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

被引:16
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
相关论文
共 44 条
  • [1] Isobaric vapor-liquid equilibrium for methanol plus dimethyl carbonate plus phosphoric-based ionic liquids
    Cai, Fufeng
    Wu, Xinying
    Chen, Chang
    Chen, Xiaochun
    Asumana, Charles
    Haque, Md Razibul
    Yu, Guangren
    [J]. FLUID PHASE EQUILIBRIA, 2013, 352 : 47 - 53
  • [2] Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
    Gao, Yangchen
    Xu, Li
    Xu, Dongmei
    Shi, Puyun
    Zhang, Zhishan
    Gao, Jun
    Wang, Yinglong
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (03) : 845 - 852
  • [3] Control of an extractive distillation process to dehydrate ethanol using glycerol as entrainer
    Gil, Ivan D.
    Gomez, Jorge M.
    Rodriguez, Gerardo
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2012, 39 : 129 - 142
  • [4] COSMO-SAC Sigma Profile Generation with Conceptual Segment Concept
    Islam, Md Rashedul
    Chen, Chau-Chyun
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (16) : 4441 - 4454
  • [5] JIA S, 2018, FLUID PHASE EQUILIBR, P1
  • [6] Experimental investigation of the influence of NaCl on the vapor-liquid equilibrium of CH3OH+H2O
    Jödecke, M
    Kamps, APS
    Maurer, G
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (01) : 138 - 141
  • [7] Ionic Liquid Screening for Ethylbenzene/Styrene Separation by Extractive Distillation
    Jongmans, Mark T. G.
    Schuur, Boelo
    de Haan, Andre B.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (18) : 10800 - 10810
  • [8] Quality Assessment Algorithm for Vapor-Liquid Equilibrium Data
    Kang, Jeong Won
    Diky, Vladimir
    Chirico, Robert D.
    Magee, Joseph W.
    Muzny, Chris D.
    Abdulagatov, Ilmutdin
    Kazakov, Andrei F.
    Frenkel, Michael
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (09) : 3631 - 3640
  • [9] Effect of dissolved salts on the vapor-liquid equilibrium relationships of three miscible binary systems at the pressure of 101.3 kPa
    Kumar, MD
    Rajendran, M
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1998, 31 (05) : 749 - 757
  • [10] Isothermal Vapor-Liquid Equilibrium Data for the Methanol plus Benzene plus Tetraphenylphosphonium Chloride System
    Kurzin, Alexander V.
    Evdokimov, Andrey N.
    Antipina, Victorija B.
    Feofanova, Mariana A.
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (03) : 1131 - 1135