首页> 外文期刊>Fluid Phase Equilibria >Density, viscosity, vapour-liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
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Density, viscosity, vapour-liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures

机译:在不同温度下,整个浓度范围内的二元体系[1-戊醇+ R-(+)-柠檬烯]的密度,粘度,蒸气-液体平衡,过量摩尔焓及其相关性

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Density and viscosity measurements in the T=(293.15-373.15)K range of pure 1-pentanol, R-(+)limonene, as well as of the binary system {x(1) 1-pentanol + (1 - x(1)) limonene} over the whole concentration range were made. The experimental results were fitted to empirical equations, which permit the calculation of these properties in the studied temperature range. Calculated values are in agreement with the experimental ones. Data of the binary mixtures were further used to calculate the excess molar volume and viscosity deviations. Excess enthalpy at 303 K and vapour-liquid equilibrium measurements in the T=(328.15-343.15)K range were also obtained for the binary system. These last experimental results were used to calculate activity coefficients and the excess molar Gibbs energy. This binary system exhibits a maximum pressure azeotrope. Excess or deviation properties were fitted to the Redlich-Kister polynomial relation to obtain their coefficients and standard deviations. Vapour pressure of 1-pentanol over the P=(2.3-95.1) kPa range were also measured. Furthermore, functional relationships between the total pressure and the mole fraction of 1-pentanol with the temperature of the azeotropic point were also deduced. These equations are useful to calculate the azeotropic point coordinates in the temperature and pressure ranges studied in this work. (C) 2010 Elsevier B.V. All rights reserved.
机译:纯1-戊醇,R-(+)柠檬烯以及二元体系{x(1)1-戊醇+(1- x(1)的T =(293.15-373.15)K范围内的密度和粘度测量))在整个浓度范围内制备range烯。将实验结果拟合到经验公式,从而可以在所研究的温度范围内计算这些特性。计算值与实验值一致。二元混合物的数据进一步用于计算过量的摩尔体积和粘度偏差。对于二元系统,还获得了303 K时的过量焓和T =(328.15-343.15)K范围内的气液平衡测量值。这些最后的实验结果用于计算活度系数和过量的摩尔吉布斯能量。该二元系统表现出最大压力共沸物。将过量或偏差属性拟合到Redlich-Kister多项式关系,以获得其系数和标准偏差。还测量了在P =(2.3-95.1)kPa范围内的1-戊醇的蒸气压。此外,还推导了总压力和1-戊醇的摩尔分数与共沸点温度之间的函数关系。这些方程对于计算在这项工作中研究的温度和压力范围内的共沸点坐标很有用。 (C)2010 Elsevier B.V.保留所有权利。

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