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Phase Equilibria of CFC Alternative Refrigerant Mixtures: 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea)+Difluoromethane (HFC-32), +1,1,1,2-Tetrafluoroethane (HFC-134a), and +1,1-Difluoroethane (HFC-152a)
Authors:J-Y Park  J S Lim  B-G Lee  Y-W Lee
Affiliation:(1) Division of Environment and Process Technology, Korea Institute of Science and Technology (KIST), P.O. Box 131, Cheongryang, Seoul, 130-650, Korea
Abstract:Isothermal vapor–liquid equilibria were measured for the binary systems difluoromethane (HFC-32)+1,1,1,2,3,3,3-heptafluoropropane (HFC-22ea) and 1,1-difluoroethane (HFC-152a)+1,1,1,2,3,3,3-heptafluoropropane at 283.15 and 303.15 K and 1,1,1,2-tetrafluoroethane (HFC-134a)+1,1,1,2,3,3,3-heptafluoropropane at 303.15 and 323.15 K in an apparatus in which both phases were recirculated. The experimental data were correlated with the Peng–Robinson equation of state using the Wong–Sandler mixing rules. Azeotropic behavior has not been found in any of the three mixtures.
Keywords:binary mixtures  HFC-227ea  HFC-32  HFC-134a  HFC-152a  Peng–  Robinson equation of state  vapor–  liquid equilibria  Wong–  Sandler mixing rule
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