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Amine Sweetening Unit with MDEA || Aspen HYSYS 

Chemiopedia
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This tutorial is about the simulation of the Amine Sweetening Unit with the MDEA solvent. The units involves are absorber, strippers, pressure vessels, heat exchanger, and pumps.
To read about the amine sweetening process please visit. www.chemiopedi...
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5 сен 2024

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Комментарии : 57   
@inaraamatullah4449
@inaraamatullah4449 2 года назад
also the flash drum is a three phase separator, for removing hydrocarbon
@Chemiopedia
@Chemiopedia 2 года назад
You can replace the two phase with three phase.
@inaraamatullah4449
@inaraamatullah4449 2 года назад
actually the flash drum is integrated to a scrubber column at the top section of the drum having a lean amine inlet for scrubbing H2S coming out in the flashed gas, so how can use that in the simulation
@Chemiopedia
@Chemiopedia 2 года назад
There is no such equipment like this im HYSYS. However, you can add flash vessel and column individually and the vapours of the flash vessel may enter in the column bottom to strip out the H2S.
@talhakhayyam4486
@talhakhayyam4486 6 месяцев назад
i followed all the steps exactly like you did but the distillation column for me is taking very long time to run and at the end it is unconverged. I tried this 3,4 times but still same issue
@ldmsm252
@ldmsm252 3 года назад
Good effort, well done
@Chemiopedia
@Chemiopedia 3 года назад
Thank you. Don't forget to subscribe
@manishakarim3397
@manishakarim3397 Год назад
Can i use this simulation with presence of H2S in the feed? I noticed your feed does not have H2S.
@Chemiopedia
@Chemiopedia Год назад
Yes, we can add H2S in feed as well. There will be no complications.
@inaraamatullah4449
@inaraamatullah4449 2 года назад
in my case the absorber column has a top packing section on top, below that there are 14 trays and below that there are again 2 more packed sections. In that case how do i correctly define the number of stages ?
@Chemiopedia
@Chemiopedia 2 года назад
Packing also has theoretical number of stages. You have to input these stages. Moreover, you can define the geometry in column internals in more detailed manner.
@filippopirontilubrano7738
@filippopirontilubrano7738 3 года назад
Thanks, well explained and uptodate
@Chemiopedia
@Chemiopedia 3 года назад
Glad it was helpful! Don't forget to subscribe.
@riograndino
@riograndino 11 месяцев назад
hello. Do you have a simulation with piperazine activator (a-mdea)?
@Chemiopedia
@Chemiopedia 11 месяцев назад
No, I am afraid not. I haven't prepared MDEA-PZ simulation yet.
@aparnaam3250
@aparnaam3250 3 года назад
can u plz explain on converging the stream after connecting the recycle stream
@Chemiopedia
@Chemiopedia 3 года назад
Are you facing any issue? If the error message appears due to recycle, it shows the variable that causing the issue. Try following steps: 1. Remove the recycle block 2. Make sure your simulation is in active mode. 3. Analyze the both stream that has to be recycle. 4. Ensure no major difference in parameters between the streams 5. If the difference is large then the recycle will not converge, so try to reduce the difference by manipulating the parameters. If the issue persist write us: support@chemiopedia.com. Don't forget to subscribe.
@uswatunkhasanah8817
@uswatunkhasanah8817 2 года назад
is this a simulation of the factory sir? may I know what is the name of the factory, sir?
@idrishammed9524
@idrishammed9524 2 года назад
which reaction set did yo add, I am curious most of the reaction are ionic reactions, can we add ionic reactions in aspen hysys, how ?
@Chemiopedia
@Chemiopedia 2 года назад
HYSYS adds reaction automatically when Acid Gas property package is used. You can see all the reactions in the properties section > reaction set
@filippopirontilubrano7738
@filippopirontilubrano7738 3 года назад
I have a question. You used from the palette a Make-up module, which I do not have. Is that module unique in your simulation?
@Chemiopedia
@Chemiopedia 3 года назад
Which version of HYSYS do you have?
@filippopirontilubrano7738
@filippopirontilubrano7738 3 года назад
@@Chemiopedia It is an older version, that is why I do not have it. Thanks any way
@sayakneogi5403
@sayakneogi5403 9 месяцев назад
I am having a severe error regarding pressure but everything is same as the video
@inaraamatullah4449
@inaraamatullah4449 2 года назад
what is the meaning of shell in series ?
@Chemiopedia
@Chemiopedia 2 года назад
Shell in series means two exchangers are installed in series. The shell out of 1st will enter the shell of second. same for tube side fluid.
@chemicalengineer96
@chemicalengineer96 4 года назад
Good effort! Keep it up..
@Chemiopedia
@Chemiopedia 4 года назад
Thank you, I will
@shoaibarshad4606
@shoaibarshad4606 Год назад
thanks a lot for the video, how do you calculate absorber and stripper stages for amine simulations.
@LPdweller
@LPdweller 2 года назад
Thank you! Maybe a silly question but is this a rate-based model or an equilibrium-based model?
@Chemiopedia
@Chemiopedia 2 года назад
Both. HYSYS adds reaction automatically when Acid Gas property package is used. You can see all the reactions in the properties section > reaction set. Don't forget to subscribe!
@inaraamatullah4449
@inaraamatullah4449 2 года назад
what is the meaning, inlet stage 1_Main Tower ? in regenerator
@Chemiopedia
@Chemiopedia 2 года назад
In stripper, the feed enters at the top stage. 1_Main Tower means the feed is at the top most tray.
@rahmounikhouloud4799
@rahmounikhouloud4799 3 года назад
THANK YOU, JUST A QUESTION IF I NEED TO USE MIXED AMINE TO OBTAIN THE BEST PERFORMANCE WHAT CAN I DO? MANY THANKS IN ADVANCE FOR ALL YOUR HELP.
@Chemiopedia
@Chemiopedia 3 года назад
You can add different amines in your component list. After doing this, you will have the option add the concentration of both amines in the make up block. You can run the case study to evaluate the model performance by varying the additives composition in the amine solution. Don't forget to subscribe to Chemiopedia.
@rahmounikhouloud4799
@rahmounikhouloud4799 3 года назад
@@Chemiopedia thanks a lot
@abdulwasi7411
@abdulwasi7411 Год назад
how much the final CO2 mole% after sweetened? (in this simulation)
@hannahmichaelareyes6172
@hannahmichaelareyes6172 2 года назад
Hello, Sir. Can I have a copy of the simulation just to check how it’s done? :)
@Chemiopedia
@Chemiopedia 2 года назад
Please write to us: support@chemiopedia.com
@inaraamatullah4449
@inaraamatullah4449 2 года назад
can you explain the SET on booster pump to MDEA for temperature control
@Chemiopedia
@Chemiopedia 2 года назад
SET ensures that the temperature of the stream is equal to the Lean MDEA stream entering the tower. The difference in the stream can cause convergence failure when you will install the recycle.
@wenwen9041
@wenwen9041 3 года назад
This is very helpful. Great taste on the bgm. What is the name of this music?
@hast66
@hast66 3 года назад
sounds like a gnossienne of Satie but?
@hashirmoghal
@hashirmoghal 4 года назад
Well thats a good one.
@harveenagill3874
@harveenagill3874 3 года назад
Hi, can this simulation be used with DEA?
@Chemiopedia
@Chemiopedia 3 года назад
The process for DEA is same however you have to adjust the operating parameters.
@harveenagill3874
@harveenagill3874 3 года назад
@@Chemiopedia would you by chance have the operating parameters? 😅
@Chemiopedia
@Chemiopedia 3 года назад
Not sure. But you can find easily on google.
@uswatunkhasanah8817
@uswatunkhasanah8817 2 года назад
sir, which factory is this from ?
@inaraamatullah4449
@inaraamatullah4449 2 года назад
it was too fast , cant follow, and no explanation either :(
@Chemiopedia
@Chemiopedia 2 года назад
If you need any help. You can write us on support@chemiopedia.com
@shabrazk5182
@shabrazk5182 3 года назад
Thank you, well explained
@Chemiopedia
@Chemiopedia 3 года назад
You are welcome!
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