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#1
Posted 17 October 2012 - 09:06 PM
I am new to this forum but have visited it many times. I would like to know if any one of you have successfully simulated a selexol stripper in Aspen hysys. The problem I have faced is that the converged solution that I get is not correct.
Selexol is proprietary physical solvent used for acid gas treating and is modeled as DEPG. But it seems that the DBR amine package that is used for the thermo package does not properly define the thermal properties of DEPG.
If any one of you can provide me any clues, please let me know
Thanks,
Atul
#2
Posted 08 November 2012 - 01:42 AM
#3
Posted 08 November 2012 - 10:57 AM
Selexol has been in use for many years now,
see this paper
www.winsim.com/news/feb1982.pdf
#4
Posted 13 November 2012 - 12:59 AM
That ChemShare paper indicates that access to their Selexol model (in 1982) required the approval of the intellectual property owner, Allied Chemical (now part of Dow Chemical).
Edited by Technical Bard, 13 November 2012 - 01:00 AM.
#5
Posted 12 December 2012 - 02:16 AM
For physical solvents, use rate bases simulation models. I will recommend Pro-Treat. You can use Aspen Plus with rate based.
#6
Posted 11 January 2013 - 03:35 PM
Attached is a standard model of a Selexol unit in .pdf format.
As you can see, it does a good job of removing sour gasses and is a viable option for gas treating.
Attached Files
Edited by RockDock, 11 January 2013 - 03:39 PM.
#7
Posted 24 May 2013 - 02:52 AM
hi dears
I am working on simulation of selexol and purisol processes with hysys.
the problem is that, I need industrial data for the accuracy of the results.
I would like to ask if anyone have the data of the industrial acid gas removal unit working with selexol or purisol process.
if no hysys file is available, others such as promax can be useful, too
thanks indeed
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