Process optimization of biodiesel production using alkaline catalysts

被引:0
|
作者
Singh, A. [1 ]
He, B. [1 ]
Thompson, J. [1 ]
Van Gerpen, J. [1 ]
机构
[1] Univ Idaho, Dept Biol & Agr Engn, Moscow, ID 83843 USA
关键词
biodiesel; alkaline catalyst; transesterfication; canola oil;
D O I
暂无
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The most commonly used method for biodiesel preparation is via transesterfication of vegetable oil using alkaline catalysts. Biodiesel yield and oil conversion are affected by operating conditions including the catalyst formulation and concentration. Application of alkaline catalysts can also lead to undesired soap formation. This study evaluated the alkaline catalyst effects on biodiesel yield and soap formation in transesterifying methanol and canola oil at different catalyst concentrations, reaction temperatures, and methanol-to-oil molar ratios. Four different alkaline catalysts, i.e., potassium hydroxide, sodium hydroxide, potassium methoxide, and sodium methoxide, were studied and compared on molar basis through a 4-factor 3-level experimental design. It was observed that methoxide catalysts led to better biodiesel yields than hydroxide catalysts. The methoxide catalysts not only accelerated the reaction but also elevated the conversion equilibrium. Based on statistical optimization, the operating conditions for maximizing biodiesel yield and minimizing soap formation were potassium methoxide as catalyst at 0.2 mol/mol (1.59% wt), reaction temperature of 50 degrees C, and methanol-to-oil molar ratio of 4.5: 1. Experimental verification gave 95.8% biodiesel yield and 0.75%wt soap.
引用
收藏
页码:597 / 600
页数:4
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