Vapor-Liquid Equilibrium for Acetonitrile plus Ethanol with Imidazole-Based Ionic Liquids as Entrainers at 101.3 kPa

被引:2
作者
Yue, Kun [1 ]
Lu, Jiani [1 ]
Chen, Peiyu [1 ]
Gu, Shaonan [1 ]
Zhou, Guowei [1 ]
机构
[1] Qilu Univ Technol, Shandong Acad Sci, Key Lab Fine Chem Univ Shandong, Sch Chem & Chem Engn,Jinan Engn Lab Multiscale Fun, Jinan 250353, Peoples R China
基金
中国国家自然科学基金;
关键词
ISOBARIC VAPOR; ETHYL-ACETATE; DIMETHYL CARBONATE; SEPARATION; OPTIMIZATION; BEHAVIOR;
D O I
10.1021/acs.jced.3c00752
中图分类号
O414.1 [热力学];
学科分类号
摘要
Vapor-liquid equilibrium (VLE) data for the ternary system of acetonitrile + ethanol + ionic liquids (ILs) were obtained at 101.3 kPa, and used ILs were 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf2]), 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([EMIM][NTf2]), and 1-butyl-3-methylimidazolium diethylphosphate ([BMIM][DEP]). The nonrandom two-liquid (NRTL) model was used to correlate the VLE data and fitted well, indicating that the minimum mole fractions of [BMIM][NTf2], [EMIM][NTf2], and [BMIM][DEP] to eliminate the azeotrope was 0.053, 0.063, and 0.065, respectively. These ILs led to an outstanding "salting-in" effect on ethanol, and the salting effect on acetonitrile was inapparent. Higher concentrations of ILs signified a stronger salt effect as well as higher equilibrium temperatures. The results indicated that [BMIM][NTf2], [EMIM][NTf2], and [BMIM][DEP] could be used as good candidate entrainers to separate acetonitrile and ethanol in extractive distillation.
引用
收藏
页码:1645 / 1654
页数:10
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