Vapor-liquid equilibria of fluoroethane (HFC-161)+2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf)

被引：29
作者：
Chen, Long-Xiang [1 ]
Hu, Peng [1 ]
Zhu, Wan-Bao [1 ]
Jia, Lei [2 ]
Chen, Ze-Shao [1 ]
机构：
[1] Univ Sci & Technol China, Dept Thermal Sci & Energy Engn, Hefei 230027, Peoples R China
[2] Hefei Gen Machinery Res Inst, Hefei 230088, Peoples R China
来源：
FLUID PHASE EQUILIBRIA | 2015年 / 392卷
基金：
中国国家自然科学基金;
关键词：
Vapor-liquid equilibria; HFC-161; HFO-1234yf; PR EoS; 2,3,3,3-TETRAFLUOROPROP-1-ENE R1234YF; BINARY-MIXTURE; TEMPERATURES; R-1234YF; PRESSURE; PHASE;
D O I：
10.1016/j.fluid.2015.02.014
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
In this study, isothermal vapor-liquid equilibrium (VLE) data were measured for the binary system of fluoroethane (HFC-161) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) over the whole composition range in the temperature range from 283.15 to 323.15 K at 10 K intervals. The experimental VLE data were correlated with the Peng-Robinson equation of state. The van der Waals (vdW) one-fluid mixing rule and the Wong-Sandler (WS) mixing rule with the non-random two-liquid (NRTL) activity coefficient model were both used. The correlation results show good agreement with the experimental data. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码：19 / 23
页数：5
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