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PROJECT REPORT PRESENTATION
“BIODIESEL –A Perspective ”
AUTHOR: MANU H NAIR
FACULTY ADVISOR :Er. PRAMOD GEORGE
PROFESSIONALADVISOR :Dr. BALAN K.
AKNOWLEDGEMENT
WE WOULD LIKE TO SINCIERELY THANK:
 DR JOHN M.GEORGE –Principal ,Caarmel Engineering College.
 DR BALAN K. Former MD to National Coir research and
development institute .(External Guide)
 ER. KISHEN KARANAKARAN – MD , TMN Biofuels, Pvt Ltd
Coimbatore.
 DR.KOCHUBABY MANJOORAN, Kochin Refinery , Kochin.
 Prof: A.D POULOUSE – H.O.D Department of Mechanical
Engineering.
 Er. PRAMOD GEORGE –Internal Guide .
 Er SHAAN .
 And all other faculty members of the Department of Mechanical
Engineering.
 All our dear friends .
2/4/2016 2
OBJECTIVES:
 Biodiesel as an alternative fuel without much
alterations in existing vehicle technologies.
 Comparative study with Petro Diesel .
 Biodiesel as a fuel and Industry for Emerging
India
2/4/2016 3
WORLD ENERGY DEPENDENCY
2/4/2016 4
WORLD OIL DEPLETION
2/4/2016 5
WHAT IS BIODIESEL?
Alternate environment friendly fuel.
From animal or plant source.
Made of long chain alkyl esters.
2/4/2016 6
BIODIESEL ON GLOBAL CONTEXT.
 Production rose by 50% from2002-09.
 Popular amongst developed countries or
ANNEX categorized countries(Kyoto protocol)
 Criticism .
a) Impact on food security.
b) Doubt of overall +ve net Carbon balance.
 Automobiles , airplanes , locomotives ,
factories, houses..etc running on Biofuel.
2/4/2016 7
BIODIESEL PRODUCTION
FEEDSTOCK
(GENERAL)
• Virgin oil feedstock
• Waste vegetable
oil (WVO)
• Animal fats
• Algae(research in
progress)
• Fungus (research
in progress)
2/4/2016 8
CASE STUDY FINDINGS FROM TMN
BIOFUELS ON FEEDSTOCK:
 Major feed stock is Cashew cornel rejection oil.
 Its an acidified oil waste.
 Imported from Indonesia from a sister concern
 R&D on various other sources underway.
2/4/2016 9
PRODUCTION TECHNIQUES
1.Direct use and
blending
2.Microemulsions
Thermal cracking
(Pyrolysis)
Transesterification
(Alcoholysis)
Other types of
transesterification
.
2/4/2016 10
1.DIRECT USE AND BLENDING:
 Direct use:
o 100% biofuel with no Petro Diesel.
o B100
 Blending :
o Usual varieties ; B5,B10,B20….B95.
o B10 means 10% Petro Diesel and 90%
Biodiesel .
2/4/2016 11
ADVANTAGES AND DISADVANTAGES OF
DIRECT USE OF VEGITABLE OILS:
 ADVANTAGES
 Liquid nature-portability,
 Heat content (80% of
diesel fuel),
 Ready availability and
 Renewability.
 DISADVANTAGES
 Higher viscosity,
 Lower volatility and
 The reactivity of
unsaturated hydrocarbon
chains
2/4/2016 12
Known problems, probable cause and potential solutions for using
straight vegetable oil in diesels
Problem Probable cause Potential solution
Short-term
1. Cold weather starting High viscosity, low cetane,
and low flash point
of vegetable oils
Preheat fuel prior to injection.
Chemically alter fuel
to an ester
2. Plugging and gumming of
filters,
lines and injectors
Natural gums (phosphatides)
in vegetable oil.
Other ash
Partially refine the oil to
remove gums. Filter to
4-microns
3. Engine knocking Very low cetane of some oils.
Improper injection
timing.
Adjust injection timing. Use
higher compression
engines. Preheat fuel prior to
injection. Chemically
alter fuel to an ester
Long-term
4. Coking of injectors on
piston
and head of engine
High viscosity of vegetable
oil, incomplete
combustion of fuel. Poor
combustion at part
load with vegetable oils
Heat fuel prior to injection.
Switch engine to diesel
fuel when operation at part
load. Chemically alter
the vegetable oil to an ester
5. Carbon deposits on piston
and head of engine
High viscosity of vegetable
oil, incomplete
Combustion of fuel. Poor
combustion at part
load with vegetable oils
Heat fuel prior to injection.
Switch engine to diesel
fuel when operation at part
load. Chemically alter
the vegetable oil to an ester
6. Excessive engine wear High viscosity of vegetable
oil, incomplete
combustion of fuel. Poor
combustion at part
load with vegetable oils.
Possibly free fatty acids
in vegetable oil. Dilution of
engine lubricating
oil due to blow-by of
Heat fuel prior to injection.
Switch engine to diesel
fuel when operation at part
load. Chemically alter
the vegetable oil to an ester.
Increase motor oil
changes. Motor oil additives
to inhibit oxidation
2. MICROEMULSIONS
 Solves the problem of high viscosity of vegetable oils.
 Are solvents live methanol, ethanol etc.
 Defined as a colloidal equilibrium dispersion of
optically isotropic fluid microstructures.
 Usually 1-150 nm range formed spontaneously from two
normally immiscible liquids and one or more ionic or
non-ionic amphiphiles
 Improve spray characteristics by explosive vaporization
of the low boiling constituents in the micelles .
 Short term performances of both ionic and non-ionic
micro emulsions of aqueous ethanol in soybean oil
nearly as good as that of No. 2 diesel, in spite of the
lower cetane number and energy content .
2/4/2016 14
TEST RESULTS SHOWING PROPERTIES
OF SHIPP NON -IONIC FUEL.
(SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio
resource Technologies ,Lincon,NE ,USA 1999.)
2/4/2016 15
2.1 THERMAL CRACKING(PYROLYSIS)
 Conversion of one substance into another by means of heat or
by heat with the aid of a catalyst .
 Heating in the absence of air or oxygen.
 And cleavage of chemical bonds to yield small molecules .
 First pyrolysis of vegetable oil was conducted in an attempt
to synthesize petroleum from vegetable oil.
.
2/4/2016 16
 The process is simple and effective compared with other
cracking processes
 Rapeseed oil pyrolyzed to produce a mixture of methyl
esters in a tubular reactor between 500 and 850°C and in
nitrogen.
2/4/2016 17
(SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review ,
Bio resource Technologies ,Lincon,NE ,USA 1999.)
2.2TRANSESTERIFICATION
(ALCOHOLYSIS)
 The reaction of a fat or oil with an alcohol to form esters
and glycerol.
 A catalyst is usually used to improve the reaction rate
and yield.
2/4/2016 18
(SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio
resource Technologies ,Lincon,NE ,USA 1999.)
2.2.1MECHANISM AND KINETICS
2/4/2016 19
(SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio
resource Technologies ,Lincon,NE ,USA 1999.)
2/4/2016 20
SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio
resource Technologies ,Lincon,NE ,USA 1999.)
FACTORS AFFECTING FREE FATTY
ACIDS IN TRANS ESTERIFICATION:
 Moisture.
 Catalyst .
 Molar ratio .
 Reaction time.
 Reaction temperature.
2/4/2016 21
THE PROCESS OF TRANSESTERIFICATION AND
DOWNSTREAM OPERATIONS
2/4/2016 22
OTHER TRANSESTERIFICATIONS
 In-situ transesterification is taken into consideration.
 Found that acid catalyzed in-situ process is better
than conventional methods .
 By increasing reaction temperature and time and by
decreasing the particle size of the soybeans and the
water content of ethanol, a purer product was
obtained.
 The separated glycerol reacted with triglycerides to
produce mono- and diglycerides, which are valuable
chemical intermediates for detergents and
emulsifiers
2/4/2016 23
PRODUCTION TECHNIQUES EMPLOYES AT
TMN BIOFUELS PVT LTD
 METHODS :
1. BASIC ESTERIFICATION
2. TRANS ESTERIFICATION
 TMN Biofuels Employs a combination of both .
 One of a kind .
2/4/2016 24
TMN BIOFUELS BIODIESEL PLANT.
2/4/2016 25
PRODUCTION
TECHNIQUES
1. Primary production technique
2. Secondary production technique
3. Tertiary production technique
2/4/2016 26
PRIMARY PRODUCTION
 Oldest and most common production technique.
2/4/2016 27
SECONDARY PRODUCTION
 Combination of esterification and trans esterification.
2/4/2016 28
Biodiesel from different grade of oils at TMN Biofuels Pvt Ltd.
TERTIARY PRODUCTION
 ALGAL SYNTHESIS
 Third generation process
 Costly and time consuming.
 Other includes fungal cultivated biodiesels and
biodiesels from coffee ground beans .(under R&D)
2/4/2016 29
SEQUENTIAL PROCESS IN MAKING BIODIESEL
FROM ALGAE
(SOURCE: ECOGENICS RESEARCH CENTRE)
 FIGURE (A) –MICRO-ALGAE AT LABS FOR
SYNTHESIS
2/4/2016 30
 FIGURE(B) – MICRO-ALGAE AT LAB BEFORE
DRYING
2/4/2016 31
 FIGURE(C) – ALGAE DRIED BEFORE OIL
EXTRACTION
2/4/2016 32
 FIGURE(C) – ALGAE DRIED BEFORE OIL
EXTRACTION
2/4/2016 33
STORAGE,HANDLING AND TRANSPORT
STABILITY
•LONG TERM STORAGE STABILITY
•STABILITY AT HIGHER TEMPERATURE AND
PRESSURE
•OXIATION STABILITY
•HIGHER LEVEL OF UNSTURATION MORE
OXIDATION OCCUR
• METAL SUCH AS COOPER, BRASS,LEAD, WILL
ACCELARATE OXIDATION PROCESS TO FORM
SEDIMENTS.
STORAGE
 COMMERCIALEY DONE BY
PROVIDING NITROGEN BLANKETS
ON STORAGE TANKS.
 AVOID CONTACT WITH OXYGEN.
 USE OF ANTIOXIDENTS.
2/4/2016 35
MICROBIAL CONTAMINATION
 AEROBIC FUNGUS, BACTERIAAND
YEST, MICROORGANISAM USUALLY
GROW AT FUEL BY WATER
CONTAMINATION.
 SULFUR FROM ALGAE REACTION
ON THE TANK SURFACE COUSES
CORROSION.
2/4/2016 36
STORAGE TANK DISPENCING EQUIPMENT AND
MATERIAL COMPATIBILITY
 THERE IS NO REACTION WITH MOST OF THE
METALS
 FAVORABLE METALS- AL,STEEL,FLURINATED
POLY ETHYLINE,TEFLON ETC….
 METALS LIKE BRASS, BRONZE, COPPER CAUSE
REACTIONS.
TRANSPORTATION
 TO AVOID CONTAMINATION DURING
TRANSPORT ENSURE THE FOLLOWING:
 TRUCKS ARE CONSTRUCTED OF
ALUMINIUM,CARBON STEEL.
 THERE IS NO RESIDUAL WATER IN TANK.
 PROPER INSPECTION OR WASH OUT BEFORE
LOADING.
BIODIESELAND PETRODIESEL:
2/4/2016 39
EXPERIMENT #1
(SOURCE :Jurgan kahl, Alex Munak , Olaf Scrader, Hendrik stein ; Comparison of
biodiesel with different diesel fuels regarding exhaust gas emissions and health
effects,2008)
 A 493 CC single cylinder, indirect injection diesel
engine equipped with one hole injector nozzle of
diameter 0.5 mm was used for performance tests
 Biodiesel from refined palm oil stearin and biodiesel
from crude coconut oil blended with diesel at various
mixing ratio.
2/4/2016 40
ENGINE SPECIFICATION
2/4/2016 41
2/4/2016 42
PROPERTIES OF DIESEL AND BIODIESEL
2/4/2016 43
Descriptions High Speed
Diesel
Low Speed
Diesel
Diesel 100%
Methyl
Ester
100%
Ethyl
Ester
Specific Gravity
@15.6/15.6
ASTM
D1298
0.81-0.87 0.920max. 0.8283 0. 8642 0.9204
Kinematic Viscosity
40, 100°C
ASTM
D445
1.8–4.1 8.0 max. 3.36 -
1.14
6.32-
2.04
23.68-5.12
Pour Point
(°C)
ASTM
D97
10 max. 16 max. 1 15 18.2
Flash Point
(°C)
ASTM
D93
52min. 66 min. 65 .73 152 199
Fire Point
(°C)
- -
74 188 210
Corrosion
ASTM
D130
No.1 max. - No.1 No.1 No.1
Carbon
Residue (%)
0.05 - 0.04 0.065 0.2
Heating Value
(KJ/Kg)
- - 47
, 330
40
,390
37
,077
RESULTS
2/4/2016 44
GRAPH 1. RELATION OF DENSITY Vs CONCENTRATIONS OF
BIODIESEL BLENDS
GRAPH 2. THE RELATION BETWEEN
VISCOSITY AT 40 C Vs CONVENTRATION OF
BIODIESEL BLENDS
2/4/2016 45
GRAPH 3. THE RELATION OF POUR POINT
Vs CONCENTRATION OF BIODIESEL
BLENDS
2/4/2016 46
GRAPH 4. THE RELATION OF FLASH POINT
Vs CONCENTRATION OF BIODIESEL
BLENDS
2/4/2016 47
GRAPH 5. THE RELATION OF FIREPONT Vs
CONCENTRATION OF BIODIESEL BLENDS .
2/4/2016 48
GRAPH 6. THE RELATION OF HEATING
VALUE Vs CONCENTRATION OF BIODIESEL
BLENDS
2/4/2016 49
2/4/2016 50
I .SPRAY ANGLE OF
DIESEL OIL .
II .SPRAY ANGLE OF
BIODIESEL OIL (REFINED
PALM OIL STEARIN)
III. SPRAY ANGLE OF BIODIESEL OIL (CRUDE
COCONUT OIL)
2/4/2016 51
ENGINE CHARECTERSTICS
2/4/2016 52
I. Comparison of brake power vs. engine speed for concentration of
biodiesels from refined palm oil stearin blend.
2/4/2016 53
II Comparison of brake power vs. engine speed for concentration of
biodiesels from crude coconut oil blend.
2/4/2016 54
III Comparison of brake power vs. engine speed for type of fuel.
Biodiesels from refined palm oil stearin blend and
crude coconut oil blend
2/4/2016 55
VI Comparison of bsfc vs. engine speed for
type of fuel.
2/4/2016 56
VII Comparison of smoke emission vs. engine
speed for type of fuel.
2/4/2016 57
EXPERIMENT#2
(SOURCE :Oelmühle Leer Connemann GmbH & Co,Comparison of biodiesel with different diesel
fuels regarding exhaust gas emissions and health effectsM, Hanover, Germany ,2007)
 Swedish low sulfur diesel fuel MK1, according to the
Swedish standard SS 15 54 35, obtained from Saybolt
Sweden AB, Gothenburg, Sweden,
 German biodiesel (rapeseed oil methylester; RME),
according to German standard E DIN 51!606, obtained
from Oelmühle Leer Connemann GmbH & Co, fossil
diesel fuel (DF) according to the European standard DIN
EN 590, obtained from Louis Dreyfus & Cie Mineralöl
GmbH, Hanover, Germany,
 a low sulfur diesel fuel with high aromatic compounds
content and flatter boiling characteristics,
 according to the European standard DIN EN 590,
obtained from Röling System Logistic Service GmbH,
Buchholz, Germany. This diesel fuel is referred to as
DF05.
2/4/2016 58
ENGINE SPECIFICATIONS
2/4/2016 59
EXPERIMENT LAYOUT
2/4/2016 60
RESULTS
2/4/2016 61
SPECIFIC CO EMISSION RATES
2/4/2016 62
SPECIFIC HC EMISSION RATES
2/4/2016 63
SPECIFIC NOx EMISSION RATES
2/4/2016 64
SPECIFIC PM EMISSION RATES
2/4/2016 65
SIZE DISTRIBUTION OF PARTICLES WITH RESPECT TO THE
NUMBER OF PARTICLES
2/4/2016 66
SPECIFIC AROMATIC HYDROCARBONS EMISSION RATES
2/4/2016 67
: SPECIFIC ALKENES EMISSION RATE
2/4/2016 68
SPECIFIC EMISSION RATES OD ALDEHYDES AND KETONES
2/4/2016 69
1.Particle emissions stratified
for solid and soluble fraction
.2. Mutagenic effects of the
particle extracts with (+S9)
and without (-S9) metabolic
activation
Conclusions to comparison :
 Biodiesel has close agreements with diesel
characteristics in a CI engine.
 Biodiesel has positive and negative effects on
the emissions
 Biodiesel from refined palm oil stearin can be
used as alternative diesel fuel for small CI
engine without any modifications.
 The mutagenicity of RME emissions is much
lower compared to fossil fuels indicating a
reduced health risk from cancer.
2/4/2016 70
INDIAN PERSPECTIVE ON BIODIESEL:
 Different from biofuel activities in many
other countries of the world .
 Based on the use of non-edible oils
 Oil-bearing trees that can grow on less
fertile land
 Portrays the biodiesel sector first
describes the biodiesel value chain in
India, laying special emphasis on the
feedstock and resulting from this – the
type of land needed for production
2/4/2016 71
BIODIESEL VALUE CHAIN IN INDIA:
2/4/2016 72
2/4/2016 73
2/4/2016 74
POTENTIAL USE OF BIODIESEL IN
INDIA
 Energy security in remote villages.
 National energy security and reduction of
crude oil imports.
 Reduction od Co2 emissions .
2/4/2016 75
Source: reports by German institute on Indian
biodiesel
2/4/2016 76
2/4/2016 77
2/4/2016 78
2/4/2016 79
MANI FINDINGS ON INDIAN
BIODIESEL PERSPECTIVE
 Only a few states encouraging
biodiesels cultivation (TBO based)
 Lack of favorable policies .
 Lack of awareness on biodiesels.
 Consumers and farmers reluctant.
2/4/2016 80
 A promising fuel for developing India
and a source of income for the
agricultural sector.
2/4/2016 81
RECOMMENDATIONS :
 Consumption of biodiesel should be favored
over fossil diesel, provided the energy and
carbon balance of biodiesel production is
positive.
 Demand-side incentives are crucial to get the
biodiesel sector going and make investment
risks more calculable.
 A considerable research effort is needed to
increase knowledge about TBO-based biodiesel
2/4/2016 82
Contd…
 Government should facilitate the productive use
of lands that are owned by various government
departments but remain unutilized
 Government should provide soft loans to
support private biofuel farming.
 Oil-bearing trees can be used among other
species in areas where forest land is assigned for
afforestation.
2/4/2016 83
 Government should preferably support ways of
cultivation that integrate oil-bearing trees into
rural production systems in a way that does not
threaten food production.
2/4/2016 84
CONCLUSIONS:
 Biodiesels is a significant sustainable
energy resource and is used all over the
world.
 Biodiesel can be used as an alternative
fuel without any modification to the
present diesel engine
 Promising alternate fuel.
2/4/2016 85
Scope :
 To do an experiment that satisfies the
concerns in India about biodiesels
being a promising alternative fuel.
 And to conduct further research on
biodiesels and new possible
feedstock.
2/4/2016 86
THANK YOU ……. 
2/4/2016 87

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biodiesel project report presentation

  • 1. PROJECT REPORT PRESENTATION “BIODIESEL –A Perspective ” AUTHOR: MANU H NAIR FACULTY ADVISOR :Er. PRAMOD GEORGE PROFESSIONALADVISOR :Dr. BALAN K.
  • 2. AKNOWLEDGEMENT WE WOULD LIKE TO SINCIERELY THANK:  DR JOHN M.GEORGE –Principal ,Caarmel Engineering College.  DR BALAN K. Former MD to National Coir research and development institute .(External Guide)  ER. KISHEN KARANAKARAN – MD , TMN Biofuels, Pvt Ltd Coimbatore.  DR.KOCHUBABY MANJOORAN, Kochin Refinery , Kochin.  Prof: A.D POULOUSE – H.O.D Department of Mechanical Engineering.  Er. PRAMOD GEORGE –Internal Guide .  Er SHAAN .  And all other faculty members of the Department of Mechanical Engineering.  All our dear friends . 2/4/2016 2
  • 3. OBJECTIVES:  Biodiesel as an alternative fuel without much alterations in existing vehicle technologies.  Comparative study with Petro Diesel .  Biodiesel as a fuel and Industry for Emerging India 2/4/2016 3
  • 6. WHAT IS BIODIESEL? Alternate environment friendly fuel. From animal or plant source. Made of long chain alkyl esters. 2/4/2016 6
  • 7. BIODIESEL ON GLOBAL CONTEXT.  Production rose by 50% from2002-09.  Popular amongst developed countries or ANNEX categorized countries(Kyoto protocol)  Criticism . a) Impact on food security. b) Doubt of overall +ve net Carbon balance.  Automobiles , airplanes , locomotives , factories, houses..etc running on Biofuel. 2/4/2016 7
  • 8. BIODIESEL PRODUCTION FEEDSTOCK (GENERAL) • Virgin oil feedstock • Waste vegetable oil (WVO) • Animal fats • Algae(research in progress) • Fungus (research in progress) 2/4/2016 8
  • 9. CASE STUDY FINDINGS FROM TMN BIOFUELS ON FEEDSTOCK:  Major feed stock is Cashew cornel rejection oil.  Its an acidified oil waste.  Imported from Indonesia from a sister concern  R&D on various other sources underway. 2/4/2016 9
  • 10. PRODUCTION TECHNIQUES 1.Direct use and blending 2.Microemulsions Thermal cracking (Pyrolysis) Transesterification (Alcoholysis) Other types of transesterification . 2/4/2016 10
  • 11. 1.DIRECT USE AND BLENDING:  Direct use: o 100% biofuel with no Petro Diesel. o B100  Blending : o Usual varieties ; B5,B10,B20….B95. o B10 means 10% Petro Diesel and 90% Biodiesel . 2/4/2016 11
  • 12. ADVANTAGES AND DISADVANTAGES OF DIRECT USE OF VEGITABLE OILS:  ADVANTAGES  Liquid nature-portability,  Heat content (80% of diesel fuel),  Ready availability and  Renewability.  DISADVANTAGES  Higher viscosity,  Lower volatility and  The reactivity of unsaturated hydrocarbon chains 2/4/2016 12
  • 13. Known problems, probable cause and potential solutions for using straight vegetable oil in diesels Problem Probable cause Potential solution Short-term 1. Cold weather starting High viscosity, low cetane, and low flash point of vegetable oils Preheat fuel prior to injection. Chemically alter fuel to an ester 2. Plugging and gumming of filters, lines and injectors Natural gums (phosphatides) in vegetable oil. Other ash Partially refine the oil to remove gums. Filter to 4-microns 3. Engine knocking Very low cetane of some oils. Improper injection timing. Adjust injection timing. Use higher compression engines. Preheat fuel prior to injection. Chemically alter fuel to an ester Long-term 4. Coking of injectors on piston and head of engine High viscosity of vegetable oil, incomplete combustion of fuel. Poor combustion at part load with vegetable oils Heat fuel prior to injection. Switch engine to diesel fuel when operation at part load. Chemically alter the vegetable oil to an ester 5. Carbon deposits on piston and head of engine High viscosity of vegetable oil, incomplete Combustion of fuel. Poor combustion at part load with vegetable oils Heat fuel prior to injection. Switch engine to diesel fuel when operation at part load. Chemically alter the vegetable oil to an ester 6. Excessive engine wear High viscosity of vegetable oil, incomplete combustion of fuel. Poor combustion at part load with vegetable oils. Possibly free fatty acids in vegetable oil. Dilution of engine lubricating oil due to blow-by of Heat fuel prior to injection. Switch engine to diesel fuel when operation at part load. Chemically alter the vegetable oil to an ester. Increase motor oil changes. Motor oil additives to inhibit oxidation
  • 14. 2. MICROEMULSIONS  Solves the problem of high viscosity of vegetable oils.  Are solvents live methanol, ethanol etc.  Defined as a colloidal equilibrium dispersion of optically isotropic fluid microstructures.  Usually 1-150 nm range formed spontaneously from two normally immiscible liquids and one or more ionic or non-ionic amphiphiles  Improve spray characteristics by explosive vaporization of the low boiling constituents in the micelles .  Short term performances of both ionic and non-ionic micro emulsions of aqueous ethanol in soybean oil nearly as good as that of No. 2 diesel, in spite of the lower cetane number and energy content . 2/4/2016 14
  • 15. TEST RESULTS SHOWING PROPERTIES OF SHIPP NON -IONIC FUEL. (SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio resource Technologies ,Lincon,NE ,USA 1999.) 2/4/2016 15
  • 16. 2.1 THERMAL CRACKING(PYROLYSIS)  Conversion of one substance into another by means of heat or by heat with the aid of a catalyst .  Heating in the absence of air or oxygen.  And cleavage of chemical bonds to yield small molecules .  First pyrolysis of vegetable oil was conducted in an attempt to synthesize petroleum from vegetable oil. . 2/4/2016 16
  • 17.  The process is simple and effective compared with other cracking processes  Rapeseed oil pyrolyzed to produce a mixture of methyl esters in a tubular reactor between 500 and 850°C and in nitrogen. 2/4/2016 17 (SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio resource Technologies ,Lincon,NE ,USA 1999.)
  • 18. 2.2TRANSESTERIFICATION (ALCOHOLYSIS)  The reaction of a fat or oil with an alcohol to form esters and glycerol.  A catalyst is usually used to improve the reaction rate and yield. 2/4/2016 18 (SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio resource Technologies ,Lincon,NE ,USA 1999.)
  • 19. 2.2.1MECHANISM AND KINETICS 2/4/2016 19 (SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio resource Technologies ,Lincon,NE ,USA 1999.)
  • 20. 2/4/2016 20 SOURCE: Fangrui Ma,Milford A. Hanna, Biodiesel Production: a review , Bio resource Technologies ,Lincon,NE ,USA 1999.)
  • 21. FACTORS AFFECTING FREE FATTY ACIDS IN TRANS ESTERIFICATION:  Moisture.  Catalyst .  Molar ratio .  Reaction time.  Reaction temperature. 2/4/2016 21
  • 22. THE PROCESS OF TRANSESTERIFICATION AND DOWNSTREAM OPERATIONS 2/4/2016 22
  • 23. OTHER TRANSESTERIFICATIONS  In-situ transesterification is taken into consideration.  Found that acid catalyzed in-situ process is better than conventional methods .  By increasing reaction temperature and time and by decreasing the particle size of the soybeans and the water content of ethanol, a purer product was obtained.  The separated glycerol reacted with triglycerides to produce mono- and diglycerides, which are valuable chemical intermediates for detergents and emulsifiers 2/4/2016 23
  • 24. PRODUCTION TECHNIQUES EMPLOYES AT TMN BIOFUELS PVT LTD  METHODS : 1. BASIC ESTERIFICATION 2. TRANS ESTERIFICATION  TMN Biofuels Employs a combination of both .  One of a kind . 2/4/2016 24
  • 25. TMN BIOFUELS BIODIESEL PLANT. 2/4/2016 25
  • 26. PRODUCTION TECHNIQUES 1. Primary production technique 2. Secondary production technique 3. Tertiary production technique 2/4/2016 26
  • 27. PRIMARY PRODUCTION  Oldest and most common production technique. 2/4/2016 27
  • 28. SECONDARY PRODUCTION  Combination of esterification and trans esterification. 2/4/2016 28 Biodiesel from different grade of oils at TMN Biofuels Pvt Ltd.
  • 29. TERTIARY PRODUCTION  ALGAL SYNTHESIS  Third generation process  Costly and time consuming.  Other includes fungal cultivated biodiesels and biodiesels from coffee ground beans .(under R&D) 2/4/2016 29
  • 30. SEQUENTIAL PROCESS IN MAKING BIODIESEL FROM ALGAE (SOURCE: ECOGENICS RESEARCH CENTRE)  FIGURE (A) –MICRO-ALGAE AT LABS FOR SYNTHESIS 2/4/2016 30
  • 31.  FIGURE(B) – MICRO-ALGAE AT LAB BEFORE DRYING 2/4/2016 31
  • 32.  FIGURE(C) – ALGAE DRIED BEFORE OIL EXTRACTION 2/4/2016 32
  • 33.  FIGURE(C) – ALGAE DRIED BEFORE OIL EXTRACTION 2/4/2016 33
  • 34. STORAGE,HANDLING AND TRANSPORT STABILITY •LONG TERM STORAGE STABILITY •STABILITY AT HIGHER TEMPERATURE AND PRESSURE •OXIATION STABILITY •HIGHER LEVEL OF UNSTURATION MORE OXIDATION OCCUR • METAL SUCH AS COOPER, BRASS,LEAD, WILL ACCELARATE OXIDATION PROCESS TO FORM SEDIMENTS.
  • 35. STORAGE  COMMERCIALEY DONE BY PROVIDING NITROGEN BLANKETS ON STORAGE TANKS.  AVOID CONTACT WITH OXYGEN.  USE OF ANTIOXIDENTS. 2/4/2016 35
  • 36. MICROBIAL CONTAMINATION  AEROBIC FUNGUS, BACTERIAAND YEST, MICROORGANISAM USUALLY GROW AT FUEL BY WATER CONTAMINATION.  SULFUR FROM ALGAE REACTION ON THE TANK SURFACE COUSES CORROSION. 2/4/2016 36
  • 37. STORAGE TANK DISPENCING EQUIPMENT AND MATERIAL COMPATIBILITY  THERE IS NO REACTION WITH MOST OF THE METALS  FAVORABLE METALS- AL,STEEL,FLURINATED POLY ETHYLINE,TEFLON ETC….  METALS LIKE BRASS, BRONZE, COPPER CAUSE REACTIONS.
  • 38. TRANSPORTATION  TO AVOID CONTAMINATION DURING TRANSPORT ENSURE THE FOLLOWING:  TRUCKS ARE CONSTRUCTED OF ALUMINIUM,CARBON STEEL.  THERE IS NO RESIDUAL WATER IN TANK.  PROPER INSPECTION OR WASH OUT BEFORE LOADING.
  • 40. EXPERIMENT #1 (SOURCE :Jurgan kahl, Alex Munak , Olaf Scrader, Hendrik stein ; Comparison of biodiesel with different diesel fuels regarding exhaust gas emissions and health effects,2008)  A 493 CC single cylinder, indirect injection diesel engine equipped with one hole injector nozzle of diameter 0.5 mm was used for performance tests  Biodiesel from refined palm oil stearin and biodiesel from crude coconut oil blended with diesel at various mixing ratio. 2/4/2016 40
  • 43. PROPERTIES OF DIESEL AND BIODIESEL 2/4/2016 43 Descriptions High Speed Diesel Low Speed Diesel Diesel 100% Methyl Ester 100% Ethyl Ester Specific Gravity @15.6/15.6 ASTM D1298 0.81-0.87 0.920max. 0.8283 0. 8642 0.9204 Kinematic Viscosity 40, 100°C ASTM D445 1.8–4.1 8.0 max. 3.36 - 1.14 6.32- 2.04 23.68-5.12 Pour Point (°C) ASTM D97 10 max. 16 max. 1 15 18.2 Flash Point (°C) ASTM D93 52min. 66 min. 65 .73 152 199 Fire Point (°C) - - 74 188 210 Corrosion ASTM D130 No.1 max. - No.1 No.1 No.1 Carbon Residue (%) 0.05 - 0.04 0.065 0.2 Heating Value (KJ/Kg) - - 47 , 330 40 ,390 37 ,077
  • 44. RESULTS 2/4/2016 44 GRAPH 1. RELATION OF DENSITY Vs CONCENTRATIONS OF BIODIESEL BLENDS
  • 45. GRAPH 2. THE RELATION BETWEEN VISCOSITY AT 40 C Vs CONVENTRATION OF BIODIESEL BLENDS 2/4/2016 45
  • 46. GRAPH 3. THE RELATION OF POUR POINT Vs CONCENTRATION OF BIODIESEL BLENDS 2/4/2016 46
  • 47. GRAPH 4. THE RELATION OF FLASH POINT Vs CONCENTRATION OF BIODIESEL BLENDS 2/4/2016 47
  • 48. GRAPH 5. THE RELATION OF FIREPONT Vs CONCENTRATION OF BIODIESEL BLENDS . 2/4/2016 48
  • 49. GRAPH 6. THE RELATION OF HEATING VALUE Vs CONCENTRATION OF BIODIESEL BLENDS 2/4/2016 49
  • 50. 2/4/2016 50 I .SPRAY ANGLE OF DIESEL OIL . II .SPRAY ANGLE OF BIODIESEL OIL (REFINED PALM OIL STEARIN)
  • 51. III. SPRAY ANGLE OF BIODIESEL OIL (CRUDE COCONUT OIL) 2/4/2016 51
  • 52. ENGINE CHARECTERSTICS 2/4/2016 52 I. Comparison of brake power vs. engine speed for concentration of biodiesels from refined palm oil stearin blend.
  • 53. 2/4/2016 53 II Comparison of brake power vs. engine speed for concentration of biodiesels from crude coconut oil blend.
  • 54. 2/4/2016 54 III Comparison of brake power vs. engine speed for type of fuel.
  • 55. Biodiesels from refined palm oil stearin blend and crude coconut oil blend 2/4/2016 55
  • 56. VI Comparison of bsfc vs. engine speed for type of fuel. 2/4/2016 56
  • 57. VII Comparison of smoke emission vs. engine speed for type of fuel. 2/4/2016 57
  • 58. EXPERIMENT#2 (SOURCE :Oelmühle Leer Connemann GmbH & Co,Comparison of biodiesel with different diesel fuels regarding exhaust gas emissions and health effectsM, Hanover, Germany ,2007)  Swedish low sulfur diesel fuel MK1, according to the Swedish standard SS 15 54 35, obtained from Saybolt Sweden AB, Gothenburg, Sweden,  German biodiesel (rapeseed oil methylester; RME), according to German standard E DIN 51!606, obtained from Oelmühle Leer Connemann GmbH & Co, fossil diesel fuel (DF) according to the European standard DIN EN 590, obtained from Louis Dreyfus & Cie Mineralöl GmbH, Hanover, Germany,  a low sulfur diesel fuel with high aromatic compounds content and flatter boiling characteristics,  according to the European standard DIN EN 590, obtained from Röling System Logistic Service GmbH, Buchholz, Germany. This diesel fuel is referred to as DF05. 2/4/2016 58
  • 62. 2/4/2016 62 SPECIFIC HC EMISSION RATES
  • 63. 2/4/2016 63 SPECIFIC NOx EMISSION RATES
  • 64. 2/4/2016 64 SPECIFIC PM EMISSION RATES
  • 65. 2/4/2016 65 SIZE DISTRIBUTION OF PARTICLES WITH RESPECT TO THE NUMBER OF PARTICLES
  • 66. 2/4/2016 66 SPECIFIC AROMATIC HYDROCARBONS EMISSION RATES
  • 67. 2/4/2016 67 : SPECIFIC ALKENES EMISSION RATE
  • 68. 2/4/2016 68 SPECIFIC EMISSION RATES OD ALDEHYDES AND KETONES
  • 69. 2/4/2016 69 1.Particle emissions stratified for solid and soluble fraction .2. Mutagenic effects of the particle extracts with (+S9) and without (-S9) metabolic activation
  • 70. Conclusions to comparison :  Biodiesel has close agreements with diesel characteristics in a CI engine.  Biodiesel has positive and negative effects on the emissions  Biodiesel from refined palm oil stearin can be used as alternative diesel fuel for small CI engine without any modifications.  The mutagenicity of RME emissions is much lower compared to fossil fuels indicating a reduced health risk from cancer. 2/4/2016 70
  • 71. INDIAN PERSPECTIVE ON BIODIESEL:  Different from biofuel activities in many other countries of the world .  Based on the use of non-edible oils  Oil-bearing trees that can grow on less fertile land  Portrays the biodiesel sector first describes the biodiesel value chain in India, laying special emphasis on the feedstock and resulting from this – the type of land needed for production 2/4/2016 71
  • 72. BIODIESEL VALUE CHAIN IN INDIA: 2/4/2016 72
  • 75. POTENTIAL USE OF BIODIESEL IN INDIA  Energy security in remote villages.  National energy security and reduction of crude oil imports.  Reduction od Co2 emissions . 2/4/2016 75
  • 76. Source: reports by German institute on Indian biodiesel 2/4/2016 76
  • 80. MANI FINDINGS ON INDIAN BIODIESEL PERSPECTIVE  Only a few states encouraging biodiesels cultivation (TBO based)  Lack of favorable policies .  Lack of awareness on biodiesels.  Consumers and farmers reluctant. 2/4/2016 80
  • 81.  A promising fuel for developing India and a source of income for the agricultural sector. 2/4/2016 81
  • 82. RECOMMENDATIONS :  Consumption of biodiesel should be favored over fossil diesel, provided the energy and carbon balance of biodiesel production is positive.  Demand-side incentives are crucial to get the biodiesel sector going and make investment risks more calculable.  A considerable research effort is needed to increase knowledge about TBO-based biodiesel 2/4/2016 82
  • 83. Contd…  Government should facilitate the productive use of lands that are owned by various government departments but remain unutilized  Government should provide soft loans to support private biofuel farming.  Oil-bearing trees can be used among other species in areas where forest land is assigned for afforestation. 2/4/2016 83
  • 84.  Government should preferably support ways of cultivation that integrate oil-bearing trees into rural production systems in a way that does not threaten food production. 2/4/2016 84
  • 85. CONCLUSIONS:  Biodiesels is a significant sustainable energy resource and is used all over the world.  Biodiesel can be used as an alternative fuel without any modification to the present diesel engine  Promising alternate fuel. 2/4/2016 85
  • 86. Scope :  To do an experiment that satisfies the concerns in India about biodiesels being a promising alternative fuel.  And to conduct further research on biodiesels and new possible feedstock. 2/4/2016 86
  • 87. THANK YOU …….  2/4/2016 87