Isobaric vapor-liquid equilibrium for ternary mixtures of acetone plus methanol plus ionic liquids at 101.3 kPa

被引:22
作者
Li, Wenxiu [1 ]
Xu, Nana [1 ]
Xu, Honghong [1 ]
Zhang, Aidi [1 ]
Zhang, Zhigang [1 ]
Zhang, Tao [1 ]
机构
[1] Shenyang Univ Chem Technol, Liaoning Prov Key Lab Chem Separat Technol, Shenyang 110142, Peoples R China
基金
美国国家科学基金会;
关键词
Vapor-liquid equilibrium; Ionic liquid; Acetone; Methanol; NRTL model; EXTRACTIVE DISTILLATION; SYSTEM; SEPARATION; ACETATE; ENTRAINERS; TETRAFLUOROBORATE; 2-PROPANOL; SOLVENT; BINARY;
D O I
10.1016/j.fluid.2017.03.014
中图分类号
O414.1 [热力学];
学科分类号
摘要
In order to avoid the pollution and the corrosion of inorganic anions, such as BF4-, SO42- and Cl-, three ionic liquids (ILs) with different organic anions (1-methylimidazolium acetate [MIM]Ac, 1-methylimidazolium 2-hydroxypropionate [MIM]HPr and 1-methyl imidazolium propionate [MIM]Pr) were studied as entrainers for separating acetone + methanol azeotropic mixture. Isobaric vapor-liquid equilibrium (VLE) data for the ternary system containing ILs were measured at 1013 kPa by using an all glass dynamic recirculating still. The experimental data are well correlated by using the nonrandom two liquid (NRTL) model. The separation ability of the three ILs follows the order: [MIM]Ac > [MIM] HPr > [MIM]Pr. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:20 / 27
页数:8
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