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TECH
Biodiesel, is a fuel composed of mono-alkyl esters of long
chain fatty acids derived from variety of vegetable oils or
animal fats, designated as B100, and confirming to different
quality standards e.g. ASTM D 6751, EN14214 or IS 15607
“ ”
 Alternative fuel for diesel engines
 Made from vegetable oil or animal fat
 Lower emissions, High flash point (>300F)
 Biodegradable, Essentially non-toxic.
 Chemically, biodiesel molecules are mono-alkyl esters produced usually
from triglyceride esters
Biodiesel
Vegetable Oil Glycerin
Alcohol
Fatty Acid
= 100% biodiesel / / /
: Transesterification (of oil)
(Europe)
(US)
(Africa, India)
• Castor Bean (Africa, China, S. America)
(Tropical areas)
: Coconut, Brazil nuts,
Jojoba, Peanuts, Cotton seed, Sunflower, and
many more
 History The concept dates back to 1885 when Dr. Rudolf Diesel
build the first diesel engine with the full intention of running it
on vegetative(Peanut oil) source.
In 1893 remembrance of this event, 10 August declared
“International Biodiesel Day”
 In 1900 ran the patented engine on any hydrocarbon
fuel available - which included gasoline and peanut oil.
Scientists discovered that the viscosity ( thickness) of
vegetable oils could be reduced in a simple chemical process
 In 1970 and that it could work well as diesel fuel in modern engine
CH2OOR1 catalyst CH2OH
|  |
CHOOR2 + 3CH3OH  3CH3OORx + CHOH
| |
CH2OOR3 CH2OH
Triglyceride 3 Methanols Biodiesel Glycerin
R1, R2, and R3 are fatty acid alkyl
groups (could be different, or the same), and
depend on the type of oil. The fatty acids
involved determine the final properties of the
biodiesel
While actually a multi-step process, the
overall reaction looks like this
 Biodiesel is made from the combination of a
triglyceride with a monohydroxy alcohol (i.e.
methanol, ethanol…). +
=
Methanol
H3C-OH
Typical Oil,
three fatty
acid chains
attached
to glycerol
Byproduct:
Glycerol to
Glycerine
+
Typical
“Biodiesel”
Methyl-
Ester
Base Catalyzed Transesterification Process
Free Fatty acids in the oils react with alkaline catalyst
to form soaps.
R-OH + KOH K-OR + H2O
Acid + KOH Soap + water
O
||
HO - C - (CH2)7 CH=CH(CH2)7CH3
Oleic Acid Potassium Hydroxide
+ KOH
O
||
K+ -O -C - (CH2)7 CH=CH(CH2)7CH3 + H2O
Potassium oleate (soap) Water
Soap formation
Excessive utilization of alkali
Loss of catalyst & reduction in yield
Slower reaction
Incomplete conversion
For best conversion FFA should be lower than
0.8%
→
 Water deactivates the catalysts. Drying of oil is required.
Water hydrolyses fats to form free fatty acids.
 Free fatty acids react with alkali catalysts forms soaps
Soaps semi solid mixture glycerol separation
• Can cause the entire product mixture to gel into a semi-
solid mass, giving headaches with separation and washing.
• Increased water use and treatment costs
• Loss of biodiesel product
Bio Diesel - Manufacture
(100 kg) (10.55 kg) (.1 kg) (100 kg) (10.55 kg)
Oil Alcohol KOH Bio Diesel Glycerin
CH2-O-COR CH2-OH
| KOH, rt, 6h |
CH-O-COR + 3R’OH 3RCOOR’ + CH-OH
| |
CH2-O-CO-R CH2-OH
BioDiesel – A better fuel vs. Diesel
Biodiesel Hydrogen
Technological Readiness Can be used in existing diesel engines, which
have already been in use for 100 years
Electrolyzing water (most likely using fossil fuel
energy) or reforming fossil fuels. Most likely non-
renewable methods with large net CO2
emissions
Fuel Distribution System Can be distributed with existing filling stations
with no changes.
No system currently exists, would take decades
to develop. Would cost 176 billion to put one
hydrogen pump at each of the filling stations in
the US.
Fossil Energy Balance [higher is better] 3.2 units (soy)
4.3 units (rapeseed)
0.66 units (steam reforming of natural gas)
Large scale fuel development cost analysis For an estimated 1691 billion, enough algae
farms could be built to completely replace
petroleum transportation fuels with biodiesel
To produce enough clean hydrogen for our
transportation needs would cost 2.5 trillion (wind
power) or 25 trillion (solar)
Safety Flash point over 300 F (considered “not
flammable”)
Highly flammable, high pressure storage tanks
pose a large risk due to store mechanical
energy, as well as flammability/explosiveness
Time scale for wide scale use 5-15 years 30-70 years optimistic assumption
Cost of engines Comparable to existing vehicles Currently 50-100 times as expensive as existing
engines.
Tank capacity required for 1,000 mile range in
conventional sedan
20 gallons 268 gallons
Biodiesel Advantages
 Produced from renewable materials – eco friendly / closed CO cycle.
 Local & self production – less reliance on foreign oil.
 Contains practically no sulfur (0.001%) – non toxic.
 Considerably decreases emissions (up to 50%).
 Easily decomposes – does not harm soil or ground water.
 Biodiesel is not hazardous material (flashpoint above 110°C).
 Eligible as fuels under international standards & specifications (world-wide).
 Eligible for CDM (Clean Development Mechanism - Kyoto Treaty).
Biodiesel can be used in existing Diesel Engines
Pure Biodiesel (B100) or blended with petroleum diesel (B20,
BXX).
Rudolf Diesel: peanut oil.
Little or no engine modifications
Use existing fuel distribution network.
Available now
LIFE CYCLE EMISSIONS – CO2
Biodiesel generates 573.96 g/bhp-h compared to 548.02 g/bhp-h for petroleum diesel
The higher CO2 levels result from more complete combustion
The overall life cycle emissions are 78.45% lower for biodiesel; direct result of carbon
cycling by the soybean plants
Biodiesel’s Closed Carbon Cycle
 Biodiesel is environmentally beneficial properties & benefit is ‘carbon
neutral’. This means that fuel produces no net output of carbon form of
carbon dioxide (CO2).
 This effect occurs oil crop grows it absorbs the CO2 as is released when
fuel is combusted.
 In fact this is not completely accurate as CO2 is released during the
production of the fertilizer required to fertilize the fields in which the oil
crops are grown.
 Fertilizer production is not the only source of pollution associated with the
production of biodiesel, other sources include the esterification process,
the solvent extraction of the oil, refining, drying and transporting
 All processes require an energy input either form of electricity or from a fuel, both
of which will generally result in the release of green house gases.
** B100 (100% biodiesel) with NOx adsorbing catalyst on vehicle
Relative emissions: Diesel and Biodiesel
0 20 40 60 80 100 120
Total Unburned HCs
CO
Particulate Matter
**NOx
Sulfates
PAHs
n-PAHs
Mutagenicity
CO2
Percent
B100 **
B20
Diesel
Oil
Content
US
gal/acr
e
Liters
oil/ha
Kg
oil/ha
Crop
50% - 55%
151
1413
1188
Castor beans
70%
287
2689
2260
Coconut
12%
18
172
145
Corn (maize)
13% - 15%
35
325
273
Cotton
30% - 35%
202
1892
1590
Jatropha
35%
635
5950
5000
Palm oil
36%
113
1059
890
Peanuts
37%
127
1190
1000
Rapeseed
15%
48
446
375
Soybean
32%
102
952
800
Sunflower
Source: www.journeyforever.com – Jan. 2007 – This data is compiled from a wide variety of
sources. The yield figures are most useful as comparative estimates, crop yields vary widely
Algae to Biodiesel
 Converts 61% of its biomass into oil
 86% of it is long chain hydrocarbons
 Drops to only 31% oil under stress
 Grows best between 22-25o
C (71-77o
F)
 Choosing an Algae
 High % of total biomass is oil
 Maintains a high % of oil even under stress
 Compatible with the area climate
 DOE concluded a 16-year study of algal biomass in 1996 (and wrote a 328-page report)
http://www.nrel.gov/docs/legosti/fy98/24190.pdf
 Conducted large-scale tests in California, New Mexico and Hawaii
With good temperatures, could harvest 50 grams of algae per sq. meter per day
Used a 1,000 m2 pond for 1 year
 UNH paper may hopefully rekindle research
 Due to the burgeoning interest in alternatives to fossil fuels, there has been
renewed research interest in Botryococcus braunii. The DOE Joint Genome
Institute is sequencing the DNA of Bb in 2009-2010
European biodiesel sales grew by 54% in 2006 to just under 5 billion litres. Since 2006,
biodiesel capacity has more than doubled. The International Energy Agency predicts that
biodiesel has the capacity to displace 1.2% of the world’s diesel just by 2013
United States and Asia, in particular India and China, where the government
target is 15% replacement of petrodiesel by 2020 (Global market survey oct.2006)
Asia – although significant market yet, relatively
small
Eastern Europe & N. America – 2nd largest markets
(FR, IT, UK) – main producers and
consumers – 75% of world
2005
– 3rd largest markets, with US as
the single largest consumer – 18% of world
– will become the 2nd largest market (China, India –
consumption & production)
Western Europe -( FR, IT, UK) – main producers and consumers –
38% of world
2010
 Name of Biodiesel started making appearance at Indian
Conferences, Workshops & Seminars in 1999
 ‘Report of the Committee on Development of Biofuel’ –
Planning Commission, GOI in 2003
 Stage I ‘Demonstration Project’ use Jatropha in 2006-
2007
 Stage II – 11 mill ha (13 MMT biodiesel) for 20% blend.
 Demonstration project started with initial grant of 11mn
for nursery raising rest is expected to be sanctioned late
this year
 First 10,000 TPA plant in Hyderabad about to start
production
 Garware100,000 TPA DMT plant modified for biodiesel
production
 A 250,000 TPA plant is being setup in Vishakhapatnam ,
A.P.
 A 100,000 TPA plant is coming up in Kakinada , A.P
Year Diesel Demand
(MT)
Biodiesel requirement for
blending (MMT)
Area Requirement for Blending
(Mha)
@
5%
@ 10% @ 20% @
5%
@ 10% @ 20%
2006-07 52.33 2.62 5.24 10.48 2.19 4.38 8.76
2011-12 66.90 3.35 6.69 13.38 3.35 5.58 11.19
 5 % mixing of Biodiesel in HSD by 2007
 20 % mixing of Biodiesel in HSD by 2012
Diesel & Biodiesel Demand, Area Required under Jatropha For Different
Blending Rates
1 Million hectare's of waste land is brought under Jatropha
cultivation
 Can yield
 0.8-1 million tons of oil
 For 66.9 MMT diesel (Projected 2011-12)
 13 MMT bio diesel for 20% blend
 11 MH land required
Biodiesel is an renewable fuel for diesel engines that can be made from
virtually any oil or fat feedstock
Biodiesel with a potential consumption of 15000 million litres can have a
retail turnover of more than 9000 mn per year
It can provide huge rural employment potential of 40 to 50 million
families and transform the rural economy
Remote village electrification and power for agriculture application –
Energy grown & used by village
The dominant factor in biodiesel production is the feedstock cost which
around 70%, with capital cost contributing only about 7 % of the product
cost. Therefore high FFA, lower quality feedstock should be promoted for
biodiesel production in India.
For meeting energy security and electricity for all, it is necessary to
develop and commission small to medium capacity biodiesel unit at village &
community level..
Maintaining product quality is also essential for the growth of the biodiesel
industry in India.
In conclusion
References
…

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Bio_diesel_Production_Technology.pptx

  • 2. Biodiesel, is a fuel composed of mono-alkyl esters of long chain fatty acids derived from variety of vegetable oils or animal fats, designated as B100, and confirming to different quality standards e.g. ASTM D 6751, EN14214 or IS 15607 “ ”  Alternative fuel for diesel engines  Made from vegetable oil or animal fat  Lower emissions, High flash point (>300F)  Biodegradable, Essentially non-toxic.  Chemically, biodiesel molecules are mono-alkyl esters produced usually from triglyceride esters Biodiesel Vegetable Oil Glycerin Alcohol Fatty Acid
  • 3. = 100% biodiesel / / / : Transesterification (of oil) (Europe) (US) (Africa, India) • Castor Bean (Africa, China, S. America) (Tropical areas) : Coconut, Brazil nuts, Jojoba, Peanuts, Cotton seed, Sunflower, and many more
  • 4.  History The concept dates back to 1885 when Dr. Rudolf Diesel build the first diesel engine with the full intention of running it on vegetative(Peanut oil) source. In 1893 remembrance of this event, 10 August declared “International Biodiesel Day”  In 1900 ran the patented engine on any hydrocarbon fuel available - which included gasoline and peanut oil. Scientists discovered that the viscosity ( thickness) of vegetable oils could be reduced in a simple chemical process  In 1970 and that it could work well as diesel fuel in modern engine
  • 5. CH2OOR1 catalyst CH2OH |  | CHOOR2 + 3CH3OH  3CH3OORx + CHOH | | CH2OOR3 CH2OH Triglyceride 3 Methanols Biodiesel Glycerin R1, R2, and R3 are fatty acid alkyl groups (could be different, or the same), and depend on the type of oil. The fatty acids involved determine the final properties of the biodiesel While actually a multi-step process, the overall reaction looks like this  Biodiesel is made from the combination of a triglyceride with a monohydroxy alcohol (i.e. methanol, ethanol…). + = Methanol H3C-OH Typical Oil, three fatty acid chains attached to glycerol Byproduct: Glycerol to Glycerine + Typical “Biodiesel” Methyl- Ester
  • 6. Base Catalyzed Transesterification Process Free Fatty acids in the oils react with alkaline catalyst to form soaps. R-OH + KOH K-OR + H2O Acid + KOH Soap + water O || HO - C - (CH2)7 CH=CH(CH2)7CH3 Oleic Acid Potassium Hydroxide + KOH O || K+ -O -C - (CH2)7 CH=CH(CH2)7CH3 + H2O Potassium oleate (soap) Water Soap formation Excessive utilization of alkali Loss of catalyst & reduction in yield Slower reaction Incomplete conversion For best conversion FFA should be lower than 0.8% →
  • 7.  Water deactivates the catalysts. Drying of oil is required. Water hydrolyses fats to form free fatty acids.  Free fatty acids react with alkali catalysts forms soaps Soaps semi solid mixture glycerol separation • Can cause the entire product mixture to gel into a semi- solid mass, giving headaches with separation and washing. • Increased water use and treatment costs • Loss of biodiesel product
  • 8. Bio Diesel - Manufacture (100 kg) (10.55 kg) (.1 kg) (100 kg) (10.55 kg) Oil Alcohol KOH Bio Diesel Glycerin CH2-O-COR CH2-OH | KOH, rt, 6h | CH-O-COR + 3R’OH 3RCOOR’ + CH-OH | | CH2-O-CO-R CH2-OH
  • 9. BioDiesel – A better fuel vs. Diesel Biodiesel Hydrogen Technological Readiness Can be used in existing diesel engines, which have already been in use for 100 years Electrolyzing water (most likely using fossil fuel energy) or reforming fossil fuels. Most likely non- renewable methods with large net CO2 emissions Fuel Distribution System Can be distributed with existing filling stations with no changes. No system currently exists, would take decades to develop. Would cost 176 billion to put one hydrogen pump at each of the filling stations in the US. Fossil Energy Balance [higher is better] 3.2 units (soy) 4.3 units (rapeseed) 0.66 units (steam reforming of natural gas) Large scale fuel development cost analysis For an estimated 1691 billion, enough algae farms could be built to completely replace petroleum transportation fuels with biodiesel To produce enough clean hydrogen for our transportation needs would cost 2.5 trillion (wind power) or 25 trillion (solar) Safety Flash point over 300 F (considered “not flammable”) Highly flammable, high pressure storage tanks pose a large risk due to store mechanical energy, as well as flammability/explosiveness Time scale for wide scale use 5-15 years 30-70 years optimistic assumption Cost of engines Comparable to existing vehicles Currently 50-100 times as expensive as existing engines. Tank capacity required for 1,000 mile range in conventional sedan 20 gallons 268 gallons
  • 10. Biodiesel Advantages  Produced from renewable materials – eco friendly / closed CO cycle.  Local & self production – less reliance on foreign oil.  Contains practically no sulfur (0.001%) – non toxic.  Considerably decreases emissions (up to 50%).  Easily decomposes – does not harm soil or ground water.  Biodiesel is not hazardous material (flashpoint above 110°C).  Eligible as fuels under international standards & specifications (world-wide).  Eligible for CDM (Clean Development Mechanism - Kyoto Treaty). Biodiesel can be used in existing Diesel Engines Pure Biodiesel (B100) or blended with petroleum diesel (B20, BXX). Rudolf Diesel: peanut oil. Little or no engine modifications Use existing fuel distribution network. Available now
  • 11. LIFE CYCLE EMISSIONS – CO2 Biodiesel generates 573.96 g/bhp-h compared to 548.02 g/bhp-h for petroleum diesel The higher CO2 levels result from more complete combustion The overall life cycle emissions are 78.45% lower for biodiesel; direct result of carbon cycling by the soybean plants Biodiesel’s Closed Carbon Cycle  Biodiesel is environmentally beneficial properties & benefit is ‘carbon neutral’. This means that fuel produces no net output of carbon form of carbon dioxide (CO2).  This effect occurs oil crop grows it absorbs the CO2 as is released when fuel is combusted.  In fact this is not completely accurate as CO2 is released during the production of the fertilizer required to fertilize the fields in which the oil crops are grown.  Fertilizer production is not the only source of pollution associated with the production of biodiesel, other sources include the esterification process, the solvent extraction of the oil, refining, drying and transporting  All processes require an energy input either form of electricity or from a fuel, both of which will generally result in the release of green house gases.
  • 12. ** B100 (100% biodiesel) with NOx adsorbing catalyst on vehicle Relative emissions: Diesel and Biodiesel 0 20 40 60 80 100 120 Total Unburned HCs CO Particulate Matter **NOx Sulfates PAHs n-PAHs Mutagenicity CO2 Percent B100 ** B20 Diesel
  • 13. Oil Content US gal/acr e Liters oil/ha Kg oil/ha Crop 50% - 55% 151 1413 1188 Castor beans 70% 287 2689 2260 Coconut 12% 18 172 145 Corn (maize) 13% - 15% 35 325 273 Cotton 30% - 35% 202 1892 1590 Jatropha 35% 635 5950 5000 Palm oil 36% 113 1059 890 Peanuts 37% 127 1190 1000 Rapeseed 15% 48 446 375 Soybean 32% 102 952 800 Sunflower Source: www.journeyforever.com – Jan. 2007 – This data is compiled from a wide variety of sources. The yield figures are most useful as comparative estimates, crop yields vary widely
  • 14. Algae to Biodiesel  Converts 61% of its biomass into oil  86% of it is long chain hydrocarbons  Drops to only 31% oil under stress  Grows best between 22-25o C (71-77o F)  Choosing an Algae  High % of total biomass is oil  Maintains a high % of oil even under stress  Compatible with the area climate  DOE concluded a 16-year study of algal biomass in 1996 (and wrote a 328-page report) http://www.nrel.gov/docs/legosti/fy98/24190.pdf  Conducted large-scale tests in California, New Mexico and Hawaii With good temperatures, could harvest 50 grams of algae per sq. meter per day Used a 1,000 m2 pond for 1 year  UNH paper may hopefully rekindle research  Due to the burgeoning interest in alternatives to fossil fuels, there has been renewed research interest in Botryococcus braunii. The DOE Joint Genome Institute is sequencing the DNA of Bb in 2009-2010
  • 15. European biodiesel sales grew by 54% in 2006 to just under 5 billion litres. Since 2006, biodiesel capacity has more than doubled. The International Energy Agency predicts that biodiesel has the capacity to displace 1.2% of the world’s diesel just by 2013 United States and Asia, in particular India and China, where the government target is 15% replacement of petrodiesel by 2020 (Global market survey oct.2006) Asia – although significant market yet, relatively small Eastern Europe & N. America – 2nd largest markets (FR, IT, UK) – main producers and consumers – 75% of world 2005 – 3rd largest markets, with US as the single largest consumer – 18% of world – will become the 2nd largest market (China, India – consumption & production) Western Europe -( FR, IT, UK) – main producers and consumers – 38% of world 2010
  • 16.  Name of Biodiesel started making appearance at Indian Conferences, Workshops & Seminars in 1999  ‘Report of the Committee on Development of Biofuel’ – Planning Commission, GOI in 2003  Stage I ‘Demonstration Project’ use Jatropha in 2006- 2007  Stage II – 11 mill ha (13 MMT biodiesel) for 20% blend.  Demonstration project started with initial grant of 11mn for nursery raising rest is expected to be sanctioned late this year  First 10,000 TPA plant in Hyderabad about to start production  Garware100,000 TPA DMT plant modified for biodiesel production  A 250,000 TPA plant is being setup in Vishakhapatnam , A.P.  A 100,000 TPA plant is coming up in Kakinada , A.P
  • 17. Year Diesel Demand (MT) Biodiesel requirement for blending (MMT) Area Requirement for Blending (Mha) @ 5% @ 10% @ 20% @ 5% @ 10% @ 20% 2006-07 52.33 2.62 5.24 10.48 2.19 4.38 8.76 2011-12 66.90 3.35 6.69 13.38 3.35 5.58 11.19  5 % mixing of Biodiesel in HSD by 2007  20 % mixing of Biodiesel in HSD by 2012 Diesel & Biodiesel Demand, Area Required under Jatropha For Different Blending Rates 1 Million hectare's of waste land is brought under Jatropha cultivation  Can yield  0.8-1 million tons of oil  For 66.9 MMT diesel (Projected 2011-12)  13 MMT bio diesel for 20% blend  11 MH land required
  • 18. Biodiesel is an renewable fuel for diesel engines that can be made from virtually any oil or fat feedstock Biodiesel with a potential consumption of 15000 million litres can have a retail turnover of more than 9000 mn per year It can provide huge rural employment potential of 40 to 50 million families and transform the rural economy Remote village electrification and power for agriculture application – Energy grown & used by village The dominant factor in biodiesel production is the feedstock cost which around 70%, with capital cost contributing only about 7 % of the product cost. Therefore high FFA, lower quality feedstock should be promoted for biodiesel production in India. For meeting energy security and electricity for all, it is necessary to develop and commission small to medium capacity biodiesel unit at village & community level.. Maintaining product quality is also essential for the growth of the biodiesel industry in India. In conclusion
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