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**#Description**
Using refprop, we have been trying to generate thermodynamic tables for a mixture of hydrogen (54.19%), nitrogen (26.32%) and water (19.49%) for the following pressure and temperat…
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I ran the file on the OPLSAA force field for n-hexadecane.However, there are a few questions that I am not quite sure about. Firstly, regarding the creation speed, the annotation is 300K, but the actu…
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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?
![image](…
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I recently found that the propsSI return **inf** when the density of nitrogen was over a certain value, and this issue usually emerged when the internal energy was negative. The result could be obtain…
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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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I have ```relative_humidity = vapor_pressure / saturated_vapor_pressure```.
According to [the IDAES docs page](https://idaes-pse.readthedocs.io/en/latest/explanations/conventions.html#thermophysic…
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**Abstract**
`PureFluid` objects are an outlier within Cantera, as they combine liquid and vapor phases into a single substance that at the same time acts as a thermo *phase* (which is a misnomer i…
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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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From meeting 1. Dec 2023 on ASC vocabulary:
Include "rate constant" etc as a sub-category of "Product type" -> "Fundamental parameter" -> "rate constant" +++.
@brissebrat Can you include a list…
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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…