R1233zd(E)
R1233zd(E) provides thermodynamic property information for refrigerant R1233zd(E) (C3ClH2F3, 1-chloro-3,3,3-trifluoropropene). The thermodynamic properties are determined from the equation of state in:
Mondejar, M.E., McLinden, M.O., Lemmon, E.W.
"Thermodynamic Properties of Trans-1-chloro-3,3,3-trifluoropropene (R1233zd(E)):
Vapor Pressure, p-rho-T Data, Speed of Sound Measurements and Equation of State,"
J. Chem. Eng. Data 2015, 60, 2477?2489
The correlation is valid for temperatures in the range between 195.15 K to 550 K for pressures less than 100 MPa.
Enthalpy and entropy values are referenced to 200 kJ/kg and 1 kJ/kg-K, respectively, for saturated liquid at 0 C. (IIR reference)
Liquid viscosity is determined using the correlation provided by:
Junwei Cui, Shaomin Yan, Shengshan Bi, and Jiangtao Wu
"Saturated Liquid Dynamic Viscosity and Surface Tension of trans-1-Chloro-3,3,3-trifluoropropene and Dodecafluoro-2-methylpentan-3-one
J. Chem. Eng. Data 2018, 63, 751-756
Gas viscosity has been estimated using a corresponding states approach (with R236a as the reference fluid) as suggested in:
Klein, S.A., McLinden, M.O., and Laesecke , A., "An improved extended corresponding states method for estimation of viscosity of pure refrigerants and mixtures", Int. J. of Refrigeration, 20, pp. 208-217, 1997
Thermal conductivity (liquid and gas) is determined using the correlation provided by:
Richard A. Perkins and Marcia L. Huber
"Measurement and Correlation of the Thermal Conductivity of trans-1-Chloro-3,3,3-trifluoropropene (R1233zd(E))"
J. Chem. Eng. Data 2017, 62, 2659-2665
Note that the critical enhancement contribution is not implemented.
Surface tension data are provided with a correlation from:
Chieko Kondou, et al.,
"Surface tension of low GWP refrigerants R1243zf, R1234ze(Z), and R1233zd(E)"
International Journal of Refrigeration, Vol. 53, (2015) pp. 80-89.