Liquid-liquid equilibria for {hexane plus benzene+1-ethyl-3-methylimidazolium ethylsulfate} at (298.2, 313.2 and 328.2) K

被引：87

作者：

Garcia, Julian ^{[1
]}

Fernandez, Adela ^{[1
]}

Torrecilla, Jose S. ^{[1
]}

Oliet, Mercedes ^{[1
]}

Rodriguez, Francisco ^{[1
]}

机构：

[1] Univ Complutense Madrid, Dept Chem Engn, E-28040 Madrid, Spain

来源：

FLUID PHASE EQUILIBRIA | 2009年 / 282卷 / 02期

关键词：

Ionic liquid; 1-Ethyl-3-methylimidazolium ethylsulfate; LLE; Extraction; Aromatics; IONIC LIQUID; BENZENE PLUS; AROMATIC-HYDROCARBONS; ATMOSPHERIC-PRESSURE; 1-ETHYL-3-METHYLIMIDAZOLIUM ETHYLSULFATE; T=298.15 K; MIXTURES; EXTRACTION; SEPARATION; SYSTEMS;

D O I：

10.1016/j.fluid.2009.05.006

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Liquid-liquid equilibria (LLE) for the ternary system {hexane + benzene + 1-ethyl-3-methylimidazolium ethylsulfate ([emim]C(2)H(5)SO(4))} have been measured at the temperatures (298.2, 313.2 and 328.2) K and atmospheric pressure. The reliability of the experimental data was tested using the Othmer-Tobias correlation. For the extractive effectiveness of the solvent, the distribution ratio and separation factor curves were plotted and compared with those Of sulfolane. In addition, the LLE data were also correlated with UNIQUAC and NRTL models in a satisfactory manner. (C) 2009 Elsevier B.V. All Fights reserved.

引用

页码：117 / 120

页数：4

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