Experimental design and optimization of castor oil transesterification process by response surface methodology

被引:7
作者
Chaudhary, Payal [1 ]
Verma, Ayushi [2 ]
Kumar, Surendra [2 ]
Gupta, V. K. [3 ]
机构
[1] Indian Inst Technol Roorkee, Ctr Transportat Syst, Roorkee, Uttar Pradesh, India
[2] Indian Inst Technol Roorkee, Dept Chem Engn, Roorkee, Uttar Pradesh, India
[3] Univ Johannesburg, Dept Appl Chem, Johannesburg, South Africa
来源
BIOFUELS-UK | 2018年 / 9卷 / 01期
关键词
Transesterification; response surface methodology; catalyst; fatty acid methyl ester; ACID METHYL-ESTERS; BIODIESEL PRODUCTION; VEGETABLE-OILS; KARANJA; FEEDSTOCK; JATROPHA; METHANOL; ETHANOL;
D O I
10.1080/17597269.2016.1249737
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the present study, optimization of biodiesel production from castor oil was investigated. The biodiesel was produced in a large lab reactor (3 L) by an acid-catalyzed transesterification process, which was designed according to 2(3) full factorial central composite design (CCD). The response surface methodology (RSM) was used to optimize the reaction conditions to achieve maximum % fatty acid methyl ester (FAME) yield. Based on a second-order polynomial equation the optimum values of the three independent parameters thus obtained were 25:1 methanol/oil molar ratio, 3 vol. % catalyst amount and 60 degrees C reaction temperature. According to the experimental results, this process gave an average % FAME yield of 76.95%. The fatty acid composition of the oil was analyzed using a gas chromatograph (GC). The developed response surface model was also validated with two different, additional sets of experimental data, and its predictions were found to be within +/- 5% deviation. Using the RSM, the effect of variation in operating parameters as methanol/oil molar ratio, catalyst amount and reaction temperature and their interaction on % fatty acid methyl ester yield were also studied.
引用
收藏
页码:7 / 17
页数:11
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