Abstract :
Solubility data of refrigerant lubricant mixtures have been modeled with cubic
equations of state (EOS): van der Waals (vdW), Soave-modified Redlich
Kwong (SRK), or Peng Robinson (PR) types. The temperature dependence on
the ``aʹʹ parameter in the EOS is modeled with a common empirical function for
pure refrigerants, including oils. For lubricants, a hypothetical oil (UniOIL) has
been developed with universal oil EOS constants, and it is valid for any kind of
lubricant oil. Only an average molecular weight is required for any type of oil.
The mixing rules for the a and b parameters of EOS are more general than the
ordinary van der Waals Berthelot formula, and a justification of such mixing
rules is discussed. The refrigerants studied are R-32, R-125, R-134a R-143a,
R-152a, R-12, R-22, R-123 and R-13B1. The lubricants are naphthenic mineral
(MO), alkylbenzene (AB HAB), and polyol ester (POE) oils, as well as model
compounds with pure component oils (hydrocarbons and POE). They are all
analyzed with the UniOIL model. Good quality experimental solubility (PTx)
data were selected from the literature and well correlated within their experi-
mental uncertainties. All the cubic EOS (vdW, SRK, and PR) having the same
type of mixing forms for the a and b parameters showed excellent fits to the
experimental PTx data with essentially the same degree of accuracy. The results
in this report are shown with the SRK type EOS.
Keywords :
Lubricants , Oils , Mixing rule , Solubility. , cubic equations of state , Refrigerants , phaseequilibria