Continuous production of biodiesel with supercritical methanol: Optimization of a scale-up plug flow reactor by response surface methodology

被引:24
|
作者
Sawangkeaw, Ruengwit [1 ]
Bunyakiat, Kunchana [1 ,2 ]
Ngamprasertsith, Somkiat [1 ,2 ]
机构
[1] Chulalongkorn Univ, Dept Chem Technol, Fuels Res Ctr, Fac Sci, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Ctr Petr Petrochem & Adv Mat, Bangkok 10330, Thailand
关键词
Biodiesel; Supercritical methanol; Plug flow reactor; Response surface methodology; Scale-up reactor; VEGETABLE-OILS; FUEL; TRANSESTERIFICATION; DENSITY;
D O I
10.1016/j.fuproc.2011.07.014
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A scale-up plug flow reactor was evaluated for the continuous production of biodiesel from refined palm kernel oil (PKO) with supercritical methanol and optimized by response surface methodology. The effects of the operating temperature (270-350 degrees C), pressure (15.0-20.0 MPa) and methanol:PKO molar ratio (20:1-42:1) were evaluated at a constant residence time of 20 +/- 2 min by using a central composite design. Analysis of variance demonstrated that a modified quadratic regression model gave the best coefficient of determination (R-2 = 0.9615) and adjusted coefficient of determination (Adj. R-2 = 0.9273). The interaction terms in the regression model illustrated small synergistic effects of both temperature-pressure and temperature-methanol:PKO molar ratio. The optimal conditions were 325 +/- 5 degrees C, 18.0 +/- 0.5 MPa and a methanol:PKO molar ratio of 42 +/- 2:1, attaining a maximum production rate of 18.0 1.5 g biodiesel/min with a fatty acid methyl ester content of 93.7 +/- 2.1%. The product obtained from the optimal conditions had high cetane number, and could be considered as a fuel additive for cetane number enhancement. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:2285 / 2292
页数:8
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