Vapor plus liquid equilibrium measurements and correlation of the binary refrigerant mixtures difluoromethane (HFC-32)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K

被引:15
作者
Bobbo, S [1 ]
Fedele, L [1 ]
Scattolini, M [1 ]
Camporese, R [1 ]
机构
[1] Natl Res Council, Inst Refrigerat, I-35127 Padua, Italy
关键词
Carnahan-Starling-DeSantis equation of state; HFC-125+HFC-236ea; HFC-32+HFC-236ea; isothermal vapor liquid equilibrium; vapor pressures;
D O I
10.1023/A:1006649704594
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isothermal vapor liquid equilibria (VLE) For the binary systems of difluoromethane (HFC-32)+1,1.1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane) (HFC-236ea) were measured at 288.6, 303.2, and 318.2 K using an apparatus in which the vapor phase was recirculated through the liquid. The phase composition at equilibrium was measured by gas chromatography, based on calibration using gravimetrically prepared mixtures. Both systems show a slight deviation from Raoult's law. The uncertainties in pressure, temperature, and vapor- and liquid-phase composition measurements were estimated to be no more than +/- 1 kPa, +/- 0.02 K, and +/-0.002 mol fraction, respectively. The data were analyzed using the Carnahan-Starling-DeSantis equation of stare.
引用
收藏
页码:781 / 791
页数:11
相关论文
共 13 条
[1]  
BARONCINI C, 1993, P INT C EN EFF REFR, P207
[2]  
BARONCINI C, 1993, HIGH TEMP HIGH PRESS, V25, P459
[3]  
BEYERLEIN AL, 1993, EPA600A93062
[4]   Vapor-liquid equilibria for difluoromethane (R32) plus and pentafluoroethane (R125) plus 1,1,1,3,3,3-hexafluoropropane (R236fa) at 303.2 and 323.3 K [J].
Bobbo, S ;
Camporese, R ;
Stryjek, R .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1999, 44 (02) :349-352
[5]   A recirculation apparatus for vapor-liquid equilibrium measurements of refrigerants. Binary mixtures of R600a, R134a and R236fa [J].
Bobbo, S ;
Stryjek, R ;
Elvassore, N ;
Bertucco, A .
FLUID PHASE EQUILIBRIA, 1998, 150 :343-352
[6]   THERMODYNAMIC PROPERTIES OF DIFLUOROMETHANE [J].
DEFIBAUGH, DR ;
MORRISON, G ;
WEBER, LA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1994, 39 (02) :333-340
[7]   Thermodynamic properties of CF3-CHF-CHF2, 1,1,1,2,3,3-hexafluoropropane [J].
Defibaugh, DR ;
Gillis, KA ;
Moldover, MR ;
Schmidt, JW ;
Weber, LA .
FLUID PHASE EQUILIBRIA, 1996, 122 (1-2) :131-155
[8]   VAPOR-LIQUID-EQUILIBRIUM FROM A HARD-SPHERE EQUATION OF STATE [J].
DESANTIS, R ;
GIRONI, F ;
MARRELLI, L .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (03) :183-189
[9]  
McLinden MO, 1998, NIST STANDARD REFERE
[10]  
Morrison G., 1996, NIST THERMODYNAMIC P