New approach of catalyst-free biodiesel production from canola oil in supercritical tert-butyl methyl ether (MTBE)

被引:34
|
作者
Farobie, Obie [1 ]
Yanagida, Takashi [2 ]
Matsumura, Yukihiko [2 ]
机构
[1] Hiroshima Univ, Dept Mech Sci & Engn, Higashihiroshima 7398527, Japan
[2] Hiroshima Univ, Inst Engn, Div Energy & Environm Engn, Higashihiroshima 7398527, Japan
关键词
Biomass; Biodiesel; Canola oil; Supercritical condition; Tert-butyl methyl ether; ACID ETHYL-ESTERS; RAPESEED OIL; SOYBEAN OIL; EXHAUST EMISSIONS; VEGETABLE-OIL; DIMETHYL CARBONATE; METHANOL; FUEL; TRANSESTERIFICATION; KINETICS;
D O I
10.1016/j.fuel.2014.06.049
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
This paper reports a novel approach for biodiesel production from canola oil in supercritical tert-butyl methyl ether (MTBE) without the addition of a catalyst. Using this technique, canola oil was reacted with MTBE to generate fatty acid methyl esters (FAMEs) and glycerol tert-butyl ether. No glycerol was obtained as a by-product in this reaction. The effects of temperature, pressure, and reaction time on product yield were investigated in supercritical MTBE. A FAME yield of 0.94 was obtained in a short reaction time of 12 min at 400 degrees C, with a molar ratio of MTBE-to-oil of 40:1, and under a pressure of 10 MPa. The kinetics of the reaction was first order, and the activation energies and pre-exponential factors were calculated from the temperature dependence of the reaction rate constants. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:172 / 181
页数:10
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