraph (g). As for any RIN
generation, producers using this new
regulatory provision would need to be
registered under RFS2 before they could
generate Delayed RINs, and would need
to comply with the recordkeeping and
reporting requirements of the
regulations.
We do not believe that this proposed
provision for Delayed RINs should be
extended to any other pathways. The
four pathways listed above are the only
pathways currently under evaluation
that would have been included in the
RFS2 final rule if we had completed the
modeling in time. Moreover, we have
provided a petition process in § 80.1416
for other fuel pathways for which
lifecycle GHG assessments have not yet
been made.
In developing this proposed provision
for Delayed RIN Generation, we have
accounted for renewable fuel producers
who are eligible for an exemption from
the 20% GHG reduction requirement for
their fuel under § 80.1403
(‘‘grandfathered’’ producers) and those
that are not. Grandfathered producers
can generate RINs for their renewable
fuel starting on July 1, 2010, but must
designate the D code as 6 for such fuel,
identifying it as conventional renewable
fuel. They must also transfer those RINs
with renewable fuel they sell. If one of
the four fuel pathways described above
is approved between July 1, 2010 and
December 31, 2010 for use of a D code
other than 6, and the producer wishes
to apply this new D code to fuel they
have already produced and transferred,
the RINs they already generated and
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transferred with renewable fuel they
produced must be accounted for. We are
proposing a process whereby these
grandfathered producers would be
required to acquire and retire RINs from
the open market with a D code of 6 prior
to the generation of Delayed RINs. The
number of RINs retired in this fashion
must be no greater than the number they
generated between July 1, 2010 and the
effective date of the new applicable
pathway. Producers who are not
grandfathered under § 80.1403 cannot
generate RINs starting on July 1, 2010,
and so would not be required to acquire
and retire any RINs prior to the
generation of Delayed RINs.
The generation of Delayed RINs
would also differ for grandfathered
producers and non-grandfathered
producers. Grandfathered producers
would base the number of Delayed RINs
they generate on the number of RINs
with a D code of 6 that they retired as
described above. In contrast, nongrandfathered producers would base the
number of Delayed RINs they generate
on the volume of renewable fuel they
produced and sold between July 1, 2010
and the effective date of the new
pathway. Since all Delayed RINs will be
generated after the renewable fuel in
question had been produced and sold,
they would be assigned a K code of 2
and thus could be sold by the producer
separately from renewable fuel.
Finally, we believe that there should
be a deadline for the generation of
Delayed RINs to ensure that they are
entering the market as close as possible
to the date of production of the
renewable fuel that they represent. We
are proposing that all Delayed RINs
must be generated within 30 days of the
effective date of a new pathway added
to Table 1 to § 80.1426 between July 1,
2010 and December 31, 2010. We
believe that 30 days would provide
sufficient time for producers who are
grandfathered to first acquire and retire
RINs from the open market, and would
be sufficient to allow any producer to
generate Delayed RINs according to the
procedures in the regulations. However,
we request comment on a longer period
within which Delayed RINs must be
generated.
We request comment on our proposed
provision for Delayed RINs.
B. Criteria and Process for Adoption of
Aggregate Approach to Renewable
Biomass for Foreign Countries
In the preamble to the final RFS2
regulations, EPA indicated that, while
we did not have sufficient data at the
time to make a finding that the aggregate
compliance approach adopted for
domestically-grown crops and crop
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residues would be appropriate for
foreign-grown feedstocks, we would
consider applying the aggregate
compliance approach for renewable
biomass on a country by country basis
if adequate land use data becomes
available.
Since promulgation of the final RFS2
regulations, we have received several
inquiries regarding the process, criteria,
and data needed for EPA to approve the
aggregate compliance approach for
planted crops and crop residue grown in
areas outside the U.S. Thus, in today’s
rule, EPA is proposing a process by
which entities may petition EPA for
approval of the aggregate compliance
approach for specified renewable fuel
feedstocks either in a foreign country as
a whole or in a specified geographical
area within a country. The proposed
regulations include a general criterion
and a number of considerations that
EPA will use in evaluating petitions.
They also include a list of submissions
that are required, absent an explanation
by petitioner of why they should not be
required for EPA to approve a petition.
The proposed rule also includes a
description of the proposed process by
which EPA would make decisions
concerning any petitions received.
1. Criterion and Considerations
In developing these proposed
regulations, EPA relied substantially on
the approach we used to determine that
an aggregate compliance approach was
appropriate for planted crops and crop
residue from U.S. agricultural land. The
fundamental finding that would be
required of EPA in approving a petition
for application of the aggregate
approach would be that an aggregate
compliance approach will provide
reasonable assurance that specified
renewable fuel feedstocks from a given
geographical area meet the definition of
renewable biomass and will continue to
meet the definition of renewable
biomass, based on the submission of
credible, reliable and verifiable data.
Based on our experience in making the
comparable finding for U.S.-grown
crops and crop residues, we are also
proposing a number of more specific
factors that would be considered in
determining whether this finding
should be made, as described below.
EPA is proposing to consider:
• Whether there has been a
reasonable identification of the
aggregate amount of agricultural land in
the specified geographical area on
December 19, 2007 that was available
for the production of the specified
feedstock(s) and that satisfy the
definition of renewable biomass, taking
into account the definitions of terms
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such as ‘‘cropland,’’ ‘‘pastureland,’’
‘‘planted crop,’’ and ‘‘crop residue’’
included in the final RFS2 regulations.
• Whether information from years
preceding and following 2007 shows
that the identified aggregate amount of
land in the specific geographical area,
called the 2007 baseline area of land, is
not likely to be exceeded in the future.
• Whether economic considerations,
legal constraints, historical land use and
agricultural practices and other factors
show that it is likely that producers of
the feedstock(s) will continue to use
agricultural land within the baseline
area of land identified into the future, as
opposed to clearing and cultivating land
not eligible under the 2007 baseline.
• Whether there is a reliable method
to evaluate on a continuing basis
whether the 2007 baseline area of land
is being or has been exceeded.
• Whether an entity has been
identified to conduct data gathering and
analysis needed for an annual EPA
evaluation of the aggregate compliance
approach if EPA grants the petition.
EPA is requesting comments on the
proposed general criterion and specific
considerations for approving the
aggregate compliance approach for nondomestically grown feedstocks. The
existing approved aggregate approach
for U.S. domestic feedstocks applies to
all crops and crop residue that could be
used in renewable fuel production. EPA
has received inquiries on the extent to
which approval could be obtained for a
single, or limited number, of feedstocks.
The proposed regulations leave open the
possibility of feedstock-specific
petitions, but EPA particularly solicits
comment on the extent to which
different or additional data submittals or
inquiries would be appropriate for such
petitions.
2. Data Sources
To make the aggregate compliance
determination for U.S. agricultural
lands, EPA obtained USDA data from
three independently gathered national
land use data sources (the Farm Service
Agency (FSA) Crop History Data, the
USDA Census of Agriculture (2007), and
the satellite-based USDA Crop Data
Layer (CDL)). Please see Section
II.C.4.c.iii. of the preamble to the final
RFS2 rule (75 FR 14701 (March 26,
2010)) for a more detailed description of
the data sources used. Using these data
sources, EPA was able assess the area of
land (acreage) available in the United
States under EISA for production of
crops and crop residues that meet the
definition of renewable biomass. In the
case of a petition to apply the aggregate
compliance approach to feedstocks from
a specific geographical area in a foreign
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country, when considering the
information and data submitted by the
petitioner, EPA will evaluate such
information on a case-by-case basis, but
suggests that petitioners obtain data
from sources that are at least as credible,
reliable, and verifiable as the USDA data
used to make the determination for U.S.
agricultural land.
When evaluating whether the data
relied on are credible, reliable, and
verifiable, EPA will take into account
whether the data is submitted by,
generated by, or approved by the
national government of the foreign
country in question, as well as how
comprehensive and accurate the data
source is. It is important for the national
government of the area seeking
consideration be involved in this
process, and we seek comment on
whether or not involvement of the
national government should be required
as part of the petitioning and/or data
submittal processes. Additionally, EPA
will take into consideration whether the
data is publically available, whether the
data collection and analysis
methodologies and information on the
primary data source are available to
EPA, and whether the data has been
generated, analyzed, and/or approved or
endorsed by an independent third party.
EPA would also take into account the
quality of the data that is available on
an annual basis for EPA’s annual
assessments of any approved aggregate
compliance approach, as well as
whether the petitioner has identified an
entity who will provide to EPA an
analysis of the data updates each year
following EPA’s approval of the
aggregate compliance approach for that
area. Furthermore, EPA will consider
agricultural land use trends from several
years preceding 2007, as well as the
years following 2007 to the time the
petition is submitted in order to
evaluate whether or not it is likely that
a 2007 baseline would be exceeded in
the future. EPA will consider whether
there are laws in place in the area for
which the petition was submitted that
might prohibit or incentivize the
clearing of new agricultural lands and
the efficacy of these laws. EPA will also
assess whether any market factors are
expected to drive an increase in the
demand for agricultural land.
3. Petition Submission
EPA is proposing that all submittals,
including the petition, supporting
documentation, and annual data and
analyses, be submitted in English. We
are also proposing that petitioners
submit specified information as part of
their formal petition submission
package, or explain why such
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information is not necessary for EPA to
approve their petition. Petitioners
would need to submit an assessment of
the total amount of land that is cropland
or pastureland that was cleared or
cultivated prior to December 19, 2007
and that was actively managed or fallow
and nonforested on that date. For
example, in assessing the amount of
total existing agricultural land in the
U.S. on the enactment date of EISA,
EPA used FSA Crop History data to
show that there were 402 million acres
of agricultural land existing in the U.S.
in 2007. Additionally, if the petitioner
is seeking approval of the aggregate
compliance approach for a particular
feedstock, they would also need to
submit an assessment of the total
amount of agricultural land dedicated to
that feedstock in 2007 within the
specified area. Petitioners would also be
required to provide EPA with maps or
electronic data identifying the
boundaries of the land in question and
a description of the feedstock(s) for
which the petitioner is submitting the
petition.
As part of the petition, the petitioner
would be required to submit to EPA
land use data that demonstrates that the
land in question is agricultural land that
was cleared or cultivated prior to
December 19, 2007 and that was
actively managed or fallow and
nonforested on that date, which may
include satellite imagery data, aerial
photography, census data, agricultural
surveys, and/or agricultural economic
modeling data. As mentioned above, the
FSA crop history data used for the U.S.
aggregate compliance approach
determination consists of annual
records of farm-level land use data that
includes all cropland and pastureland
in the U.S. EPA also considered USDA
Census of Agriculture data, which
consists of a full census of the U.S.
agricultural sector once every five years,
as well as the USDA Nation Agricultural
Statistics Service (NASS) Crop Data
Layer (CDL), which is based on satellite
data.
In establishing the total amount of
existing agricultural land for the U.S.
aggregate compliance approach
determination, EPA relied on the RFS2
definitions of the relevant terms,
including planted crops, crop residue,
and agricultural land, which is defined
as consisting of cropland, pastureland
and CRP land. EPA will take into
consideration whether the data
submitted by the petitioner relies on
comparable definitions. For purposes of
RFS2, planted crops are defined as all
annual or perennial agricultural crops
from existing agricultural land that may
be used as feedstocks for renewable fuel,
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such as grains, oilseeds, sugarcane,
switchgrass, prairie grass, duckweed,
and other species (but not including
algae species or planted trees),
providing they were intentionally
applied by humans to the ground, a
growth medium, a pond or tank, either
by direct application as seed or plant, or
through intentional natural seeding or
vegetative propagation by mature plants
introduced or left undisturbed for that
purpose. Crop residue is defined as the
biomass left over from the harvesting or
processing of planted crops from
existing agricultural land and any
biomass removed from existing
agricultural land that facilitates crop
management (including biomass
removed from such lands in relation to
invasive species control or fire
management), whether or not the
biomass includes any portion of a crop
or crop plant. Cropland is defined as
land used for production of crops for
harvest and includes cultivated
cropland, such as for row crops or closegrown crops, and non-cultivated
cropland, such as for horticultural or
aquatic crops. Pastureland is land
managed for the production of
indigenous or introduced forage plants
for livestock grazing or hay production,
and to prevent succession to other plant
types. It is important to note that EPA
considers pastureland to be distinctly
different from rangeland, which may be
used for livestock grazing, but is not
managed to prevent succession to other
plant types. Finally, CRP land is land
enrolled in the US Conservation Reserve
Program (administered by USDA’s Farm
Service Agency), which encourages
farmers to convert highly erodible
cropland or other environmentally
sensitive acreage to vegetative cover,
such as tame or native grasses, wildlife
plantings, trees, filterstrips, or riparian
buffers. EPA recognizes that the CRP is
only applicable to U.S. agricultural
land. EPA solicits comments on whether
the final rules should allow EPA to
consider land that is equivalent or
similar to US CRP land as existing
agricultural land for purposes of RFS2compliant feedstock cultivation in a
foreign country, and whether EPA
should be able to make such a
determination in the context of a
petition for application of the aggregate
approach to a foreign country.
The petitioner would also be required
to provide EPA with historical land use
data for the land in question, covering
the years from prior to 2007 to the
current year. For the U.S. aggregate
compliance approach determination,
EPA analyzed the FSA Crop History
data from the years 2005 through 2007
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and the USDA Census of Agriculture
from 1997 through 2007, finding that
there was an overall decade trend of
contraction of agricultural land
utilization in the U.S. The petitioner
would need to provide a description of
any applicable laws, agricultural
practices, economic considerations, or
other relevant factors that had or may
have an effect on the use of the land in
question. For the U.S. aggregate
compliance approach determination,
EPA also took in account the EISA
renewable fuel obligations, the
unsuitability and high cost of
developing previously undeveloped
land for agricultural purposes, as well as
projected increases in crop yields on
existing agricultural land.
Finally, the petitioner would be
required to provide EPA with a plan
describing how the entity who will, on
a continuing yearly basis, conduct any
data gathering and analysis necessary to
assist EPA in its annual assessment of
any approved aggregate approach. In the
plan, the petitioner would describe the
data, the data source, and the schedule
on which the data would be updated
and made available to EPA and the
public. Additionally, the plan would
include the entity’s strategy and
schedule for conducting an annual
analysis of the data and providing it to
EPA.
4. Petition Process
We believe that it will be important to
incorporate a public comment
component into EPA’s deliberations on
a petition made to incorporate an
aggregate compliance approach for a
new area. EPA plans to publish a
Federal Register notice informing the
public of incoming petitions, with
information on how to view the
petitions and any supporting
information. EPA proposes to then
accept public comment on the petition
for a specified period of time. Once the
public comment period closes, EPA will
make an assessment, taking into account
the information submitted in the
petition as well as the comments
received, and will then publish a
decision in the Federal Register to
either approve or deny the petitioner’s
request. If the petition has been
approved, the Federal Register notice
will specify an effective date at which
time producers using the specified
feedstocks from the specified areas
identified in EPA’s approval will be
subject to the aggregate compliance
approach requirements in 40 CFR
80.1454(g) in lieu of the renewable
biomass recordkeeping and reporting
requirements. In the event that the
annual data submitted by the petitioner
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is insufficient to demonstrate that the
baseline amount of land has not been
exceeded or if the annual data is not
submitted in a timely manner, EPA will
make a finding that the baseline acreage
has been exceeded and producers using
crops or crop residue from the specified
area will be subject to the individual
recordkeeping and reporting
requirements described in the
regulations. EPA is seeking comments
on this proposed process. Additionally,
EPA requests comment on whether the
burden associated with the petition
process is reasonable, and how it might
be minimized while still remaining
adequately robust. Specific estimates
about the time and cost of preparing a
petition will be published in
Information Collection Request
associated with this proposed
rulemaking.
VI. Public Participation
We request comment on all aspects of
this proposal. This section describes
how you can participate in this process.
wwoods2 on DSKDVH8Z91PROD with PROPOSALS3
A. How do I submit comments?
We are opening a formal comment
period by publishing this document. We
will accept comments during the period
indicated under DATES in the first part
of this proposal. If you have an interest
in the proposed standards and changes
to the RFS regulations described in this
document, we encourage you to
comment on any aspect of this
rulemaking. We also request comment
on specific topics identified throughout
this proposal.
Your comments will be most useful if
you include appropriate and detailed
supporting rationale, data, and analysis.
Commenters are especially encouraged
to provide specific suggestions for any
changes that they believe need to be
made. You should send all comments,
except those containing proprietary
information, to our Air Docket (see
ADDRESSES in the first part of this
proposal) before the end of the comment
period.
You may submit comments
electronically, by mail, or through hand
delivery/courier. To ensure proper
receipt by EPA, identify the appropriate
docket identification number in the
subject line on the first page of your
comment. Please ensure that your
comments are submitted within the
specified comment period. Comments
received after the close of the comment
period will be marked ‘‘late.’’ EPA is not
required to consider these late
comments. If you wish to submit
Confidential Business Information (CBI)
or information that is otherwise
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protected by statute, please follow the
instructions in Section VI.B.
B. How should I submit CBI to the
agency?
Do not submit information that you
consider to be CBI electronically
through the electronic public docket,
https://www.regulations.gov, or by email. Send or deliver information
identified as CBI only to the following
address: U.S. Environmental Protection
Agency, Assessment and Standards
Division, 2000 Traverwood Drive, Ann
Arbor, MI 48105, Attention Docket ID
EPA–HQ–OAR–2010–0133. You may
claim information that you submit to
EPA as CBI by marking any part or all
of that information as CBI (if you submit
CBI on disk or CD–ROM, 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 CBI). Information so
marked will not be disclosed except in
accordance with procedures set forth in
40 CFR part 2.
In addition to one complete version of
the comments that include any
information claimed as CBI, a copy of
the comments that does not contain the
information claimed as CBI must be
submitted for inclusion in the public
docket. If you submit the copy that does
not contain CBI on disk or CD–ROM,
mark the outside of the disk or CD–ROM
clearly that it does not contain CBI.
Information not marked as CBI will be
included in the public docket without
prior notice. If you have any questions
about CBI or the procedures for claiming
CBI, please consult the person identified
in the FOR FURTHER INFORMATION
CONTACT section.
VII. Statutory and Executive Order
Reviews
A. 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’’
because it raises novel legal or policy
issues. Accordingly, EPA submitted this
action to the Office of Management and
Budget (OMB) for review under EO
12866 and any changes made in
response to OMB recommendations
have been documented in the docket for
this action.
The economic impacts of the RFS2
program on regulated parties, including
the impacts of the required volumes of
renewable fuel, were already addressed
in the RFS2 final rule promulgated on
March 26, 2010 (75 FR 14670). This
action proposes the percentage
standards applicable in 2011 based on
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42265
the volumes that were analyzed in the
RFS2 final rule. This action also
proposes two new regulatory provisions
that have been determined to have no
adverse economic impact on regulated
parties since they would increase
flexibility to produce qualifying
renewable fuel under the RFS2 program.
B. 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 2398.01.
This proposed regulation has a
provision that EPA would use to
authorize renewable fuel producers
using foreign-grown feedstocks to use an
aggregate approach to comply with the
renewable biomass verification
provisions, similar to that applicable to
producers using crops and crop residue
grown in the United States. See
discussion in Section V.B. For this
authorization, foreign based entities
could petition EPA for approval of the
aggregate compliance approach for
specified renewable fuel feedstocks
either in a foreign country as a whole or
in a specified geographical area within
a country. This petition request for
crops from foreign grown land areas
would be voluntary. If approved by
EPA, such a petition would allow
biomass produced in a foreign country
or geographical area to be counted as
feedstock to make renewable fuel under
the RFS2 program. Other actions in this
proposed regulation would not impose
any new information collection burdens
on regulated entities beyond those
already required under RFS2. The
submission of this information is
required in order for EPA to evaluate
and act on the petitions. Respondents
may assert claims of business
confidentiality (CBI) for any or all of the
information they submit. We do not
believe that most respondents would
characterize the information they
submit to us under this information
collection as CBI. However, any
information claimed as confidential
would be treated in accordance with 40
CFR Part 2 and established Agency
procedures. Information that is received
without a claim of confidentiality may
be made available to the public without
further notice to the submitter under 40
CFR 2.203.
EPA estimates that there would be 15
respondents (petitioners), submitting 15
responses (petitions) in response to this
provision. The estimated burden annual
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burden, assuming 15 respondents,
would be 200 hours and annual cost is
$14,196. Burden is defined at 5 CFR
1320.3(b).
An agency may not conduct or
sponsor, and a person is not required to
respond to, a collection of information
unless it displays a currently valid OMB
control number. The OMB control
numbers for 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, EPA has established
a public docket for this rule, which
includes this ICR, under Docket ID
number EPA–HQ–OAR–2010–0133.
Submit any comments related to the ICR
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 July 20, 2010, a
comment to OMB is best assured of
having its full effect if OMB receives it
by August 19, 2010. The final rule will
respond to any OMB or public
comments on the information collection
requirements contained in this proposal.
C. Regulatory Flexibility Act
The Regulatory Flexibility Act (RFA)
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act or any
other statute unless the agency certifies
that the rule will not have a significant
economic impact on a substantial
number of small entities. Small entities
include small businesses, small
organizations, and small governmental
jurisdictions.
For purposes of assessing the impacts
of today’s rule on small entities, small
entity is 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-for-profit
enterprise which is independently
owned and operated and is not
dominant in its field.
After considering the economic
impacts of today’s proposed rule on
small entities, we certify that this
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proposed action will not have a
significant economic impact on a
substantial number of small entities.
This rule sets the annual standard for
cellulosic biofuels, proposes a
regulatory provision for the generation
of Delayed RINs, and establishes criteria
for foreign countries to adopt an
aggregate approach of compliance with
the renewable biomass provision similar
to that used in the U.S. However, the
impacts of the RFS2 program on small
entities were already addressed in the
RFS2 final rule promulgated on March
26, 2010 (75 FR 14670). Therefore, this
proposed rule will not impose any
additional requirements on small
entities. We continue to be interested in
the potential impacts of the proposed
rule on small entities and welcome
comments on issues related to such
impacts.
D. Unfunded Mandates Reform Act
This action contains no Federal
mandates under the provisions of Title
II of the Unfunded Mandates Reform
Act of 1995 (UMRA), 2 U.S.C. 1531–
1538 for State, local, or tribal
governments or the private sector. The
action imposes no enforceable duty on
any State, local or tribal governments or
the private sector. Therefore, this action
is not subject to the requirements of
sections 202 or 205 of the UMRA.
This action is also not subject to the
requirements of section 203 of UMRA
because it contains no regulatory
requirements that might significantly or
uniquely affect small governments.
E. Executive Order 13132: Federalism
This action does not have federalism
implications. It will not have substantial
direct effects on the States, on the
relationship between the national
government and the States, or on the
distribution of power and
responsibilities among the various
levels of government, as specified in
Executive Order 13132. This proposed
rule does not have federalism
implications. It will not have substantial
direct effects on the States, on the
relationship between the national
government and the States, or on the
distribution of power and
responsibilities among the various
levels of government, as specified in
Executive Order 13132. Thus, Executive
Order 13132 does not apply to this rule.
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.
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F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This action does not have tribal
implications, as specified in Executive
Order 13175 (65 FR 67249, November 9,
2000). This proposed rule does not have
tribal implications, as this rule will be
implemented at the Federal level and
impose compliance costs only on
transportation fuel refiners, blenders,
marketers, distributors, importers, and
exporters. Tribal governments would be
affected only to the extent they purchase
and use regulated fuels. Thus, Executive
Order 13175 does not apply to this
action.
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
EPA interprets EO 13045 (62 FR
19885, April 23, 1997) as applying only
to those regulatory actions that concern
health or safety risks, such that the
analysis required under section 5–501 of
the EO has the potential to influence the
regulation. This action is not subject to
EO 13045 because it does not establish
an environmental standard intended to
mitigate health or safety risks and
because it implements specific
standards established by Congress in
statutes.
H. 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.
I. 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. NTTAA directs EPA to provide
Congress, through OMB, explanations
when the Agency decides not to use
available and applicable voluntary
consensus standards.
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This proposed rulemaking does not
involve technical standards. Therefore,
EPA is not considering the use of any
voluntary consensus standards.
J. Executive Order 12898: Federal
Actions to Address Environmental
Justice in Minority Populations and
Low-Income Populations
VIII. Statutory Authority
Statutory authority for this action
comes from section 211 of the Clean Air
Act, 42 U.S.C. 7545. Additional support
for the procedural and compliance
related aspects of today’s proposal,
including the proposed recordkeeping
requirements, come from Sections 114,
208, and 301(a) of the Clean Air Act, 42
U.S.C. Sections 7414, 7542, and 7601(a).
List of Subjects in 40 CFR Part 80
Environmental protection, Air
pollution control, Diesel Fuel, Fuel
additives, Gasoline, Imports, Labeling,
Motor vehicle pollution, Penalties,
Reporting and recordkeeping
requirements.
wwoods2 on DSKDVH8Z91PROD with PROPOSALS3
Dated: July 9, 2010.
Lisa P. Jackson,
Administrator.
For the reasons set forth in the
preamble, 40 CFR part 80 is proposed to
be amended as follows:
PART 80—REGULATION OF FUELS
AND FUEL ADDITIVES
1. The authority citation for part 80
continues to read as follows:
Authority: 42 U.S.C. 7414, 7542, 7545, and
7601(a).
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Jkt 220001
§ 80.1426 How are RINs generated and
assigned to batches of renewable fuel by
renewable fuel producers or importers?
*
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 action does not
relax the control measures on sources
regulated by the RFS2 regulations and
therefore will not cause emissions
increases from these sources.
VerDate Mar<15>2010
2. Section 80.1426 is amended by
revising paragraph (e)(1) and adding
paragraph (g) to read as follows:
*
*
*
*
(e) * * *
(1) Except as provided in paragraph
(g)(7) of this section for delayed RINs,
the producer or importer of renewable
fuel must assign all RINs generated to
volumes of renewable fuel.
*
*
*
*
*
(g) Delayed RIN generation. Parties
who produce or import renewable fuel
may generate delayed RINs to represent
renewable fuel volumes that have
already been transferred to another
party if those renewable fuel volumes
can be described by a pathway that has
been added to Table 1 to § 80.1426 on
or after July 1, 2010 and before January
1, 2011.
(1) When a new pathway is added to
Table 1 to § 80.1426, EPA will specify
the effective date of that new pathway.
(2) Delayed RINs must be generated
within 30 days of the effective date of
the rule in which the pathway is added.
(3) Delayed RINs may only be
generated to represent renewable fuel
produced or imported between July 1,
2010 and the effective date of the rule
in which the pathway is added.
(4) If a party originally generated and
transferred RINs with renewable fuel
volumes, and those RINs can be
described by a pathway added to Table
1 to § 80.1426 on or after July 1, 2010
and before January 1, 2011, that party
must retire a number of gallon-RINs
prior to generating delayed RINs.
(i) The number of gallon-RINs retired
must not exceed the number of gallonRINs originally generated to represent
the renewable fuel volumes produced or
imported between July 1, 2010 and the
effective date of the rule in which the
pathway is added.
(ii) Retired RINs must have a D code
of 6.
(iii) Retired RINs must have a K code
of 2.
(iv) Retired RINs must have been
generated in 2010.
(5) For parties that retire RINs
pursuant to paragraph (g)(4) of this
section, the number of delayed gallonRINs generated shall be equal to the
number of gallon-RINs retired.
(6) For parties that did not retire RINs
pursuant to paragraph (g)(4) of this
section, the number of delayed gallonRINs generated shall be determined
pursuant to paragraph (f) of this section.
(i) The standardized volume of fuel
(Vs) used to determine the RIN volume
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42267
(VRIN) under paragraph (f) of this section
shall be the standardized volume of
renewable fuel produced or imported
between July 1, 2010 and the effective
date of the rule in which the pathway
is added.
(ii) The renewable fuel for which
delayed RINs are generated must be
described by a pathway that has been
added to Table 1 to § 80.1426 on or after
July 1, 2010 and before January 1, 2011.
(7) All delayed RINs generated by a
renewable fuel producer must be
generated on the same date.
(8) Delayed RINs shall have a K code
of 2.
(9) The D code that shall be used in
delayed RINs generated shall be the D
code specified in Table 1 to § 80.1426
which corresponds to the pathway that
describes the producer’s operations.
3. Section 80.1454 is amended by
revising paragraph (g) introductory text
to read as follows:
§ 80.1454 What are the recordkeeping
requirements under the RFS Program?
*
*
*
*
*
(g) Aggregate compliance with
renewable biomass requirement. Any
producer or RIN-generating importer of
renewable fuel made from planted crops
or crop residue from existing U.S.
agricultural land as defined in
§ 80.1401, or any producer or RINgenerating importer of renewable fuel
made from feedstock covered by a
petition approved pursuant to § 80.1457,
is subject to the aggregate compliance
approach and is not required to
maintain feedstock records unless EPA
publishes a finding that the 2007
baseline amount of agricultural land has
been exceeded or that the criterion in
§ 80.1457(a) is no longer satisfied.
*
*
*
*
*
4. Section 80.1457 is added to read as
follows:
§ 80.1457 Petition process for international
aggregate compliance approach.
(a) EPA may approve a petition for
application of the aggregate compliance
approach to non-U.S. planted crops and
crop residues from existing foreign
agricultural land if it determines that an
aggregate compliance approach will
provide reasonable assurance that
specified renewable fuel feedstocks
from a given geographical area meet the
definition of renewable biomass and
will continue to meet the definition of
renewable biomass, based on the
submission of credible, reliable, and
verifiable data.
(1) As part of its evaluation, EPA will
consider:
(i) Whether there has been a
reasonable identification of the
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aggregate amount of agricultural land in
the specified geographical area as of
December 19, 2007 that was available
for the production of the specified
feedstock(s) and that satisfy the
definition of renewable biomass;
(ii) Whether information from years
preceding and following 2007 shows
that the 2007 amount of agricultural
land identified in paragraph (a)(1)(i) of
this section is not likely to be exceeded
in the future;
(iii) Whether economic
considerations, legal constraints,
historical land use and agricultural
practices, and/or other factors show that
it is likely that producers of the
feedstock(s) will continue to use
agricultural land within area of land
identified in paragraph (a)(1)(i) of this
section in the future as opposed to
clearing and cultivating land that was
not included in that area of land.
(iv) Whether there is a reliable
method to evaluate on a continuing
basis whether the 2007 area of land
identified in paragraph (a)(1)(i) of this
section is being exceeded; and
(v) Whether an entity has been
identified to conduct data gathering and
analysis needed for the evaluation
specified in paragraph (a)(1)(iv) of this
section, for submission to EPA on an
annual basis if EPA grants the petition.
(2) [Reserved]
(b) Any petition submitted under
paragraph (a) of this section must be in
the English language, and must include
all of the following, or an explanation of
why it is not needed for EPA to approve
the petition:
(1) Maps or electronic data identifying
the boundaries of the land for which the
petitioner seeks approval of an aggregate
compliance approach.
(2)(i) For petitions regarding crops or
crop residue, the total amount of land
that is cropland or pastureland within
the geographic boundaries specified in
paragraph (b)(1) of this section that was
cleared or cultivated prior to December
19, 2007 and that was actively managed
or fallow and nonforested on that date,
and the total amount of land that is
cropland or pastureland within the
geographic boundaries specified in
paragraph (b)(1) of this section that was
not cleared or cultivated prior to
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December 19, 2007 and actively
managed or fallow and nonforested on
that date.
(ii) If the petitioner is seeking
approval of the aggregate compliance
approach for a particular planted crop
or crop residue, the total amount of land
within the geographic boundaries
specified in paragraph (b)(1) of this
section that was used for the production
of that feedstock in 2007 and that was
actively managed or fallow and
nonforested on that date, and the total
amount of land within the geographic
boundaries specified in paragraph (b)(1)
of this section that was used for the
production of that feedstock in 2007
that was not cleared or cultivated prior
to December 19, 2007 and actively
managed or fallow and nonforested on
that date.
(3) A description of the feedstock(s)
for which the petitioner is submitting
the petition.
(4) Land use data that demonstrates
that the land in question in paragraph
(b)(1) of this section is cropland or
pastureland that was cleared or
cultivated prior to December 19, 2007
and that was actively managed or fallow
and nonforested on that date, which
may include any of the following:
(i) Satellite imagery data.
(ii) Aerial photography.
(iii) Census data.
(iv) Agricultural surveys.
(v) Agricultural economic modeling
data.
(5) Historical land use data for the
land within the geographic boundaries
specified in paragraph (b)(1) of this
section to the current year, which may
include any of the following:
(i) Satellite imagery data.
(ii) Aerial photography.
(iii) Census data.
(iv) Agricultural surveys.
(v) Agricultural economic modeling
data.
(6) A description of any applicable
laws, agricultural practices, economic
considerations, or other relevant factors
that had or may have an effect on the
use of the land within the geographic
boundaries specified in paragraph (b)(1)
of this section.
(7) A plan describing how the
petitioner will identify an entity who
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will, on a continuing basis, conduct data
gathering, analysis, and submittal to
assist EPA in making an annual
determination of whether the criterion
specified in paragraph (a) of this section
remains satisfied.
(8) Any additional information the
Administrator may require.
(c) If EPA approves a petition it will
issue a Federal Register notice
announcing its decision and specifying
an effective date for the application of
the aggregate compliance approach to
the specified feedstock(s) from the
specific geographical area. Thereafter,
the specified feedstocks from the
specified area will be covered by the
aggregate compliance approach set forth
in § 80.1454(g), or as otherwise specified
pursuant to paragraph (d) of this
section.
(d) If EPA grants a petition to
establish an aggregate compliance
approach for a specified feedstock(s)
from a specific geographical area, it may
include any conditions that EPA
considers appropriate in light of the
conditions and circumstances involved.
(e)(1) EPA may withdraw its approval
of the aggregate approach for the area
and feedstocks in question if:
(i) EPA determines that the data
submitted pursuant to the plan
described in paragraph (b)(7) of this
section does not demonstrate that the
amount of cropland and pastureland
within the geographic boundaries
covered by the approved petition does
not exceed the 2007 baseline amount of
land;
(ii) EPA determines based on other
information that the criterion specified
in paragraph (a) of this section is no
longer satisfied; or
(iii) EPA determines that the data
needed for its annual evaluation has not
been collected and submitted in a
timely and appropriate manner.
(2) If EPA withdraws its approval,
then producers using feedstocks from
that area will be subject to the
individual recordkeeping and reporting
requirements of § 80.1454(b) through (d)
in accordance with the schedule
specified in § 80.1454(g).
[FR Doc. 2010–17281 Filed 7–19–10; 8:45 am]
BILLING CODE 6560–50–P
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Agencies
[Federal Register Volume 75, Number 138 (Tuesday, July 20, 2010)]
[Proposed Rules]
[Pages 42238-42268]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: 2010-17281]
[[Page 42237]]
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Part III
Environmental Protection Agency
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40 CFR Part 80
Regulation of Fuels and Fuel Additives: 2011 Renewable Fuel Standards;
Proposed Rule
Federal Register / Vol. 75 , No. 138 / Tuesday, July 20, 2010 /
Proposed Rules
[[Page 42238]]
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ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 80
[EPA-HQ-OAR-2010-0133; FRL-9175-8]
RIN 2060-AQ16
Regulation of Fuels and Fuel Additives: 2011 Renewable Fuel
Standards
AGENCY: Environmental Protection Agency (EPA).
ACTION: Notice of proposed rulemaking.
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SUMMARY: Under the Clean Air Act Section 211(o), as amended by the
Energy Independence and Security Act of 2007 (EISA), the Environmental
Protection Agency is required to set the renewable fuel standards each
November for the following year based on gasoline and diesel
projections from EIA. Additionally, EPA is required to set the
cellulosic biofuel standard each year based on the volume projected to
be available during the following year, using EIA projections and
assessments of production capability from industry. This regulatory
action proposes these annual standards for cellulosic biofuel, biomass-
based diesel, advanced biofuel, and renewable fuels that apply to all
gasoline and diesel produced or imported in year 2011. This action also
presents two proposed changes to the RFS2 regulations. The first would
create a temporary and limited means for certain renewable fuel
producers to generate delayed RINs after they have produced and sold
renewable fuel. This proposed provision would apply only to those
producers who use canola oil, grain sorghum, pulpwood, or palm oil to
produce renewable fuel. The second proposed regulatory provision would
establish criteria for foreign countries to adopt an aggregate approach
to compliance with the renewable biomass provision akin to that
applicable to the U.S.
DATES: Comments must be received on or before August 19, 2010.
Hearing: We do not expect to hold a public hearing. However, if we
receive such a request we will publish information related to the
timing and location of the hearing and the timing of a new deadline for
public comments.
ADDRESSES: Submit your comments, identified by Docket ID No. EPA-HQ-
OAR-2010-0133, by one of the following methods:
https://www.regulations.gov: Follow the online instructions
for submitting comments.
E-mail: asdinfo@epa.gov.
Mail: Air and Radiation Docket and Information Center,
Environmental Protection Agency, Mailcode: 2822T, 1200 Pennsylvania
Ave., NW., Washington, DC 20460.
Hand Delivery: EPA Docket Center, EPA West Building, Room
3334, 1301 Constitution Ave., NW., Washington, DC 20460. Such
deliveries are only accepted during the Docket's normal hours of
operation, and special arrangements should be made for deliveries of
boxed information.
Instructions: Direct your comments to Docket ID No. EPA-HQ-OAR-
2010-0133. EPA's policy is that all comments received will be included
in the public docket without change and may be made available online at
https://www.regulations.gov, including any personal information
provided, unless the comment includes information claimed to be
Confidential Business Information (CBI) or other information whose
disclosure is restricted by statute. Do not submit information that you
consider to be CBI or otherwise protected through https://www.regulations.gov or e-mail. The https://www.regulations.gov Web site
is an ``anonymous access'' system, which means 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. For additional instructions on submitting
comments, go to Section I.B of the SUPPLEMENTARY INFORMATION section of
this document.
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 Air and Radiation
Docket and Information Center, 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 Air Docket is (202) 566-
1742.
FOR FURTHER INFORMATION CONTACT: Julia MacAllister, Office of
Transportation and Air Quality, Assessment and Standards Division,
Environmental Protection Agency, 2000 Traverwood Drive, Ann Arbor, MI
48105; Telephone number: 734-214-4131; Fax number: 734-214-4816; E-mail
address: macallister.julia@epa.gov, or Assessment and Standards
Division Hotline; telephone number 734-214-4636; E-mail address
asdinfo@epa.gov.
SUPPLEMENTARY INFORMATION:
I. General Information
A. Does this action apply to me?
Entities potentially affected by this proposed rule are those
involved with the production, distribution, and sale of transportation
fuels, including gasoline and diesel fuel or renewable fuels such as
ethanol and biodiesel. Potentially regulated categories include:
----------------------------------------------------------------------------------------------------------------
NAICS \1\ Examples of potentially regulated
Category codes SIC \2\ codes entities
----------------------------------------------------------------------------------------------------------------
Industry............................... 324110 2911 Petroleum Refineries.
Industry............................... 325193 2869 Ethyl alcohol manufacturing.
Industry............................... 325199 2869 Other basic organic chemical
manufacturing.
Industry............................... 424690 5169 Chemical and allied products merchant
wholesalers.
Industry............................... 424710 5171 Petroleum bulk stations and terminals.
Industry............................... 424720 5172 Petroleum and petroleum products
merchant wholesalers.
[[Page 42239]]
Industry............................... 454319 5989 Other fuel dealers.
----------------------------------------------------------------------------------------------------------------
\1\ North American Industry Classification System (NAICS).
\2\ Standard Industrial Classification (SIC) system code.
This table is not intended to be exhaustive, but rather provides a
guide for readers regarding entities likely to be regulated by this
proposed action. This table lists the types of entities that EPA is now
aware could potentially be regulated by this proposed action. Other
types of entities not listed in the table could also be regulated. To
determine whether your activities would be regulated by this proposed
action, you should carefully examine the applicability criteria in 40
CFR part 80. If you have any questions regarding the applicability of
this proposed action to a particular entity, consult the person listed
in the preceding 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.
Outline of This Preamble
I. Executive Summary
A. Statutory Requirements for Cellulosic Biofuel
B. Assessment of 2011 Cellulosic Biofuel Volume
C. Advanced Biofuel and Total Renewable Fuel
D. Proposed Percentage Standards
II. Volume Production and Import Potential for 2011
A. Cellulosic Biofuel
1. Domestic Cellulosic Ethanol
2. Domestic Cellulosic Diesel
3. Other Domestic Cellulosic Biofuels
4. Imports of Cellulosic Biofuel
5. Summary of Volume Projections
B. Potential Limitations
C. Advanced Biofuel and Total Renewable Fuel
D. Biomass-Based Diesel
III. Proposed Percentage Standards for 2011
A. Background
B. Calculation of Standards
1. How are the standards calculated?
2. Small Refineries and Small Refiners
IV. Cellulosic Biofuel Technology Assessment
A. What pathways are valid for the production of cellulosic
biofuel?
B. Cellulosic Feedstocks
C. Emerging Technologies
1. Biochemical
a. Feedstock Handling
b. Biomass Pretreatment
c. Hydrolysis
i. Acid Hydrolysis
ii. Enzymatic Hydrolysis
d. Fuel Production
e. Fuel Separation
f. Process Variations
g. Current Status of Biochemical Conversion Technology
h. Major Hurdles to Commercialization
2. Thermochemical
a. Ethanol Based on a Thermochemical Platform
b. Diesel and Naphtha Production Based on a Thermochemical
Platform
3. Hybrid Thermochemical/Biochemical Processes
4. Pyrolysis and Depolymerization
a. Pyrolysis Diesel Fuel and Gasoline
b. Catalytic Depolymerization
5. Catalytic Reforming of Sugars to Gasoline
V. Proposed Changes to RFS2 Regulations
A. Delayed RIN Generation for New Pathways
B. Criteria and Process for Adoption of Aggregate Approach to
Renewable Biomass for Foreign Countries
1. Criterion and Considerations
2. Data Sources
3. Petition Submission
4. Petition Process
VI. Public Participation
A. How do I submit comments?
B. How should I submit CBI to the agency?
VII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation and Coordination With
Indian Tribal Governments
G. Executive Order 13045: Protection of Children From
Environmental Health Risks and Safety Risks
H. Executive Order 13211: Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use
I. National Technology Transfer Advancement Act
J. Executive Order 12898: Federal Actions to Address
Environmental Justice in Minority Populations and Low-Income
Populations
VIII. Statutory Authority
I. Executive Summary
The Renewable Fuel Standard (RFS) program began in 2007 following
the requirements in Clean Air Act (CAA) section 211(o) which were
implemented through the Energy Policy Act of 2005 (EPAct). The
statutory requirements for the RFS program were subsequently modified
through the Energy Independence and Security Act of 2007 (EISA),
resulting in the release of revised regulatory requirements on March
26, 2010 \1\. In general, the transition from the RFS1 requirements of
EPAct to the RFS2 requirements of EISA will occur on July 1, 2010.
---------------------------------------------------------------------------
\1\ 75 FR 14670.
---------------------------------------------------------------------------
EPA is required to determine and publish the applicable annual
percentage standards for each compliance year by November 30 of the
previous year. The determination of the applicable standards under RFS2
requires the EPA to conduct an in-depth evaluation of the volume of
qualifying cellulosic biofuel that can be supplied in the following
year. If the projected
[[Page 42240]]
volume of cellulosic biofuel production is less than the required
volume specified in the statute, EPA must lower the required volume
used to set the annual cellulosic biofuel percentage standard to the
projected volume of production. We must also determine whether the
advanced biofuel and/or total renewable fuel volumes should be reduced
by the same or a lesser amount. Since these evaluations will be based
on evolving information about emerging segments of the biofuels
industry, and may result in the required volumes differing from those
in the statute, we believe that a notice-and-comment rulemaking process
is appropriate. Today's notice provides our evaluation of the projected
production of cellulosic biofuel for 2011, and proposed percentage
standards for compliance year 2011. We will complete our evaluation
based on comments received in response to this proposal, the Production
Outlook Reports due to the Agency on September 1, 2010, the estimate of
projected biofuel volumes that the EIA is required to provide to EPA by
October 31, and other information that becomes available, and will
finalize the standards for 2011 by November 30, 2010.
Today's proposed rule does not include an assessment of the
environmental impacts of the standards we are proposing for 2011. All
of the impacts of the RFS2 program were addressed in the RFS2 final
rule published on March 26, 2010, including impacts of the biofuel
standards specified in the statute. Today's rulemaking simply proposes
the standards for 2011 whose impacts were already analyzed previously.
Today's notice also presents two proposed changes to the RFS2
regulations. The first would create a temporary and limited means for
certain renewable fuel producers to generate RINs after they have
produced and sold renewable fuel. This proposed provision for ``Delayed
RINs'' would apply only to those producers who use canola oil, grain
sorghum, pulpwood, or palm oil to produce renewable fuel, and only if
EPA determines that fuel pathways utilizing these feedstocks provide
appropriate greenhouse gas reductions as compared to baseline fuels to
enable EPA to list the pathways in Table 1 to Sec. 80.1426. We are
proposing that the provision for Delayed RINs would apply only to these
four feedstocks because we would have included them in the final RFS2
rule if the lifecycle analyses had been completed in time. The
greenhouse gas (GHG) lifecycle impacts of these four feedstocks are
currently being analyzed as a supplement to the RFS2 final rule and are
expected to be completed in 2010. The second proposed regulatory
provision would establish criteria for EPA to use in determining
whether to authorize renewable fuel producers using foreign-grown
feedstocks to use an aggregate approach to compliance with the
renewable biomass verification provisions, akin to that applicable to
producers using crops and crop residue grown in the United States.
Further discussion of both of these proposed provisions can be found in
Section V.
Finally, we note that in the RFS2 final rule we also stated our
intent to make two announcements each year:
Set the price for cellulosic biofuel waiver credits that
will be made available to obligated parties in the event that we reduce
the volume of cellulosic biofuel below the volume required by EISA.
Announce the results of our assessment of the aggregate
compliance approach for verifying renewable biomass requirements for
U.S. crops and crop residue, and our conclusion regarding whether the
aggregate compliance provision will continue to apply.
For both of these determinations EPA will use specific sources of
data and a methodology laid out in the RFS2 final rule. We intend to
present the results of both of these determinations in the final rule
following today's proposal.
A. Statutory Requirements for Cellulosic Biofuel
The volumes of renewable fuel that must be used under the RFS2
program each year (absent an adjustment or waiver by EPA) are specified
in CAA 211(o)(2). These volumes for 2011 are shown in Table I.A-1.
Table I.A-1--Required Volumes in the Clean Air Act for 2011
[Bill gal]
------------------------------------------------------------------------
Ethanol
Actual equivalent
volume volume
------------------------------------------------------------------------
Cellulosic biofuel.......................... 0.25 \a\ 0.25
Biomass-based diesel........................ 0.80 1.20
Advanced biofuel............................ 1.35 1.35
Renewable fuel.............................. 13.95 13.95
------------------------------------------------------------------------
\a\ This value assumes that all cellulosic biofuel would be ethanol. If
any portion of the renewable fuel used to meet the cellulosic biofuel
volume mandate has a volumetric energy content greater than that for
ethanol, this value will be higher.
By November 30 of each year, the EPA is required under CAA 211(o)
to determine and publish in the Federal Register the renewable fuel
standards for the following year. These standards are to be based in
part on transportation fuel volumes estimated by the Energy Information
Administration (EIA) for the following year. The calculation of the
percentage standards is based on the formulas in Sec. 80.1405(c) which
express the required volumes of renewable fuel as a volume percentage
of gasoline and diesel sold or introduced into commerce in the 48
contiguous states plus Hawaii.
The statute requires the EPA to determine whether the projected
volume of cellulosic biofuel production for the following year is less
than the minimum applicable volume shown in Table I.A-1. If this is the
case, then the standard for cellulosic biofuel must be based upon the
volume projected to be available rather than the applicable volume in
the statute. In addition, if EPA reduces the required volume of
cellulosic biofuel below the level specified in the statute, the Act
also indicates that we may reduce the applicable volume of advanced
biofuels and total renewable fuel by the same or a lesser volume.
As described in the final rule for the RFS2 program, we intend to
examine EIA's projected volumes and other available data including the
Production Outlook Reports required under Sec. 80.1449 in making the
determination of the appropriate volumes to require for 2011. Since the
first set of Production Outlook Reports are not due until September 1,
2010, they were not available for today's proposal but will be
considered for development of the
[[Page 42241]]
final rule to be released by November 30, 2010.
B. Assessment of 2011 Cellulosic Biofuel Volume
To estimate the volume of cellulosic biofuel that could be made
available in the U.S. in 2011, we researched all potential production
sources by company and facility. This included sources that were still
in the planning stages, those that were under construction, and those
that are already producing some volume of cellulosic ethanol,
cellulosic diesel, or some other type of cellulosic biofuel. We
considered all pilot and demonstration plants as well as commercial
plants. From this universe of potential cellulosic biofuel sources we
identified the subset that had a possibility of producing some volume
of qualifying cellulosic biofuel for use as transportation fuel in
2011. We then conducted a rigorous process of contacting all of these
producers to determine which ones were actually in a position to
produce and make available any commercial volumes of cellulosic biofuel
in 2011. Based on information gathered in this process, we estimated
the maximum potentially available 2011 volumes. For the final rule, we
will specify the projected available volume for 2011 that will be the
basis for the percentage standard for cellulosic biofuel. To determine
the projected available volume, we will consider factors such as the
current and expected state of funding, the status of the technology and
contracts for feedstocks, and progress towards construction and
production goals. A complete list of all the factors we expect to
consider in this process is provided in Section II.A.5.
In our assessment we evaluated both domestic and foreign sources of
cellulosic biofuel. Of the domestic sources, we estimated that seven
facilities have the potential to make volumes of cellulosic biofuel
available for transportation use in the U.S. in 2011. We also
determined that one facility in Canada has the potential to export some
cellulosic biofuel to the U.S. These facilities are listed in Table
I.B-1 along with our estimate of the maximum potentially available
volume.
Table I.B-1--Maximum Potentially Available Cellulosic Biofuel Plant Volumes for 2011
----------------------------------------------------------------------------------------------------------------
Maximum potentially
available volume
Company Location Fuel type (million ethanol-
equivalent gallons)
----------------------------------------------------------------------------------------------------------------
AE Advanced Fuels Keyes.............. Keyes, CA.............. Ethanol................ 0.5
Agresti Biofuels..................... Pike County, KY........ Ethanol................ 1
Bell Bio-Energy...................... Atlanta, GA............ Diesel feedstock....... 11.9
Cello Energy......................... Bay Minette, AL........ Diesel................. 8.5
DuPont Dansico....................... Vonore, TN............. Ethanol................ 0.15
Fiberight............................ Blairstown, IA......... Ethanol................ 2.8
Iogen Corporation.................... Ottawa, Ont............ Ethanol................ 0.25
KL Energy Corp/WBE................... Upton, WY.............. Ethanol................ 0.4
------------------------
Total............................ ....................... ....................... 25.5
----------------------------------------------------------------------------------------------------------------
The volumes in Table I.B-1 for each facility represent the volume
that would be produced in 2011 based upon the owner's expected month of
startup and an assumed period of production rampup for testing and
process validation. However, none of the facilities we evaluated are
currently producing cellulosic biofuel at the rates they project for
2011. Moreover, there are other uncertainties associated with each
facility's projected volume that could result in less production volume
in 2011 than the maximum potentially available values shown in Table
I.B-1. These uncertainties include outstanding issues in areas such as
technology, funding, and construction. Historical successes in meeting
various past milestones also play a role in assessing the likelihood of
meeting future milestones. A detailed discussion of these uncertainties
is presented in Section II.A. Finally, the volumes that should be
considered for setting the 2011 standard are those that result from
valid cellulosic biofuel pathways in Table 1 to Sec. 80.1426. As
described more fully in Section IV.A, some of the facilities in Table
I.B-1 may use feedstocks that have not yet been subjected to lifecycle
analyses to determine if the pathway meets the applicable GHG
thresholds.
Based on our preliminary assessment for this NPRM, we believe that
we could justify a 2011 cellulosic biofuel volume requirement of at
least 6.5 million ethanol-equivalent gallons, and potentially as high
as 25.5 million gallons. For the final rule we will use additional
information that becomes available after publication of this proposal
and a more precise assessment of the uncertainties associated with each
facility to determine the projected available volume on which to base
the cellulosic biofuel percentage standard for 2011.
C. Advanced Biofuel and Total Renewable Fuel
As described in Section I.A above, the statute indicates that we
may reduce the applicable volume of advanced biofuel and total
renewable fuel if we determine that the projected volume of cellulosic
biofuel production for 2011 falls short of the statutory volume of 250
million gallons. As shown in Table I.B-1, we are proposing a
determination that this is the case. Therefore, we also needed to
evaluate the need to lower the required volumes for advanced biofuel
and total renewable fuel.
We first considered whether it appears likely that the required
biomass-based diesel volume of 0.8 billion gallons can be met with
existing biodiesel production capacity in 2011. As discussed in Section
II.D, we believe that the 0.8 billion gallon standard can indeed be
met. Since biodiesel has an Equivalence Value of 1.5, 0.8 billion
physical gallons of biodiesel would provide 1.20 billion ethanol-
equivalent gallons that can be counted towards the advanced biofuel
standard of 1.35 billion gallons. Of the remaining 0.15 bill gallons,
up to 0.026 bill gallons would be met with the proposed volume of
cellulosic biofuel. Based on our analysis as described in Section II.C,
there may be sufficient volumes of other advanced biofuels, such as
imported sugarcane ethanol, additional biodiesel, or renewable diesel,
such that the standard for advanced biofuel could remain at the
statutory level of 1.35 billion gallons. However, uncertainty in
[[Page 42242]]
the potential volumes of these other advanced biofuels coupled with the
range of potential production volumes of cellulosic biofuel could
provide a rationale for lowering the advanced biofuel standard. If we
do not simultaneously lower the required volume for total renewable
fuel, the result would be that additional volumes of conventional
renewable fuel, such as corn-starch ethanol, would be produced,
effectively replacing some advanced biofuels. In today's NPRM we are
proposing that neither the required 2011 volumes for advanced biofuel
nor total renewable fuel be lowered below the statutory volumes.
However, we request comment on whether the advanced biofuel and/or
total renewable fuel volume requirements should be lowered if, as we
propose, EPA lowers the required cellulosic biofuel volume from that
specified in the Act.
D. Proposed Percentage Standards
The renewable fuel standards are expressed as a volume percentage,
and are used by each refiner, blender or importer to determine their
renewable fuel volume obligations. The applicable percentages are set
so that if each regulated party meets the percentages, and if EIA
projections of gasoline and diesel use are accurate, then the amount of
renewable fuel, cellulosic biofuel, biomass-based diesel, and advanced
biofuel used will meet the volumes required on a nationwide basis. To
calculate the percentage standard for cellulosic biofuel for 2011, we
have used a potential volume range of 6.5-25.5 million ethanol-
equivalent gallons (representing 5-17.1 million physical gallons). For
the final rule, EPA intends to pick a single value from within this
range to represent the projected available volume on which the 2011
percentage standard for cellulosic biofuel will be based. We are also
proposing that the applicable volumes for biomass-based diesel,
advanced biofuel, and total renewable fuel for 2011 will be those
specified in the statute. These volumes are shown in Table I.D-1.
Table I.D-1--Proposed Volumes for 2011
----------------------------------------------------------------------------------------------------------------
Actual volume Ethanol equivalent volume
----------------------------------------------------------------------------------------------------------------
Cellulosic biofuel....................... 5-17.1 mill gal............. 6.5-25.5 mill gal.
Biomass-based diesel..................... 0.80 bill gal............... 1.20 bill gal.
Advanced biofuel......................... 1.35 bill gal............... 1.35 bill gal.
Renewable fuel........................... 13.95 bill gal.............. 13.95 bill gal.
----------------------------------------------------------------------------------------------------------------
Four separate standards are required under the RFS2 program,
corresponding to the four separate volume requirements shown in Table
I.D-1. The specific formulas we use to calculate the renewable fuel
percentage standards are contained in the regulations at Sec. 80.1405
and repeated in Section III.B.1. The percentage standards represent the
ratio of renewable fuel volume to non-renewable gasoline and diesel
volume. The projected volumes of gasoline and renewable fuels used to
calculate the standards are provided by EIA's Short-Term Energy Outlook
(STEO) \2\. The projected volume of transportation diesel used to
calculate the standards is provided by EIA's 2010 Annual Energy Outlook
(early release version).\3\ Because small refiners and small refineries
are also regulated parties beginning in 2011 \4\, there is no small
refiner/refinery volume adjustment to the 2011 standard as there was
for the 2010 standard. Thus, the increase in the percentage standards
relative to 2010 appears smaller than would otherwise be the case,
since more obligated parties will be participating in the program. The
proposed standards for 2011 are shown in Table I.D-2. Detailed
calculations can be found in Section III.
---------------------------------------------------------------------------
\2\ The March 2010 issue of STEO was used for today's proposal.
We intend to use the October 2010 version for the final rule.
\3\ EIA has recommended the use of the Annual Energy Outlook
(AEO) rather than the Short Term Energy Outlook as a better
representation of the estimated transportation sector diesel fuel
use. We will use the most recent version of AEO in the final values
of the standards.
\4\ The Department of Energy concluded that there is no reason
to believe that any small refinery would be disproportionately
harmed by inclusion in the proposed RFS2 program for 2011 and
beyond. See DOE report ``EPACT 2005 Section 1501 Small Refineries
Exemption Study'', (January 2009). We will revisit extensions to the
exemption for small refiners and refineries if DOE revises their
study and provides a different conclusion, or an individual small
refinery is able to demonstrate that it will suffer a
disproportionate economic hardship under the RFS program.
Table I.D-2--Proposed Percentage Standards for 2011
------------------------------------------------------------------------
Percent
------------------------------------------------------------------------
Cellulosic biofuel...................................... 0.004-0.015
Biomass-based diesel.................................... 0.68
Advanced biofuel........................................ 0.77
Renewable fuel.......................................... 7.95
------------------------------------------------------------------------
II. Volume Production and Import Potential for 2011
In order to project production volumes of cellulosic biofuel in
2011 for use in setting the percentage standards, we collected
information on individual facilities that have the potential to produce
qualifying volumes for consumption as transportation fuel, heating oil,
or jet fuel in the U.S. in 2011. This section describes the potential
volumes that we believe could be produced or imported in 2011 as well
as the uncertainties associated with those volumes. The volumes listed
in this section do not represent the projected available volume of
cellulosic biofuel that will be used to finalize the cellulosic biofuel
percentage standard for 2011. Rather, for today's NPRM we have assessed
the maximum potentially available volume for 2011, which is intended to
represent an upper bound of the volume of fuel that may be produced and
made available. The production of cellulosic biofuel remains highly
uncertain, and EPA expects that the volume of cellulosic biofuel used
to set the 2011 percentage standard will be a lesser volume than this
maximum potentially available volume. Section III describes the
conversion of our maximum potentially available volumes for cellulosic
biofuel into a range of percentage standards.
While the 2011 volume projections in today's proposal were based on
our own assessment of the cellulosic biofuel industry, by the time we
announce the final 2011 volumes and percentage standards we will have
additional information. First, in addition to comments in response to
today's proposal, we will have updated and more detailed information
about how the industry is progressing in 2010. Second, by September 1
all registered producers and importers of renewable fuel must submit
Production Outlook Reports describing their expectations for new or
expanded biofuel supply for the next five years, according to Sec.
80.1449. Finally, by October 2010 the Energy
[[Page 42243]]
Information Administration (EIA) is required by statute to provide EPA
with an estimate of the volumes of transportation fuel, biomass-based
diesel, and cellulosic biofuel projected to be sold or introduced into
commerce in the U.S. in 2011.
A. Cellulosic Biofuel
The task of projecting the volume of cellulosic biofuels that will
be produced in 2011 is a difficult one. Currently there are no
facilities consistently producing cellulosic biofuels for commercial
sale. Announcements of new projects, changes in project plans, project
delays, and cancellations occur with great regularity. Biofuel
producers face not only the challenge of the scale up of innovative,
first-of-a-kind technology, but also the challenge of securing funding
in a difficult economy.
In order to project cellulosic biofuel production in 2011, EPA has
tracked the progress of over 100 biofuel production facilities. From
this list of facilities we used publicly available information, as well
as information provided by DOE and USDA, to determine which facilities
were the most likely candidates to produce cellulosic biofuel and make
it commercially available in 2011. Each of these companies was
contacted by EPA in order to determine the current status of their
facilities and discuss their commercialization plans for the coming
years. Our estimate of the maximum potentially available cellulosic
biofuel production in 2011 is based on the information we received in
conversations with these companies as well as our own assessment of the
likelihood of these facilities successfully producing cellulosic
biofuel in the volumes indicated.
A brief description of each of the companies we believe may produce
cellulosic biofuel and make it commercially available can be found
below. These companies have been grouped according to the type of
biofuel they produce. For the purpose of setting the cellulosic biofuel
standard for 2011 this is a convenient grouping, as the number of RINs
generated per gallon of fuel produced is dependent on the type of fuel.
A more in depth discussion of the technologies used to produce
cellulosic biofuels can be found in Section IV.
In today's NPRM EPA is proposing a range, rather than a single
value, for the required 2011 cellulosic biofuel volume. At a minimum,
we believe that a volume of 6.5 million gallons could be justified
based on currently available information. This is the cellulosic
biofuel volume that was required in 2010, and absent a waiver for some
portion of this volume, producers will be aiming to meet it. Therefore,
it is reasonable to project that this same volume could, at minimum,
also be produced in 2011.
For a maximum potentially available cellulosic biofuel volume for
2011, we are proposing 25.5 million ethanol equivalent gallons,
representing the highest volume of fuel that can reasonably be expected
to be produced and made available based on current information. In
order for this volume of cellulosic biofuel to be produced in 2011,
each of the companies discussed below would have to achieve their
production targets in their projected timeframes. However, historical
trends among cellulosic biofuel producers suggests that this is
unlikely to be the case, as there are many factors which have the
potential to result in production delays. For instance, several of the
companies we considered when setting the 2010 cellulosic biofuel
standard have yet to sell cellulosic biofuel in the United States and
appear unlikely to do so by the end of 2010. This fact demonstrates the
uncertainty of cellulosic biofuel production estimates, and is one of
many factors EPA will consider when setting the cellulosic biofuel
standard for 2011.
The rest of this section describes the analyses that were used as
the basis for this maximum value. We will continue to gather more
information to help inform our decision on the final cellulosic biofuel
standard for 2011, and we will specify a single volume in the final
rule that will be the basis for the cellulosic biofuel percentage
standard for 2011.
1. Domestic Cellulosic Ethanol
Based on our assessment of the cellulosic biofuel industry we
believe that there are five companies in the United States with the
potential to produce cellulosic ethanol and make it commercially
available in 2011. These companies are AE Biofuels, Agresti Biofuels,
DuPont Danisco Cellulosic Ethanol, Fiberight, and KL Energy
Corporation. This section will provide a brief description of each of
these companies and our assessment of their potential fuel production
in 2011. This section also provides a brief update on companies from
whom we do not expect any commercial sales of transportation fuel in
2011 in the U.S. but were included in prior assessments.
AE Biofuels is a company that plans to convert corn cobs and corn
stover to ethanol using an enzymatic hydrolysis. They plan to use an
integrated process that converts both starch and cellulose to ethanol.
In August 2008 they opened a demonstration plant in Butte, Montana to
test their technology and gather information for their first commercial
scale plant. AE Biofuels has reached a lease agreement with Cilion to
operate Cilion's 55 MGY corn ethanol plant in Keyes, CA under the name
AE Advanced Fuels Keyes. This facility has been idled since April 2009
and will require repairs before being operational. AE Biofuels plans to
start up production with a starch feedstock in late-2010 and then begin
to transition some production to cellulosic feedstock in mid-2011. AE
Biofuels plans to eventually use up to 25% cellulosic feedstock for
ethanol production in this facility. EPA projects that up to 0.5
million gallons of ethanol may be produced by this facility in 2011.
Agresti Biofuels plans to produce ethanol from separated municipal
solid waste (separated MSW) at a facility in Pike County, Kentucky.
Their process uses a gravity pressure vessel licensed from GeneSyst to
crack the lignin in their feedstock and then a combination of weak
bases and acids to convert the cellulose and hemicellulose into simple
sugars for later fermentation into ethanol. Agresti plans to begin
construction on their first production facility in Pike County sometime
in the summer of 2010 and hope to be producing ethanol by the end of
2011. The full production capacity of this facility will be 20 million
gallons of ethanol per year. Due to the fact that construction on this
facility has not yet begun and production is not expected until late in
2011 EPA expects no more than 1 million gallons of cellulosic ethanol
to be produced by Agresti Biofuels in 2011.
DuPont Danisco Cellulosic Ethanol (DDCE) began start up operations
at a small demonstration facility in Vonore, Tennessee in early 2010.
This facility has a maximum production capacity of 250,000 gallons of
ethanol per year and uses an enzymatic hydrolysis process to convert
corn cobs into ethanol. The main purpose of this facility is not to
produce ethanol to be sold commercially, but rather to provide
information for the future construction and optimization of larger,
commercial scale cellulosic ethanol production facilities. DDCE have
indicated that they do not intend to produce more than 150,000 gallons
of ethanol in 2011 from the Vonore facility.
Fiberight is another company planning to convert MSW to ethanol.
Fiberight purchased a small corn ethanol plant in Blairstown, IA and
has converted it to produce cellulosic ethanol. They use an enzymatic
hydrolysis process, with enzymes
[[Page 42244]]
provided by Novozymes, to convert the cellulosic waste materials to
simple sugars and eventually to ethanol. Fiberight has a unique enzyme
recycle and recovery process that allows them to affordably use high
concentrations of enzymes to increase the speed and conversion rate of
the cellulose to simple sugars. Fiberight plans to begin ethanol
production in the summer of 2010 and ramp up to full production
capacity of 5.7 million gallons of ethanol per year by late 2011. Based
on company estimates, EPA projects Fiberight could produce as much as
2.8 million gallons of cellulosic ethanol in 2011.
The fifth company that EPA is aware of with the potential to
produce cellulosic ethanol in 2011 is KL Energy Corporation. KL Energy
has a small facility in Upton, Wyoming that uses an enzymatic
hydrolysis process to convert wood chips and wood waste to ethanol.
This facility has a maximum annual production volume of 1.5 million
gallons and has been operational since the fall of 2007. Since KL
Energy completed construction on this facility they have been slowly
ramping up production and gathering information to optimize this and
future ethanol production facilities. KL has informed EPA that they
intend to produce 400,000 gallons of cellulosic ethanol from their
Upton, WY facility in 2011.
In addition to the five companies mentioned above, EPA is also
tracking the progress of more than 70 ethanol production facilities in
various stages ranging from construction to planning stages. Several of
these companies, including Abengoa, BlueFire Ethanol, Coskata, Fulcrum,
POET, and Vercipia all intend to begin the production and commercial
sale of cellulosic ethanol in 2012. These facilities range in maximum
production capacity from 10 to 100 million gallons of ethanol. EPA
anticipates a significant increase in the production and sale of
cellulosic ethanol in 2012, and strong continued growth in the
following years. In addition, if any of these or other companies
accelerates their production plans to make cellulosic biofuel available
for commercial sale in 2011, we will take those volumes into account in
our final rule.
2. Domestic Cellulosic Diesel
EPA is also aware of two companies in the United States with the
potential of producing cellulosic diesel fuel in 2011. The first of
these companies is Cello Energy. Cello Energy plans to use a catalytic
depolymerization process to produce diesel fuel from wood chips and
hay. Cello currently has a structurally complete facility in Bay
Minette, Alabama with an annual production capacity of 20 million
gallons of diesel per year. While having a structurally complete
facility puts Cello ahead of many other potential biofuel producers
they have yet to be able to produce biofuel at anywhere near the
production capacity. They are currently assessing feedstock preparation
and handling issues that must be resolved before they are able to again
attempt start up and production at this facility. If these issues are
successfully addressed EPA believes that Cello could, at most, produce
up to 5 million gallons (8.5 million ethanol equivalent gallons) of
cellulosic diesel fuel in 2011.
Another potential producer of cellulosic biofuel in 2011 is Bell
Bio-Energy. Bell Bio-Energy uses proprietary organisms to convert waste
materials to liquid fuels and compost in a single step. The company
currently has an agreement in place for the sale of the compost they
produce and are searching for a location for their first plant and a
partner to supply the waste materials they intend to use as feedstock.
The liquid fuel they produce is not a finished transportation fuel, but
could be upgraded to jet or diesel fuel. Bell Bio-Energy is currently
working with a refining company to analyze the fuel they produce and
determine the extent of upgrading necessary for the fuel to qualify as
transportation fuel. They plan to begin construction on their first
facility, which will have an annual fuel production capacity of 14.4
million gallons per year, as soon as a suitable site and partner are
found. The simplicity and low capital costs of Bell Bio-Energy's single
step production process allow them to construct plants very rapidly, in
as little as six weeks. This would make it possible for Bell Bio-Energy
to produce cellulosic biofuel in 2011 despite the fact that they have
not yet begun construction on their first commercial scale facility. It
is unclear when fuel will be produced at this facility, and whether it
would qualify under the RFS2 program. If Bell Bio-Energy is successful
in producing and upgrading their fuel EPA estimates the maximum volume
of fuel they could produce in 2011 would be 7 million gallons (11.9
million ethanol equivalent gallons) of jet or diesel fuel.
EPA is also tracking the progress of 17 other facilities that plan
to produce cellulosic diesel. Flambeau Rivers Biofuels, New Page, and
Terrabon are planning on opening commercial scale cellulosic diesel
facilities in 2012. Both Bell Bio-Energy and Cello have plans to build
additional facilities if their initial projects are successful. As with
cellulosic ethanol, cellulosic diesel production has the potential for
rapid growth in 2012 and the following years.
3. Other Domestic Cellulosic Biofuels
We are currently unaware of any companies in the United States
planning on producing cellulosic biofuel other than ethanol and diesel
and making it commercially available. EPA is currently tracking the
efforts of 10 companies that plan to produce fuels such as gasoline,
jet fuel, dimethyl ether (DME), and others. Many of these companies
have reported that they are still developing their technologies and
waiting for funding, and that they are not expecting to make any
cellulosic fuel commercially available until 2012 at the earliest.
There are several companies, such as Gevo and Virent, with small
demonstration facilities who intend to produce other fuels from
cellulosic feedstocks, but are currently optimizing their technology
with sugar or starch feedstocks. EPA anticipates that in the future
this may be a significant source of cellulosic biofuel, however we are
only expecting cellulosic ethanol and diesel to be produced in 2011.
4. Imports of Cellulosic Biofuel
In addition to the companies located in the United States, EPA is
also aware of two Canadian companies with the potential for cellulosic
biofuel production in 2011. If this fuel was imported into the United
States, these companies would be eligible to participate in the RFS2
program. Counting on cellulosic biofuel produced internationally in
setting the 2011 standard brings with it the additional uncertainty
associated with the fact that the fuel may be used locally rather than
imported into the United States.
Iogen uses a steam explosion pre-treatment process followed by
enzymatic hydrolysis to produce cellulosic ethanol from wheat, oat, and
barley straw. They have a demonstration facility with an annual
production capacity of 500,000 gallons of ethanol located in Ontario,
Canada. This facility has been operational and producing small volumes
of ethanol since 2004. So far all of the ethanol produced by this
facility has been used locally and in racing and other promotional
events. Iogen, however, is exploring the possibility of participating
in the RFS2 program. If they do decide to import ethanol to the United
States, EPA projects that they could provide as much as 250,000 gallons
of cellulosic ethanol in 2011 based on production volumes from previous
years.
[[Page 42245]]
Another Canadian company with the potential to produce cellulosic
ethanol in 2011 is Enerkem. Enerkem plans to use a thermo-chemical
process to gasify separated MSW and other waste products and then use a
catalyst to convert the synthesis (syn) gas into ethanol. Enerkem is
currently finishing construction on a 1.3 million gallon per year
facility in Westbury, Quebec and plans to begin producing ethanol in
the summer of 2010. They are also planning a 10 million gallon per year
facility in Edmonton, Alberta, however production from this facility is
not expected until 2012. Enerkem has informed EPA that they plan to
market ethanol they produce locally, and have no intentions to import
cellulosic ethanol into the United States. We are therefore not
projecting any available cellulosic fuel from Enerkem in 2011.
While Canada may be the most likely source of imported cellulosic
biofuels due to its close proximity, it is possible that cellulosic
biofuels produced in other countries may be imported into the United
States as well. Another potential source of cellulosic biofuel imports
is Brazil, due to its established ethanol industry and history of
importing ethanol into the United States. EPA is aware of several
companies exploring the possibility of cellulosic biofuel production in
Brazil; however none of these companies are likely to make cellulosic
biofuels commercially available in the United States in 2011. With the
exception of Iogen, as mentioned above, EPA has not projected imports
of cellulosic biofuels from outside the United States in 2011.
5. Summary of Volume Projections
The information EPA has gathered on the potential cellulosic
biofuel producers in 2011, summarized in Section II.A above, allows us
to project a maximum potentially available biofuel volume for each
facility in 2011. After the appropriate ethanol equivalence value has
been applied to the volumes of those facilities producing diesel fuel,
the overall maximum potentially available volume of cellulosic biofuels
for 2011 can be calculated by summing the maximum potential of each
facility. EPA is not proposing to set the 2011 cellulosic biofuel
standard at this maximum potentially available volume, rather this is
intended to serve as an upper bound. This information is summarized in
Table II.A.5-1 below.
Table II.A.5-1--Cellulosic Biofuel Maximum 2011 Potentially Available Volume
--------------------------------------------------------------------------------------------------------------------------------------------------------
Maximum 2011
Earliest potentially Ethanol
Company name Location Feedstock Fuel Capacity (MGY) production available equivalent
volume (MG) gallons (MG)
--------------------------------------------------------------------------------------------------------------------------------------------------------
AE Advanced Fuels Keyes....... Keyes, CA........ Corn, then Ethanol......... 20 June 2011........ 0.5 0.5
stover.
Agresti Biofuels.............. Pike County, KY.. MSW............. Ethanol......... 20 Oct. 2011........ 1 1
Bell Bio-Energy............... Atlanta, GA...... MSW or other Diesel Feedstock 14.4 June 2011........ 7 11.9
cellulosic
biomass.
Cello Energy.................. Bay Minette, AL.. Wood, hay....... Diesel.......... 20 Online........... 5 8.5
DuPont Danisco \a\............ Vonore, TN....... Corn cobs, then Ethanol......... 0.25 Online........... 0.15 0.15
switchgrass.
Fiberight \a\................. Blairstown, IA... MSW............. Ethanol......... 6 April 2010....... 2.8 2.8
Iogen......................... Ottawa, Ontario.. Wheat, oat & Ethanol......... 0.5 Online........... 0.25 0.25
barley straw.
KL Energy \a\................. Upton, WY........ Wood............ Ethanol......... 1.5 Online........... 0.4 0.4
�������������������������������
Total..................... ................. ................ ................ .............. ................. 17.1 25.5
--------------------------------------------------------------------------------------------------------------------------------------------------------
\a\ Maximum Production/Import Potential represents company estimate.
It is important to note that this maximum potentially available
volume of 17.1 million gallons of cellulosic biofuel, or 25.5 million
ethanol equivalent gallons, is not the volume on which the final 2011
cellulosic biofuel standard will be based. This number represents the
maximum amount of fuel EPA believes could reasonably be expected to be
produced or imported and made available for use as transportation fuel,
heating oil, or jet fuel in 2011. It incorporates some reductions from
the annual production capacity of each facility based on when the
facilities anticipate fuel production will begin and assumptions
regarding a ramp up period to full production. However, as stated
earlier, in order for this volume of cellulosic biofuel to be produced
in 2011, each of the companies listed in Table II.A.5-1 would have to
achieve their production targets in their projected timeframes. The
history of the cellulosic biofuels industry has many examples of delays
in achieving full production capacity in new facilities. Also, there
are many other factors that increase the uncertainty of fuel production
facilities being able to achieve their maximum potential production.
These factors may include:
Difficulty/delays in securing necessary funding.
Delays in permitting and/or construction.
Difficulty in scale up, especially for 1st of their kind
technologies.
Volumes from pilot and demonstration plants may not be
sold commercially.
Not all feedstocks may qualify to produce cellulosic RINs;
some still awaiting evaluation of lifecycle impacts.
Likelihood that fuels produced internationally will be
exported to the United States rather than consumed locally.
Each of the facilities listed in Table II.A.5-1 may experience some
of the difficulties listed above, and as a result may produce a volume
of fuel less than that listed as their maximum 2011 potentially
available volume. Despite this uncertainty, EPA believes that the
volume of cellulosic biofuel produced in 2011 will, at minimum, be able
to meet or exceed the 2010 standard of 6.5 million ethanol equivalent
gallons. However, we will have more detailed and accurate information
for the final rule, including the first round of Production Outlook
Reports, due on
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September 1, 2010 \5\ which will provide information from each producer
or importer on the type or types of fuel they plan to make available,
the volume of fuel, and the number of RINs they plan to generate for
the next five calendar years.\6\ Therefore, in today's NPRM we are
proposing a range of values, from a minimum of 6.5 million ethanol
equivalent gallons to a maximum of 25.5 million ethanol equivalent
gallons for the 2011 cellulosic biofuel standard. As time progresses
and we are able to track whether or not the cellulosic biofuels
producers are able to meet the construction and ramp up schedules they
have presented, we will have a better idea of the appropriate volume of
fuel that we can reasonably expect to be produced and made commercially
available in 2011. Additionally, each year by October 31 EIA is
required to provide an estimate of the volume of cellulosic biofuel
they expect to be sold or introduced into commerce in the United States
in the following year. EPA will consider this information as well when
finalizing a single volume for use in setting the 2011 cellulosic
biofuel standard.
---------------------------------------------------------------------------
\5\ In future years, Production Outlook Reports will be due on
March 1. As a result, they may be considered during development of
the NPRM in year 2011 and beyond.
\6\ For more information on the annual production outlook
reports see Sec. 80.1449 of the RFS2 regulations.
---------------------------------------------------------------------------
Although we are currently projecting that the potentially available
volume of cellulosic biofuel in 2011 will be in the range of 6.5 to
25.5 million ethanol-equivalent gallons, we expect that volumes of
cellulosic biofuel will increase rapidly in the years following 2011.
As stated before, we are aware of more than 100 companies that are
actively investigating or making plans to produce cellulosic biofuel in
the near future. Many of these companies intend to begin construction
in 2011 or 2012. We will be monitoring these companies carefully as we
project the potential volumes of cellulosic biofuel for years 2012 and
beyond.
B. Potential Limitations
In addition to production capacity, a variety of other factors have
the potential to limit the amount of cellulosic biofuel that can be
produced and used in the U.S. For instance, there may be limitations in
the availability of qualifying cellulosic feedstocks at reasonable
prices. Most of the cellulosic biofuel producers that we project will
produce commercial volumes in 2011 have indicated that they will use
some type of cellulosic waste, such as separated municipal solid waste,
wastes from the forestry industry, and agricultural residues. Based on
the analyses of cellulosic feedstock availability in the RFS2 final
rule, we believe that there will be significantly more than enough
sources of these feedstocks for 2011. For producers that intend to use
dedicated energy crops, we do not believe that the availability of
existing cropland will limit production in 2011. We plan to continue to
evaluate the availability of valid feedstocks in future years as the
required volumes of cellulosic biofuel increase.
Another factor that has the potential to limit the amount of
renewable fuel that can be produced and used in the U.S. is
distribution and storage capacity. In the longer term, most biofuels
are expected to be produced in the heartland of the country and then be
shipped towards the coasts, flowing roughly in the opposite direction
of petroleum-based fuels. The physical and chemical nature of many of
these biofuels may limit the extent to which they can be shipped and/or
stored fungibly with petroleum-based fuels. As a result, new and
expanded rail, barge and tank truck transport will need to be put in
place. Dedicated biofuels pipelines are also being investigated. For
instance, a short gasoline pipeline in Florida is currently shipping
batches of ethanol.\7\ Evaluations are also currently underway
regarding the feasibility of constructing a new dedicated ethanol
pipeline from the Midwest to the East coast.\8\ However, for 2011 the
volumes of cellulosic biofuel are small enough that long-distance
transport will be unnecessary; with the exception of foreign-produced
biofuels, much of the cellulosic biofuel volumes can be consumed in
regions close to their production facilities. We also expect existing
distribution and storage capacity to be sufficient to accommodate