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Dr. Sanjeev Saraf
3rd May 2007
Diesel engines are 25% more efficient than
gasoline engines
In Europe, there is a shift away from gasoline
engines
In the U.S., diesel engines may gain
prominence
◦ Rising gas prices
◦ Increasing efficiency requirements
Produced from vegetable oil / animal fat
◦ Transesterification
Low sulfur
Domestic feedstock
Government subsidies
Source: NBB
• In 2006, there were 105 Biodiesel production facilities with a
maximum annual capacity of 864 million gallons
Source: NBB
• 77 new plants under construction
• 8 expansion
Source: NBB
Subsidies
◦ Blenders
◦ Producers
◦ State credits
Renewable Fuels Act (RFA) Bill
◦ Blending renewable fuel with fossil fuels
◦ 8 billion gallons of biofuels by 2012
US petroleum diesel consumption
◦ ~50 billion gallons/year
Biodiesel production
◦ 50 gal/acre (Soya)
Displace petroleum diesel?
◦ 1.5 million sq. miles
◦ ~ 6 times TX
◦ ~ 40% of the U.S. total area
Vegetable oil
◦ Soya
◦ Canola
◦ Rapeseed
◦ Yellow grease
Animal fat
◦ Lard
◦ Beef tallow
◦ Chicken fat
CH2-O-C-R1
CH-O-C(=O)-R2
CH2-O-C-R3
O
O
Chemical extraction
◦ Solvents e.g. hexane
Physical extraction
Thermal polymerization
Thermal degradation
Free Fatty Acid
Higher unsaturation
Agriculture land
◦ Soya competes with food industry
◦ Higher prices
Alternate feedstock
Vegetable oil
◦ Degumming
Yellow grease
◦ Dewater
◦ Filter
◦ FFA reduction
Deodorization
CH2-O-C-R1
CH-O-C(=O)-R2
CH2-O-C-R3
O
O
+ R-OH
R-O-C-R1
R-O-CO-R2
R-O-C-R3
O
O
CH2-OH
CH-OH
CH2-OH
+
Oil/Fat
Triaceylglycerol (TAG)
Alcohol
Fatty acid alkyl ester
Biodiesel
Glycerol
Catalyst
CH2-O-C-R1
CH-O-C(=O)-R2
CH2-O-C-R3
O
O
+ H-OH
H-O-C-R1
H-O-CO-R2
H-O-C-R3
O
O
CH2-OH
CH-OH
CH2-OH
+
Oil/Fat
Triaceylglecerol (TAG)
Water
Free Fatty acid (FFA)
Glycerol
Catalyst
Free Fatty Acid – Saponification
◦ FFA + NaOH Soap
CH2-O-C-R1
CH-O-C(=O)-R2
CH2-O-C-R3
O
O
+ R-OH
R-O-C-R1
R-O-CO-R2
R-O-C-R3
O
O
CH2-OH
CH-OH
CH2-OH
+
Oil/Fat
Triaceylglecerol (TAG)
Alcohol
Fatty acid alkyl ester
Biodiesel
Glycerol
Catalyst
TAG + CH3OH ⇔ DAG + R1COOCH3
DAG + CH3OH ⇔ MAG + R2COOCH3
MAG + CH3OH ⇔ Glycerol + R3COOCH3
%methylestersformed
Reaction Timeme
Mass transfer controlled Kinetic controlled
NRe
Temp
♦♦ 9393--98% conversion in 198% conversion in 1--hour at 60hour at 60 ooCC (Source: Freedman, Ibid, 1986)(Source: Freedman, Ibid, 1986)
–– Soyabean, sunflower, peanut, cottonseedSoyabean, sunflower, peanut, cottonseed
Non-reactive co-solvent
◦ MTBE
◦ THF
Environmental considerations
Methanol
◦ Reacts at room temperature
◦ Flammable
Higher alcohol
◦ Higher temperature
◦ Different catalyst
Branched alcohol
◦ Fatty acid esters have higher cetane numbers
Alkali
CatalystCatalyst
BiodieselBiodiesel
yieldyield
(mol %)(mol %)
TriglycerideTriglyceride
saponificationsaponification
(mol %)(mol %)
Methyl esterMethyl ester
in glycerolin glycerol
(mol%)(mol%)
Sodium hydroxideSodium hydroxide 85.1985.19 0.100.10 5.655.65 0.180.18 6.046.04 0.050.05
Sodium methoxideSodium methoxide 98.6498.64 0.350.35 0.040.04 0.030.03 0.110.11 0.030.03
Potassium hydroxidePotassium hydroxide 90.190.1 0.360.36 3.463.46 0.110.11 3.003.00 0.110.11
Potassium methoxidePotassium methoxide 97.5497.54 0.270.27 0.130.13 0.050.05 0.430.43 0.070.07
Source: Vincente, Biosource Technology, 2004
Acid catalyzed
◦ Slower than base-catalyzed
◦ No saponification side reaction
◦ High FFA content
>0.5 wt%
◦ Waste vegetable oil (WVO)
> 2%
Reactor
Vegetable Oil
Catalyst
Methanol
Biodiesel
• Free fatty acids
less than 0.5 wt %
• Moisture free
• Ensure transesterification
reaction is complete
• Fuel meets ASTM
D6751 requirements
Titration or other
analytical techniques
ASTM specified tests
Source: EPA, “A Comprehensive Analysis of Biodiesel Impacts on Exhaust Emissions”,
EPA420-P-02-001, Oct. 2002
Source: Amman and Siegla, Aerosol Science and Technology, 1982
Solidification at lower temperatures
◦ Plugging
Additives
Oxidation
◦ Long term storage
Unsaturated FAME are more prone to
oxidation stability
Unsaturated compounds have lower melting points
Antioxidant additive
Feb. 2006: A fire at American Biofuel’s
Biodiesel plant in Bakersfield, CA destroyed
the entire plant . The fire was caused by a
methanol spill. (Source:Biodiesel Magazine, April 2006, page 15)
In 2005, a man repairing glycerin storage
tank in a biodiesel facility in Staten Island
died due to an explosion (Source: New York Times, “Repair Work
Possible Cause of Fatal Blast”, June 5, 2005.)
June 2006: Fire destroys a biodiesel plant in
Canby (Source: KGW, Channel 8)
PSM?
By-product
Soap
Huntsman, Dow
◦ propylene glycol
BQ 9000
ASTM tests
◦ D7651: Biodiesel Fuel Blend Stock (B100) for Middle
Distillate Fuels
Alternate feedstock
Extraction technologies
Solid catalyst
◦ IER / Zeolite
Continuous operations

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Biodiesel 2007