Vapor-Liquid Equilibrium for the difluoromethane (R32)+n-butane (R600) system

被引:13
作者
Fedele, L
Bobbo, S
Scattolini, M
Camporese, R
Stryjek, R
机构
[1] CNR, Inst Bldg Technol, Div Padova, I-35127 Padua, Italy
[2] Polish Acad Sci, Inst Phys Chem, PL-01224 Warsaw, Poland
关键词
D O I
10.1021/je049874h
中图分类号
O414.1 [热力学];
学科分类号
摘要
Vapor-liquid equilibria (VLE) for the difluoromethane (R32) + n-butane (R600) system that shows liquid-phase immiscibility below 246 K were measured at (263.15, 278.15, and 293.15) K by means of a static analytical method. The (T-P-x-y) VLE data were correlated using various equations of state and various mixing rules to compare the ability of these models to correlate data for this strongly nonideal system. The correlation of the VLE data and published VLLE data shows that the system is azeotropic at temperatures higher than the upper critical end point, UCEP, (246 K), heterohomoazeotropic between (246 and 230) K, and heteroazeotropic below 230 K. A comparison with the available VLE data in the literature was performed.
引用
收藏
页码:44 / 48
页数:5
相关论文
共 17 条
[1]   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
[2]   Mutual solubility and VLLE correlation for the R32+R290 system [J].
Bobbo, S ;
Fedele, L ;
Camporese, R ;
Scattolini, M ;
Stryjek, R .
FLUID PHASE EQUILIBRIA, 2003, 212 (1-2) :245-255
[3]   VLLE measurements and their correlation for the R32+R600 system [J].
Bobbo, S ;
Fedele, L ;
Camporese, R ;
Stryjek, R .
FLUID PHASE EQUILIBRIA, 2003, 210 (01) :45-56
[4]   VLE measurements and modeling for the strongly positive azeotropic R32+propane system [J].
Bobbo, S ;
Fedele, L ;
Camporese, R ;
Stryjek, R .
FLUID PHASE EQUILIBRIA, 2002, 199 (1-2) :175-183
[5]   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
[6]   VLLE measurements and correlation for the pentafluoroethane (R125)+n-butane (R600) system [J].
Fedele, L ;
Bobbo, S ;
Camporese, R ;
Stryjek, R .
FLUID PHASE EQUILIBRIA, 2004, 222 :283-289
[7]  
FEDELE L, UNPUB
[8]   NEW MIXING RULES IN SIMPLE EQUATIONS OF STATE FOR REPRESENTING VAPOR-LIQUID-EQUILIBRIA OF STRONGLY NON-IDEAL MIXTURES [J].
HURON, MJ ;
VIDAL, J .
FLUID PHASE EQUILIBRIA, 1979, 3 (04) :255-271
[9]  
Lemmon E.W., 2002, NIST Reference Fluid Thermodynamic and Transport Properties -REFPROP, Version 7.0
[10]   A Helmholtz energy equation of state for calculating the thermodynamic properties of fluid mixtures [J].
Lemmon, EW ;
Tillner-Roth, R .
FLUID PHASE EQUILIBRIA, 1999, 165 (01) :1-21