Pilot-scale production of biodiesel from waste cooking oil using kettle limescale as a heterogeneous catalyst

被引:61
作者
Aghel, Babak [1 ]
Mohadesi, Majid [1 ]
Ansari, Ahmadreza [1 ]
Maleki, Mahmoud [1 ]
机构
[1] Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran
关键词
Biodiesel; Waste cooking oil; Optimization; Semi-industrial pilot; Microreactor; PALM OIL; VEGETABLE-OIL; OPTIMIZATION; TRANSESTERIFICATION; REACTOR;
D O I
10.1016/j.renene.2019.04.100
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study aimed to evaluate and optimize a pilot-scale microreactor to convert waste cooking oil (WCO) into biodiesel using kettle limescale. Box-Behnken design was used to determine the optimum conditions for producing biodiesel. Effects of main variables including reaction temperature, catalyst concentration, and alcohol/oil volume ratio were evaluated at a constant residence time of 10 min. Based on the results of analysis of variance, the quadratic regression model had the best coefficient of determination (R-2 = 0.9930) and adjusted coefficient of determination (R-Adj.(2)= 0.9804). After the optimization of temperature, catalyst concentration, and methanol/oil volume ratio, the residence time was optimized to achieve the maximum purity of the produced biodiesel. At a reaction temperature of 61.7 degrees C, catalysts concentration (oil based) of 8.87 wt %, methanol to oil volume ratio of 1.7:3, and a residence time of 15 min, we observed the optimal conditions for obtaining a maximum biodiesel purity of 93.41%. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:207 / 214
页数:8
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