Thermodynamic modeling of refrigerants using the statistical associating fluid theory with variable range. 2. Applications to binary mixtures

Industrial and Engineering Chemistry Research

Volumn 44, Issue 13, 2005, Pages 4806-4814

  Swaminathan, Saravanan ^a   Visco Jr , Donald P ^a  

^a Tennessee Technological University   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

GLOBAL WARMING POTENTIAL (GWP); OZONE DEPLETION; OZONE-DEPLETION POTENTIAL (ODP); VAPOR LIQUID EQUILIBRIA (VLE);

CHLOROFLUOROCARBONS; CORRELATION METHODS; HYDROCARBONS; MIXTURES; OZONE; PARAMETER ESTIMATION; PHASE EQUILIBRIA; STATISTICAL METHODS; VAPOR PRESSURE;

REFRIGERANTS;

REFRIGERANT;

EID: 22544468835     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie048862m     Document Type: Article

References (34)

1. Zipfel, L.; Barthelemy, P.; Dournel, P. The next generation blowing agents: from one single product to a product range. J. Cell Plast. 1999, 35, 345.
2. Kagawa, N.; Uematsu, M.; Watanabe, K. Theoretical analysis of heat pump cycle characteristics with pure refrigerants and binary refrigerant mixtures. 1. Cycle characteristics with pure refrigerants. Nippon Reito Kyokai Ronbunshu 1990, 7, 43.
3. Swaminathan, S.; Visco, D. P. Thermodynamic modeling of refrigerants using statistical associating fluid theory with variable range. 1. Pure components. Ind. Eng. Chem. Res. 2005, 44, 4798-4805.
4. Patel, N. C.; Teja, A. S. A new cubic equation of state for fluids and fluid mixtures. Chem. Eng. Sci. 1982, 37, 463.
5. Patel, N. C. Improvements of the Patel-Teja equation of state. Int. J. Thermophys. 1996, 17, 673.
6. Iwai, Y.; Margerum, M.; Lu, R.; Benjamin C. Y. A new three-parameter cubic equation of state for polar fluids and fluid mixtures. Fluid Phase Equilib. 1988, 42, 21.
7. Barolo, M.; Bertucco, A.; Scalabrin, G. Prediction of vapor-liquid equilibria of refrigerant mixtures by a cubic group-contribution equation of state. Sci. Tech. Froid 1994, 501.
8. Morrison, J. D.; Barley, M. H.; Murphy, F. T.; Parker, I. B.; Wheelhouse, R. W. The use of an MHV-2 equation of state for modeling the thermodynamic properties of refrigerant mixtures. Int. J. Thermophys. 1995, 16, 1165.
9. Lemmon, E. W.; Jacobsen, R. T. A generalized model for the thermodynamic properties of mixtures. Int. J. Thermophys. 1999, 20, 825.
10. Elvassore, N.; Barolo, M.; Bertucco, A. Group-contribution equation of state for the prediction of vapor-liquid equilibria of mixtures containing hydrofluorocarbons and alkanes. Ind. Eng. Chem. Res. 1998, 37, 3105.
11. Galindo, A.; Whitehead, P. J.; Jackson, G.; Burgess, A. N. Prediction of phase equilibria of refrigerant mixtures of difluoroethane (HFC-32), 1,1,1,2-tetrafluoroethane (HFC-134a) and pentafluoroethane (HFC-125) using SAFT-VR. J. Phys. Chem. B 1998, 102, 7632.
12. Galindo, A.; Davies, L. A.; Gil-Villegas, A.; Jackson G. The thermodynamics of mixtures and the corresponding mixing rules in the SAFT-VR approach for potentials of variable range. Mol. Phys. 1998, 93, 241.
13. Reklaitis, G. V.; Ravindran, A.; Ragsdell, K. M. Engineering Optimization-Methods and Applications; Wiley-Interscience: New York, 1983.
14. Parker, R. C.; Shankland, I. R. Azeotropic-like compositions of 1,1,1,3,3-pentafluoropropane and hydrocarbons. U.S. Patent 5,-677,358, 1997, Allied Signal NJ.
15. Stein, F. R.; Proust, P. C. Vapor-liquid equilibria of the trifluoromethane-trifluorochloromethane system. J. Chem. Eng. Data 1971, 16, 389.
16. Bobbo, S.; Fedele, L.; Scattolini, M.; Camporese, R. Isothermal VLE measurements for the binary mixtures HFC-134a+HFC-245fa and HC-600a+HFC-245fa. Presented at the 14th Symposium on Thermophysical Properties, Colorado, June 25-30, 2000.
17. Piacentini, A.; Stein, F. P. An experimental and correlative study of the vapor-liquid equilibria of the tetrafluoromethane-trifluoromethane system. Chem. Eng. Prog. Symp. Ser. 1967, 63, 28.
18. Barley, M. H.; Morrison, J. D.; O'Donnel, A.; Parker, I. B.; Peterbridge, S.; Wheelhouse, R. W. Vapour-liquid equilibrium data for binary mixtures of some new refrigerants. Fluid Phase Equilib. 1997, 140, 183.
19. Gil-Villegas, A.; Galindo, A.; Whitehead, P. J.; Mills, S. J.; Jackson, G. Statistical associating fluid theory for chain molecules with attractive potentials of variable range. J. Chem. Phys. 1997, 106, 4168.
20. Swaminathan, S.; Visco, D. P. Exploring the Importance of Pure Component Parameterization Procedures in Predicting Mixture Phase Properties via Equations of State, (to be submitted).
21. Zipfel, L. HFC-365mfc, a major step in the development of new HFC blowing agents for polyurethane foams for construction. Proceedings of Polyurethanes, 1999.
22. 2-R23 and their correlation by equation of state. Fluid Phase Equilib. 1992, 73, 147.
23. Maezawa, Y.; Sato, H.; Watanabe, K. Saturated liquid densities and bubble-point pressures of the binary HCFC22-HFC152a system. Fluid Phase Equilib. 1991, 61, 263.
24. Yada, N.; Uematsu, M.; Watanabe, K. Study of PVTx properties for binary R152a + R114 system. Trans. Jar 1998, 5, 107.
25. Valtz, A.; Laugler, S.; Richon, D. Bubble pressures and saturated liquid molar volumes of trifluorotrichloroethane-fluo-rohydrocarbon mixtures, experimental data and modelization. J. Chem. Eng. Data 1987, 32, 397.
26. Park, Y. M.; Jung, M. Y. Vapor-liquid equilibria for the pentafluoroethane (HFC-125) + propane (R-290) system. J. Chem. Eng. Data 2002, 47, 818.
27. Valtz, A.; Coquelet, C.; Baba-Ahmed, A.; Richon, D. Vapor-liquid equilibrium data for the propane + 1,1,1,2,3,3,3-heptafluo-ropropane (R 227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 Mpa. Fluid Phase Equilib. 2002, 202, 29.
28. Bobbo, S.; Artico, G.; Fedele, L.; Scattolini, M.; Camporese, R. Vapor-liquid equilibrium measurements and correlation of the binary refrigerant mixture propane (HC-290) + 1,1,1,2,3,3,3-heptafluoropropane (HFC 227ea) at 278.15, 293.15, and 308.15 K. J. Chem: Eng. Data 2002, 47, 839.
29. Lim, J. S.; Park, J.; Lee, B. G.; Kim, J. Phase equilibria of chlorofluorocarbon alternative refrigerant mixtures. Binary systems of trifluoromethane + isobutane at 283.15 and 293.15 K and 1,1,1-trifluoroethane + isobutane at 323.15 and 333.15 K. J. Chem. Eng. Data 2000, 45, 734.
30. Lim, J. S.; Park, J.; Lee, B. G.; Kim, J. Phase equilibria of chlorofluorocarbon alternative refrigerant mixtures. Binary systems of isobutane + 1,1,1,2-tetrafluoroethane, + 1,1-difluoroethane, + difluoromethane. J. Chem. Eng. Data 1999, 44, 1226.
31. Coquelet, C.; Valtz, A.; Baba-Ahmed, A.; Richon, D. Vapor-liquid equilibria data for the azeotropic difluoromethane + propane system at temperatures from 294.83 to 343.26 K and pressures up to 5.4 Mpa. J. Chem. Eng. Data 2003, 48, 317.
32. Lim, J. S.; Park, J.; Lee, B. G. Phase equilibria of HFC mixtures: Binary mixtures of trifluoromethane + 1,1-difluoroethane and trifluoromethane + 1,1,1-trifluoroethane at 283.15 and 293.15 K. J. Chem. Eng. Data 2002, 47, 582.
33. Lee, B. G.; Park, J.; Lim, J. S.; Lee, Y. Vapor-liquid equilibria of isobutane + pentafluoroethane (HFC-125) at 293.15 to 313.15 K and + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) at 303.15 to 323.15 K. J. Chem. Eng. Data 2000, 45, 760.
34. Perry, R. H.; Green, D. W.; Perry's Chemical Engineers' Handbook, 7th ed.; McGraw-Hill: New York, 1997.