Vapor plus liquid equilibrium measurements and correlation of the binary refrigerant mixtures difluoromethane (HFC-32)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K
S. Bobbo et al., Vapor plus liquid equilibrium measurements and correlation of the binary refrigerant mixtures difluoromethane (HFC-32)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K, INT J THERM, 21(3), 2000, pp. 781-791
Isothermal vapor liquid equilibria (VLE) For the binary systems of difluoro
methane (HFC-32)+1,1.1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroe
thane (HFC-125)+1,1,1,2,3,3-hexafluoropropane) (HFC-236ea) were measured at
288.6, 303.2, and 318.2 K using an apparatus in which the vapor phase was
recirculated through the liquid. The phase composition at equilibrium was m
easured by gas chromatography, based on calibration using gravimetrically p
repared mixtures. Both systems show a slight deviation from Raoult's law. T
he uncertainties in pressure, temperature, and vapor- and liquid-phase comp
osition measurements were estimated to be no more than +/- 1 kPa, +/- 0.02
K, and +/-0.002 mol fraction, respectively. The data were analyzed using th
e Carnahan-Starling-DeSantis equation of stare.