首页> 外文期刊>Fluid Phase Equilibria >Vapor-liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa
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Vapor-liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa

机译:2,3-丁二醇与正丁醇,乙酸正丁酯和乙酸乙酯在101.3 kPa的二元混合物的汽液平衡

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摘要

Isobaric vapor-liquid equilibria data have been determined at 101.3kPa for the binary mixtures of (2,3-butanediol+n-butanol), (2,3-butanediol + ethyl acetate) and (2,3-butanediol + butyl acetate). Thermodynamic consistency has been tested for all vapor-liquid equilibria data. The non-ideality of the vapor phase has been considered by using Hayden-O'Connell equation. The activity coefficients have been correlated satisfactorily with Margules, Wilson, NRTL, and UNIQUAC models. (c) 2007 Elsevier B.V. All rights reserved.
机译:(2,3-丁二醇+正丁醇),(2,3-丁二醇+乙酸乙酯)和(2,3-丁二醇+乙酸丁酯)的二元混合物的等压蒸气-液体平衡数据已确定为101.3kPa 。已针对所有气液平衡数据测试了热力学一致性。通过使用Hayden-O'Connell方程考虑了气相的非理想性。活度系数已与Margules,Wilson,NRTL和UNIQUAC模型令人满意地相关。 (c)2007 Elsevier B.V.保留所有权利。

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