Modeling and Experimental Validation of the Thermophysical Properties of a POE+R1233zd(E) Mixture
Authors/Creators
- 1. University of Liege, Thermodynamics Laboratory, Liege, Belgium
- 2. Technische Universitat Dresden, Schaufler Chair of Refrigeration, Cryogenics and Compressor Technology, Dresden, Germany
Description
Reliable data of the properties of lubricant + refrigerant mixtures are essential in many applications to assess the
behavior of refrigeration and heat pump systems. The accurate modeling of all required thermophysical properties
(including density, viscosity, thermal conductivity, enthalpy, entropy, and phase equilibria) remains a key challenge
today.
In this work, thermophysical property measurements of a "pure" POE lubricant and its mixture with the refrigerant
R1233zd(E) were carried out in the temperature range from 283.15 to 373.15 K with pressures up to 1.2 MPa, using
experimental facitilies from the Technische Universitat Dresden. Based on the modelling approach developed by Yang
et al. (Ind. Eng. Chem. Res. 2023, 44, 18736-18749), the thermophysical properties of the "pure" POE and its mixture
with R1233zd(E) are modeled in much larger temperature and pressure ranges. This model is a semi-empirical approach
making use of a small amount of experimental data ( density, viscosity, thermal conductivity and heat capacity) of the
pure lubricant to obtain the lubricant's fluid constants ( e.g., critical temperature). Subsequently, some experimental
bubble point pressure data of the mixture were used to fit the binary interaction parameters in mixing rules, which
enable mixture predictions. The predictions of this model are compared with those of the classical empirical models
employed for lubricant + refrigerant mixtures, specifically the Henderson equations for density and viscosity, and
the Cavestri equation for the vapor pressure. The results show a better agreement with the experimental data for the
empirical modeling approach for both the density and viscosity, while the vapor pressure data prediction accuracies
are even for both approaches. In particular, the viscosity prediction of the thermodynamic approach are not good for
the mixture, with a root mean square relative error of 40%. Finally, the two modelling approaches are compared on
other modeling aspects than accuracy, for instance, the number of experimental data required, the ability to predict
other properties and the physical sense of the calibrated parameters, making the approach developed by Yang et al. a
convenient option in many applications.
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Modeling and Experimental Validation of the Thermophysical Properties of a POE+R1233zd(E) Mixture.pdf
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