Kinetics of base-catalyzed transesterification of triglycerides from Pongamia oil

被引:48
作者
Karmee, S. K.
Chandna, D.
Ravi, R.
Chadha, A. [1 ]
机构
[1] Indian Inst Technol, Dept Chem, Madras 600036, Tamil Nadu, India
[2] Indian Inst Technol, Dept Chem Engn, Madras 600036, Tamil Nadu, India
[3] Indian Inst Technol, Dept Biotechnol, Madras 600036, Tamil Nadu, India
关键词
biodiesel; DG; kinetics; MG; Pongamia oil; TG; transesterification;
D O I
10.1007/s11746-006-5040-z
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The kinetics of transesterification of Pongamia oil using methanol at 60 degrees C were studied. The forward as well as the reverse rate constants of all three steps involved in the tramsesterification of Pongamia oil are reported for the first time. Among the forward rate constants, the one governing the conversion of TG to DG was the highest and the one for DG to MG was the lowest. A distinct feature of the present work is the direct estimation of the equilibrium constants of all three steps by measuring the concentrations of TG, DG, and MG at very long reaction times. This reduced the number of parameters to be determined from the kinetic data by one-half, thereby leading to more accurate estimation of the rate constants. The equilibrium constant of the final step involving the conversion of MG to methyl ester and glycerol was at least an order of magnitude greater than that of the first two reaction steps. A detailed comparison was made with kinetic parameters reported in literature. The trend in the relative magnitudes of the rate constants appears to be unique to Pongamia oil.
引用
收藏
页码:873 / 877
页数:5
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