Vapor-liquid equilibria for pentafluoroethane + propane and difluoromethane + propane systems over a temperature range from 253.15 to 323.15 K

Fluid Phase Equilibria

Volumn 211, Issue 2, 2003, Pages 273-287

  Kim, Ju Hyok ^a   Kim, Min Soo ^a   Kim, Youngil ^b  

^a Seoul National University   (South Korea)

^b Korea Institute of Science and Technology   (South Korea)

Author keywords

Azeotrope; Difluoromethane; Peng Robinson EoS; Pentafluoroethane; Propane; Vapor liquid equilibria

Indexed keywords

BINARY MIXTURES; FLUORINE CONTAINING POLYMERS; PRESSURE EFFECTS; PROPANE;

BUBBLE POINT PRESSURE;

PHASE EQUILIBRIA;

ETHANE; FLUORENE DERIVATIVE; FLUOROMETHANE; PROPANE;

AZEOTROPIC MIXTURE; EQUATION OF STATE; ETHANE; METHANE; PROPANE; VAPOR-LIQUID EQUILIBRIUM;

APPARATUS; ARTICLE; CHEMICAL INTERACTION; COMPARATIVE STUDY; CORRELATION ANALYSIS; EXPERIMENT; ISOTHERM; LIQUID; MEASUREMENT; MODEL; PARAMETER; PRESSURE; TEMPERATURE; VAPOR;

EID: 0037485687     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0378-3812(03)00237-1     Document Type: Article

References (8)

1. C.D. Holcomb, J.W. Magee, J.L. Scott, S.L. Outcalt, W.M. Haynes, NIST Technical Note 1397, Boulder, CO, USA, 1997.
2. Bobbo S., Fedele L., Camporese R., Stryjek R. Fluid Phase Equilib. 199:2002;153-160.
3. Bobbo S., Fedele L., Camporese R., Stryjek R. Fluid Phase Equilib. 199:2002;175-183.
4. Higashi Y. Int. J. Thermophys. 20:1999;507-518.
5. Valtz A., Coquelet C., BabaAhmed A., Richon D. Fluid Phase Equilib. 5030:2002;1-19.
6. Park J.Y., Lim J.S., Lee B.G. Fluid Phase Equilib. 194197:2002;981-993.
7. Peng D.Y., Robinson D.B. Ind. Eng. Chem. Fundam. 15:1976;59-64.
8. M.O. McLinden, S.A. Klein, E.W. Lemmon, A.P.G. Peskin, NIST Thermodynamic Properties of Refrigerants and Refrigerant Mixtures Database (REFPROP), Version 6.0, National Institute of Standards and Technology, Boulder, CO, USA, 1998.