期刊
JOURNAL OF CHEMICAL AND ENGINEERING DATA
卷 56, 期 12, 页码 4875-4880出版社
AMER CHEMICAL SOC
DOI: 10.1021/je200816z
关键词
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资金
- Ministry of Education and Science of Spain
- FEDER of the European Union [CTQ2010-18848/PPQ]
Isobaric vapor liquid equilibria (VLE) for the binary systems ethanol + 1-ethyl-3-methylimidazolium dicyanamide ([emim] [DCA]) and water + [emim] [DCA] as well as the VLE for the ternary system ethanol + water + [emim] [DCA] have been obtained at 100 kPa using a recirculating still. The effect of [emim] [DCA] on the ethanol + water system has been compared with that produced by another ionic liquid reported in the literature on the basis of the variation of solvent activity coefficients in ionic liquid (IL) + molecular solvent binary systems. From the results, [emim][DCA] appears as one of the best entrainers for the extractive distillation of the ethanol + water mixtures, causing the azeotrope to disappear at 100 kPa for ionic liquid mole fractions as low as 0.019. The experimental data were fitted with the Mock's electrolyte nonrandom two-liquid (NRTL) model, with a good agreement.
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