TY - JOUR
T1 - A corresponding state equation for compressed liquid isochoric heat capacity of pure and mixture refrigerants
AU - Sheng, Bowen
AU - Zhao, Yanxing
AU - Dong, Xueqiang
AU - Yan, Han
AU - Zhong, Quan
AU - Wang, Jingzhou
AU - Shen, Jun
AU - Gong, Maoqiong
N1 - Publisher Copyright:
© 2020
PY - 2021/4
Y1 - 2021/4
N2 - This work proposed a simple corresponding state equation depending on reduced temperature to predict compressed liquid isochoric heat capacity (cv) for HCs, HCFCs, HFCs and HFOs pure and mixtures at 0.3 < Tr < 1 and 0.5 < pr < 10. The generalized constant coefficients A and B were determined by regression of 1738 experimental cv data for 16 refrigerants including HCs, HFCs, HCFCs and HFOs in compressed liquid states (ρ > 2ρc). With known critical parameters, acentric factor and ideal gas isochoric heat capacity, the developed equation can represent the compressed liquid cv well with the average absolute relative deviation (AARD) of 1.82%. Compared with the generalized equation of Zhong et al. (2019a) and the special multiproperty equations in REFPROP 10.0 software, the proposed equation is slightly poor in accuracy, but simpler in form and requires fewer parameters. In addition, liquid cv data of 13 pure and 9 mixtures were used to verify the prediction performance of the developed equation and the applicability to the mixtures. The equation in this work is in good agreement with the experiment cv data of 9 pure and 9 mixtures including HCs, HFCs, HCFCs and HFOs, but the large deviation for 4 substances (N2, CO2, H2O and CH3OH).
AB - This work proposed a simple corresponding state equation depending on reduced temperature to predict compressed liquid isochoric heat capacity (cv) for HCs, HCFCs, HFCs and HFOs pure and mixtures at 0.3 < Tr < 1 and 0.5 < pr < 10. The generalized constant coefficients A and B were determined by regression of 1738 experimental cv data for 16 refrigerants including HCs, HFCs, HCFCs and HFOs in compressed liquid states (ρ > 2ρc). With known critical parameters, acentric factor and ideal gas isochoric heat capacity, the developed equation can represent the compressed liquid cv well with the average absolute relative deviation (AARD) of 1.82%. Compared with the generalized equation of Zhong et al. (2019a) and the special multiproperty equations in REFPROP 10.0 software, the proposed equation is slightly poor in accuracy, but simpler in form and requires fewer parameters. In addition, liquid cv data of 13 pure and 9 mixtures were used to verify the prediction performance of the developed equation and the applicability to the mixtures. The equation in this work is in good agreement with the experiment cv data of 9 pure and 9 mixtures including HCs, HFCs, HCFCs and HFOs, but the large deviation for 4 substances (N2, CO2, H2O and CH3OH).
KW - Compressed liquid
KW - Corresponding state equation
KW - Isochoric heat capacity
KW - Refrigerants
UR - http://www.scopus.com/inward/record.url?scp=85100067831&partnerID=8YFLogxK
U2 - 10.1016/j.ijrefrig.2020.12.016
DO - 10.1016/j.ijrefrig.2020.12.016
M3 - Article
AN - SCOPUS:85100067831
SN - 0140-7007
VL - 124
SP - 20
EP - 29
JO - International Journal of Refrigeration
JF - International Journal of Refrigeration
ER -