Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study

被引:53
|
作者
Rodriguez-Cabo, B. [1 ]
Soto, A. [1 ]
Arce, A. [1 ]
机构
[1] Univ Santiago de Compostela, Dept Chem Engn, E-15782 Santiago De Compostela, Spain
来源
关键词
Desulfurization; Ionic liquids; Liquid-liquid equilibrium; C(2)mim][NTf2; LIQUID-LIQUID EQUILIBRIA; IONIC LIQUIDS; EXTRACTIVE DESULFURIZATION; DEEP DESULFURIZATION; ALIPHATIC-HYDROCARBONS; REFINERY STREAMS; BINARY-SYSTEMS; THIOPHENE; IMIDAZOLIUM; GASOLINE;
D O I
10.1016/j.jct.2012.08.031
中图分类号
O414.1 [热力学];
学科分类号
摘要
A tendency to use polysubstituted pyridinium-based ionic liquids for desulfurization of fuel-oils is being very remarkable during last years. Are these ones the most suitable ionic liquids for this purpose? The possibility of using a much cheaper ionic liquid, 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide, has been studied in this work. With this aim, LLE data of the {[C(2)mim][NTf2] + thiophene + toluene}, {[C(2)mim][NTf2] + thiophene + n-hexane} and {[C(2)mim][NTf2] + pyridine + n-hexane} ternary systems have been obtained at T = 298.15 K and atmospheric pressure. The NRTL and UNIQUAC models have been used to correlate the obtained data. Solute distribution ratios and selectivities have been calculated and a comparison with data obtained previously for other ionic liquids has been established. It was found that both cation and anion clearly affect to these thermodynamic parameters. According not just to solubility, but also in terms of selectivity and cost, [C(2)mim][NTf2] can be a competitive desulfurization solvent. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:248 / 255
页数:8
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