Search found 51 matches

by hkooijman
02 January 2024, 17:28
Forum: COCO (AmsterCHEM)
Topic: solver problem when using Chemsep property package
Replies: 5
Views: 60068

Re: solver problem when using Chemsep property package

Ghadi, I suspect the PSRK fitted group interaction parameters (GIPs) does not extrapolate to temperatures above 300 degrees C. Your incoming stream is 1400 C! I checked and the PSRK model flash worked up to 500 C but then its limits are reached, most likely because one of the GIPs approaches to valu...
by hkooijman
28 April 2021, 17:22
Forum: Process Modelling Components
Topic: Air Separation Unit from COCO Sample Flowsheets
Replies: 2
Views: 30192

Re: Air Separation Unit from COCO Sample Flowsheets

I computed the first ratio incorrectly and as a result the product slate changed. I corrected the calculation and saw the flow ratio's needed to be 7.85 and 0.17. I then noticed that the rich liquid feed to the low pressure column was changing its quality (i.e. the ratio of L/V). This is because I h...
by hkooijman
28 April 2021, 11:48
Forum: Process Modelling Components
Topic: Air Separation Unit from COCO Sample Flowsheets
Replies: 2
Views: 30192

Re: Air Separation Unit from COCO Sample Flowsheets

Yes it is possible but you need to carefully adjust two specifications for the low pressure column that is flow rate specific, namely the side stream rates out of the low pressure column to (1) the waste and (2) the argon side rectification column. I suggest you to first replace them by relative flo...
by hkooijman
21 February 2021, 17:33
Forum: ChemSep Property Package
Topic: Error with Chemsep Property Package and Heater/Cooler unit
Replies: 5
Views: 15015

Re: Error with Chemsep Property Package and Heater/Cooler un

This is fixed with release 8v25 of ChemSep of 17th Feb 2021
-Harry
by hkooijman
06 October 2020, 14:08
Forum: TEA Thermodynamic server (AmsterCHEM)
Topic: combining two property packages within one
Replies: 13
Views: 30600

Re: combining two property packages within one

an interesting idea. I guess this should be fixed at the PME level? I mean CS/copp makes a whole set of properties available like the K values, enthalpies and entropies, as well as physical properties but it is the PME that should offer the choice to not all use a cocktail of propeties i.e. K values...
by hkooijman
06 October 2020, 14:03
Forum: ChemSep Property Package
Topic: property package for condensable polar gases
Replies: 5
Views: 15351

Re: property package for condensable polar gases

Why don't you share the collected validation data on the forum? Then there is more information to help you.

Harry
by hkooijman
16 September 2020, 20:35
Forum: ChemSep Property Package
Topic: editing Extended Antoine parameters within Chemsep
Replies: 3
Views: 12093

Re: editing Extended Antoine parameters within Chemsep

Please download and install a new ChemSep LITE. This weekend an update was made available that should help to fix the problem of not storing information.
-Harry
by hkooijman
10 October 2019, 22:06
Forum: COCO (AmsterCHEM)
Topic: Absorber
Replies: 8
Views: 18423

Re: Absorber

You should consider running parametric studies inside ChemSep. To do so, open up the column and go to the cape-open panel. First switch off Cape-Open properties. This will allow you to run parametric studies on the column. Then define your thermo again. Once you defined that, you can solve inside th...
by hkooijman
10 September 2019, 23:21
Forum: COCO (AmsterCHEM)
Topic: crude oil
Replies: 4
Views: 11499

Re: crude oil

Enter ChemSep gui. Please start the PCD manager by clicking on the Benzene ring icon. Now close the existing opened library with File-Close. Navigate to Edit-Add Pseudo. Select Kesler-Lee 1976 for the Tc and Pc, w and Mw. Use Riazi-Daubert 1980 for the Vc and CpIG. You can use Twu 1984 for viscosity...
by hkooijman
28 January 2019, 21:59
Forum: COCO (AmsterCHEM)
Topic: distillation bug
Replies: 19
Views: 81998

Re: distillation bug

There was a bug in the most recent version of ChemSep that caused the assignment of CAPE-OPEN parameters to fail. This is fixed. It is better to reconnect all information to ensure the parameters are passed on. I don't know whether your operation can work though, that is something you need to check ...

Go to advanced search