Methanol recycling in the production of biodiesel in a membrane reactor

被引:60
作者
Cao, Peigang [1 ]
Dube, Marc A. [1 ]
Tremblay, Andre Y. [1 ]
机构
[1] Univ Ottawa, Dept Chem Engn, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
biodiesel; membrane reactor; recycling;
D O I
10.1016/j.fuel.2007.05.048
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 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
Membrane reactor technology was used to overcome challenges in biodiesel production. The membrane reactor produces a permeate stream which readily phase separates at room temperature into a fatty acid methyl ester (FAME)-rich non-polar phase and a methanol- and glycerol-rich polar phase. To decrease the overall methanol:oil molar ratio in the reaction system, the polar phase was recycled. Three recycle ratios were tested: 100%, 75% and 50%, at the same residence time and operating conditions. The permeate consistently separated to yield a FAME-rich non-polar phase containing a minimum of 85 wt.%) FAME (the remainder being methanol) as well as a methanol/glycerol polar phase. At the highest recycle ratio, the FAME concentration ranged from 85.7 to 92.4 wt.% in the FAME-rich non-polar phase. In addition, the overall molar ratio of methanol:oil in the reaction system was significantly decreased to 10:1 while maintaining a FAME production rate of 0.04 kg/min. As a result, a high purity FAME product was produced. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:825 / 833
页数:9
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