TY - JOUR
T1 - Liquid densities of alternative refrigerants blended with difluoromethane, pentafluoroethane, and 1,1,1,2-tetrafluoroethane
AU - Widiatmo, J. V.
AU - Fujimine, T.
AU - Sato, H.
AU - Watanabe, K.
PY - 1997/1/1
Y1 - 1997/1/1
N2 - Measurements of the bubble-point pressures and the saturated-liquid densities of the binary mixtures difluoromethane + 1,1,1,2-tetrafluoroethane (R-32 + R-134a) and pentafluoroethane + 1,1,1,2-tetrafluoroethane (R-125 + R-134a) and the ternary mixture difluoromethane + pentafluoroethane + 1,1,1,2-tetrafluoroethane (R-32 + R-125 + R-134a) are presented. The estimated uncertainties of ±15 mK in temperature, ±12 kPa in pressure, ±0.2% in density, and ±0.3 mol % in composition are reported. The Peng-Robinson equation and the modified Hankinson-Brobst-Thomson equation have been optimized to represent the measured properties satisfactorily. The calculated temperature glides of the mixtures of the present interest have also been presented.
AB - Measurements of the bubble-point pressures and the saturated-liquid densities of the binary mixtures difluoromethane + 1,1,1,2-tetrafluoroethane (R-32 + R-134a) and pentafluoroethane + 1,1,1,2-tetrafluoroethane (R-125 + R-134a) and the ternary mixture difluoromethane + pentafluoroethane + 1,1,1,2-tetrafluoroethane (R-32 + R-125 + R-134a) are presented. The estimated uncertainties of ±15 mK in temperature, ±12 kPa in pressure, ±0.2% in density, and ±0.3 mol % in composition are reported. The Peng-Robinson equation and the modified Hankinson-Brobst-Thomson equation have been optimized to represent the measured properties satisfactorily. The calculated temperature glides of the mixtures of the present interest have also been presented.
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U2 - 10.1021/je9602327
DO - 10.1021/je9602327
M3 - Article
AN - SCOPUS:0001168820
SN - 0021-9568
VL - 42
SP - 270
EP - 277
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
IS - 2
ER -