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IOSR Journal of Mechanical and Civil Engineering (IOSR-JMCE)
e-ISSN: 2278-1684,p-ISSN: 2320-334X, Volume 11, Issue 6 Ver. IV (Nov- Dec. 2014), PP 66-68
www.iosrjournals.org
www.iosrjournals.org 66 | Page
Optimization and Standardisation of Waste Cooking Oil into Bio-
Diesel
Mr.Ankit Kumar, Rahul Rana,NavdeepNandal,Mohit Singh, Narender Singh
Department of Mechanical Engineering,Affilated to KurukshetraUniversity,Kurukshetra
Guru Nanak Institutions, Mullana, Ambala,India
Abstract: The study was conducted to investigate the optimum conditions for biodiesel formation from waste
cooking oil coming after alkaline transesterification process in combination with methanol. Some important
variables such as volumetric ratio, types of reactants and catalytic activities were selected to obtain a high
quality biodiesel fuel with the specification of American Society Of Testing and Materials. The research
investigates the biodiesel obtained under optimum conditions from waste cooking oil of good quality and could
be used as a diesel fuel which considered as potential use of waste cooking oil.
Keywords: Biodeisel, methanol, waste oil, transesterification.
Abbreviations: Waste cooking oil, American Society Of Testing and Materials.
I. Introduction
New alternative and renewable fuel(biodiesel) has received a considerable attention recently due to
occurance of oil depletion, global warming and green house effect. Biodiesel is a good alternative energy which
is one of the most promising energy sources. In accordance with the US standards specifications of biodiesel, it
is non toxic, biodegradable, produced from renewable sources and contributes a minimal amount of net green
house gases and contributes such as CO2and NO2 emission and sulphur to the atmosphere.The high viscocity
and poor volatility are major limitations of vegetable oil for their utilisation as fuel in diesel engines. Among
more then 350 identified oil bearing crops only sunflower, soyabean are considered as potential alternative fuel
for diesel engines. The large amount of waste cooking oil was produced from restaurents, catering establishment
and food industries every year. The objective of this study were to compare optimum conditions of fatty acids
methyl easter and potential use of waste cooking oil.
II. Materials and Methods
Materials: Waste cooking oil, Potassium Hydroxide, Methanol.
Method: Transesterification reaction
H2C—OOC—R1 CH3—OOC—R1H2C—OH
HO—OOC—R2+3CH3OH =CH3—OOC—R2 + H2C—OH
H2O—OOC—R3 CH3—OOC—R3H2C—OH
Cereals Methanol Biodiesel Glycerol
The vegetable oil must be chemically altered or blended with diesel fuel to prevent premature engine
failure. Blending, cracking emulsification of vegetable oil may be overcome the problems such as deposit
formation, carbon buildup and lubrication oil contamination which otherwise cause premature engine failure.
Literature
Refaat et al. (2008) have reported transesterification of waste vegetable oil with methanol and
potassium hydroxide for the product of biodiesel. The best yield percentage was obtained using a methanol/oil
molar ratio of 6:1, potassium hydroxide as catalyst (1%) and 65oC temperature for one hour. The yield
percentage obtained from vegetable oil was comparable to that obtained from neat vegetable oil which reached
96.15% under optimum condition. The produced biodiesel fuel, whether from neat vegetable oil or waste
vegetable oil, was within the recommended standards of biodiesel fuel. Fan et al. (2009) have performed the two
step transesterification reaction of recycled canola oil due ti its higher fatty acids content. The results showed
that alkali-catalized that was carried out at 6/1 molar ratio of methanol to oil and 1% KOH produced biodiesel.
Theory
Optimization And Standardisation Of Waste Cooking Oil Into Bio-Diesel
www.iosrjournals.org 67 | Page
Table1.Taguchi design of experiment technique
Variables: A, B, C
Levels: 1, 2, 3
Table2.Process parameters selected for standardisation of transesterification process
S.No. Optimizing parameters Level selected
1 Catalyst concentration(%) 0.5, 0.75, 1
2 Alcohol concentration(%) 5, 10, 15
3 Reaction time(min.) 45, 60, 75
4 Reaction temperature(C) 60
Waste cooking oil sample: 160gm.
Procedure
1. Take 160 gm of waste cooking oil in a conical flask.
2. In a separate flask mix 1% KOH & 15% of methanol by weight of WCO.
3. Add this solution to oil sample.
4. Maintain the above sample at 60oC for 60 min at constant stiring in water bath shaker.
5. After this put the sample in separating funnel for 24 hours so that glycerine will settle to the bottom and can
be drained off.
6. The liquid left in seperatinf funnel is crude biodiesel as it contains alcohol and catalyst in it.
7. Now boil the biodiesel to get pure, moisture free biodiesel.
Table3.Standardisationoftransesterificationprocess parameters regarding waste cooking oil
S.No Catalyst
(%)
Alcoh
ol (%)
Time
(min)
Yield
(%)
Viscocity
(mm^2/sec)
Flash
Point (o
C)
Fire
Point (o
C)
1 0.5 5 45 84.3 1.2 195 245
2 0.5 10 60 90.6 2.3 190 240
3 0.5 15 75 81.84 4.17 195 245
4 0.75 5 60 89.37 0.4 197 242
5 0.75 10 75 93.75 3.1 100 130
6 0.75 15 45 99.2 12.5 190 220
7 1 5 75 75.1 7.02 192 242
8 1 10 45 81.25 4.10 188 240
9 1 15 60 84.37 17.15 185 225
Fig.1 Specimens
Exp.No. A B C
1 1 1 1
2 1 2 2
3 1 3 3
4 2 1 2
5 2 2 3
6 2 3 1
7 3 1 3
8 3 2 1
9 3 3 2
Optimization And Standardisation Of Waste Cooking Oil Into Bio-Diesel
www.iosrjournals.org 68 | Page
III. Results
Analyzing biodiesel achieved under optimum condition
The obtained biodiesel from both applying transesterification process have lower viscocity at 60 0C.
The waste cooking oil could be consumed as fuel in diesel engines but main obstacle to use oil as fuel in diesel
as its high viscocity which creates problem in aitomisation of fuel spray and operation of fuel injectors.The
obtained resut is sample no. 3. This sample has accurate result with accurate viscocity, flash point and fire point
ranges in ASTM standards. Viscocity ranges from 2-6, flash point ranges from 170-200 oC and fire point ranges
from 220-250 oC.
Effect of oil to methanol ratio
In the graph 1 percentage of methanol is in x axis and percentage of yield is in y axis.
Effect of KOH concentration
In the graph 2 percentage of KOH is in x axis and percentage of yield is in y axis.
Effect of time
In the graph 3change in time is in x axis and percentage of yield is in y axis.
IV. Conclusion
The overall studies based on production of biodiesel from waste cooking oil is successful. The
produced biodiesel was of good quality within the array of standard method specification and production yield
was set up to 99.2% under optimal condition. The research indicate that the production of biodiesel from waste
cooking oil has bit significant difference and also the research highlighted that waste cooking oil could be used
potentially by following innovation. The best result is exp. no. 3 with viscocity varies in standard range. Also its
flash point and fire point varies in standard range.
Reference
[1]. Prakash, N., Jose, A., A., Devanasan, M.G. and Viruthagiri, T. (2006),”Optimization of Karanja oil transesterification”, Indian
journal of chemistry technology.
[2]. Prasad, V.S. Mohapatra, S.K. Sharma, J.K. and Bali, P.L.(2011),”Performance and evaluation of a diesel engine fuelled with
filtered Pongamia oil and its standardisation characterstics”, Vol.1, pp.65-73.
[3]. Karanwal,P.andwootthikanokkam, S.(2010),” Optimization of biodiesel production from Jatrophacurcas L. oil via alkali-
catalyzedmethanolysis”, Journal of Sustainable energy and environment,Vol.1, pp.105-109.
[4]. Fan, X., Burton, R. and Austic, G. (2009),”Preparation and characterization of biodiesel produced from recycled canola oil”, The
open Fuel and energy science journal, Vol.2, pp.113-118.
8.5
9
9.5
10
0 20 40 60 80
8
9
10
0 5 10 15 20
8
9
10
0 0.5 1 1.5

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J011646668

  • 1. IOSR Journal of Mechanical and Civil Engineering (IOSR-JMCE) e-ISSN: 2278-1684,p-ISSN: 2320-334X, Volume 11, Issue 6 Ver. IV (Nov- Dec. 2014), PP 66-68 www.iosrjournals.org www.iosrjournals.org 66 | Page Optimization and Standardisation of Waste Cooking Oil into Bio- Diesel Mr.Ankit Kumar, Rahul Rana,NavdeepNandal,Mohit Singh, Narender Singh Department of Mechanical Engineering,Affilated to KurukshetraUniversity,Kurukshetra Guru Nanak Institutions, Mullana, Ambala,India Abstract: The study was conducted to investigate the optimum conditions for biodiesel formation from waste cooking oil coming after alkaline transesterification process in combination with methanol. Some important variables such as volumetric ratio, types of reactants and catalytic activities were selected to obtain a high quality biodiesel fuel with the specification of American Society Of Testing and Materials. The research investigates the biodiesel obtained under optimum conditions from waste cooking oil of good quality and could be used as a diesel fuel which considered as potential use of waste cooking oil. Keywords: Biodeisel, methanol, waste oil, transesterification. Abbreviations: Waste cooking oil, American Society Of Testing and Materials. I. Introduction New alternative and renewable fuel(biodiesel) has received a considerable attention recently due to occurance of oil depletion, global warming and green house effect. Biodiesel is a good alternative energy which is one of the most promising energy sources. In accordance with the US standards specifications of biodiesel, it is non toxic, biodegradable, produced from renewable sources and contributes a minimal amount of net green house gases and contributes such as CO2and NO2 emission and sulphur to the atmosphere.The high viscocity and poor volatility are major limitations of vegetable oil for their utilisation as fuel in diesel engines. Among more then 350 identified oil bearing crops only sunflower, soyabean are considered as potential alternative fuel for diesel engines. The large amount of waste cooking oil was produced from restaurents, catering establishment and food industries every year. The objective of this study were to compare optimum conditions of fatty acids methyl easter and potential use of waste cooking oil. II. Materials and Methods Materials: Waste cooking oil, Potassium Hydroxide, Methanol. Method: Transesterification reaction H2C—OOC—R1 CH3—OOC—R1H2C—OH HO—OOC—R2+3CH3OH =CH3—OOC—R2 + H2C—OH H2O—OOC—R3 CH3—OOC—R3H2C—OH Cereals Methanol Biodiesel Glycerol The vegetable oil must be chemically altered or blended with diesel fuel to prevent premature engine failure. Blending, cracking emulsification of vegetable oil may be overcome the problems such as deposit formation, carbon buildup and lubrication oil contamination which otherwise cause premature engine failure. Literature Refaat et al. (2008) have reported transesterification of waste vegetable oil with methanol and potassium hydroxide for the product of biodiesel. The best yield percentage was obtained using a methanol/oil molar ratio of 6:1, potassium hydroxide as catalyst (1%) and 65oC temperature for one hour. The yield percentage obtained from vegetable oil was comparable to that obtained from neat vegetable oil which reached 96.15% under optimum condition. The produced biodiesel fuel, whether from neat vegetable oil or waste vegetable oil, was within the recommended standards of biodiesel fuel. Fan et al. (2009) have performed the two step transesterification reaction of recycled canola oil due ti its higher fatty acids content. The results showed that alkali-catalized that was carried out at 6/1 molar ratio of methanol to oil and 1% KOH produced biodiesel. Theory
  • 2. Optimization And Standardisation Of Waste Cooking Oil Into Bio-Diesel www.iosrjournals.org 67 | Page Table1.Taguchi design of experiment technique Variables: A, B, C Levels: 1, 2, 3 Table2.Process parameters selected for standardisation of transesterification process S.No. Optimizing parameters Level selected 1 Catalyst concentration(%) 0.5, 0.75, 1 2 Alcohol concentration(%) 5, 10, 15 3 Reaction time(min.) 45, 60, 75 4 Reaction temperature(C) 60 Waste cooking oil sample: 160gm. Procedure 1. Take 160 gm of waste cooking oil in a conical flask. 2. In a separate flask mix 1% KOH & 15% of methanol by weight of WCO. 3. Add this solution to oil sample. 4. Maintain the above sample at 60oC for 60 min at constant stiring in water bath shaker. 5. After this put the sample in separating funnel for 24 hours so that glycerine will settle to the bottom and can be drained off. 6. The liquid left in seperatinf funnel is crude biodiesel as it contains alcohol and catalyst in it. 7. Now boil the biodiesel to get pure, moisture free biodiesel. Table3.Standardisationoftransesterificationprocess parameters regarding waste cooking oil S.No Catalyst (%) Alcoh ol (%) Time (min) Yield (%) Viscocity (mm^2/sec) Flash Point (o C) Fire Point (o C) 1 0.5 5 45 84.3 1.2 195 245 2 0.5 10 60 90.6 2.3 190 240 3 0.5 15 75 81.84 4.17 195 245 4 0.75 5 60 89.37 0.4 197 242 5 0.75 10 75 93.75 3.1 100 130 6 0.75 15 45 99.2 12.5 190 220 7 1 5 75 75.1 7.02 192 242 8 1 10 45 81.25 4.10 188 240 9 1 15 60 84.37 17.15 185 225 Fig.1 Specimens Exp.No. A B C 1 1 1 1 2 1 2 2 3 1 3 3 4 2 1 2 5 2 2 3 6 2 3 1 7 3 1 3 8 3 2 1 9 3 3 2
  • 3. Optimization And Standardisation Of Waste Cooking Oil Into Bio-Diesel www.iosrjournals.org 68 | Page III. Results Analyzing biodiesel achieved under optimum condition The obtained biodiesel from both applying transesterification process have lower viscocity at 60 0C. The waste cooking oil could be consumed as fuel in diesel engines but main obstacle to use oil as fuel in diesel as its high viscocity which creates problem in aitomisation of fuel spray and operation of fuel injectors.The obtained resut is sample no. 3. This sample has accurate result with accurate viscocity, flash point and fire point ranges in ASTM standards. Viscocity ranges from 2-6, flash point ranges from 170-200 oC and fire point ranges from 220-250 oC. Effect of oil to methanol ratio In the graph 1 percentage of methanol is in x axis and percentage of yield is in y axis. Effect of KOH concentration In the graph 2 percentage of KOH is in x axis and percentage of yield is in y axis. Effect of time In the graph 3change in time is in x axis and percentage of yield is in y axis. IV. Conclusion The overall studies based on production of biodiesel from waste cooking oil is successful. The produced biodiesel was of good quality within the array of standard method specification and production yield was set up to 99.2% under optimal condition. The research indicate that the production of biodiesel from waste cooking oil has bit significant difference and also the research highlighted that waste cooking oil could be used potentially by following innovation. The best result is exp. no. 3 with viscocity varies in standard range. Also its flash point and fire point varies in standard range. Reference [1]. Prakash, N., Jose, A., A., Devanasan, M.G. and Viruthagiri, T. (2006),”Optimization of Karanja oil transesterification”, Indian journal of chemistry technology. [2]. Prasad, V.S. Mohapatra, S.K. Sharma, J.K. and Bali, P.L.(2011),”Performance and evaluation of a diesel engine fuelled with filtered Pongamia oil and its standardisation characterstics”, Vol.1, pp.65-73. [3]. Karanwal,P.andwootthikanokkam, S.(2010),” Optimization of biodiesel production from Jatrophacurcas L. oil via alkali- catalyzedmethanolysis”, Journal of Sustainable energy and environment,Vol.1, pp.105-109. [4]. Fan, X., Burton, R. and Austic, G. (2009),”Preparation and characterization of biodiesel produced from recycled canola oil”, The open Fuel and energy science journal, Vol.2, pp.113-118. 8.5 9 9.5 10 0 20 40 60 80 8 9 10 0 5 10 15 20 8 9 10 0 0.5 1 1.5