Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Aspen Plus: Nrtl-Model Parameter Butanol-Water Mixture

inf.dil. activity coefficient nrtl aspen properties

This topic has been archived. This means that you cannot reply to this topic.
1 reply to this topic
Share this topic:
| More

#1 Antonia

Antonia

    Brand New Member

  • Members
  • 2 posts

Posted 15 January 2013 - 08:41 AM

Hallo!

I'm trying to regress DECHEMA DATA in Aspen Plus for the NRTL-model.
Implemented Data sources give wrong activity coefficients at my conditions. VLE works well around 100°C, but my simulation is at low BuOH concentration and room temperature.

When I implement DATA from DECHEMA, ASPEN regresses good NRTL Parameters,( like NRTL/1,NRTL/2,...), but with this regression the VLE is wrong.

If I have a separation step at room temperature and a distillation downstream, is the only possibility for the simulation to have a different model at each unit? (VLE at distillation and regressed model at separation step)
Does anyone know how ASPEN calculates the NRTL model? How can I get a model, with these two combined?

I'm looking forward for your replies.
Thanks for your help.

Antonia

#2 Antonia

Antonia

    Brand New Member

  • Members
  • 2 posts

Posted 17 January 2013 - 08:48 AM

hallo!

I solved the problem on my own.
To make a model, which works at room temperature and VLE, I used both data sources (infinite activity coefficient Data and VLE Data) for one regression. The weight of the data sources is equal with 1. Comparison with different weights doesn't influence the results.
This model calculates gamma and VLE almost perfectly.

greetings
Antonia




Similar Topics