TY - JOUR
T1 - Investigation of pρTx properties for R1234ze(E) + R134a mixtures in the gas phase
AU - Zhang, Haiyang
AU - Dong, Xueqiang
AU - Zhong, Quan
AU - Li, Huiya
AU - Gong, Maoqiong
AU - Shen, Jun
AU - Wu, Jianfeng
N1 - Publisher Copyright:
© 2016 Elsevier Ltd and IIR
PY - 2017/1/1
Y1 - 2017/1/1
N2 - In this work, 101 gaseous pressure–density–temperature–mole fraction (pρTx) measurements for trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + 1,1,1,2-tetrafluoroethane (R134a) binary mixtures were measured along with seven isotherms from 270.351 to 300.276 K by using a compact single-sinker densimeter. The mixtures consisted of four mole fractions of R1234ze(E) from 0.4338 to 0.6356, corresponding to mass fractions of R1234ze(E) from 0.4613 to 0.6610. The experimental standard uncertainties in temperature, pressure, mole fraction, and density were estimated to be less than 5 mK, 200 Pa, 0.0003, and 0.05%, respectively. The Peng–Robinson (PR) equation of state with vdW one-fluid mixing rules and a truncated virial equation of state were employed to correlate the experimental data. The correlated results from different models are consistent with each other, and the virial model gives the best description of the experimental pρTx data with average absolute relative pressure and density deviations of 0.088% and 0.093%, respectively.
AB - In this work, 101 gaseous pressure–density–temperature–mole fraction (pρTx) measurements for trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + 1,1,1,2-tetrafluoroethane (R134a) binary mixtures were measured along with seven isotherms from 270.351 to 300.276 K by using a compact single-sinker densimeter. The mixtures consisted of four mole fractions of R1234ze(E) from 0.4338 to 0.6356, corresponding to mass fractions of R1234ze(E) from 0.4613 to 0.6610. The experimental standard uncertainties in temperature, pressure, mole fraction, and density were estimated to be less than 5 mK, 200 Pa, 0.0003, and 0.05%, respectively. The Peng–Robinson (PR) equation of state with vdW one-fluid mixing rules and a truncated virial equation of state were employed to correlate the experimental data. The correlated results from different models are consistent with each other, and the virial model gives the best description of the experimental pρTx data with average absolute relative pressure and density deviations of 0.088% and 0.093%, respectively.
KW - Equation of state
KW - R1234ze(E)
KW - R134a
KW - Single-sinker densimeter
KW - pρTx
UR - https://www.scopus.com/pages/publications/84992411993
U2 - 10.1016/j.ijrefrig.2016.08.016
DO - 10.1016/j.ijrefrig.2016.08.016
M3 - Article
AN - SCOPUS:84992411993
SN - 0140-7007
VL - 73
SP - 144
EP - 153
JO - International Journal of Refrigeration
JF - International Journal of Refrigeration
ER -