Study on the kinetics of enzymatic interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor

被引:112
|
作者
Xu, YY [1 ]
Du, W [1 ]
Liu, DH [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
关键词
biodiesel; kinetics; lipase; interesterification; methyl acetate;
D O I
10.1016/j.molcatb.2004.12.013
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 new route for biodiesel production using methyl acetate instead of methanol as the acyl acceptor was proposed in our previous research, and it has been found that this novel route could enhance the stability of the immobilized lipase greatly. In this paper, the kinetics of lipase catalyzed interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor was further studied. First, a simplified model based on Ping Pong Bi Bi with substrate competitive inhibition mechanism was proposed to describe the reaction kinetics of the interesterification. During our further study, it was observed that three consecutive and reversible reactions occurred in the interesterification of triglycerides and methyl acetate. So, a kinetic model based on mass balance of three second-order reversible reactions was developed and the reaction rate constant, k, was determined by solving the differential rate equations of the reaction system. The results showed that k(DG-MG) (0.1124) and k(MG-TA) (0.1129) were much higher than k(TG-DG) (0.0311), which indicated that the first step reaction was the limit step for the overall interesterification. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:241 / 245
页数:5
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