Transesterification kinetics of Camelina sativa oil on metal oxide catalysts under conventional and microwave heating conditions

被引:91
作者
Patil, Prafulla [1 ]
Gude, Veera Gnaneswar [1 ]
Pinappu, Saireddy [1 ]
Deng, Shuguang [1 ]
机构
[1] New Mexico State Univ, Dept Chem Engn, Las Cruces, NM 88003 USA
关键词
Biodiesel; Camelina sativa oil; Transesterification kinetics; Heterogeneous catalysts; Microwave-heating; BIODIESEL PRODUCTION; SOYBEAN OIL;
D O I
10.1016/j.cej.2011.02.030
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The reaction kinetics of transesterification of Camelina sativa oil using metal oxide catalysts under the conventional heating and the microwave-heating conditions were investigated. The transesterification reaction rates and the fatty acid methyl ester (FAME) conversion rates were determined using heterogeneous metal oxide catalysts, i.e., BaO, CaO, MgO and SrO and two different heating methods. It was observed during the kinetic studies in this work that the Bat) and SrO catalysts generated higher FAME yields than the CaO and MgO catalysts. A comparison between the conventional heating and the microwave-assisted transesterification processes showed that the reaction rate constants obtained in the microwave-assisted transesterification process are of two orders of magnitude higher than those obtained with the conventional heating method. Therefore, it can be well concluded that the heating method and solid catalysts play vital roles in improving the reaction kinetics and optimizing the reactors for biomass conversion to biodiesel. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:1296 / 1300
页数:5
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