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Firstly, thank you for all your efforts with this project!
I was translating some of my old HYSIM/HYSYS training material into DWSim and ran into a problem with the dew point calculation (Spec P-Vf, calc T). I set the attached sim to demonstrate the issue.
DWSim Version 8.8.3
Describe the bug
The P-Vf flash doesn't calculate the right fluid temperature.
To Reproduce
PLEASE ATTACH THE ZIPPED FLOWSHEET FILE and/or inform the steps to reproduce the behavior:
Stream 12 is the vapor product stream exiting 2 phase separator V-2. It is in equilibrium with stream 13. Hence, stream 12 is a saturated vapor. It's at -10C and around 40 barg.
I copied the compositions from stream 12 to Stream 12-P-Vf-Flash and performed a P-Vf flash, i.e., P around 40 barg and Vf = 1. It should return a T of around -10C. Instead it returns a temperature of around -58 C. DPCU-03.zip
Dear DWSim team,
Firstly, thank you for all your efforts with this project!
I was translating some of my old HYSIM/HYSYS training material into DWSim and ran into a problem with the dew point calculation (Spec P-Vf, calc T). I set the attached sim to demonstrate the issue.
DWSim Version 8.8.3
Describe the bug
The P-Vf flash doesn't calculate the right fluid temperature.
To Reproduce
PLEASE ATTACH THE ZIPPED FLOWSHEET FILE and/or inform the steps to reproduce the behavior:
Stream 12 is the vapor product stream exiting 2 phase separator V-2. It is in equilibrium with stream 13. Hence, stream 12 is a saturated vapor. It's at -10C and around 40 barg.
I copied the compositions from stream 12 to Stream 12-P-Vf-Flash and performed a P-Vf flash, i.e., P around 40 barg and Vf = 1. It should return a T of around -10C. Instead it returns a temperature of around -58 C.
DPCU-03.zip
Thanks,
Rafil ([email protected])
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