Experimental vapour-liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane

被引:11
作者
Subramoney, Shalendra Clinton [1 ]
Valtz, Alain [2 ]
Coquelet, Christophe [1 ,2 ]
Richon, Dominique [1 ]
Naidoo, Paramespri [1 ]
Ramjugernath, Deresh [1 ]
机构
[1] Univ KwaZulu Natal, Sch Engn, Thermodynam Res Unit, Durban, South Africa
[2] MINES ParisTech, CTP Ctr Thermodynam Proc, F-77305 Fontainebleau, France
基金
新加坡国家研究基金会;
关键词
Vapour-liquid equilibrium; Static-analytic" method; ROLSI (TM); Fluorocarbon; 1,1,2,3,3,3-Hexafluoro-1-propene; 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane; Hexafluoropropylene; Hexafluoropropylene oxide; 1-Butene; EQUATION-OF-STATE; THERMODYNAMIC PROPERTIES; CUBIC EQUATIONS; PRESSURES; TEMPERATURES; REFRIGERANTS; DENSITIES; SYSTEM;
D O I
10.1016/j.jct.2013.01.017
中图分类号
O414.1 [热力学];
学科分类号
摘要
Novel isothermal (P-x-y) vapour-liquid equilibrium data are reported at three temperatures for each of the (1,1,2,3,3,3-hexafluoro-1-propene + 1-butene), (2,2,3-trifluoro-3-(trifluoromethyl) oxirane + 1-butene), and (difluoromethane + 1-butene) binary systems. The experimental values were measured on a "static-analytic" type apparatus which utilized two electromagnetic ROLSI (TM) capillary samplers for repeatable and reliable equilibrium phase sampling and handling. The VLE results are correlated with in-house thermodynamic software based on the "PR-MC-WS-NRTL" model which comprises the Mathias-Copeman alpha function, Wong-Sandler mixing rule, and non-random two-liquid local composition activity model introduced in the Peng-Robinson equation of state. A maximum pressure azeotrope is observed at all temperatures studied for the (2,2,3-trifluoro-3-(trifluoromethyl) oxirane + 1-butene), and (difluoromethane + 1-butene systems), but not for the 1,1,2,3,3,3-hexafluoro-1-propene system. Liquid-liquid immiscibility is not observed for any of the systems studied over the range of temperatures investigated. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:18 / 26
页数:9
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