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首页> 外文期刊>The Journal of Chemical Thermodynamics >Experimental analysis of vapour-liquid phase equilibria for binary systems of diethyl carbonate with methyl, ethyl, isopropyl, n-butyl and isoamyl acetates at 95 kPa
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Experimental analysis of vapour-liquid phase equilibria for binary systems of diethyl carbonate with methyl, ethyl, isopropyl, n-butyl and isoamyl acetates at 95 kPa

机译:碳酸二乙基,乙基,异丙基,正丁基和95kPA乙烯基乙酸二乙酸二元体系汽液相平衡的实验分析

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Experimental analysis of vapour-liquid phase equilibrium (VLE) for five binary pairs of diethyl carbonate (DEC) with methyl acetate, ethyl acetate, isopropyl acetate, n-butyl acetate and isoamyl acetate was carried out in this study. VLE data were generated experimentally at local atmospheric pressure of 95 kPa in a glass dynamic recirculation still. Reliability of data was checked with the thermodynamic consistency tests by Van Ness, infinite dilution, pure component and mean absolute deviation test. Experimental data was found to be thermodynamically consistent with all tests and data was regressed with Wilson, NRTL and UNIQUAC activity coefficient models to determine binary interaction parameters. Binary pair of DEC with n-butyl acetate has shown azeotropic behaviour with minimum boiling azeotrope and a close boiling behaviour through-out the composition range. No azeotropic behaviour was observed for the rest of the binary pairs. (c) 2020 Elsevier Ltd.
机译:本研究在本研究中对乙酸甲酯,乙酸乙酯,乙酸乙酸乙酯,乙酸正丁酯,乙酸二丁酯,乙酸二丁酯,乙酸丁酯和异戊酯的五二烯碳酸二乙酯(DED)进行汽液相平衡(VLE)的实验分析。 在玻璃动态再循环中在95kPa的局部大气压下实验产生VLE数据。 通过van ness,无限稀释,纯组分和平均绝对偏差试验检查数据的可靠性。 发现实验数据与所有测试和数据一起与威尔逊,NRTL和uniquac活动系数模型回归,以确定二进制交互参数。 用正丁酸正丁酸丁酯二进制对DED显示了具有最小沸点的共沸性行为,并通过组成范围的沸腾行为。 没有对二元对的其余部分观察到共沸行为。 (c)2020 Elsevier Ltd.

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