Batch (one- and two-stage) production of biodiesel fuel from rapeseed oil

被引:2
|
作者
Gwi-Taek Jeong
Don-Hee Park
机构
[1] Chonnam National University,School of Biological Sciences and Technology
[2] Chonnam National University,Faculty of Applied Chemical Engineering
[3] Chonnam National University,Research Institute for Catalysis
[4] Chonnam National University,Biotechnology Research Institute
[5] Chonnam National University,Institute of Bioindustrial Technology
来源
关键词
Biodiesel fuel; transesterification; rapeseed oil; two stage;
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学科分类号
摘要
Biodiesel fuel is an alternative and renewable energy source, which may help to reduce air pollution, as well as our dependence on petroleum for energy. Several processes have already been developed for the production of biodiesel. Alkali-catalyzed transesterification with short-chain alcohols, for example, generates high yields of methyl esters in short reaction times. In this study, we have evaluated the efficacy of batch (one- and two-stage) transesterification of rapeseed oil in the production of rapeseed methyl ester. The conversion of rapeseed oil exhibited similar reaction patterns and yields in 30- and 1-L reaction systems. Approximately 98% of the rapeseed oil was converted at 400 rpm within 20 min, under the following conditions: 1% (w/w) KOH, 1∶10 methanol molar ratio, and at 60°C. In the 30-L, two-stage transesterification process, approx 98.5% of the rapeseed oil was converted at a 1∶4.5 molar ratio and 1% (w/w) KOH at 60°C for 30 min (first reaction condition), and at a 1∶1 molar ratio and 0.2% (w/w) KOH at 60°C for 30 min (second reaction condition).
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页码:668 / 679
页数:11
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