Catalysis for the Biorefinery.pdf
Transcript of Catalysis for the Biorefinery.pdf
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These slides were presented at the NSF Catalysis for Biorenewables
Conversion Workshop, held in Arlington, Virginia on April 13 and 14,
2004. These slides may not be altered or reproduced for
distribution. Any use of these slides must include an acknowledgment
of the author, their affiliation, and the National Science Foundation.
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Cameron, Cargill NSF Catalysis for Biorenewables Conversion Workshop
Catalysis for the Biorefinery
Douglas C. Cameron
NSF Workshop onCatalysis for
Biorenewables
Conversion
April 13, 2004
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Overview of Cargill
Founded in 1865 Private ownership
>95,000 employees
~65 countries
88 business units
>1,000 locations ~$60 billion in sales
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Agricultural
Value chainfood
feed Biobased
matls
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HydrocarbonTypical synthetic process
oil, gas
naphtha, gas
ethylene, propylene,
butadiene
acrylic, acetic,
maleic, propionic,
propylene oxide,
butanol
CarbohydrateTypical bioprocess
corn/ biomass
starch/ cellulose
Glucose/
other sugars
citric, itaconic, lactic
(PLA), Isosorbide, 3HP
Vegetable OilsTypical process
soybean
oil
fatty acids
soy polyols,
polymerintermediates
Industrial Products
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Cargill Biorefinery, Eddyville, Iowa
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Cargill Biorefinery, Blair, Nebraska
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Cargill Dow (CD) polymer plant, Blair, NE
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Drivers for the Bio-Industrial Revolution
Better products for consumers
More economical for industryand consumers
More dependable, renewableand lower-cost feedstocks
More environmentally friendlyproducts/processes; smallerenvironmental footprint
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Enabling the Bio-Industrial Revolution
Feedstock prices will continue to drop in realterms- Improvements in agronomic practices
- Biomass conversion technologies
Processing technology must evolve- Government must invest in basic research
- Industry must commit to invest and develop process technologyrelated to aqueous processing of dilute solutions
- New catalysts, both biological and chemical, are required
- Novel combinations of catalytic steps is needed
Product development is critical- Platform chemical concept
- Partnerships between traditional chemical and agricultural firms willneed to emerge
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Renewable Feedstocks will become
competitive with petrochemical feedstocks
0
10
20
30
40
50
60
70
80
73 75 77 79 81 83 85 87 89 91 93 95 97 99 01 03
0
5
10
15
20
25
30
35
40
Glucose Price (cents/pound)
Oil Price
($/barrel)
Crude Soybean Oil
(cents/pound)
Soyb
ean
oil,glu
cose
(cents/pound)
Oil($/barrel)
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Impact of Processing Improvements
Today Future
Processing
Gra
in
Fermentation
Feedstocks
?
Relative Cost
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Current Cargill BiorefineryIndustrial
ProductsProcessing Refining Intermediates
Citric acid
Itaconic
LysineLactic acid
Ethanol
*3-HP
*Isosorbide
Oil
Lubricants
CoatingsPolyols
Plasticizers
Thermoplastics
Urethanes
Specialtypolyesters
Monomers
Plastic
intermediates
Feedstocks:
Corn
SoyWheat
Palm
Canola Oil
Sugar
SunflowerFlax Oil
Biomass
Carbohydrate
Modified
Starches
Glucose
Protein,
Fiber
Food &
Feed
FermentationFeedstocks
Fatty acids
Glycerol
* Intermediates under development
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Vegetable oil-based examples
Current business
(Industrial Oils and Lubricants)
Emerging applications
Soybean Oil
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Industrial Oils and Lubricants
Base oils and esters
Formulated Hydraulic Fluids
Agri-SperseTM
Water Dispersable Lubricants
OxicureTM Coatings
BioTrans Transformer Dielectric Oils
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Emerging Applications of Vegetable oils
VegetableOil
Urethanepolyols
Fatty acids(biodiesel)
Glycerol
Olefins
9-decenoicAcid (9DA)
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Billions of Pounds (MDI, TDI, Polyether Polyol)
3.5
3.0
2.5
2.0
1.5
1.0
0.5
0
4.0
`62 `64 `66 `68 `70 `72 `74 `76 `78 `80 `82 `84 `86 `88 `90 `92 `94`54 `56 `58 `60 `96`98 `00 02
4.5
5.0
Flexible foams
CASE
Rigidfoams
US Polyurethane MarketCameron, Cargill NSF Catalysis for Biorenewables Conversion Workshop
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Urethane Polyols
2.5 billion pounds per year of urethanepolyols are sold in the US each year
capacity expansion for propylene oxide-basedpolyether polyols require huge capital investments
and raw material prices are under constantupward pressure.
Cargill Industrial Bioproducts is developingoil-based alternative to PO-based polyols withimproved performance at cost parity or better
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Metathesis chemistry applied to vegetable oils
Rubber, latex,polymersdienes
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Unsaturatedfatty acids
H2C=CH2
LLDPE,synthetic
lubricants
-olefins
9-decenoic(9DA)
Severalapplications
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Advances driven by new catalyst technology
RuCl
Cl
PR3
PR3Ru
Cl
Cl
PR3
NN
N
CHC(CH3)2Ph
MoCH3(CF3)2CO
CH3(CF3)2CO
CH(CH3)2
(CH3)2CH
Schrock catalyst Grubbs catalyst 2nd GenerationGrubbs catalyst
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Metathesis Catalyst Platform ConceptMetathesis Catalyst Platform Concept
9 - Decenoic
Amino Decanoic(Nylon 10)
Decanol
(Solvents, Plasticizers, Surfactants)
C-18 Diacid(Polymers)
Epoxy Resins
(Coatings)
Sebacic
(Nylon 6, 10)
Capric
(Surfactant, Synthetic Lube)
10, 11-Dioctyleicosane
(Lubricant)
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Carbohydrate-based examples
Glucaric acid
3-hydroxypropionic acid (3-HP)
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OH
OH
OH
O
HO
OH
HO
HO
OH
OH
OH
OH
(OH)2OPO
(OH)2OPO
OPO(OH)2
OPO(OH)2
OPO(OH)2
OPO(OH)2
COOH
OH
OH
OH
O
OH
HOOC
COOH
OH
HO
OH
OH
Enzyme catalysis?
Chemical catalysis?
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Phytic acid
glucose
inositol
Glucaric acid
Glucuronic acid
Phytase
or
Acid catalysis
fermentation
Chemical
or
Enzyme
Oxidation
Myo-inositol
oxygenase
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PLA
CH3-CH-COOH|
OH
GlucoseEsters
Propyleneglycol
100%theoretical yield
anaerobic2-hydroxypropionicacid (lactic acid)
3-hydroxypropionic
acid
CH2-CH2-COOH|
OH
Glucose?
?
?
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3-HP
Glucose
Pyruvate
Lactate
Malonyl-CoA
Glycerol
-alanine
Metabolic pathway design
Design criteria: Energetics Maximum theoretical yield Availability of enzymes / genes Co-factor requirements of enzymes Intellectual property/FTO
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Directed evolution from known enzyme with similarfunction
Lysine 2,3-aminomutase
Lysine 5,6-aminomutase
Find natural aminomutase Anaerobic enrichment on -alanine as sole carbon source
Approaches to getting alanine 2,3-
aminomutase
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Structural relationship between lysine and
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Structural relationship between lysine and
alanineNH2
H2NO
OH
NH2
O
OH
-lysine-alanine
Lysine 2,3-
aminomutase
Alanine 2,3-
aminomutase
O
OHNH2
O
OHNH2
-alanineH2N -lysine
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Microbial catalysis/fermentation
Chemicalcatalysis
Derivativesof 3HP
Glucose 3HP
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Application of 3-HP: High Solubility of 3HP Ca++ salt
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pp g y
0.1 0.4 1.1 1.2 7
3550
100
0
20
40
60
80
100
120
citrate
malate
citrate-m
alate
glycolate
lactate
acetate
propionate
3H
P
gramsof
salt/100mlwater
>
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O O
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OH
O
OH
n
O
O OHO OH
1,3-propanediol
EEPhydrogenation
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CH2 OH
O
CH2NH2
O
3-hydroxypropionic acid
poly(hydroxypropionate)HO OH
O
oxidation
dehydrationHO OH
OOacrylamide
malonic acid
acrylic acid
Corn or other
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Corn or other
biomass
Chemical andenzymatic
Glucose
Fermentation (metabolic engineering)
3-HP
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Poly 3-HP
microbial
Acid andpowdered
copperMn-promoted
copper
Malonic acidPd and Pt
Acrylic acid 1,3-propanediol
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syncretic
\Syn*cret"ic\, a. Uniting and blending
together different systems, as of
philosophy, morals, or religion.
The biorefinery requires the blending together of different systemsof chemistry and catalysisheterogeneous, homogeneous,
enzymatic, microbial:
Syncretic chemistry??
Summary and future
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Summary and future
considerations The biorefinery is already a reality
Carbohydrate and vegetable oil prices are likely to decreaserelative to petroleum prices
The chemical industry will increasingly use renewable rawmaterials such as vegetable oils and carbohydrates
Thoughtful combination of chemical, enzymatic and microbialcatalysis (syncretic chemistry?) is essential to realize the fullpotential of the biorefinery
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Acknowledgments
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AcknowledgmentsCargill BioTDC
Cargill Process Solutions TDC
Cargill Scientific Resources
Codexis
Pacific Northwest National Labs (PNNL)
Cargill Industrial Bioproducts
U.S. Department of Energy (DOE)
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