Liquid-liquid phase equilibrium measurements and modeling for systems involving {soybean oil plus ethyl esters plus (ethanol plus water)}

被引:24
|
作者
Dagostin, Joao L. A. [1 ]
Mafra, Marcos R. [1 ]
Ramos, Luiz P. [2 ]
Corazza, Marcos L. [1 ]
机构
[1] Univ Fed Parana, Dept Chem Engn, BR-81531990 Curitiba, PR, Brazil
[2] Univ Fed Parana, Dept Chem, BR-81531990 Curitiba, PR, Brazil
关键词
LLE; Biodiesel; Soybean oil; Ethanol; NRTL; BIODIESEL PRODUCTION; THERMOPHYSICAL PROPERTIES; ANHYDROUS ETHANOL; TERNARY-SYSTEMS; VEGETABLE-OILS; IONIC LIQUID; CANOLA OIL; GLYCEROL; TRANSESTERIFICATION;
D O I
10.1016/j.fuel.2014.10.049
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
This work reports a new set of experimental data for the liquid-liquid equilibrium for {soybean oil + soybean oil ethyl esters + (ethanol + water)} systems at atmospheric pressure and at T = (298.15, 313.15 and 323.15) K, while pseudobinary solubility data were obtained for the system {soybean oil + (ethanol + water)} at temperatures from 278.15 to 348.15 K. The liquid-phase compositions were measured by gravimetry, refractive index and Karl Fischer methods. Solubility curves (binodal) were obtained for each temperature by the cloud-point method. The NRTL activity coefficient model was used to correlate experimental tie-line data. Predicted values were close to experimental ones indicating a good correlation for the thermodynamic model used. (C) 2014 Published by Elsevier Ltd.
引用
收藏
页码:164 / 172
页数:9
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