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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
来源:
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.
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页码:207 / 214
页数:8
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