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flash_pt = pff.equilibrium.flash_pt()
composition = {'propane': 0.01, 'butane': 0.5, 'isobutane': 0.15,
'pentane': 0.2, 'hexane': 0.14}
temperature = 366.48
pressure = 1.039e6
…
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I'm user REFPROP ver.10 and calculate the mixture properties with Excel add-in.
I have a problem with calculating "Temperature" from "Pressure and Enthalpy" in Mixture of para-hydrogen and methane.
…
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Hi, I encounter the same problem as in https://github.com/facebookresearch/LAMA/issues/10.
And I found the reason why 2 examples are filtered is that the `obj_label` are `1970s` and `1990s`. And in `…
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I am using Reprop 10.0.
I am trying to make a simple program in Intel Visual Fortran that would call Refprop. So far I only am using 1 command from Refprop: just trying to set the fluid via SETFLUI…
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I'm having some problems calling ABFLSHdll using Python, hope you can help
### Description
You can see that I have proportioned a mixture whose components are butane and ethylene respectively.…
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Hi,
I am working on implementing Gibbs Ensemble Monte Carlo (GEMC) simulations using OpenMM. GEMC simulations require handling two simulation boxes (contexts) simultaneously, each representing diff…
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Hi, I have tried to use this program to calculate the vapor-liquid equilibrium at a constant temperature, such as the following mixture, but I am not very good at using this program.
 This is how I loaded my REFP…
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Though probably not vice-versa without careful balance work.
This means Oxygen, Nitrogen, Plasma (this is somewhat important so maybe make it not condense by normal means), Water Vapor, Nitrous Oxi…
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Hello, I call Flash to separate the gas from the liquid stream. But after the Flash, all the gas in the feed stream is transferred to the gas phase stream, shouldn't some CO2 be dissolved in the water…