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Measurement and prediction of vapor-liquid equilibria of ternary systems containing ionic liquids

机译:含离子液体的三元体系气液平衡的测量和预测

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摘要

For the first time vapor-liquid equilibrium (VLE) data for ternary systems containing ionic liquids are reported. The data were measured by means of a computer-operated static VLE apparatus at 353.15 K with the ionic liquids 1-ethyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide [EMIM](+)[(CF3SO2)(2)N](-) and 1-butyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide [BMIM](+)[(CF3SO2)(2)N](-) and acetone, 2-propanol and water. The experimental VLE data of the binary systems were correlated using the Wilson. NRTL and UNIQUAC models. The errors using Wilson, NRTL, and UNIQUAC are 3.92%, 1.45%, and 1.53%. The g(E)-model parameters of the binary systems were used to predict the VLE behavior of the ternary systems and the predictions were compared to the experimental datasets. The errors using Wilson-, NRTL-, and UNIQUAC-parameters are 5.61%, 7.22%, and 5.02%. (C) 2004 Elsevier B.V. All rights reserved.
机译:首次报道了含离子液体的三元系统的气液平衡(VLE)数据。数据是通过计算机操作的静态VLE装置在353.15 K下用离子液体1-乙基-3-甲基咪唑鎓双(三氟甲基磺酰基)酰亚胺[EMIM](+)[(CF3SO2)(2)N]测量的(-)和1-丁基-3-甲基-咪唑双(三氟甲基磺酰基)酰亚胺[BMIM](+)[(CF3SO2)(2)N](-)和丙酮,2-丙醇和水。二元系统的实验VLE数据使用Wilson进行关联。 NRTL和UNIQUAC模型。使用Wilson,NRTL和UNIQUAC的错误分别为3.92%,1.45%和1.53%。二元系统的g(E)模型参数用于预测三元系统的VLE行为,并将预测结果与实验数据集进行比较。使用Wilson-,NRTL-和UNIQUAC参数的误差为5.61%,7.22%和5.02%。 (C)2004 Elsevier B.V.保留所有权利。

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