Phase Equilibria of Chlorofluorocarbon Alternative Refrigerant Mixtures
Byung Gwon Lee, Ji Young Park, Jong Sung Lim, Sung Yong Cho, Kun You Park
Abstract
Byung Gwon Lee, Ji Young Park, Jong Sung Lim, Sung Yong Cho, Kun You Park
Abstract
Isothermal vapor−liquid equilibrium data were determined for binary systems of difluoromethane/1,1,1,2-tetrafluoroethane (HFC-32/HFC-134a), difluoromethane/pentafluoroethane (HFC-32/HFC-125), difluoromethane/1,1,1-trifluoroethane (HFC-32/HFC-143a), and difluoromethane/1,1-difluoroethane (HFC-32/HFC-152a). The vapor and liquid compositions and pressures were measured in a circulation-type apparatus at 303.15 K and 323.15 K. The experimental data were compared with literature results and correlated with the Canahan−Starling−De Santis equation of state within the uncertainty of ±1.0%.
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Isothermal vapor−liquid equilibrium data were determined for binary systems of difluoromethane/1,1,1,2-tetrafluoroethane (HFC-32/HFC-134a), difluoromethane/pentafluoroethane (HFC-32/HFC-125), difluoromethane/1,1,1-trifluoroethane (HFC-32/HFC-143a), and difluoromethane/1,1-difluoroethane (HFC-32/HFC-152a). The vapor and liquid compositions and pressures were measured in a circulation-type apparatus at 303.15 K and 323.15 K. The experimental data were compared with literature results and correlated with the Canahan−Starling−De Santis equation of state within the uncertainty of ±1.0%.
Key concepts: Difluoromethane, Refrigerant, Chemistry, Isothermal process, Fluorocarbon, Chlorofluorocarbon, Thermodynamics, Phase equilibrium