Vapor-liquid equilibria for 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

Journal of Chemical and Engineering Data

Volumn 45, Issue 5, 2000, Pages 760-763

  Lee, Byung Gwon ^a   Park, Ji Young ^a   Lim, Jong Sung ^a   Lee, Youn Woo ^a   Lee, Chang Ha ^b  

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

^b Yonsei University   (South Korea)

Author keywords

[No Author keywords available]

Indexed keywords

CORRELATION METHODS; EQUATIONS OF STATE; FLUORINE COMPOUNDS; GIBBS FREE ENERGY; ISOTHERMS; MATHEMATICAL MODELS; PARAFFINS; PHASE EQUILIBRIA; PROPANE;

HEPTAFLUOROPROPANE; HURON-VIDAL RULES; ISOBUTANE; PENG-ROBINSON-STRYJEK-VERA EQUATIONS; PENTAFLUOROETHANE;

BINARY MIXTURES;

EID: 0034272170     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je9902847     Document Type: Article

References (7)

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3. Orbey, H.; Sandler, S. I. Modeling Vapor-Liquid Equilibria-cubic equation of state and their mixing rules; Cambridge University Press: 1998.
4. Huron, M.; Vidal, J. New mixing rules in simple equations of state for representing vapor-liquid equilibria of strongly nonideal mixtures. Fluid Phase Equilib. 1979, 3, 255-271
5. Lee, B. G.; Park, J. Y.; Lim, J. S.; Cho, S. Y.; Park, K. Y. Phase Equilibria of Chlorofluorocarbon Alternative Refrigerant Mixtures J. Chem. Eng. Data 1999, 44, 190-192
6. Lim, J. S.; Park, J. Y.; Lee, B. G.; Lee, Y. W.; Kim, J. D. Phase Equilibria of CFC Alternatives Refrigerant Mixtures; Binary systems of Trifluoromethane + isobutane at 283.15 and 293.15K and 1,1,1-Trifluoroethane + isobutane at 323.15 and 333.15 K. J. Chem. Eng. Data 1999, 44, 1226-1230.
7. Huber, M.; Gallagher, J.; McLinden, M. O.; Morrison, G. Thermodynamic Properties of Refrigerants and Refrigerant Mixtures Database (REFPROP), V.6.01, NIST, 1996.