离子液体
化学
甲苯
环丁砜
非随机双液模型
酰亚胺
庚烷
烷基
萃取(化学)
三元运算
液-液萃取
物理化学
有机化学
分析化学(期刊)
活度系数
溶剂
水溶液
催化作用
计算机科学
程序设计语言
作者
Silvia García Fernández-Villa,Marcos Larriba,Julián García,José S. Torrecilla,Francisco Rodrı́guez
摘要
The good stability and suitable polarity of the 1-alkyl-3-methyl bis(trifluoromethylsulfonyl)imide ionic liquids have prompted their use as solvents for the extraction of mixtures of aromatic and aliphatic hydrocarbons. In this paper, aiming to extend the study of these ionic liquids, the liquid−liquid equilibrium for the systems toluene + heptane + [mmim][Tf2N], [emim][Tf2N], [bmim][Tf2N], or [hmim][Tf2N] at T = 313.2 K were determined. The experiments with [mmim][Tf2N] and [emim]Tf2N have shown good results in the separation of toluene from heptane compared with the distribution ratio and separation factor of sulfolane in the whole range of composition. The degree of consistency of the experimental LLE data was ascertained by applying the Othmer−Tobias correlation. The phase diagrams for the ternary systems were plotted, and the tie lines correlated with the NRTL model compare satisfactorily with the experimental data.
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