Acetone Absorber HenrysLaw
Moderator: jasper
Acetone Absorber HenrysLaw
I was attempting to take the Acetone Absorber Henrys Law example in Chemsep and put into a COCO flowsheet. After several warnings I get "failed to solve unit Column_1. Flash (PVF) failed on bottom product" Attached is the fsd. Any help would be appreciated.
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- AcetoneAbsorber.fsd
- (63.94 KiB) Downloaded 870 times
Re: Acetone Absorber HenrysLaw
Had to add activity coefficients to property package. If I go and zero out the undefined NTRL parameters I get the simulation to solve.
Re: Acetone Absorber HenrysLaw
Sorry for the delay in responding; I was travelling.
The property package uses Peng Robinson, not NTRL. Is this intended? Why are you using different thermo in the column than in the flowsheet?
The property package uses Peng Robinson, not NTRL. Is this intended? Why are you using different thermo in the column than in the flowsheet?
Re: Acetone Absorber HenrysLaw
I changed the COCO property package to NTRL. I then did a comparison of COCO and ChemSep. The only real major difference I came up with was the reported liquid discharge temperature of Column 2. COCO reports a temperature of 56.9216 °C. If you call up the ChemSep GUI the temperature of 33.4175 °C is reported.
This was basically an academic exercise to learn more about COCO and how to become more effective in its use.
This was basically an academic exercise to learn more about COCO and how to become more effective in its use.
- Attachments
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- Acetone Absorber COCO ChemSep comparison.fsd
- (244.5 KiB) Downloaded 855 times