Vapor-liquid equilibrium of HFC-32/134a and HFC-125/134a systems

被引：17
|
作者：
Kim, CN
Park, YM
机构：
[1] Ajou Univ, Dept Mech Engn, Paldal Gu, Suwon 442749, South Korea
[2] Ajou Univ, Sch Mech & Ind Engn, Paldal Gu, Suwon 442749, South Korea
来源：
INTERNATIONAL JOURNAL OF THERMOPHYSICS | 1999年 / 20卷 / 02期
关键词：
activity coefficients; binary interaction parameters; equation of state; fugacity coefficients; HFC-32/134a mixture; HFC-125/134a mixture; thermodynamic consistency; vapor-liquid equilibrium;
D O I：
10.1023/A:1022605104490
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
A vapor-liquid equilibrium apparatus has been developed and used to obtain data for the binary HFC-32/134a and HFC-125/134a systems. Twenty-two equilibrium data are obtained for the HFC-32/134a system over the temperature range from 258.15 to 283.15 K at 5 K intervals and the composition range from 0.2 to 0.8 liquid mole fraction. Twenty-five equilibrium data are obtained for the HFC-125/134a system over the temperature range from 263.15 to 303.15 K at 10 K intervals and the composition range from 0.18 to 0.81 liquid mole friction. These data have been tested and found to be thermodynamically consistent. Based upon the present data, the binary interaction parameters of the Carnahan-Starling-De Santis (CSD) and Redlich-Kwong-Soave (RKS) equations of slate are calculated for five isotherms for the HFC-125/134a mixture and six isotherms for the HFC-32/134a mixture. The calculated results from the CSD equation are compared with data in the open literature.
引用
收藏
页码：519 / 530
页数：12
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