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首页> 外文期刊>Fluid Phase Equilibria >Temperature and composition dependence of excess Gibbs energy in the system of tetraglyme (1) + decane (2): Evaluation by simultaneous correlation of limiting activity coefficients, liquid-liquid equilibrium, and calorimetric data
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Temperature and composition dependence of excess Gibbs energy in the system of tetraglyme (1) + decane (2): Evaluation by simultaneous correlation of limiting activity coefficients, liquid-liquid equilibrium, and calorimetric data

机译:四甘醇二甲醚(1)+癸烷(2)系统中过量吉布斯能量的温度和成分依赖性:通过同时关联极限活度系数,液-液平衡和量热数据进行评估

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摘要

Properties related to vapor-liquid and liquid-liquid equilibria in the binary system of tetraglyme (1) + alkane (2) were measured, collected from literature, and subsequently simultaneously correlated using the Redlich-Kister equation and basic thermodynamic relationships. The Inert Gas Stripping method was used for measurement of limiting activity coefficients of alkanes (pentane, hexane, heptane, and octane) in tetraglyme in the temperature interval from 288.15 to 313.15 K. The limiting activity coefficient of decane in tetraglyme was obtained by extrapolation of these experimental data in a homologous line of alkanes. Liquid-liquid equilibria were measured by direct analytical and turbidity methods. Excess enthalpy and excess heat capacity data were collected from the literature. As the studied system shows an upper critical Solubility temperature and a "W-shape" composition dependence of the excess heat capacity, a high number, namely 17, of correlation equation parameters were needed for a precise description of the temperature and composition dependence of the excess Gibbs energy and related physical properties.
机译:测量了四甘醇二甲醚(1)+烷烃(2)的二元系统中与气液平衡和液液平衡有关的性质,从文献中收集了这些性质,随后同时使用Redlich-Kister方程和基本的热力学关系进行了关联。在288.15至313.15 K的温度区间内,采用惰性气体汽提法测量四甘醇二甲醚中的烷烃(戊烷,己烷,庚烷和辛烷)的极限活度系数。这些实验数据在同系烷烃中。液-液平衡通过直接分析和浊度法测量。从文献中收集了过量的焓和过量的热容量数据。由于所研究的系统显示出较高的临界溶解度温度和过剩热容量的“ W形”成分依赖性,因此需要大量(即17个)相关方程参数来精确描述其温度和成分依赖性。多余的吉布斯能量和相关的物理性质。

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