I see what you are saying Ray. My confusion comes from my limited(learning) knowledge about flamelet table generation. I have experience generating flamelet tables using FlameMaster. In that code I could specify an equation of state to use. I think it had Ideal, Peng-Robinson, and SRK. My original thought was that because FlameMaster was querying an EOS equation, I could insert a code in between the query and the EOS that directed the query information to a REFPROP tabulation of the species.
I want to make sure I understand your explanation for why REFPROP would fail in my plan.
At one state of a combustion process there may be N species that were generated from say 2 original species(fuel and oxidizer). The governing equations may need a mixture density at that state. A weighted sum of the densities of the individual species weighted by their mass fraction can be used to compute a mixture density. The Ideal Gas and Peng-Robinson equations of state would be able to at least estimate a value of the density for all of the species from the information about the atomic structure of the atoms that compose the species and the pressure and temperature of the species. Whereas REFPROP only has properties for common species, so it can not provide an estimate for the N intermediate species.
I appreciate your insight into my question Ray.
Thank you,
Chris