TY - JOUR
T1 - Saturated liquid densities and bubble-point pressures of the binary HFC 152a+HCFC 142b system
AU - Maezawa, Y.
AU - Widiatmo, J. V.
AU - Sato, H.
AU - Watanabe, K.
PY - 1991/11/1
Y1 - 1991/11/1
N2 - Forty-eight sets of the saturated liquid densities and bubble-point pressures of the binary HFC 152a + HCFC 142b system were measured with a magnetic densimeter coupled with a variable-volume cell. The measurements obtained at four compositions, 20, 40, 60, and 80 wt%, of HFC 152a cover a range of temperatures from 280 to 400 K. The experimental uncertainties in temperature, pressure, density, and composition were estimated to be within ±15mK, ±20kPa, ±0.2%, and between -0.14 and ±0.01 wt% HFC 152a (-0.01 and + 0.14 wt% HCFC 142b), respectively. The purities of the samples were 99.9 wt% for HFC 152a and 99.8 wt% for HCFC 142b. A binary interaction parameter, kij, in the Peng-Robinson equation of state was determined as a function of temperature for representing the bubble-point pressures. On the other hand, two constant binary-interaction parameters, kij and lij, were introduced into the mixing rule of the Hankinson-Brobst-Thomson equation for representing the saturated liquid densities.
AB - Forty-eight sets of the saturated liquid densities and bubble-point pressures of the binary HFC 152a + HCFC 142b system were measured with a magnetic densimeter coupled with a variable-volume cell. The measurements obtained at four compositions, 20, 40, 60, and 80 wt%, of HFC 152a cover a range of temperatures from 280 to 400 K. The experimental uncertainties in temperature, pressure, density, and composition were estimated to be within ±15mK, ±20kPa, ±0.2%, and between -0.14 and ±0.01 wt% HFC 152a (-0.01 and + 0.14 wt% HCFC 142b), respectively. The purities of the samples were 99.9 wt% for HFC 152a and 99.8 wt% for HCFC 142b. A binary interaction parameter, kij, in the Peng-Robinson equation of state was determined as a function of temperature for representing the bubble-point pressures. On the other hand, two constant binary-interaction parameters, kij and lij, were introduced into the mixing rule of the Hankinson-Brobst-Thomson equation for representing the saturated liquid densities.
KW - HCFC 142b (CH CClF)
KW - HFC 152a (CH CHF)
KW - bubble-point pressure
KW - mixtures
KW - refrigerants
KW - saturated liquid density
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U2 - 10.1007/BF00503517
DO - 10.1007/BF00503517
M3 - Article
AN - SCOPUS:0007033192
SN - 0195-928X
VL - 12
SP - 1029
EP - 1038
JO - International Journal of Thermophysics
JF - International Journal of Thermophysics
IS - 6
ER -