Optimization of Process Parameters for Biodiesel Production Using Response Surface Methodology

The effect of five process parameters namely: reaction time, reaction temperature, stir speed, catalyst concentration and methanol-oil ratio on the transesterification process of waste frying oil to biodiesel were investigated. Optimization of the five process parameters and their quadratic cross effect was carried out using a four level-five factor central composite experimental design model and response surface methodology with each factor varied over four levels. Taking the biodiesel yield as the response of the designed experiment, the data obtained were statistically analysed to get a suitable model for optimization of biodiesel yield as a function of the five independent process parameters. The optimization produced 30 feasible solutions whose desirability equals to 1 and the selected (most desirable) condition was found to be: reaction time (3 hrs), reaction temperature (58°C), stir speed (305.5 rpm), catalyst concentration (1.4 wt%) and methanol to oil ratio (6:1), while the optimum yield of biodiesel for this condition was found to be 91.6%. The developed model was tested and validated for adequacy by substituting random experimental values as input parameters and the output parameters from the developed model were close to the experimental values. The biodiesel properties were characterized and the results obtained were found to satisfy the standard for both the ASTM D 6751 and EN 14214.

[1]  Babak Salamatinia,et al.  Intensification of biodiesel production from vegetable oils using ultrasonic-assisted process: Optimization and kinetic , 2013 .

[2]  Don-Hee Park,et al.  Optimization of Biodiesel Production from Castor Oil Using Response Surface Methodology , 2009, Applied biochemistry and biotechnology.

[3]  O. A. Aworanti,et al.  Statistical optimization of process variables for biodiesel production from waste cooking oil using heterogeneous base catalyst. , 2013 .

[4]  C. C. Enweremadu,et al.  Optimization and Modeling of Process Variables of Biodiesel Production from Marula Oil using Response Surface Methodology , 2015 .

[5]  Don-Hee Park,et al.  Optimization of transesterification of animal fat ester using response surface methodology. , 2009, Bioresource technology.

[6]  Matti Leisola,et al.  Optimization of enzymatic transesterification of rapeseed oil ester using response surface and principal component methodology , 1999 .

[7]  Institiut Penyelidikan Minyak Kelapa Sawit Malaysia,et al.  The palm oil industry , 1982 .

[8]  A. Abdullah,et al.  Alkaline Earth Metal Oxide Catalysts for Biodiesel Production from Palm Oil: Elucidation of Process Behaviors and Modeling Using Response Surface Methodology , 2013 .

[9]  S. Bhatia,et al.  Biodiesel production from palm oil via heterogeneous transesterification , 2009 .

[10]  G. Box,et al.  Empirical Model-Building and Response Surfaces. , 1990 .

[11]  Fang Wang,et al.  Lipase catalyzed methanolysis to produce biodiesel: Optimization of the biodiesel production , 2006 .

[12]  G Antolín,et al.  Optimisation of biodiesel production by sunflower oil transesterification. , 2002, Bioresource technology.

[13]  Ignacio E. Grossmann,et al.  Optimization and heat and water integration for biodiesel production from cooking oil and algae , 2011 .

[14]  Takuya Fukumura,et al.  Biodiesel production using anionic ion-exchange resin as heterogeneous catalyst. , 2007, Bioresource technology.

[15]  Rubens Maciel Filho,et al.  Optimization of biodiesel production from castor oil , 2006, Applied biochemistry and biotechnology.

[16]  Naresh Chandra Saxena The palm oil industry in Malaysia and its need for agricultural engineers. , 1980 .