Transesterification of soybean oil in four-way micromixers for biodiesel production using a cosolvent

被引:39
|
作者
Rahimi, Masoud [1 ]
Mohammadi, Faezeh [1 ]
Basiri, Mojdeh [1 ]
Parsamoghadam, Mohammad Amin [1 ]
Masahi, Mohammad Moein [1 ]
机构
[1] Razi Univ, Dept Chem Engn, CFD Res Ctr, Kermanshah, Iran
关键词
Microreactor; Cosolvent; Biodiesel production; Optimization; Response surface methodology; METHYL-ESTERS; PALM OIL; KINETICS;
D O I
10.1016/j.jtice.2016.04.023
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, transformation of soybean oil into fatty acid methyl ester (FAME) was studied in different four-way micromixers. Hexane was added to the reaction system as a cosolvent for mass transfer intensification. A three-level-five-factorial Central Composite Design using Response Surface Methodology was employed to optimize the reaction conditions. The main factors affecting the FAME content (wt.%) i.e. reaction temperature, residence time, hexane to methanol volumetric ratio, oil to methanol volumetric ratio and mixer configuration were discussed. The optimum combinations for transesterification to achieve a predicted maximum FAME of 97.67% were found. At this optimum condition, the observed FAME content was found to be 98.8%. The closeness of the experimental results and predicted values demonstrated that the regression model is significant. In the present work, residence time was reduced in an order of seconds (3-15 s), which it has not been fulfilled in the previous works. (C) 2016 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:203 / 210
页数:8
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