Vapor-Liquid Equilibrium Measurements for 2,3,3,3-Tetrafluoroprop-1-ene + Butane at Temperatures from 283.15 to 323.15 K

被引：11
|
作者：
Hu, Peng [1 ]
Zhang, Nan [1 ]
Chen, Long-Xiang [2 ]
Cai, Xu-Dong [1 ]
机构：
[1] Univ Sci & Technol China, Dept Thermal Sci & Energy Engn, Hefei 230027, Anhui, Peoples R China
[2] Chinese Acad Sci, Haixi Inst, Quanzhou Inst Equipment Mfg, Jinjiang, Peoples R China
来源：
JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2018年 / 63卷 / 05期
基金：
中国国家自然科学基金;
关键词：
R1234YF; HFO-1234YF; PRESSURE;
D O I：
10.1021/acs.jced.7b01073
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
Vapor-liquid equilibrium (VLE) property measurements for 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + butane (HC-600) were carried out. The range of temperature is from 283.15 to 323.15 K, and the corresponding range of pressure is from 0.148 to 1.30 MPa. The experimental uncertainties in pressure, temperature, and mole fraction are estimated within 3.5 kPa, 5 mK, and 0.003, respectively. Peng-Robinson (PR) equation of state coupling with Wong-Sandler (WS) mixing rule and van der Waals (vdW) mixing rule were used to correlate the experimental VLE data of HFO-1234yf/HC-600. Both of the two models reproduce the VLE property of HFO-1234yf/HC-600 with high accuracy, and PR-WS-NRTL model gave slightly more accurate VLE calculations. Azeotropic behavior was found at high mole fraction of HFO-1234yf.
引用
收藏
页码：1507 / 1512
页数：6
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