December 10, 2010BRINGING AGRICULTURE AND ENERGY TOGETHER

WHAT IS BIODIESEL?

Fuel from a Source of Oils & Fats... AN ALTERNATIVE GREEN FUEL…

Fatty Acid Methyl Esters can be used directly as Diesel or Blend with Diesel…

RUDOLF DIESELDesigned Diesel Engine in 1894 to Run on

Peanut Oil

“ “The use of vegetable oils for engine fuels may seem The use of vegetable oils for engine fuels may seem insignificant today. But such oils may become in the insignificant today. But such oils may become in the course of time as important as petroleum and the coal tar course of time as important as petroleum and the coal tar products of the present time.products of the present time."" 

-An Extract from Diesel’s Speech in 1912

FEED STOCK FOR BIODIESEL • Rapeseed (Germany)

• Sunflower oil

• Soybean oil (USA & Brazil)

• Palm oil (Malaysia)

• Linseed, olive oils (Spain)

• Cottonseed oil (Greece)

• Beef tallow (Ireland), lard, used frying oil (Austria), Jatropha (Nicaragua & South America, India), Guang-Pi (China)

• Used oil ( Austria)

WHAT IS BIODIESEL?F a t t y A c i d a l k y l e s t e r p r e p a r e d f r o m a n y o i l o r f a t ( a n i m a l o r v e g e t a b l e s o u r c e )

C H 2 - O - CO

R

C H - O - CO

RA l k a l i

A c i d+ M e t h a n o l R C

O

O M e+

C H 2 - O H

C H - O H

C H 2 - O HC H 2 - O - CO

R

O I L / F A T( T R I G L Y C E R I D E )

F a t t y A c i d M e t h y l E s t e r( B i o d i e s e l )

G l y c e r o l

R - CO

O H+ M e t h a n o l

A c i dR - C

O

O M e

F a t t y A c i d F a t t y A c i d M e t h y l E s t e r F a t t y A c i d M e t h y l e s t e r i s a w e l l k n o w m o l e c u l e f o r v e g e t a b l e o i l i n d u s t r y I n t e r m e d i a t e f o r f a t t y a l c o h o l s & o l e o c h e m i c a l s

T R A N S E S T E R I F I C A T I O N

E S T E R I F I C A T I O N

WHY BIODIESEL?• SUSTAINABILITY

• POLLUTION THREAT

• REDUCTION OF GREEN HOUSE GAS EMISSIONS

• REGIONAL (RURAL) DEVELOPMENT

• SOCIAL STRUCTURE & AGRICULTURE

• SECURITY OF SUPPLY

IMPORTANCE OF BIODIESEL

• Environment friendly• Clean burning• Renewable fuel

• No engine modification• Increase in engine life• Biodegradable and non-toxic• Easy to handle and store

Comprehensive Emissions Analysis for Biodiesel

B20 B100

• NOx 0 +10%• PM -10.1% -47%• HC -21.1% -66%• CO -11.0% -47%• Sulfates -20% -100% (Causes acid rain)• Fuel Economy (B20) -1-2%

B20: 20% biodiesel in diesel

BIODIESEL-WHY LOWER EMISSIONS ?

• Biodiesel has High Cetane• In Built Oxygen Content• Burns Fully• Has No Sulphur• No Aromatics• Complete CO2 Cycle

Exploration

Refining

Use in Cars and Trucks

Fossil CO2 Release to Atmosphere

PETRO-DIESEL CO2 CYCLE13 POUNDS OF FOSSIL CO2 RELEASED PER GALLON BURNED

BIODIESEL CO2 CYCLENO FOSSIL CO2 RELEASED ; NO GLOBAL WARMING

Biodiesel Production

Use in Cars and TrucksOil Crops

Renewable CO2

DIESEL & BIODIESEL DEMAND, AREA REQUIRED UNDERJATROPHA FOR DIFFERENT BLENDING RATES

(Biofuel Document of Indian Govt, 2002)

Year Disel Demand

MMT

Biodiesel @ 5% MMT

Area for 5%

Mha

Biodiesel @ 10% MMT

Area for 10% Mha

Biodiesel @ 20% MMT

Area for 20% Mha

2001-02 39.81 1.99 NA 3.98 NA 7.96 NA

2006-07 52.33 2.62 2.19 5.23 4.38 10.47 8.76

2011-12 66.90 3.35 2.79 6.69 5.58 13.38 11.19

December, 2009 –Indian Biofuel PolicyAn indicative target of 20% by 2017 for the blending of biofuels – bioethanol and bio-diesel

ROAD BLOCKS FOR BIODIESEL INDUSTRY… Feedstock Scarcity Food Vs Fuel Controversy Initial Enthusiasm Coming Down Non-edible Oil Production not Encouraging Effluent-based Traditional Technologies for

High FFA Oils Pricing of Biodiesel is Not Attractive to

Anybody Algal Oils – Long way to go…

WHAT IS THE CHALLENGE? V E R Y S I M P L E C H E M I S T R Y … H a n d l i n g m u l t i - f e e d s t o c k i s t h e r e a l c h a l l e n g e V E R Y L O W F F A – o n l y T r a n s e s t e r i f i c a t i o n

H I G H F F A – E S T E R I F I C A T I O N f o l l o w e d b y T R A N S E S T E R I F I C A T I O N

> 9 9 % Y i e l d s – t o a c h i e v e g o o d q u a l i t y F A M E – w i t h o u t d i s t i l l a t i o n ! ! R e c o v e r y o f g o o d q u a l i t y g l y c e r o l f o r e c o n o m i c f e a s i b i l i t y W a s t e W a t e r R e c y c l i n g G o o d p r e - t r e a t m e n t ( l o w e r p h o s p h o r u s p p m l e v e l s )

C H 2 - O - CO

R

C H - O - CO

RA l k a l iA c i d

+ M e t h a n o l R CO

O M e +

C H 2 - O H

C H - O H

C H 2 - O HC H 2 - O - CO

R

O I L / F A T( T R I G L Y C E R I D E )

F a t t y A c i d M e t h y l E s t e r( B i o d i e s e l )

G l y c e r o l

R - CO

O H+ M e t h a n o l

A c i dR - C

O

O M e

F a t t y A c i d B i o d i e s e l

MAJOR CONCERN…FEED STOCK

Present Global Production of Biodiesel ~ 14 million metric tons

Only <50% of Capacity of the Installed Biodiesel Plants Being Utilized…

This Scenario Indicates Several Road Blocks for Biodiesel Industry

Main Concern is the Feed Stock. Edible Vegetable Oil Expected to Remain the Major

Feedstock for the Production of Biodiesel Countries like India Propagating Non-edible Oils like

Jatropha & Karanja, but not Much Progress Animal Fats and Used Cooking Oils – Several

Limitations

GLOBAL MAJOR VEGETABLE OIL SCENARIO

Million metric tons

VEGETABLE OIL 2005/06 2006/07 2007/08 2008/09 2009/10

Palm 35.98 37.35 41.31 43.19 45.88

Soybean 34.61 36.39 37.51 36.26 37.88

Rapeseed 17.24 17.03 18.31 20.22 22.12

Sunflowerseed 10.59 10.61 9.73 11.46 11.31

Peanut 4.95 4.50 4.83 5.15 4.56

Palm Kernel 4.38 4.44 4.85 5.10 5.50

Cottonseed 4.62 4.86 5.00 4.72 4.66

Coconut 3.47 3.26 3.49 3.64 3.67

Olive 2.66 2.91 2.84 2.97 2.99

Total 118.49 121.33 127.86 132.70 138.57 Source: Oilseeds: World Markets and Trade, USDA, March 2010

39.05

20.3

11.57

5.06

13

44.62008-09

15.96

9.39

5

11.59

32.89

33.51

2004-05106 million

134 million

@ 7 mt/yr

2019-20

@ 5 mt/yr

190 million

Change in World Vegetable Oil Scenario…

1950’s30 million

78

50

29

13

614

Palm

Soybean

Rape seed

Sunflower

Cottonseed

Others.

DISTRIBUTION OF VEGETABLE OIL PRODUCTION IN INDIA

OIL 2004-05

MMT 2005-06

MMT 2007-08 MMT

2008-09 MMT

2009-10 MMT

Rape / Mustard 2.13 2.27 1.51 2.15 2.05 Soya 0.87 1.07 1.44 1.33 1.28 Groundnut 1.00 0.99 1.17 0.82 0.61 Rice Bran 0.68 0.73 0.80 0.85 0.80 Cottonseed 0.72 0.77 1.05 0.90 1.08 Sunflower 0.55 0.56 0.51 0.40 0.34 Coconut 0.42 0.42 0.42 0.42 0.43 Castor 0.34 0.38 0.41 0.46 0.42 Sesame 0.19 0.13 0.16 0.17 0.21 Niger 0.04 0.02 0.01 0.01 0.02 Safflower 0.06 0.06 0.05 0.05 0.04 Linseed Palm oil

0.09 0.04

0.09 0.05

0.08 0.06

0.06 0.07

0.07 0.06

Oils from expelled cakes

0.38 0.41 0.47 0.41 0.39

Minor oilseeds 0.08 0.08 0.10 0.10 0.06 TOTAL 7.59 8.03 8.20 8.20 7.88

Source: SEA

INDIAN VEGETABLE OIL PRODUCTION AND IMPORT STATUS

(million tones)

Year Domestic Edible Oil Production

Import of Edible Oils

2009-10 7.9 8.8 2008-09 8.2 8.2 2007-08 8.2 5.6 2006-07 7.72 4.71 2005-06 8.03 4.42 2004-05 7.59 5.04 2003-04 7.78 4.28 2002-03 5.12 5.38 2001-02 6.67 4.42 2000-01 5.81 4.83

Source: SEA

BIODIESEL - INDIAN SCENARIO

Presently importing about 8.8 million tones of edible oil – ~50% of consumption

Clean oils are not available for biodiesel production in the country

Non-edible Oils & Acid Oil – Not more than 5 lakh tones

To wait till Jatropha / Karanja plantation comes to reality - Oil production only after 2 to 3 years!!

TREE-BORNE OILS

Tree-borne oils will be major source for Indian Biodiesel

Most oils are dark

Possess disagreeable smell

Contain non-lipid constituents with variety of structural features

Above problems aggravate by hostile conditions during collection, storage and processing

Depending on the nature of the non-lipid constituents special processing methods have to be developed

Any technology in Indian scenario should take care of multi-feed stocks (high FFA and Unsap)

JATROPHA PLANT WITH SEEDS

KARANJA FLOWERS SEEDS

COMPONENTS RESPONSIBLE (PRESENT IN

CURDUE OIL) FOR LOW QUALITY BIODIESEL

Gums

Free fatty acids

Waxes

Unsaponifiables

Pigments

Neutralization

Transesterification 2-Stage process

Neutralization & Distillation Washing & Drying

PROCESS FOR BIODIESEL PRODUCTION

Distilation

*Esterification step is only for high FFA oils Not necessary for low FFA oils

Esterification

CRUDE OIL/ DEGUMMED OIL

Acid catalyst* Methanol

FATTY ACID METHYL ESTER TRIGLYCERIDE

Methanol Alkaline catalyst

SETTLING TANK

FATTY ACID METHYL ESTER GLYCERINE LAYER With Methanol and Alkali

METHANOL CRUDE GLYCEROL 80%

BIODIESEL

POTASSIUM SULPHATE (Fertilizer)

PRE-TREATMENTS BEFORE TRANSESTERIFICATION

TO HANDLE GUMS AND FFA

Physical Refining Degumming and Bleaching followed by removal of FFA by Deacidification (High Temperature Distillation)

Chemical Refining Removal of FFA using alkali neutralization - Heavy loss of Neutral oil along with Soap (2.5 times of FFA)

Esterification Converts FFA to Methyl esters (increases yield of Biodiesel) – Most appropriate option

NEWER APPROACHES Flexible process for handling variable quality feed stocks with

high FFA and unsaponifiables

Efficient conversions using traditional catalysts like NaOH / KOH / H2SO4

Catalyst-free esterification and transesterification Application of heterogeneous catalysts for both esterification

and transesterification Biotechnological approaches using lipases Microbial production of oil or fatty acid methyl ester Value addition to by-products

ADVANTAGES OF HETEROGENOUS CATALYSTS

Substantial reduction of waste/by-product generation

Savings on catalyst cost – Recycling

Considerably greater increase in reactor throughput

Smaller heat exchange areas – Reduced costs

Greater ease of automation and continuous processing

Sustainable reduction in operating costs

Reduction in chemical use (Catalysts, reagents used to neutralize catalysts)

Reduction in effluents

LIMITATIONS OF REPORTED SOLID ACID CATALYSTS

Most of catalysts reported requires

Higher temperatures Pressure

Reusability of catalyst not so good

Many of them are water sensitive

LIPASE CATALYZED PREPARATION OF BIODIESEL

CH-O-C-R

O

O

CH2-O-C-R

O

CH2-O-C-R

+CH3OH

R-C-OMe

O

CH-OH

CH2-OH

CH2-OH

Triglyceride FFABiodiesel Glycerol

LipaseR-COOH +

• Both esterification and transesterification at Room-temperature or less than 50°C• Immobilized enzymes can be recycled upto 20 to 30 times • Still unfavorable for commercial exploitation • Methanol or ethanol denatures the lipase• Lot of scope for biotechnological revolution in this area

GLYCEROL + H2SO4 CARBON-ACID CATALYST

In situ Carbonization and Sulfonation

GLYCERL-BASED CARBON ACID CATALYST – NEW INNOVATION

INDIAN & PCT PATENTS FILED, 2007 & 2008ChemSusChem, 2008

CARBON-ACID CATALYST

Powder XRD pattern

13C MAS NMR Spectrum

Scanning Electron Microscope (SEM) image

FT-IR Spectrum

CHARACTERIZATION OF GLYCEROL-BASED CARBON ACID CATALYST

XSP Spectrum Raman spectrum

CARBON ACID CATALYST

SO3H

GLYCEROL

OH OH

OHSO3HSO3H

SO3H

SO3H

Conc. H2SO4/ heat

SO3H

SO3H

SO3H

HO3S

HO3S

HO3SHO3S

In situ Carbonization & Sulfonation

Elemental Analysis, X-ray Diffraction, SEM, FT-IR, 13C MAS NMR, XSP Spectrum, Raman Spectrum, TG/DTA Analysis, Potentiometric Titration and BET Surface Area

Characterization…

HOW TO MAKE BIODIESEL CHEAPER?

Efficient Process for Biodiesel Production – Presence of Minimum Amounts of Triglyceride, Diglyceride and Mongoglycerides in the Biodiesel

Phytochemicals & Nutraceuticals of Oil &

Other Parts of the Tree (Leaves, Flowers, Bark etc.)

Alternate Applications for Oilseed Cake (Rich

in Starch and Protein Newer Applications for Glycerol

TREE-BORNE LIPIDS & OTHER USEFUL CONSTITUENTS

LEAF LIPIDS

- Rich in Biologically Active Constituents - Internal Lipids

Acid glycerols, hydroxyl fatty acids etc., - Epicuticular waxes

Rich in Hydrocarbons, wax esters, aldehydes, ketones, steryl esters, acetates, fatty alcohols, sterols, triterpenols, fatty acids, etc.

SEED OILS

- Edible oils, Structured fats, Industrial Oleochemicals like Biopesticides, Phytochemicals, Nutraceuticals like Gums (lecithin), Tocopherols, Phytosterols, Glycerol

SEED CAKES

- Rich Source for protein and starch - Good Fertilizer - Starch and protein based surfactants

KARANJA BIOREFINERY

KARANJA SEEDS

Bioactive Constituents

Cake Oil Lubricant Base Oils & Additives

Protein,Starch, Oil

Varieties of Products like Surfactants, Lubricants,Fertilizer etc.

Fatty Acid AlkylEsters

Crude Glycerol

Minor Constituents

LubricantBase Oils & Additives

Bioactive Constituents

Different Grades of Glycerol

Variety of Value Added Products

Sponsored by Department of Science & Technology Rs. 18.6 Millions

BIODIESEL PROCESS

Esterification Neutralization Transesterification

Separation

Non-edible Oils with FFA

Alcohol +

Acid Catalyst

Alcohol

Alcohol + Base Catalyst

Glycerol

Biodiesel

Nature of this crude glycerol is different from the glycerol produced by Fat Splitting or the Edible oil-based biodiesel glycerol

Glycerol ~ 50% Alcohol Water Biodiesel Catalyst Soap Salts Minor Constituents

POTENTIAL DERIVATIVES OF GLYCEROL

Structured Lipids

Oxidation Products

Glyceryl Ethers

Prodrugs

Triacetin, Glycerol carbonate type of by-products (in place of glycerol production)

MAJOR APPLICATIONS OF OILSEED CAKES- PRESENT STATUS

Edible Oilseed Cakes

Source of Protein in Case of Clean Cakes like Groundnut, Soybean, etc.

Animal Feed Formulations

Non-edible Oilseed Cakes

Manure

To Explore for Variety of Applications

JATROPHA / KARANJA CAKES Huge Quantities of Jatropha / Karanja Cakes if

these Plantations Suceed…

Every Tonne of Biodiesel Results in about 2 tonnes of Oilseed Cake

Oilseed Cakes – Real Asset for the Nation as they are Biodegradable

Potential Feedstock – To Make Biodiesel Industry More Attractive

To Develop variety of Products from these Cakes

COMPOSITION OF JATROPHA AND KARANJA OILSEED CAKES

Constituent Jatropha Karanja Nitrogen/Protein (wt %) 4-6/25-40 4-7/25-40 Carbohydrate (wt %) 15-20 15-20 Fibre (wt %) 15-20 15-20 Ash (wt %) 3-5 3-5 Phosphorus (wt %) 1.5-3 1-2 Potassium (wt %) 1-2 0.5-1.5 Calcium (wt %) <1 <1 Magnesium (wt %) <1 <0.5 Zinc, Copper, Magnesium, Boron (ppm) <100 <100 Sulphur (ppm) <3000 <4000

* Compositions may not be authentic as all the results are isolated / very old reports

BIOREFINERY OF OILSEED CAKES – POTENTIAL PATHWAYS

OILSEED CAKE (BIOMASS)

Oil

Deoiled Cake

Protein

Carbohydrates

Composite Materials, Surfactants

Fermentation

Biogas (Methane-rich)

Syngas

Bioactive Constituents

Carbon Source for Microbial Lipids / Enzymes

Protein Hydrolysate Surfactants

Fertilizer

Bioethanol

Fuel, Chemicals

Lubricants, Surfactants, Polymers

BIOETHANOL FROM CAKES Currently, Ethanol is made from Corn Grain Starch /

Sugarcane Molasses

Newer Feedstocks Required to Meet the Future Demands

Oilseed Cakes / Hulls – Potential Feedstock as they are Made up of Cellulosic Materials

Efficiency of the Pre-treatment and Fermentation Process has to be Optimized based on the Yield of Free Sugars and Ethanol

CARBON SOURCE FOR MICOBIAL GROWTH

For the Production of Microbial Lipids / Non-lipids or

Enzymes – Carbon Source Required

Microbial Degradation of Solid Agricultural Waste (Carbon Source) is a Natural Process

Known / Specific Microbial Strains may Produce Desired Products / Enzymes in Presence of a Carbon Source

Oilseed Cakes can be Directly Used as Carbon and Energy Source for Microbial Growth / Production of Desired Products for Many Potential Applications

To Produce Extra Cellular Enzymes such as Proteases, Lipases, Xylanase and Cellulase by Solid-state Fermentation

BIOMETHANATION OF OILSEED CAKES Several Biogas Plants not in Use for Want of

Feedstock

Oilseed Cakes – Excellent Feedstock

0.25 to 0.35 cubic meters of Biogas can be Produced from 1 kg of Jatropha Cake with 70-80% Methane Content [Satish Lele (www.Svlele.com)]

Area of Plot, 300m2 ; Manpower, Two unskilled; Power Supply, 1 kw; Cost, Rs. 5 Lakhs

Methane gas – For Generating Electricity – To Promote On-farm Energy Self-sufficiency

Left out Slurry from the Bioreactor – Serves as Organic Manure

Continuous Biodiesel Pilot Plant (10 kg/hr)

Studies on Physico-chemical Properties of Jatropha/Karanja Seeds (AP State Govt)

60 kg/hr Expeller for Jatropha/Karanja Seeds

Pre-treatment Pilot Plant (15 kg) for Crude Oil

Batch (50 kg) and Continuous (10 kg/hr) Biodiesel Process (AP State Govt & DBT)

Carbon Catalyst from Glycerol for Esterification / Transesterification (CSIR)

Development of Value added products from Karanja oil, cake and glycerol (DST)

Screening of Minor Oils for Biodiesel Production (DST)

Algal Oil-based Biodiesel (Collaborative Project) (DBT, NMITLI)

Exploratory studies on lipase-assisted preparation of biodiesel to enhance

stability to lipase

Established State of Art Facilities for Vegetable Oils, Biodiesel, Lubricants Research (CSIR, DST)

BIODIESEL – IICT’S PROGRAMME

Expeller Pre-treatment Plant

Thank you…