Solvent extraction of aromatic sulfur compounds from n-heptane using the 1-ethyl-3-methylimidazolium tricyanomethanide ionic liquid

被引:101
作者
Krolikowski, Marek [1 ]
Walczak, Klaudia [1 ]
Domanska, Urszula [1 ,2 ]
机构
[1] Warsaw Univ Technol, Dept Phys Chem, Fac Chem, PL-00664 Warsaw, Poland
[2] Univ KwaZulu Natal, Sch Engn, Thermodynam Res Unit, ZA-4041 Durban, South Africa
关键词
Desulfurization; Extraction; (Liquid plus liquid) phase equilibria; Ternary system; EMIM][TCM; Ionic liquid; ALIPHATIC-HYDROCARBONS; FUEL-OILS; THIOPHENE; DESULFURIZATION; EQUILIBRIA; SEPARATION;
D O I
10.1016/j.jct.2013.05.048
中图分类号
O414.1 [热力学];
学科分类号
摘要
The ionic liquid 1-ethyl-3-methylimidazolium tricyanomethanide ([EMIM][TCM]) has been tested as a solvent for the separation of sulfur compounds from aliphatic hydrocarbon. Liquid-liquid phase equilibrium data have been determined for ternary systems containing the ionic liquid, thiophene or benzothiophene and n-heptane. The influence of temperature on the separation of thiophene from n-heptane was determined. High solubility of sulfur compounds and practical immiscibility of aliphatic hydrocarbon in ionic liquid have been found. The values of selectivity and solute distribution ratios have been calculated for all systems and compared with literature data for other 1-ethyl-3-methylimidazolium-based ionic liquids. High values of selectivity were obtained. The experimental data were correlated using the NRTL equation, and the binary interaction parameters have been reported. The phase equilibria diagrams for the ternary mixtures including the experimental and calculated tie-lines have been presented. (c) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:168 / 173
页数:6
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