Biodiesel production from waste cooking oil in a microtube reactor

被引:49
|
作者
Tanawannapong, Yuttapong [1 ]
Kaewchada, Amaraporn [2 ]
Jaree, Attasak [1 ]
机构
[1] Kasetsart Univ, Dept Chem Engn, Fac Engn, Ctr Excellence Petrochem & Mat Technol, Bangkok 10900, Thailand
[2] King Mongkuts Univ Technol N Bangkok, Fac Sci Appl, Dept Agroind Technol, Bangkok 10800, Thailand
关键词
Biodiesel; Waste cooking oil; Microtube reactor; CATALYZED TRANSESTERIFICATION; FUEL; FFA;
D O I
10.1016/j.jiec.2012.07.007
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Waste cooking oil (WCO) was used to produce biodiesel in a microtube reactor. First, the acid value of the WCO was reduced from 3.96 mg KOH/g to less than 1 mg KOH/g via acid catalyzed esterification. The effects of the methanol-to-WCO molar ratio (4.5:1-18:1), the H2SO4 concentration (0.5-2 wt.%), reaction temperature (55-70 degrees C), and reaction time (5-20 s) were studied. The optimal conditions were 9:1 methanol-to-WCO molar ratio, 1 wt.% H2SO4, 65 degrees C and 5 s of reaction time. Triglycerides in the product from the first step were transesterified with methanol and alkaline catalyst. Methyl ester content of the biodiesel was 91.76%. (C) 2012 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:37 / 41
页数:5
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