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115/22/2006
Future Opportunities for Biomass Fuels and Power
Dr. Richard L. Bain, Principal EngineerBiorefinery Analysis & Exploratory Research GroupNational Bioenergy Center
SmallWood 2006
Richmond, VA
May 16, 2006
5/22/2006 2
Disclaimer and Government License
This work has been authored by Midwest Research Institute (MRI) under Contract No. DE-AC36-99GO10337 with the U.S. Department of Energy (the “DOE”). The United States Government (the “Government”) retains and the publisher, by accepting the work for publication, acknowledges that the Government retains a non-exclusive, paid-up, irrevocable, worldwide license to publish or reproduce the published form of this work, or allow others to do so, for Government purposes.
Neither MRI, the DOE, the Government, nor any other agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe any privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not constitute or imply its endorsement, recommendation, or favoring by the Government or any agency thereof. The views and opinions of the authors and/or presenters expressed herein do not necessarily state or reflect those of MRI, the DOE, the Government, or any agency thereof.
5/22/2006 3
Biomass Share of U.S. Energy Supply (2004 data)
Source: Renewable Energy Trends 2004; Energy Information Administration, August 2005.Note: Total U.S. Energy Supply is 100.278 QBtu; Energy Information Administration, August 2005.
Biomass 47%
Wind 2%
Hydroelectric 45%
Geothermal 5%Solar <1%
Renewable 6%
Natural Gas 23% Nuclear 8%
Petroleum 40% Coal 23%
5/22/2006 4
United States Biomass Consumption in 2004(Quadrillion Btu)
Reference: Annual Energy Outlook 2006, Energy Information Administration, Table A17
Commercial0.09
Residential0.41
Ethanol0.28
Electric Power0.44
Industrial1.63
5/22/2006 5
U.S. Biopower Generation, 1981-2004
Year1980 1985 1990 1995 2000 2005
Gen
erat
ion
(TW
h/an
num
)
0
10
20
30
40
50
60
70
Net
Sum
mer
Cap
acity
(MW
)
0
2000
4000
6000
8000
10000
12000
Generation Capacity
5/22/2006 6
Ethanol Production
0123456789
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
2011
2012
Cellulosic Ethanol2005 EPACT RFS - MinimumU.S. Ethanol Production
• Renewable Fuels Standard mandates 7.5 billion gallons by 2012• Total US gasoline market ~140 billion annual gallons
Actual and Projected U.S. Ethanol Production 1999-2012Billion Gallons of Production
Source: December 2005 Ethanol Today Magazine
5/22/2006 7
U.S. Biodiesel Production
0
10
20
30
40
50
60
70
80
1999 2000 2001 2002 2003 2004 2005
U.S
. Pro
duct
ion,
m
illio
n ga
llons
per
yea
r
Total US distillate fuels market is approximately 60 billion gallons per year
5/22/2006 8
Biomass StrengthsBiomass is:
AbundantRenewableCarbon-neutralThe only sustainable source of hydrocarbons.
Biomass can:
Fill the gap between energy demand and petroleum availability in the near term.Be a renewable source of hydrogen in the long term.
5/22/2006 9
Sources of Lignocellulosic Biomass
38-50%5-13%
23-32%15-25%
Lignin
OtherCellulose(Glucose sugar)
Hemicellulose(Pentose sugars)
(“Young clean coal”)
Softwoods
Grasses
Hardwoods
Crop residues
MSW
(Extractives, ash, etc.)
5/22/2006 10
U.S. Biomass Resource Potentials Corn (largest volume grain and source of EtOH in U.S.)
Potential to displace 10-20% of our gasoline
Soybeans, fats & greases (largest sources of biodiesel)Potential to displace 5-10% of our diesel
Over 1 billion tons/year of lignocellulosic biomass (trees, grasses, etc.) could be available in the U.S.
Potential to displace 50-70% of our gasoline
Short-term: improve cost and efficiency of corn ethanol & biodieselMid to Long-term: focus on lignocellulose (trees, grasses, & residues)
FoodFoodSuppliesSupplies
Not a FoodNot a FoodSupplySupply
5/22/2006 11
U.S. Biomass Resource Assessment• Updated resource assessment - April 2005• Jointly developed by U.S. DOE and USDA• Referred to as the “Billion Ton Study”
5/22/2006 12
Based on ORNL & USDA Resource Assessment Study by Perlach et.al. (April 2005) http://www.eere.energy.gov/biomass/pdfs/final_billionton_vision_report2.pdf
The 1.3 Billion Ton Biomass ScenarioBillion Barrel of Oil Equivalents
5/22/2006 13
Chemical Conversion
Lignocellulosics (polysaccharides)
Hydrolysis
Sugars
Fermentation
Lignin
Pretreatment
Starches
Primary Conversion Routes for “Biomass”
Combustion
Gasification/Pyrolysis
5/22/2006 14
Chemical industry investing in higher value products from glucose
NatureWorks LLCduPont
Both corn ethanol and chemical industries are investigating biomass to extended sugar resources
Shell investing in biomass ethanol technology (Iogen, Canada)
300 dry ton/day gasifier at
Burlington Electric, VT
Cargill Dow Dedicates PLA Refinery April 2002
•Ethanol industry at 4 billion gal/yr based on corn starch•Corn mills investing in process improvements and higher value products
–ADM–Broin–Abengoa
EthanolEthanol
5/22/2006 15
The Structures are Very DifferentGlucose
Xylose
G
Lignin
Sugars:
Polysaccharides in Lignocellulosic Biomass:
X
Starches: GlucoseGlucose
5/22/2006 16
Biochemical Conversionfor Ethanol via PT/Hyd/Ferm
SSF
Simultaneous saccharification & Fermentation - SSF
Fermentationof C5 & C6
SugarsConditioning
5/22/2006 17
Cost of Ethanol via PT/Hyd/Ferm
$0.00
$1.00
$2.00
$3.00
$4.00
$5.00
$6.00
2000 2005 2010 2015 2020
Min
imum
Eth
anol
Sel
ling
Pric
e ($
/gal
)
State of Technology Estimates
Feed $53/ton
2005 Yield65 gal/ton
Feed $35/tonYield 90 gal/ton Feed $35/ton
Yield 104 gal/ton
Costs in 2002 Dollars
EnzymeConversionFeedstockCurrent DOE Cost TargetsPresident's Initiative
Integrated large-scaleBC/TC processing
5/22/2006 18
Griffin Industries, USA and Bruck Industries, Austria
BiodieselBiodiesel
Sep 2004: 60 Mil gal/yr dedicated capacity in U.S.
5/22/2006 19
Biodiesel - Basic TechnologyVegetable oils Recycled Greases
Dilute AcidEsterification
Transesterification
Crude Glycerin
Refining
Crude biodiesel
Biodiesel
Sulfur +methanol
Methanol + KOH
Glycerinrefining
Glycerin
Methanolrecovery
5/22/2006 20
Oils, Fats & Greases as Bio-renewable Petroleum Refinery Feedstocks
• Co-processing of oils and greases with petroleum fractions
• Utilize existing process capacity
• Potential for lower conversion costs (than FAME)
• Higher quality diesel blending component
• G/D flexibility
CatalyticCracker
DistillateHydrotreater
Oils andGreases
Green Gasoline& Olefins
GreenDiesel
ISBL Petroleum Refinery
Based on Presentations at 1st International Biorefinery Workshop, Washington DC, July 20-21, 2005- Future Energy for Mobility, James Simnick, BP- From Bioblending to Biorefining, Veronique Hervouet, Total- Opportunities for Biorenewables in Petroleum Refineries, Jennifer Holmgren, UOP
5/22/2006 21
Green Diesel and Biodiesel Yields
12% glycerol
83-8696% diesel
.025.05Operating cost $/gal
8.7% methanol
100
Biodiesel
12-16% water,C02
Green DieselFeed
2-5
1.5-3.8
100
% Lt HC
Products
% H2
% Oil or Grease
Marinangeli, R., et.al. (2005). “Opportunities for Biorenewables in Oil Refineries: Final Technical Report,” UOP, Des Plaines, IL; DOE Report No. DE-FG36-05GO15085.
5/22/2006 22
Diesel Properties
.78.883Density g/ml
0 to -100 to +10 % change in NOx emission
265-320340-355Distillation 10-90% pt
<10ppm<10ppmSulfur content4438Heating Value (lower) MJ/kg
011% Oxygen
-5 to -30-5 Cloud Point oC
80-9050Cetane
Green DieselBiodiesel (FAME)
Marinangeli, R., et.al. (2005). “Opportunities for Biorenewables in Oil Refineries: Final Technical Report,” UOP, Des Plaines, IL; DOE Report No. DE-FG36-05GO15085
5/22/2006 23
Gasification Cleanup Synthesis
Conversionor Collection Purification
Separation Purification
Pyrolysis
OtherConversion*
Biomass
Biomass Thermochemical Conversionfor Fuels and Chemicals PRODUCTS
• Hydrogen• Alcohols• FT Gasoline• FT Diesel• Olefins• Oxochemicals• Ammonia• SNG
• Hydrogen• Olefins• Oils• Specialty Chem
• Hydrogen• Methane• Oils• Other
5/22/2006 24
Fuels from Syngas
SyngasCO + H2
Bottom Ash Removal
InjectorScrews
High/Low PressureGasifier
Cyclone(Optional)
AIR/O2
BARK & SLUDGE
O2/AIR / STEAM
Fluidized Bed
Freeboard Disengaging Zone
SYNGAS
Bottom Ash Removal
InjectorScrews
High/Low PressureGasifier
Cyclone(Optional)
AIR/O2
BARK & SLUDGE
O2/AIR / STEAM
Fluidized Bed
Freeboard Disengaging Zone
SYNGAS
Acetic Acid
Formaldehyde
MTBE
PolypropyleneAcrylonitrile
PolyethyleneEthylene Glycoll h l f
Ammonia Diesel Additives
Ethanol
Mixed Alcohols
Methanol
Olefins
Refineries
Hydrogen
Urea
Fischer Tropsch FuelsWaxAlpha-olefins
DME
5/22/2006 25
PreliminarySeparation
C3 +
Alcohols
Mixed AlcoholSynthesis
260-350°C30-175 bar
Alkali promotedMoS2 catalyst
SyngasCompression
CrudeProducts
High PSyngas
ScrubbedSyngas
EthanolMixed
Alcohols
MethanolRecycle
ProductSeparation
Thermochemical Conversionfor Ethanol via Gasification
5/22/2006 26
Cost of Ethanol via Gasification
$0.00
$0.50
$1.00
$1.50
$2.00
$2.50
2000 2005 2010 2015 2020
Min
imum
Eth
anol
Sel
ling
Pric
e ($
per
gal
lon)
ConversionFeedstockPrevious DOE Cost TargetsPresident's Initiative
State of Technology Estimates
Integrated with Biochemical Processing
104 gal/ton total yield
Biorefinery Residues67 gal/ton
Costs in 2002 Dollars
ForestResources56 gal/ton
5/22/2006 27
Fast Pyrolysis of BiomassFast pyrolysis is a thermal process that rapidly heats biomass to a carefully controlled temperature (~500°C) and then very quickly (<2 sec) cools the volatile products formed in the reactor.Fast pyrolysis:
Offers the unique advantage of producing a liquid that can be stored and transportedHas been developed in many configurationsAt present is at relatively early stage of development.
5/22/2006 28
Electricity Transport Fuel
Heat
Bio -oil
Extract
UpgradeBoiler
Applications of Bio Oils
Chemicals
5/22/2006 29
Bio-oil is water miscible and is comprised of many oxygenated organic chemicals.
• Dark brown mobile liquid,• Combustible,• Not readily miscible with hydrocarbons,• Heating value ~ 17 MJ/kg,• Density ~ 1.2 kg/l,• Acid, pH ~ 2.5,• Pungent odour,• “Ages” - viscosity increases with time
Fast Pyrolysis and Bio-oil as Feed to Power Plant or Petroleum Refinery
Based on research at NREL (1990 - 2000), Colin Schaverien presentation
5/22/2006 30
Other Productsof Interest:• Heating oil• PF resins• FCC feed• DDU feed
Variation of Pyrolysis-based Biorefinery
Aromatic Chemicals and/or
Gasoline Blending
Fermentation orHydrogenation ofAqueous Phase (Carbohydrates)
Fast Pyrolysis Of Biomass
Fractionation and/or
Deoxygenation
LigninDerivatives
CarbohydrateDerivatives
5/22/2006 31
DOE Goal: 30 by 30 - Replace 30% of Today’s Gasoline in 2030 with Biofuels
5/22/2006 32
Integrated Biorefinery Elements
5/22/2006 33
Ethanol via bioconversion
Corn Stover 10,000 dMT/day
Ethanol1,035,000 gpd
Lignin-rich Residue 2,932 dMT/day
Steam &Power
Coal-FiredCHP Plant
GasificationAlcohol
Synthesis
Chemical Alcohols
SyngasEthanol
215,400 gpd
Ethanol1,250,400 gpd
438.0 MM gal/yrCoal
MESP = $0.60/gal EtOH
gpd (gal/dry ton lignin)7,900 Methanol (2)
39,100 n-Propanol (12)15,100 n-Butanol (5)6,900 n-Pentanol (2)
Ethanol yield = 113 gal/dry ton stover
Integrated Biorefinery
5/22/2006 34
For More Information About
The National Renewable Energy Laboratory: www.nrel.gov
DOE’s Biomass Program:
http://www.eere.energy.gov/biomass/
Alternative Fuels:
www.afdc.doe.gov