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首页> 外文期刊>The Journal of Chemical Thermodynamics >(Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
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(Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures

机译:(蒸气-液体)平衡和(乙醇+甘油)或(水+甘油)二元混合物在多个温度下的吉布斯自由能函数和过量

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The vapor pressures of (ethanol + glycerol) and (water + glycerol) binary mixtures were measured by means of two static devices at temperatures between (273 and 353 (or 363)) K. The data were correlated with the Antoine equation. From these data, excess Gibbs free energy functions (G~E) were calculated for several constant temperatures and fitted to a fourth-order Redlich-Kister equation using the Barker method. The (ethanol + glycerol) binary system exhibits positive deviations in G~E where for the (water + glycerol) mixture, the G~E is negative for all temperatures investigated over the whole composition. Additionally, the NRTL, UNIQUAC and Modified UNIFAC (Do) models have been used for the correlation or prediction of the total pressure.
机译:(乙醇+甘油)和(水+甘油)二元混合物的蒸气压通过两个静态装置在(273和353(或363))K之间的温度下测量。数据与Antoine方程相关。根据这些数据,计算出几个恒定温度下的多余吉布斯自由能函数(G〜E),并使用Barker方法将其拟合到四阶Redlich-Kister方程。 (乙醇+甘油)二元体系的G〜E值显示正偏差,其中(水+甘油)混合物的G_E值在整个组合物中的所有温度均为负值。此外,NRTL,UNIQUAC和Modified UNIFAC(Do)模型已用于总压力的相关或预测。

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