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Optimization of Biodiesel  Daniel Velasquez 20.903.659
Macroestructura   • CONTENT  • ITEM  • SUBTOPIC
CONTENT optimization of biodiesel production in fat and oil feedstocks, including mahua oil [15], Jatropha oil [16], waste rapeseed oil [17] and animal fat [18]. RSM can be illustrated with threedimensional plots by presenting the response in function of two factors and keeping the other constant. It is visualized by the yield of biodiesel in relation to the temperature, methanol to oil ratio and Catalyst concentration.
Transesterification reaction yield as a function of temperature and methanol to oil ratio at Catalyst concentration of 0.679%wt. This figure show that temperature and molar ratio of alcohol to oil have a direct effect on the yield of methyl ester but until the near boiling temperature of alcohol and 6:1 molar ratio, then yield of biodiesel decreased with increasing the temperature and molar ratio of alcohol to oil. A few works reported the reaction at room temperature; most of the researches have focused on the transesterification at near boiling point of alcohol. Temperature has an important influence on speed of reaction and led to higher conversion of ester.
Optimization of extraction condition In order to optimize reaction condition, the first partial derivatives of the regression model were equated to zero according to X1, X2, and X3 respectively. The result was calculated as follows: X1=48, X2=6.825 and X3=0.679. Under such condition, the yield of biodiesel was predicted to be 97.54%. The experimental work at this condition was performed due to maximum experimental yield. In this work, highest yield of methyl ester at temperature of 48°C, catalyst concentration of 0.679%wt, 290 rpm of stirrer, 2h and methanol to oil ratio of 6.825:1 is obtained 98.181%.
ITEM Biodiesel produced by transesterification of triglycerides with alcohol, is the newest form of energy that has attracted the attention of many researchers due to various advantages associated with its usages. Response surface methodology based on a five level, three variables central composite design is used to analyze the interaction effect of the transesterification reaction variables such as temperature, catalyst concentration and molar ratio of methanol to oil on biodiesel yield. The linear terms of temperature and catalyst concentration followed by the linear term of oil to methanol ratio, the quadratic terms of catalyst concentration and oil to methanol ratio and the interaction between temperature and catalyst concentration and also the interaction between temperature and molar ratio of methanol to oil had significant effects on the biodiesel production (p<0.05). Maximum yield for the production of methyl esters from sunflower oil was predicted to be 98.181% under the condition of temperature of 48°C, the molar ratio of methanol to oil of 6.825:1, catalyst concentration of 0.679 wt%, stirring speed of 290 rpm and a reaction time of 2h
SUBTOPIC Response surface methodology was successfully applied for transesterification of methanol. The high regression coefficients of the secondorder polynomial showed that the model was well fitted to the experimental data The ANOVA implied that molar ratio of alcohol to oil; reaction temperature and concentration of catalyst have the great significant factor affecting the yield of biodiesel. The biodiesel production has a negative quadratic behavior by temperature, molar ratio of alcohol to oil; reaction temperature and concentration of catalyst. It was predicted that the optimum reaction condition within the experimental range would be the molar ratio of 6.825:1 and temperature of 48°C and concentration of KOH equal to 0.679wt%. At the optimum condition we can reach to yield of 98.181%. The methyl ester which produced at optimum conditions has acceptable properties and compared well with petro-diesel. It has lower sulfur, carbon residue and acid number than petro-diesel, but kinematic viscosity, cetane number and heating value of petro-diesel is some better relative to biodiesel. Finally, we can conclude which biodiesel will be a suitable alternative for replacement of petro-diesel without any modification in engine.

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Optimization of Biodiesel Production

  • 1. Optimization of Biodiesel Daniel Velasquez 20.903.659
  • 2. Macroestructura • CONTENT • ITEM • SUBTOPIC
  • 3. CONTENT optimization of biodiesel production in fat and oil feedstocks, including mahua oil [15], Jatropha oil [16], waste rapeseed oil [17] and animal fat [18]. RSM can be illustrated with threedimensional plots by presenting the response in function of two factors and keeping the other constant. It is visualized by the yield of biodiesel in relation to the temperature, methanol to oil ratio and Catalyst concentration.
  • 4. Transesterification reaction yield as a function of temperature and methanol to oil ratio at Catalyst concentration of 0.679%wt. This figure show that temperature and molar ratio of alcohol to oil have a direct effect on the yield of methyl ester but until the near boiling temperature of alcohol and 6:1 molar ratio, then yield of biodiesel decreased with increasing the temperature and molar ratio of alcohol to oil. A few works reported the reaction at room temperature; most of the researches have focused on the transesterification at near boiling point of alcohol. Temperature has an important influence on speed of reaction and led to higher conversion of ester.
  • 5. Optimization of extraction condition In order to optimize reaction condition, the first partial derivatives of the regression model were equated to zero according to X1, X2, and X3 respectively. The result was calculated as follows: X1=48, X2=6.825 and X3=0.679. Under such condition, the yield of biodiesel was predicted to be 97.54%. The experimental work at this condition was performed due to maximum experimental yield. In this work, highest yield of methyl ester at temperature of 48°C, catalyst concentration of 0.679%wt, 290 rpm of stirrer, 2h and methanol to oil ratio of 6.825:1 is obtained 98.181%.
  • 6. ITEM Biodiesel produced by transesterification of triglycerides with alcohol, is the newest form of energy that has attracted the attention of many researchers due to various advantages associated with its usages. Response surface methodology based on a five level, three variables central composite design is used to analyze the interaction effect of the transesterification reaction variables such as temperature, catalyst concentration and molar ratio of methanol to oil on biodiesel yield. The linear terms of temperature and catalyst concentration followed by the linear term of oil to methanol ratio, the quadratic terms of catalyst concentration and oil to methanol ratio and the interaction between temperature and catalyst concentration and also the interaction between temperature and molar ratio of methanol to oil had significant effects on the biodiesel production (p<0.05). Maximum yield for the production of methyl esters from sunflower oil was predicted to be 98.181% under the condition of temperature of 48°C, the molar ratio of methanol to oil of 6.825:1, catalyst concentration of 0.679 wt%, stirring speed of 290 rpm and a reaction time of 2h
  • 7. SUBTOPIC Response surface methodology was successfully applied for transesterification of methanol. The high regression coefficients of the secondorder polynomial showed that the model was well fitted to the experimental data The ANOVA implied that molar ratio of alcohol to oil; reaction temperature and concentration of catalyst have the great significant factor affecting the yield of biodiesel. The biodiesel production has a negative quadratic behavior by temperature, molar ratio of alcohol to oil; reaction temperature and concentration of catalyst. It was predicted that the optimum reaction condition within the experimental range would be the molar ratio of 6.825:1 and temperature of 48°C and concentration of KOH equal to 0.679wt%. At the optimum condition we can reach to yield of 98.181%. The methyl ester which produced at optimum conditions has acceptable properties and compared well with petro-diesel. It has lower sulfur, carbon residue and acid number than petro-diesel, but kinematic viscosity, cetane number and heating value of petro-diesel is some better relative to biodiesel. Finally, we can conclude which biodiesel will be a suitable alternative for replacement of petro-diesel without any modification in engine.