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We arehere
2050 1850
THE WORLD IS ADDICTED TO OIL.
IT’S TIME FOR AN INTERVENTION.
FUEL
Change your fuel …..change the world
BIOETHAN
OL
Bioethanol production from fruits
and vegetable wastes
Archana T Janamatti
10876
What is bioethanol?
• Bio-ethanol is ethyl alcohol or grain alcohol that is
derived exclusively from the fermentation of plant
carbohydrates (sugar or starch)
• Chemically bioethanol is C2H5
 One of the widely used alternative automotive fuel in
the world (majority of the production and
consumption takes place in Brazil & U.S.A )
Mustafa et al., 2009
World bioethanol production
COUNTRIES
USA
BRAZIL
CHINA
INDIA
Largest Bioethanol
Producer
204 Bioethanol
Production Plants
Corn
USA
Fourth
largest
producer,
Sugarcane
molasses
INDIA
1st
Generation
Biofuels
2nd
Generation
Biofuels
3rd
Generation
Biofuels
Bioethanol
Biodiesel, Bio-
ethyl tertiary
butyl ether and
Biogas
Bioethanol, Biodiesel,
Biomethyl, Biobuthyl,
Biomethyl tertiary
buthyl ether and
Biomethane,
Biohydrogen etc.
Biofuels from Algaes or
Genetically Modified
Vegetables and by
Integrated Biorefinery
Technology
Second
generation
(lignocellulosic
biomass)
fruits and vegetable
waste, grass, Crop
residue, wood , forest
thinnings
Third generation
Algal biomass
Ring Chart 2
Placeholderfor your own sub headline
First
generation
(food or starchy
crops)
Sugarcane
Corn
Palm oil
Sweet sorghum
Sugarbeet
Rice
Wheat
Potato and tapioca
Feed stocks for
Bioethanol
production
Food Vs Fuel
No, But I can offer
you a gallon of
Ethanol
CANT YOU SEE IM TRYING
TO FIGHT FOR GLOBAL
WARMING
30–40% - discarded as wasteSolid waste disposal problem –
environment pollution
Generated from farm to fork
Generated from processing units
account for 30–50% of the input
materials
Peel, Pomace, seed, core, stone
India is the second largest
producer of fruits &
vegetables
No waste is waste until it is wasted…….
Losses and wastage (%) Waste
Generated
(Million
Tonnes)
Processing Distribution consumption
India 25 10 7 1.81
China 2 8 15 31.98
Phillippines 25 10 7 6.53
Malaysia 25 10 7 0.68
Sharma et al., 2016
Moisture
(g)
Protein
(g)
Fiber (g) Carbohydrate
(g)
Apple
pomace
3.97 4.45 48.70 48 Joshi &
Attri (2006)
Pineapple
peel
9.4 8.7 - 29.1 Bandikari et
al.(2004)
Banana peel 10.5 6.02 - 17.8 Sharoba et
al. (2013)
Potato solid
waste
85-87 3-5 19.86 27-35 Arapaglau
et al.(2010)
Orange peel 4.23 5.97 28.56 25.92 Sharoba et
al. (2013)
Cauliflower
leaves
8.6 16.1 28 24 Wadhwat et
al. (2006)
Composition of fruits and vegetable waste (per 100gm)
Production Methods of Bioethanol
Sugar-based
Bioethanol
Production
Starch-based
Bioethanol
Production
Lignocellulose-
based
Bioethanol
Production
Fruits and vegetable waste based
Bioethanol Production
Pretreatment
Dehydration
Distillation
Fermentation
Hydrolysis
Feedstocks
Bioethanol
Fruits and vegetable waste based
Bioethanol Production
Pretreatment
Dehydration
Distillation
Fermentation
Hydrolysis
Feedstocks
Bioethanol
Physical
Pretreatment
Chemical Pretreatment
Physicochemical Pretreatment
Biological Pretreatment
Acid hydrolysis
Enzymatic hydrolysis
Case studies
To optimize the fermentation parameters (inoculum concentration,
temperature and incubation period) for maximizing ethanol production
using co-cultures of Saccharomyces cerevisisae G and Pachysolen
tannophilus MTCC 107.
Objectiv
e:
Case Study -I
Kinnow waste Banana peel
Cellulose (%) 23.48 28.67
Hemicellulose (%) 20.54 18.40
Total sugar (mg /g) 79.10 92.88
Reducing sugar
(mg/g)
23.07 36.83
Composition of kinnow waste and banana peel
Materials and methods:
Kinnow waste (Peel + segment membranes + seeds) : Banana peel mixed in the
ratio 4:6
Steam explosion (vertical autoclave at 15 psi for 1.0 h)
Simultaneous saccharification and fermentation (SSF)
Enzymatic saccahrification – Cellulase from Trichoderma reesei RUT C -30 at 4 FPU g -1
Fermentation – Saccharomyces cerevisiae G and Pachysolen tannophilus
Inoculum concentration for ethanol production
0.394 gg -1 6% S. c and 4% P. t
Effect of different temperature and incubation period on ethanol yield
Conclusion:
• The temperature - 30 0C
• Inoculum size of Saccharomyces cerevisae G 6% (v/v) and
Pachysolen tannophilus MTCC 1077 4% (v/v)
• Incubation period of 48 hours
These optimized fermentation parameters could be used for
further scaling up of the process to a pilot scale or commercial
fermenter
BIOMASS AND BIOENERGY 69 (2014) 66-70
Residues of dates from the food
industry as a new cheap feedstock for
ethanol production Sofien et al., 2014
Case Study -II
Objective:
To evaluate the feasibility of production of bioethanol from
substrate with a high level of sugar (date by-products).
Material and methods:
Saccharomyces cerevisiae
Zygosaccharomyces rouxii
Candida pelliculosa
Sugar concentration of culture medium -174 kg m -3 and 358 kg m -3
100 µL of yeast suspension
Batch fermentation – 28 °C for 72 hour
Growth of yeasts in medium
containing 174 kg m -3 sugar
Growth of yeasts in medium
containing 358 kg m -3 sugar
0 18 24 42 48 66 72 180 24 42 48 66 72
Parameters 174 kg m -3 (C1) 358 kg m -3 (C2)
S. cerevisiae Z. rouxii C. pelliculosa S. cerevisiae Z. rouxii C. pelliculosa
Eq Glu
consumed (%)
94.0 ± 0.2
67.0 ± 2.0 71.0 ± 0.1 4.0 ± 0.1 41.0 ± 0.2 3.0± 0.4
Ethanol
(Kg m -3)
63.0 ± 0.1 33.0 ± 2.0 41.0 ± 0.3
**
55.0 ± 1.0
**
Glycerol
(Kg m -3)
5.0 ± 0.1 4.6 ± 0.1 4.6 ± 0.1
**
10.0 ± 0.1
**
Q ethanol
(Kg m-3 h-1)
0.9 ± 0.1 0.5 ± 0.1 0.6 ± 0.1
**
0.8 ± 0.1
**
Y EtOH/S 38.0 ± 0.5 29.0 ± 0.1 34.0 ± 0.2
**
38.0 ± 0.1
**
Table: Ethanol production from date syrup containing 174 kg m -3 and 358 kg m -3
sugar concentration
** - < limit of detection
Conclusion
• The choice of yeast strain effect the bioethanol
production
• The maximum ethanol from concentrated date syrup
could be achieved by Zygosaccharomyces rouxii
• It is preferable to use S. cerevisiae if the culture
medium is less concentrated in sugar
Bioethanol production from grape and sugar
beet pomaces by solid-state fermentation
Case Study -III
Rodriguez et al., 2010
Objective: To study the ethanol production from grape
and sugar beet pomaces by solid -state fermentation
Materials and methods:
Saccharomyces cerevisae PM -16 (10 8 cells/ g of pomace)
Liquid fermentation on sugar beet juice (LF-SBJ)
Solid state fermentation on sugar beet and grape pomace
Incubated in anaerobic environment at 28 °C for 96 hours
SSF-GP : Solid state fermentation on grape pomace
SSF – SBP : Solid state fermentation on beet pomace
LF-SBJ : Liquid fermentation on sugar beet juice
A
B
Ethanol yield Consumption of sugar
Conclusion:
• Ethanol was found more concentrated in solid state fermentation
• Maximum ethanol concentration was found in 48 hour of
fermentation.
• Decrease of waste mass
• Technological and economical advantage of solid state fermentation
could be studied further
Ethanol yield based on consumed sugars and percentage of the
theoretical yield at 48 h of fermentation
Bioethanol production from taro waste using thermo-
tolerant yeast Kluveromyces marxianus K21
Wu et al.,2016
Objective: To establish an effective process to produce bioethanol from
taro waste using thermo-tolerant yeast Kluyveromyces marxianus K21
Material and methods
• Taro waste- outer core of taro corm with residual taro starch and cork
• Enzyme hydrolysis of starch
Liquification: α-Amylase (0.9 ml)
Saccharification: Amyloglucosidase ( 30 µL)
• Fermentation: 24 to 72 h at 40 °C
• Basal medium: 40 g of glucose
• Taro waste medium: Taro waste
Fermentation in basal and Taro waste medium
18.17 g/L , 1.30 g/L
Kinetic parameters of four different concentration of taro
waste in medium
Kinetic parameters of different inoculum size
SHF SSF
DESCRIIPTION 40 °C 45 °C 50 °C 40 °C 45 °C 50 °C
Ethanol (g/L) 43.46 43.01 19.15 48.98 47.5 20.86
Sugar consumed (g/L) 96.84 97.96 49.62 - - -
Productivity (g/L/h) 1.73 1.48 0.66 2.23 1.98 0.95
Theoretical yield (%) 87.83 86.02 - - - -
Kinetic parameter of K. marxianus K21 by the SHF and SSF under
different temperatures
- The values cannot be obtained due simultaneously starch hydrolysis and
fermentation
Conclusion
Taro waste is an attractive agricultural waste to
produce bioethanol
100 g/L Taro waste loading amount
5% inoculum
40 °C temperature
SSF fermentation method
Ethanol production from potato peel
waste (PPW) Arapoglou et al., 2010
Composition of potato peel waste
Materials and methods
• S. cerevisae var. bayanus – 6% inoculum size
• Acid hydrolysis - 0.5 M HCl
Enzymes
1. Viscozyme L - Aspergillus aculeatus
2. Ternamyl 120 L -B. licheniformis
3. Liquozyme Supra - Bacillus lichneniformis
4. Celluclast 1.5 L - Trichoderma reesei
Fermentation - 32 °C for 2 days
Fermentable sugar released from enzymatic hydrolysis
L: Liquozyme
T: Ternamyl
V: Viscozyme
Acid hydrolysis
Fermentable sugar – 18.15 g L-1
Consumed sugar – 14.08 gL-1
Effect of different enzyme combinations on ethanol production
L: Liquozyme
T: Ternamyl
V: Viscozyme
Acid hydrolysis
Ethanol – 6.97 g L-1
Product yield (Y p/s) – 0.46 gL-1
Theoretical yield – 92%
Conclusion
• Enzymatic hydrolysis liberates a higher amount of fermentable reducing
sugar
• The enzyme combination Ternamyl 0.24 KNU + Viscozyme 12 FBGU +
Celluclast 1% produced maximum ethanol yield
• The results demonstrated that potato peel waste can efficiently used for
ethanol production
Conclusion
• Inoculum, enzyme and substrate concentrates besides
temperature, time and incubation period plays
important role in obtaining good ethanol yield
• Ethanol yield indicates that fruits and vegetable waste
are potential candidate for bioethanol production
India imports nearly 70 % of its annual
crude petroleum requirement (~ 110
million tons)
Expenditure on crude purchase is in the
range of Rs. 1600 billion/ year
The notification on EBP (Ethanol blending
programme) was approved by Government
of India (GOI) - 5% ethanol doping in
petrol is mandatory in 9 states and 4 union
territories with effect from 1st January
2003
The national policy on biofuel (2009)
approved by GOI has planned to 20%
biofuel blending (biodiesel and bioethanol)
by 2017
Due to insufficient supply
of the sugar molasses the
government of india is
not able to meet 5 %
blending
Thus India have to look
beyond sugar cane
molasses
Fruits and vegetables
waste could be a
promising solution
In 1925, Henry Ford quoted ethanol as
“The fuel of the future”. “The fuel of the
future is going to come from apples,
weeds, sawdust almost anything. There is
fuel in every bit of vegetable matter that
can be fermented”. Today Henry Ford’s
futuristic vision significance can be easily
understood
THANKYOU

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Bioethanol production from fruits and vegetable wastes

  • 1.
  • 3.
  • 4. THE WORLD IS ADDICTED TO OIL. IT’S TIME FOR AN INTERVENTION. FUEL Change your fuel …..change the world
  • 6. Bioethanol production from fruits and vegetable wastes Archana T Janamatti 10876
  • 7. What is bioethanol? • Bio-ethanol is ethyl alcohol or grain alcohol that is derived exclusively from the fermentation of plant carbohydrates (sugar or starch) • Chemically bioethanol is C2H5  One of the widely used alternative automotive fuel in the world (majority of the production and consumption takes place in Brazil & U.S.A ) Mustafa et al., 2009
  • 8. World bioethanol production COUNTRIES USA BRAZIL CHINA INDIA Largest Bioethanol Producer 204 Bioethanol Production Plants Corn USA Fourth largest producer, Sugarcane molasses INDIA
  • 9. 1st Generation Biofuels 2nd Generation Biofuels 3rd Generation Biofuels Bioethanol Biodiesel, Bio- ethyl tertiary butyl ether and Biogas Bioethanol, Biodiesel, Biomethyl, Biobuthyl, Biomethyl tertiary buthyl ether and Biomethane, Biohydrogen etc. Biofuels from Algaes or Genetically Modified Vegetables and by Integrated Biorefinery Technology
  • 10.
  • 11. Second generation (lignocellulosic biomass) fruits and vegetable waste, grass, Crop residue, wood , forest thinnings Third generation Algal biomass Ring Chart 2 Placeholderfor your own sub headline First generation (food or starchy crops) Sugarcane Corn Palm oil Sweet sorghum Sugarbeet Rice Wheat Potato and tapioca Feed stocks for Bioethanol production
  • 12. Food Vs Fuel No, But I can offer you a gallon of Ethanol CANT YOU SEE IM TRYING TO FIGHT FOR GLOBAL WARMING
  • 13. 30–40% - discarded as wasteSolid waste disposal problem – environment pollution Generated from farm to fork Generated from processing units account for 30–50% of the input materials Peel, Pomace, seed, core, stone India is the second largest producer of fruits & vegetables No waste is waste until it is wasted…….
  • 14. Losses and wastage (%) Waste Generated (Million Tonnes) Processing Distribution consumption India 25 10 7 1.81 China 2 8 15 31.98 Phillippines 25 10 7 6.53 Malaysia 25 10 7 0.68 Sharma et al., 2016
  • 15. Moisture (g) Protein (g) Fiber (g) Carbohydrate (g) Apple pomace 3.97 4.45 48.70 48 Joshi & Attri (2006) Pineapple peel 9.4 8.7 - 29.1 Bandikari et al.(2004) Banana peel 10.5 6.02 - 17.8 Sharoba et al. (2013) Potato solid waste 85-87 3-5 19.86 27-35 Arapaglau et al.(2010) Orange peel 4.23 5.97 28.56 25.92 Sharoba et al. (2013) Cauliflower leaves 8.6 16.1 28 24 Wadhwat et al. (2006) Composition of fruits and vegetable waste (per 100gm)
  • 16. Production Methods of Bioethanol Sugar-based Bioethanol Production Starch-based Bioethanol Production Lignocellulose- based Bioethanol Production
  • 17. Fruits and vegetable waste based Bioethanol Production Pretreatment Dehydration Distillation Fermentation Hydrolysis Feedstocks Bioethanol
  • 18.
  • 19. Fruits and vegetable waste based Bioethanol Production Pretreatment Dehydration Distillation Fermentation Hydrolysis Feedstocks Bioethanol Physical Pretreatment Chemical Pretreatment Physicochemical Pretreatment Biological Pretreatment Acid hydrolysis Enzymatic hydrolysis
  • 21. To optimize the fermentation parameters (inoculum concentration, temperature and incubation period) for maximizing ethanol production using co-cultures of Saccharomyces cerevisisae G and Pachysolen tannophilus MTCC 107. Objectiv e: Case Study -I
  • 22. Kinnow waste Banana peel Cellulose (%) 23.48 28.67 Hemicellulose (%) 20.54 18.40 Total sugar (mg /g) 79.10 92.88 Reducing sugar (mg/g) 23.07 36.83 Composition of kinnow waste and banana peel
  • 23. Materials and methods: Kinnow waste (Peel + segment membranes + seeds) : Banana peel mixed in the ratio 4:6 Steam explosion (vertical autoclave at 15 psi for 1.0 h) Simultaneous saccharification and fermentation (SSF) Enzymatic saccahrification – Cellulase from Trichoderma reesei RUT C -30 at 4 FPU g -1 Fermentation – Saccharomyces cerevisiae G and Pachysolen tannophilus
  • 24. Inoculum concentration for ethanol production 0.394 gg -1 6% S. c and 4% P. t
  • 25.
  • 26. Effect of different temperature and incubation period on ethanol yield
  • 27. Conclusion: • The temperature - 30 0C • Inoculum size of Saccharomyces cerevisae G 6% (v/v) and Pachysolen tannophilus MTCC 1077 4% (v/v) • Incubation period of 48 hours These optimized fermentation parameters could be used for further scaling up of the process to a pilot scale or commercial fermenter
  • 28. BIOMASS AND BIOENERGY 69 (2014) 66-70 Residues of dates from the food industry as a new cheap feedstock for ethanol production Sofien et al., 2014 Case Study -II
  • 29. Objective: To evaluate the feasibility of production of bioethanol from substrate with a high level of sugar (date by-products). Material and methods: Saccharomyces cerevisiae Zygosaccharomyces rouxii Candida pelliculosa Sugar concentration of culture medium -174 kg m -3 and 358 kg m -3 100 µL of yeast suspension Batch fermentation – 28 °C for 72 hour
  • 30. Growth of yeasts in medium containing 174 kg m -3 sugar Growth of yeasts in medium containing 358 kg m -3 sugar 0 18 24 42 48 66 72 180 24 42 48 66 72
  • 31. Parameters 174 kg m -3 (C1) 358 kg m -3 (C2) S. cerevisiae Z. rouxii C. pelliculosa S. cerevisiae Z. rouxii C. pelliculosa Eq Glu consumed (%) 94.0 ± 0.2 67.0 ± 2.0 71.0 ± 0.1 4.0 ± 0.1 41.0 ± 0.2 3.0± 0.4 Ethanol (Kg m -3) 63.0 ± 0.1 33.0 ± 2.0 41.0 ± 0.3 ** 55.0 ± 1.0 ** Glycerol (Kg m -3) 5.0 ± 0.1 4.6 ± 0.1 4.6 ± 0.1 ** 10.0 ± 0.1 ** Q ethanol (Kg m-3 h-1) 0.9 ± 0.1 0.5 ± 0.1 0.6 ± 0.1 ** 0.8 ± 0.1 ** Y EtOH/S 38.0 ± 0.5 29.0 ± 0.1 34.0 ± 0.2 ** 38.0 ± 0.1 ** Table: Ethanol production from date syrup containing 174 kg m -3 and 358 kg m -3 sugar concentration ** - < limit of detection
  • 32. Conclusion • The choice of yeast strain effect the bioethanol production • The maximum ethanol from concentrated date syrup could be achieved by Zygosaccharomyces rouxii • It is preferable to use S. cerevisiae if the culture medium is less concentrated in sugar
  • 33. Bioethanol production from grape and sugar beet pomaces by solid-state fermentation Case Study -III Rodriguez et al., 2010
  • 34. Objective: To study the ethanol production from grape and sugar beet pomaces by solid -state fermentation Materials and methods: Saccharomyces cerevisae PM -16 (10 8 cells/ g of pomace) Liquid fermentation on sugar beet juice (LF-SBJ) Solid state fermentation on sugar beet and grape pomace Incubated in anaerobic environment at 28 °C for 96 hours
  • 35. SSF-GP : Solid state fermentation on grape pomace SSF – SBP : Solid state fermentation on beet pomace LF-SBJ : Liquid fermentation on sugar beet juice A B Ethanol yield Consumption of sugar
  • 36. Conclusion: • Ethanol was found more concentrated in solid state fermentation • Maximum ethanol concentration was found in 48 hour of fermentation. • Decrease of waste mass • Technological and economical advantage of solid state fermentation could be studied further Ethanol yield based on consumed sugars and percentage of the theoretical yield at 48 h of fermentation
  • 37. Bioethanol production from taro waste using thermo- tolerant yeast Kluveromyces marxianus K21 Wu et al.,2016
  • 38. Objective: To establish an effective process to produce bioethanol from taro waste using thermo-tolerant yeast Kluyveromyces marxianus K21 Material and methods • Taro waste- outer core of taro corm with residual taro starch and cork • Enzyme hydrolysis of starch Liquification: α-Amylase (0.9 ml) Saccharification: Amyloglucosidase ( 30 µL) • Fermentation: 24 to 72 h at 40 °C • Basal medium: 40 g of glucose • Taro waste medium: Taro waste
  • 39. Fermentation in basal and Taro waste medium 18.17 g/L , 1.30 g/L
  • 40. Kinetic parameters of four different concentration of taro waste in medium
  • 41. Kinetic parameters of different inoculum size
  • 42. SHF SSF DESCRIIPTION 40 °C 45 °C 50 °C 40 °C 45 °C 50 °C Ethanol (g/L) 43.46 43.01 19.15 48.98 47.5 20.86 Sugar consumed (g/L) 96.84 97.96 49.62 - - - Productivity (g/L/h) 1.73 1.48 0.66 2.23 1.98 0.95 Theoretical yield (%) 87.83 86.02 - - - - Kinetic parameter of K. marxianus K21 by the SHF and SSF under different temperatures - The values cannot be obtained due simultaneously starch hydrolysis and fermentation
  • 43. Conclusion Taro waste is an attractive agricultural waste to produce bioethanol 100 g/L Taro waste loading amount 5% inoculum 40 °C temperature SSF fermentation method
  • 44. Ethanol production from potato peel waste (PPW) Arapoglou et al., 2010
  • 45. Composition of potato peel waste
  • 46. Materials and methods • S. cerevisae var. bayanus – 6% inoculum size • Acid hydrolysis - 0.5 M HCl Enzymes 1. Viscozyme L - Aspergillus aculeatus 2. Ternamyl 120 L -B. licheniformis 3. Liquozyme Supra - Bacillus lichneniformis 4. Celluclast 1.5 L - Trichoderma reesei Fermentation - 32 °C for 2 days
  • 47. Fermentable sugar released from enzymatic hydrolysis L: Liquozyme T: Ternamyl V: Viscozyme Acid hydrolysis Fermentable sugar – 18.15 g L-1 Consumed sugar – 14.08 gL-1
  • 48. Effect of different enzyme combinations on ethanol production L: Liquozyme T: Ternamyl V: Viscozyme Acid hydrolysis Ethanol – 6.97 g L-1 Product yield (Y p/s) – 0.46 gL-1 Theoretical yield – 92%
  • 49. Conclusion • Enzymatic hydrolysis liberates a higher amount of fermentable reducing sugar • The enzyme combination Ternamyl 0.24 KNU + Viscozyme 12 FBGU + Celluclast 1% produced maximum ethanol yield • The results demonstrated that potato peel waste can efficiently used for ethanol production
  • 50. Conclusion • Inoculum, enzyme and substrate concentrates besides temperature, time and incubation period plays important role in obtaining good ethanol yield • Ethanol yield indicates that fruits and vegetable waste are potential candidate for bioethanol production
  • 51. India imports nearly 70 % of its annual crude petroleum requirement (~ 110 million tons) Expenditure on crude purchase is in the range of Rs. 1600 billion/ year The notification on EBP (Ethanol blending programme) was approved by Government of India (GOI) - 5% ethanol doping in petrol is mandatory in 9 states and 4 union territories with effect from 1st January 2003 The national policy on biofuel (2009) approved by GOI has planned to 20% biofuel blending (biodiesel and bioethanol) by 2017 Due to insufficient supply of the sugar molasses the government of india is not able to meet 5 % blending Thus India have to look beyond sugar cane molasses Fruits and vegetables waste could be a promising solution
  • 52. In 1925, Henry Ford quoted ethanol as “The fuel of the future”. “The fuel of the future is going to come from apples, weeds, sawdust almost anything. There is fuel in every bit of vegetable matter that can be fermented”. Today Henry Ford’s futuristic vision significance can be easily understood

Editor's Notes

  1. Exhaustible fossil fuels represents 80% of the total world energy supply. At constant production and consumption, the presently known reserves of oil will last around 41 years, natural gas 64 years, and coal 155 years Although very simplified, such an analysis illustrates why fossil fuels cannot be considered as the world’s main source of energy for more than one or two generations. Clearly fossil fuel reserves are finite - it's only a matter of when they run out - not if.  Globally - every year we currently consume the equivalent of over 11 billion tonnes of oil in fossil fuels. Crude oil reserves are vanishing at the rate of 4 billion tonnes a year1 – if we carry on at this rate without any increase for our growing population or aspirations, our known oil deposits will be gone by 2052.
  2. Increase on world’s energy demand and the progressive depletion of oil reserves motivate the search for alternative energy resources, especially for those derived from renewable materials such as biomass. Global concern about climate change and the consequent need to diminish greenhouse gases emissions have encouraged the use of bioethanol as a gasoline replacement or additive
  3. Biofuel is the fuel which is produced from organic products and wastes. The common commercially used biofuels are bioethanol, biodiesel and biomethane. Bioethanol is made from sugar, algae, wheat and sugar beet Biodiesel is made from vegetable oil, algal lipids, animal fats Biomethane can be produced from waste organic material, sewage, agriculture waste and domestic wastes.
  4. Looking the bioethanol production statistics, all around the world the largest producer is USA. The country has two hundred and four bioethanol plants and produces bioethanol from corn. Brazil the second bioethanol producer, it has three hundred thirty five bioethanol plants. Brazil produced bioethanol from sugar cane. And the third producer is China, produces from corn. Also cassava and sweet patato are competitive feedstocks for China.
  5. Biofuels are basically classified into four groups considering their production methods and feedstocks. First generation biofuels are produced from agricultural feedstocks. Especially bioethanol is obtained from sugar- and starch-based feedstocks. Second generation biofuels are…..Production of these fuels targets the usage of non-food feedstocks and is converted from lignocellulose-based feedstocks. Third generation biofuels are fuels obtained from algae, or liquid or solid biofuels obtained by integrated biorefinery technology from trees, grass, weeds, wastes, residues, and new oilseeds, or biofuels produced from genetically modified vegetables containing less lignin and more cellulose. Fourth generation biofuels, also known as carbon negative biofuels, are obtained from genetically modified raw materials. It is mainly aimed to provide lower carbon dioxide (CO2) emissions released to the atmosphere with the developed technologies. It is unknown how soon after 2030 they will be used commercially.
  6. Production method of bioethanol differs according to the feedstock used. Here is the production diagram of the bioethanol. Extraction for sugar based feedstock, saccharification for starch-based feedstock are applied. For cellulose-based feedstock, first pretreatment and hydrolysis is applied to convert fermentable sugars. After fermentation, fermented mash is distilled and dehydrated to produce bioethanol with 99% purity.
  7. Lignocellulose-based bioethanol depends on pretreatment, hydrolysis, fermentation, distillation and dehydration steps. Plant cell microfibrils are composed of cellulose, hemicellulose and lignin. To release the pentose and hexose sugars for fermentation, this structure should be broke down. Because of the robust structure of plant wall cell, it requires pretreatment to improve enzyme accessibility in enzymatic hydrolysis. In brief, pretreatment is essential