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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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Hello.
I am trying to plot a simplified (enthalpy vs pressure) thermodynamic cycle using refrigerant R245fa, for an ORC calculation.
The issue is that when I use CoolProp's PropertyPlot() as a bac…
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Hi,
I followed Python installation.
I have Linux, and Python 3.8.6.
I install CoolProp using `pip install coolprop`, and it does import in Python.
This is CoolProp version 6.4.1
But I f…
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When trying to determine parameters based on particular dry bulb temps and specific enthalpies, I'm getting an overflow error from Excel.
Example formula:
= HAPropsSI("W","Tdb",29.4+273.15,"H",62…
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Small comment for discussion @jbscoggi .
Many CFD codes use as a reference temperature T=0K instead of the 298.15K used by M++.
I recommend the creation of a function like:
shiftingConstantToZeroKe…
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Issue can be reproduced using `inputs_3d_C.128.avgbase.dr ` for uneven base state spacing, and `inputs_3d_C.128.avgbase.dx ` for even base state spacing. Both tests fail after approx. 20 time steps, n…
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Based on this paper: https://www.researchgate.net/publication/226804783_Heat_transfer_during_the_melting_of_ice_around_a_horizontal_isothermal_cylinder
The current enthalpy-porosity model should be…
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Using this as reference:
http://www.nt.ntnu.no/users/skoge/book-cep/diagrams/additional_diagrams/Propylene%20col.pdf (it says that this chart is based on Allprops)
H = 100e3 J/kg and P = 1e6 Pa shou…
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**Reported by fcasella on 23 Jan 2009 00:23 UTC**
A few general considerations about the energy balance equations in Modelica_Fluid
The energy balance equation for 1D systems includes a term
d/dx(m_…
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I need to know how I can find the output such as enthalpy by reading excel file of steam table by inputting temperature/pressure in the input field, means when we input temperature/pressure it should …