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Calculating the enthalpy of a mix gas like R407F. Gives an error.
Dim X As New SharpFluids.MediaType("HEOS", "R407F.mix")
Dim R407F As New SharpFluids.Fluid(X)
Exception
System.ApplicationExc…
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Some old notes, running binary alloy model:
> parameters = {
> "temperature_rayleigh_number": 8.,
> "concentration_rayleigh_number": -9.,
> "prandtl_number": 7.,
> "stefan_numbe…
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When using ABFLSHdll with inputs such as T and H, to get proper output values for D, for example, H must be entered in molar units. This contradicts what is written in issue 260: "Only the very top l…
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The current upper-bound limitation for the calculation of thermodynamic and transport properties is 100 atm (10 MPa). For the simulation of higher total pressure rocket nozzles, coefficients for enth…
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### Description
I'm unable to use mixtures (.mix file or using the & symbol) using the C# SWIG wrapper in a windows forms solution. For years my company has used R134A and provided a pressure entha…
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[mixing steam and humid air.xlsx](https://github.com/ibell/coolprop/files/903609/mixing.steam.and.humid.air.xlsx)
It seems that the temperature of the mixture calculated from the enthalpy returns 0 K…
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Description
I'm trying to compute the enthalpy of MM at P=19.273 bar and s=638.43 j/(kg K) using PropsSI. Every time that the function in Python:
import CoolProp.CoolProp as CP
CP.PropsSI("H","…
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I've been asked about the following:
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Do you know if there is a simple way to build variables i…
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Mixture Properties: Which mixture properties do we intend to use in fitting for Sage? For Parsley, we used **enthalpy of mixing and excess molar volume** for benchmarking; should we use these for trai…
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Steam model is built on ` Modelica.Media.StandardWater`. Few tasks need to be done before making a pull request.
- [ ] pass temperature and enthalpy inversion test.