Liquid-liquid equilibria for pseudoternary systems:: isooctane-benzene-(methanol plus water)

被引:18
|
作者
García-Flores, BE
de Doz, MG
Trejo, A
机构
[1] Inst Mexicano Petr, Programa Ingn Mol, Ciencias Basicas, Mexico City 07730, DF, Mexico
[2] Area Invest Termofis, Mexico City 07730, DF, Mexico
关键词
experiments; hydrocarbons; isowater curves; liquid-liquid equilibrium; methanol; tie-lines;
D O I
10.1016/j.fluid.2004.12.003
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-liquid equilibrium data are presented for the pseudoternary systems isooctane-benzene-(90 mass% methanol + 10 mass% water) at 298.15 K and isooctane-benzene-(80 mass% methanol + 20 mass% water) at 298.15 and 308.15 K, under atmospheric pressure. The experimental tie-line data obtained define the binodal curve for each one of the studied systems which depending on the amount of water present show type I or type II liquid-liquid phase diagrams. In order to obtain a general view of the effect of water on the partitioning of methanol and hence on the size of the two-phase region we have also determined experimentally 'isowater' tolerance curves for the system isooctane-benzene-methanol at 298.15 K, hence the tie-line data were also obtained for the ternary system. The experimental tie-line data for the four systems studied were correlated with the NRTL and UNIQUAC solution models obtaining a very good reproduction of the experimental behaviour. (c) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:121 / 130
页数:10
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