TY - JOUR
T1 - Measurements of bubble point pressure and saturated liquid density for ((R1234yf + R290))
AU - Zhong, Quan
AU - Li, Huiya
AU - Dong, Xueqiang
AU - Zhang, Haiyang
AU - Zhao, Yanxing
AU - Guo, Hao
AU - Shen, Jun
AU - Gong, Maoqiong
N1 - Publisher Copyright:
© 2017 Elsevier Ltd
PY - 2018/3
Y1 - 2018/3
N2 - In this paper, bubble point pressures and saturated liquid densities of {2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) + propane (R290)} binary mixtures were measured using a compact single-sinker densimeter. Measurements were carried out over temperatures from (255.048 to 300.135) K and mole fractions of R1234yf at (0.113, 0.217, 0.322, 0.422, 0.533, 0.625). The experimental standard uncertainties were estimated to be less than 5 mK for the temperature, 2 kPa for the pressure, 0.003 for the mole fraction and 0.02% for the density. The experimental bubble point pressures were correlated by the Peng-Robinson equation of state, while the experimental saturated liquid densities were represented with the VDNS and our modified Rackett equations. In addition, saturated liquid densities of azeotropy point at temperatures T = (253.150, 263.150, 273.150, 283.150 and 293.150) K were determined based on our previous and present work.
AB - In this paper, bubble point pressures and saturated liquid densities of {2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) + propane (R290)} binary mixtures were measured using a compact single-sinker densimeter. Measurements were carried out over temperatures from (255.048 to 300.135) K and mole fractions of R1234yf at (0.113, 0.217, 0.322, 0.422, 0.533, 0.625). The experimental standard uncertainties were estimated to be less than 5 mK for the temperature, 2 kPa for the pressure, 0.003 for the mole fraction and 0.02% for the density. The experimental bubble point pressures were correlated by the Peng-Robinson equation of state, while the experimental saturated liquid densities were represented with the VDNS and our modified Rackett equations. In addition, saturated liquid densities of azeotropy point at temperatures T = (253.150, 263.150, 273.150, 283.150 and 293.150) K were determined based on our previous and present work.
KW - (R1234yf + R290)
KW - Bubble point pressure
KW - Equation of state
KW - Saturated liquid density
KW - Single-sinker densimeter
UR - http://www.scopus.com/inward/record.url?scp=85033361452&partnerID=8YFLogxK
U2 - 10.1016/j.jct.2017.10.016
DO - 10.1016/j.jct.2017.10.016
M3 - Article
AN - SCOPUS:85033361452
SN - 0021-9614
VL - 118
SP - 77
EP - 81
JO - Journal of Chemical Thermodynamics
JF - Journal of Chemical Thermodynamics
ER -