离子液体
化学
优等
非随机双液模型
酰亚胺
甲苯
苯
萃取蒸馏
活度系数
物理化学
环己烷
热力学
有机化学
蒸馏
催化作用
水溶液
物理
作者
Ryo Kato,Michael Krummen,Jürgen Gmehling
标识
DOI:10.1016/j.fluid.2004.05.009
摘要
Vapor–liquid equilibria (VLE) and excess enthalpies (HE) have been measured for the hydrocarbons hexane, 1-hexene, cyclohexane, cyclohexene, benzene and toluene with the ionic liquids 1-metyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide [MMIM]+ [(CF3SO2)2N]−, 1-ethyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide [EMIM]+ [(CF3SO2)2N]−, 1-butyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide [BMIM]+ [(CF3SO2)2N]−, 1-metyl-3-methyl-imidazolium ethylsulfate [EMIM]+ [C2H5OSO3]− and pyridiniumethoxyethylsulfate [C5H5NH]+ [C2H5OC2H4OSO3]− at 353.15 K, 303.15 K and 333.15 K, respectively. The experimental VLE and HE data were correlated together with available activity coefficients at infinite dilution γi∞ using the NRTL and UNIQUAC models and the relative van der Waals volume and surface area parameters r and q estimated by the Bondi method. The overall average errors using NRTL and UNIQUAC model are 4.6% and 4.8% for VLE, 1.7% and 1.9% for γi∞ and 3.6% and 3.2% for HE.
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