Kinetics of sunflower oil methanolysis at low temperatures

被引:144
作者
Stamenkovic, Olivera S. [1 ]
Todorovic, Zoran B. [1 ]
Lazic, Miodrag L. [1 ]
Veljkovic, Vlada B. [1 ]
Skala, Dejan U. [2 ]
机构
[1] Univ Nis, Fac Technol, Leskovac 16000, Serbia
[2] Univ Belgrade, Fac Technol & Met, Belgrade 11000, Serbia
关键词
biodiesel; kinetics; mass transfer; methanolysis; sunflower oil;
D O I
10.1016/j.biortech.2007.02.028
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The kinetics of the sunflower oil methanolysis process was studied at lower temperatures (10-30 degrees C). The sigmoidal kinetics of the process was explained by the mass transfer controlled region in the initial heterogenous regime, followed by the chemical reaction controlled region in the pseudo-homogenous regime. A simple kinetic model, which did not require complex computation of the kinetic constants, was used for simulation of the TG conversion and the FAME formation in the latter regime: the fast irreversible second-order reaction was followed by the slow reversible second-order reaction close to the completion of the methanolysis reaction. The mass transfer was related to the drop size of the dispersed (methanol) phase, which reduced rapidly with the progress of the methanolysis reaction. This was attributed to the formation of the emulsifying agents stabilizing the emulsion of methanol drops into the oil. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1131 / 1140
页数:10
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