Separation of azeotrope (ethanol and ethyl methyl carbonate) by different imidazolium-based ionic liquids: Ionic liquids interaction analysis and phase equilibrium measurements

被引:77
作者
Wang, Ping [1 ]
Xu, Dongmei [1 ]
Yan, Peisong [1 ]
Gao, Jun [1 ]
Zhang, Lianzheng [1 ]
Wang, Yinglong [2 ]
机构
[1] Shandong Univ Sci & Technol, Coll Chem & Environm Engn, Qingdao 266590, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
基金
中国国家自然科学基金;
关键词
Extraction; Ionic liquids; Liquid-liquid equilibrium; Ethyl methyl carbonate; Ethanol; COSMO-SAC MODEL; TERNARY-SYSTEMS; 298.15; K; EXTRACTIVE DISTILLATION; THIOGLYCOLIC ACID; AQUEOUS-SOLUTION; PLUS ETHANOL; T=298.15 K; PREDICTION; MIXTURES;
D O I
10.1016/j.molliq.2018.04.001
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
To separate the azeotrope of ethanol and ethyl methyl carbonate (EMC) using ionic liquids (Is), the sigma-profiles of imidazolium-based ILs with different anions [BF4](-), [HSO4](-), [PF6](-) and [ClO4](-) were calculated by the COSMO-SAC model. Based on the analysis results, 1-ethyl-3-methylimidazolium hydrosulfate ([Emim][HSO4]), 1-propyl-3-methylimidazolium hydrosulfate ([Prmim][HSO4]), 1-butyl-3-methyl-imidazolium hydrosulfate ([Bmim] [HSO4]) were selected as extractants to separate ethanol and EMC. The liquid-liquid tie-line data for the ternary systems ethanol + EMC + Its were measured at 298.15 K under 101.3 kPa, and the influence of ILs with the different alkyl chain length of the cations on the phase behavior was explored. The distribution coefficient and selectivity were calculated to evaluate the extraction capacity of the studied ILs. Meanwhile, the NRTL model was adopted to correlate the experimental results, and the interaction parameters of the NRTL model were also optimized. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:89 / 95
页数:7
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