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Phase Equilibria for Perfluoroethane plus (n-Perfluorohexane or n-Perfluorooctane) Binary Systems: Measurement and Modeling

机译:全氟乙烷加(正全氟己烷或正全氟辛烷)二元体系的相平衡:测量和建模

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Isothermal vaporliquid equilibrium (VLE) data are presented for binary systems of perfluoroethane with either n-perfluorohexane or n-perfluorooctane. The measurements were performed at five temperatures ranging from (272.80 to 312.92) K for the perfluoroethane + n-perfluorohexane binary system and at four temperatures ranging from (282.89 to 312.95) K for the perfluoroethane + n-perfluorooctane binary system. Vapor pressure data were measured for perfluoroethane, n-perfluorohexane, and n-perfluorooctane. The data was measured using a static-analytic type apparatus. The expanded uncertainties in temperature, pressure, and both the liquid and vapor compositions (mole fractions) were estimated as 0.09 K, 0.01 MPa, and 0.015 and 0.006, respectively. The VLE data were correlated with the PengRobinson equation of state utilizing the classical one-fluid mixing rule. The experimental data were accurately represented by the model. The relative deviations in pressure and composition were within 1%. The critical region of the phase envelope was well represented by the model.
机译:给出了全氟乙烷与正全氟己烷或正全氟辛烷的二元体系的等温气液平衡(VLE)数据。对于全氟乙烷+正全氟己烷二元体系,在(272.80至312.92)K的五个温度范围内进行测量;对于全氟乙烷+正全氟辛烷二元体系,在(282.89至312.95)K的四个温度范围内进行测量。测量了全氟乙烷,正全氟己烷和正全氟辛烷的蒸气压数据。使用静态分析型仪器测量数据。温度,压力以及液体和蒸汽成分(摩尔分数)的不确定性分别扩大为0.09 K,0.01 MPa和0.015和0.006。利用经典的单流体混合规则,将VLE数据与PengRobinson状态方程相关联。该模型准确地表示了实验数据。压力和组成的相对偏差在1%以内。该模型很好地表示了相位包络的关键区域。

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