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Hi @allanleal!
I'm opening this issue because we have been facing some difficulties combining the E-UNIQUAC model with Fugacity models for gas phases even for simple systems and for "mild" temperat…
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Saturation calls with PQ inputs might not be handled correctly in the [REFPROP mixture backend line 1623 and below](https://github.com/CoolProp/CoolProp/blob/master/src/Backends/REFPROP/REFPROPMixture…
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Summary of what @jrelliottoh said:
> Eq 3 and 4 of the att pdf seem to be missing the lnZ terms. Did you have some discussion that I didn’t know about? How did these terms go missing?
` yield different results compared to the regular pressure method `substance.p()` when the qu…
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### Description
In the REFPROP backends (REPROPMixtureBackend and REFPROPBackend), some member functions, particularly referring saturated properties, aren't implemented yet. However, they are nece…
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The chemical potential of SPC/E water at 300 K can be found in [this post on the Cassandra forum](https://cassandra.nd.edu/index.php/forum/cassandra-software/310-chemical-potential-for-spc-e-water-at-…
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Hello, if I customize a substance, and the reference phase of the substance is liquid and solid state, respectively, could I consult you what phase does the added vapor pressure equation (the followin…