首页> 外文期刊>Fluid Phase Equilibria >Vapor-liquid equilibria and excess volumes of the binary systems ethanol plus ethyl lactate, isopropanol plus isopropyl lactate and n-butanol plus n-butyl lactate at 101.325 kPa
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Vapor-liquid equilibria and excess volumes of the binary systems ethanol plus ethyl lactate, isopropanol plus isopropyl lactate and n-butanol plus n-butyl lactate at 101.325 kPa

机译:汽液平衡和过量体积的二元体系:乙醇加乳酸乙酯,异丙醇加乳酸异丙酯和正丁醇加乳酸正丁酯,体积为101.325 kPa

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摘要

Isobaric vapor-liquid equilibrium data have been experimentally determined at 101.3 kPa for the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate. No azeotrope was found in any of the systems. All the experimental data reported were thermodynamically consistent according to the point-to-point method of Fredenslund. The activity coefficients were correlated with the NRTL and UNIQUAC liquid-phase equations and the corresponding binary interaction parameters are reported. The densities and derived excess volumes for the three mixtures are also reported at 298.15 K. © 2005 Elsevier B.V. All rights reserved.
机译:对于乙醇+乳酸乙酯,异丙醇+乳酸异丙酯和正丁醇+乳酸正丁酯二元体系,已在101.3 kPa上通过实验确定了等压蒸气-液体平衡数据。在任何系统中均未发现共沸物。根据Fredenslund的点对点方法,报告的所有实验数据在热力学上都是一致的。活度系数与NRTL和UNIQUAC液相方程相关,并报告了相应的二元相互作用参数。三种混合物的密度和导出的过量体积也据报道为298.15K。 2005 Elsevier B.V.保留所有权利。

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