Separation abilities of three acetate-based ionic liquids for benzene-methanol mixture through vapor-liquid equilibrium experiment at 101.3 kPa

被引:15
|
作者
Li, Wenxiu [1 ]
Yin, Haiying [1 ]
Guo, Hongfan [1 ]
Li, Jipeng [1 ]
Zhang, Tao [1 ]
机构
[1] Shenyang Univ Chem Technol, Liaoning Prov Key Lab Chem Separat Technol, Shenyang 110142, Liaoning, Peoples R China
基金
美国国家科学基金会;
关键词
Vapor liquid phase equilibrium; Ionic liquids; Benzene; Methanol; NRTL model; EXTRACTIVE DISTILLATION PROCESS; PRESSURE-SWING DISTILLATION; PLUS DIMETHYL CARBONATE; ISOBARIC VAPOR; ETHYL-ACETATE; BINARY-SYSTEMS; TERNARY MIXTURES; WATER; 2-PROPANOL; ALGORITHM;
D O I
10.1016/j.fluid.2019.03.022
中图分类号
O414.1 [热力学];
学科分类号
摘要
Three ionic liquids (ILs) with acetate anion (1-hexyl-3-methylimidazolium acetate, [HMIM][OAC]; 1-octyl-3-methylimidazolium acetate, [OMIM][OAC]; and 1-decyl-3-methylimidazolium acetate, [DMIM] [OAC]) were studied as entrainers for separating the benzene-methanol binary azeotrope. Isobaric vapor liquid equilibrium (VLE) data for the ternary systems of benzene + methanol + IL were measured at 101.3 kPa. The VLE data were well correlated by using the nonrandom two-liquid (NRTL) model. The relative volatility of benzene to methanol is enhanced with the increase in IL content. The azeotropic phenomenon of benzene-methanol mixture can be completely eliminated when IL content reaches a specific value. After the azeotropy of benzene-methanol mixture is completely eliminated, the separation ability of the three ILs follows the order [HMIM][OAC] > [OMIM][OAC] > [DMIM][OAC]. The separation abilities of the three ILs were further analyzed with the help of their sigma-profiles. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:80 / 87
页数:8
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