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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Vapor-Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K
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Vapor-Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K

机译:含全氟丁烷(R610)与一氧化碳或一氧化氮的二元体系在(293、313和333)K时的汽液平衡(VLE)数据和热力学建模

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摘要

Isothermal vapor—liquid equilibrium data are presented for binary systems containing perfluorobutane with carbon monoxide or nitric oxide. The measurements were undertaken for both systems at three temperatures ranging from (293 to 333) K, with pressures ranging from (0.965 to 16.130) MPa. The measured data were successfully correlated via the direct method using the Peng—Robinson equation of state incorporating the Mathias—Copeman/Stryjek—Vera alpha function and the Wong—Sandler mixing rule utilizing the nonrandom two-liquid (NRTL) activity coefficient model.
机译:给出了包含全氟丁烷与一氧化碳或一氧化氮的二元系统的等温汽液平衡数据。在这两种系统中,在(293至333)K的三个温度范围内,压力在(0.965至16.130)MPa的范围内进行测量。测得的数据已通过直接方法成功结合,使用了结合了Mathias-Copeman / Stryjek-Vera alpha函数的Peng-Robinson状态方程和利用非随机两液(NRTL)活性系数模型的Wong-Sandler混合规则。

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