Kinetic study on lipase-catalyzed biodiesel production from waste cooking oil

被引:28
|
作者
Liu, Shihong [1 ]
Nie, Kaili [1 ,3 ]
Zhang, Xin [1 ]
Wang, Meng [1 ]
Deng, Li [1 ,3 ]
Ye, Xianchun [3 ]
Wang, Fang [2 ]
Tan, Tianwei [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Life Sci & Technol, Beijing Bioproc Key Lab, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
[3] Amoy BUCT Ind Biotechnovat Inst, Amoy 361022, Peoples R China
关键词
Fatty acid methyl ester; Candida sp 99-125; Kinetic; Modeling; Waste cooking oil; ENZYMATIC-SYNTHESIS; TRANSESTERIFICATION; OPTIMIZATION; CONVERSION; REACTOR; ESTERS; FUEL;
D O I
10.1016/j.molcatb.2013.10.009
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
A kinetic model of the biodiesel production from waste cooking oil using Candida sp. 99-125 lipase as catalyst was established in this paper. The limited reaction steps in the model were considered to be the hydrolysis of glycerides and the esterification of free fatty acids, while the methanolysis of glycerides were considered to be negligible. Matlab programming platform was used to estimate the parameters of the model. A series of experiments were conducted to verify the validity of the model. The results showed that the model could adequately simulate the reaction results of biodiesel production at different lipase loadings, substrate ratios and initial water concentrations. The agreement between experimental data and calculated values was good, which could prove the validity of the kinetic model. Moreover, the results of biodiesel production using a twelve-step methanol feeding method and a three-step methanol feeding method could be simulated well by the kinetic model. The results indicated that the model could also simulate the biodiesel production using methanol step-wise addition. (C) 2013 Published by Elsevier B.V.
引用
收藏
页码:43 / 50
页数:8
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