A kinetic study of quicklime-catalyzed sunflower oil methanolysis

被引:43
|
作者
Miladinovic, Marija R. [1 ]
Krstic, Jugoslav B. [2 ]
Tasic, Marija B. [1 ]
Stamenkovic, Olivera S. [1 ]
Veljkovic, Vlada B. [1 ]
机构
[1] Univ Nis, Fac Technol, Leskovac 16000, Serbia
[2] Univ Belgrade, Inst Chem Technol & Met, Ctr Catalysis & Chem Engn, Belgrade 11000, Serbia
来源
关键词
Biodiesel; CaO; Kinetics; Methanolysis; Modeling; Quicklime; SOLID BASE CATALYST; WASTE FRYING OILS; SOYBEAN OIL; BIODIESEL PRODUCTION; HETEROGENEOUS CATALYST; VEGETABLE-OIL; SUPPORTED CAO; RAPESEED OIL; TRANSESTERIFICATION; SHELL;
D O I
10.1016/j.cherd.2013.11.023
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The quicklime-catalyzed sunflower oil methanolysis was studied at mild reaction conditions. Quicklime (calcined at 550 degrees C for 4h) in amounts of 1.0, 2.5, 5.0 and 10.0% (based on the oil weight) and different molar ratios of methanol-to-oil (6:1, 12:1 and 18:1) were employed to investigate their influence on the methyl esters content and the kinetics of the methanolysis reaction. The optimal methanol-to-oil molar ratio and quicklime amount for achieving the highest fatty acid methyl esters content were established to be 12:1 and 5% (based on the oil weight), respectively. The sigmoidal kinetics of quicklime-catalyzed methanolysis reaction was described by a model which included the changing mechanism of the reaction and the triacylglycerols mass transfer limitation. The kinetic parameters were determined and correlated with the process variables. A good agreement between the kinetic model and the experimental data for all applied reaction conditions was observed. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1740 / 1752
页数:13
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