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Production of Drop-in fuels from cellulosic biomass
Jesse Q. Bond, Syracuse University
UC Riverside, UMASS Amherst, UW Madison, U Delaware
Pacific Rim Biotechnology Summit
December 9, 2013
Overview
• Conceptual illustration of the challenges of drop in fuel production
• Deconstruction/Reconstruction
• Key functional groups in biomass conversion • Oxygen Removal
• C-C bond formation
• Outline a xylan/cellulose based strategy for heavy fuel production
Lignin
Hemicellulose
40-50%
25-35%
15-20%
Cellulose
Lignin
Hemicellulose
40-50%
25-35%
15-20%
Cellulose
Gasoline
Diesel Fuel
Jet Fuel
Lignin
Hemicellulose
25-35%
15-20%
40-50%
Cellulose
Gasoline
Diesel Fuel
Jet Fuel
Lignin
Hemicellulose
25-35%
15-20%
40-50%
Cellulose
Challenges
• Solid, polymeric feedstock
• High Oxygen content
• Relatively small monomers
• Complex!
Gasoline
Diesel Fuel
Jet Fuel
Cellulose
Gasoline
Diesel Fuel
Jet Fuel
Sugars
xylose
glucose
Primary Intermediates
furfural
5-HMF
levulinic acid
Secondary Intermediates
40-50%
25-35%
15-20%
Depolymerize (Hydrolysis)
Partial Oxygen removal C-C bond formation De-functionalization
Primary functional groups
Hydroxyls Carbonyls Alkenes
Heterocycles
Primary functional groups
Hydroxyls
Sugars
Polyols
Alcohols
Carbonyls Alkenes
Heterocycles
Primary functional groups
Hydroxyls
Sugars
Polyols
Alcohols
Carbonyls
Aldehydes
Ketones
Carboxylic acids
Alkenes
Heterocycles
Primary functional groups
Hydroxyls
Sugars
Polyols
Alcohols
Carbonyls
Aldehydes
Ketones
Carboxylic acids
Alkenes
Heterocycles
2-Butene ethylene
Primary functional groups
Hydroxyls
Sugars
Polyols
Alcohols
Carbonyls
Aldehydes
Ketones
Carboxylic acids
Alkenes
Heterocycles
2-Butene ethylene
MTHF DMTHF
Oxygen Removal (C-O bond cleavage) Dehydration
H+
T > 150 ○C + H2O
Oxygen Removal (C-O bond cleavage) Dehydration
H+
H+
H+
T > 150 ○C
T > 100 ○C
T > 100 ○C
+ H2O
+ H2O
+ H2O
Oxygen Removal (C-O bond cleavage)
• Acid catalyzed reactions
• Any number of materials • Aluminosilicates (SiO2-Al2O3)
• Sulfonated resins (A70)
• Mineral acids (H2SO4)
Dehydration
H+
H+
H+
T > 150 ○C
T > 100 ○C
T > 100 ○C
+ H2O
+ H2O
+ H2O
Oxygen Removal (C-O bond cleavage) Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2
Ni, Pt, Ru
Oxygen Removal (C-O bond cleavage) Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2
Ni, Pt, Ru
+H2
Ni, Pt, Ru
+2H2, -H2O
Ni, Pt, Ru
Oxygen Removal (C-O bond cleavage) Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2
Ni, Pt, Ru
+H2
Ni, Pt, Ru
+2H2, -H2O
Ni, Pt, Ru
-H2O
-H2O
-H2O
H+
H+
H+
Oxygen Removal (C-O bond cleavage) Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2
Ni, Pt, Ru
+H2
Ni, Pt, Ru
+2H2, -H2O
Ni, Pt, Ru
-H2O
-H2O
-H2O
H+
H+
H+
+H2
Ni, Pt, Ru
+H2
Ni, Pt, Ru
+H2
Ni, Pt, Ru
Oxygen Removal (C-O bond cleavage) Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2, -H2O
Pt,Ru,Ni
+H2, -H2O
Pt, Ru, Ni
+3H2, -2H2O
RuCu, CuCrO4
Oxygen Removal (C-O bond cleavage)
• Hydrodeoxygenation • Hydrogenation (Metals)
• Saturation of C=C bonds • Convert C=O to C-OH • Cleave C-OH bonds via hydrogenolysis
• Dehydration (Acids) • Cleaves C-OH bonds • Forms C=C bonds
• Bifunctional Catalyts • Pt/SiO2-Al2O3
Hydrogenation, Hydrogenolysis, and Hydrodeoxygenation
+H2, -H2O
Pt,Ru,Ni
+H2, -H2O
Pt, Ru, Ni
+3H2, -2H2O
RuCu, CuCrO4
Oxygen Removal (C-C bond cleavage) Decarboxylation and Decarbonylation
+ CO2 Decarboxylation
H+ or metal catalyzed
Oxygen Removal (C-C bond cleavage) Decarboxylation and Decarbonylation
+ CO + H2O
+ CO2 Decarboxylation
H+ or metal catalyzed
Decarbonylation H+ or metal catalyzed
Oxygen Removal (C-C bond cleavage)
+2H2, -H2O
Ni, Pt, Ru
-H2O
H+
+H2
Ni, Pt, Ru
Decarboxylation and Decarbonylation
+ CO + H2O
+ CO2 Decarboxylation
H+ or metal catalyzed
Decarbonylation H+ or metal catalyzed
xylose
glucose
furfural
5-HMF levulinic acid
Production of primary platforms
xylans H+
+H2O
H+
-3H2O
H+
-3H2O
H+
+2H2O, -HCOOH
H+
+H2O
cellulose
xylose
glucose
furfural
5-HMF levulinic acid
Production of primary platforms
xylans H+
+H2O
H+
-3H2O
H+
-3H2O
H+
+2H2O, -HCOOH
H+
+H2O
cellulose
Options for FFA and LA?
Aldol Condensation Base catalyst
Furfural Furfural Upgrading
Aldol Condensation Base catalyst
Furfural
Aldol Condensation Base catalyst
Furfural Upgrading
Aldol Condensation Base catalyst
Furfural
Aldol Condensation Base catalyst
Linear Alkanes C8 – C13
Metal
H2
Metal
Metal/Acid
H2
H2
Furfural Upgrading
Aldol Condensation Base catalyst
Furfural
Aldol Condensation Base catalyst
Linear Alkanes C8 – C13
Metal
H2
Metal
Metal/Acid
H2
H2
Furfural Upgrading
Aldol Condensation Base catalyst
Furfural
Aldol Condensation Base catalyst
Linear Alkanes C8 – C13
Metal
H2
Metal
Metal/Acid
H2
H2
Furfural Upgrading
Levulinic Acid
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
g-valerolactone
Levulinic Acid
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
g-valerolactone Pentenoic acid
Levulinic Acid
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
H+
g-valerolactone Pentenoic acid
Levulinic Acid
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
H+ H+
-CO2
g-valerolactone Pentenoic acid
Levulinic Acid Branched Alkanes
C12 – C20
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
H+ H+
-CO2
H+
Ni, Pt, Pd, Ru H2
g-valerolactone Pentenoic acid
Levulinic Acid Branched Alkanes
C12 – C20
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
H+ H+
-CO2
H+
Ni, Pt, Pd, Ru H2
g-valerolactone Pentenoic acid
Levulinic Acid Branched Alkanes
C12 – C20
Levulinic Acid Upgrading
4-HPA
+H2 Ru/C
-H2O H+
H+ H+
-CO2
H+
Ni, Pt, Pd, Ru H2
Summary of xylan/glucan pathway
• Furfural fuel yields presently 80% of theoretical maximum • Limiting yield: xylan losses during pretreatment
• LA fuel yields presently 70% of theoretical maximum • Relatively low selectivity in LA production
• Preliminary economics are not competitive with petroleum • Also not astronomical (MSP ~ $5.00 /gallon)
• Warrants future consideration as a pathway to distillates
Acknowledgements
• Charles Wyman (UCR) • Taiying Zhang • Rajeev Kumar
• Jim Dumesic (UW) • David Martin Alonso
• George Huber (UW) • Ani Upadhye
• Raul Lobo (UD) • Andrew Foster
• Geoff Tompsett (WPI)
• DARPA, DOE
Acknowledgements This work was supported through funding from the Defense Advanced Research Projects Agency (Surf-cat: Catalysts for Production of JP-8 range molecules from Lignocellulosic Biomass). The views, opinions, and/or findings contained in this article/presentation are those of the author/presenter and should not be interpreted as representing the official views or policies, either expressed or implied, of the Defense Advanced Research Projects Agency or the Department of Defense. In addition, this work was supported in part by the U.S. Department of Energy Office of Basic Energy Sciences and the New York State Energy Research and Development Authority (NYSERDA). References Bond, J.Q., Martin Alonso, D., and Dumesic, J.A., “Catalytic strategies for the conversion of lignocellulosic carbohydrates to fuels and chemicals,” in Aqueous Pretreatment of Plant Biomass for Biological and Chemical Conversion to Fuels and Chemicals, Wyman CE, Ed, Wiley Blackwell, Oxford, UK, 2013 Martin Alonso, D., Bond, J.Q., and Dumesic, J.A., “Catalytic Conversion of Biomass to Biofuels,” Green Chemistry, 2010, 12, 1493–1513. Bond, J.Q., et. al., Production of renewable jet fuel range alkanes and commodity chemicals from integrated catalytic processing of biomass, Energy and Environmental Science, In review.