Kinetics of the base-catalyzed sunflower oil ethanolysis

被引：96

作者：

Marjanovic, Ana V. ^{[1
]}

Stamenkovic, Olivera S. ^{[1
]}

Todorovic, Zoran B. ^{[1
]}

Lazic, Miodrag L. ^{[1
]}

Veljkovic, Vlada B. ^{[1
]}

机构：

[1] Fac Technol, Leskovac 16000 7, Serbia

来源：

FUEL | 2010年 / 89卷 / 03期

关键词：

Biodiesel; Ethanolysis; Kinetics; Modeling; Sunflower oil; BIODIESEL PRODUCTION; SOYBEAN OIL; VEGETABLE-OILS; RAPESEED OIL; ETHYL-ESTERS; TRANSESTERIFICATION; METHANOLYSIS; OPTIMIZATION; FUELS; TRIGLYCERIDES;

D O I：

10.1016/j.fuel.2009.09.025

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

The kinetics of the sunflower oil ethanolysis process using NaOH as a catalyst was studied at different reaction conditions. The reaction system was considered as a pseudo-homogeneous one with no mass transfer limitations. It was also assumed that the chemical reaction rate controlled the overall process kinetics. A simple kinetic model consisting of the irreversible second-order reaction followed by the reversible second-order reaction close to the completion of the ethanolysis reaction was used for the simulation of the triglyceride conversion and the fatty acid ethyl ester formation. The proposed kinetics model fitted the experimental data well. (C) 2009 Elsevier Ltd. All rights reserved.

引用

页码：665 / 671

页数：7

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