Liquid-liquid equilibrium during ethanolysis of soybean oil

被引:9
作者
Ferreira, Marcela Cravo [1 ]
Bessa, Larissa C. B. A. [1 ]
Meirelles, Antonio J. A. [1 ]
Caldas Batista, Eduardo Augusto [1 ]
机构
[1] Univ Estadual Campinas, UNICAMP, Fac Food Engn FEA, EXTRAE,Dept Food Engn DEA, BR-13083970 Campinas, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Ethanolysis; Liquid-liquid equilibrium; Ethanol; Biodiesel; UNIFAC; VEGETABLE-OILS; THERMOPHYSICAL PROPERTIES; BIODIESEL PRODUCTION; PHASE-EQUILIBRIUM; SYSTEMS; TRANSESTERIFICATION; MONOACYLGLYCEROLS; PREDICTION; DIACYLGLYCEROLS; CANOLA;
D O I
10.1016/j.fluid.2018.06.020
中图分类号
O414.1 [热力学];
学科分类号
摘要
This study obtained the liquid-liquid equilibrium (LLE) data for systems involved in the stepwise ethanolysis of soybean oil. Experiments were performed in a 1:9 M ratio (soybean oil:ethanol), at a reaction temperature of 303 K, in two different catalyst concentrations (0.02% and 0.5% of NaOH). Data on phase equilibrium allowed analyzing the presence of biphasic and monophasic regions during the ethanolysis and the phase distribution of partial acylglycerols and esters. Two different sets of UNIFAC binary interaction parameters were used to test their ability to predict the data obtained. As expected, the original parameters could not describe well this kind of system. Nevertheless, an alternative set of parameters obtained from the literature, adjusted to the liquid-liquid equilibrium data of systems in biodiesel production, was able to properly predict these LLE experimental data. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:286 / 293
页数:8
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