Amine Sweetening Unit with MDEA || Aspen HYSYS

  Рет қаралды 19,602

Chemiopedia

Chemiopedia

Күн бұрын

Пікірлер: 57
@ldmsm252
@ldmsm252 3 жыл бұрын
Good effort, well done
@Chemiopedia
@Chemiopedia 3 жыл бұрын
Thank you. Don't forget to subscribe
@shabrazk5182
@shabrazk5182 3 жыл бұрын
Thank you, well explained
@Chemiopedia
@Chemiopedia 3 жыл бұрын
You are welcome!
@chemicalengineer96
@chemicalengineer96 4 жыл бұрын
Good effort! Keep it up..
@Chemiopedia
@Chemiopedia 4 жыл бұрын
Thank you, I will
@riograndino
@riograndino Жыл бұрын
hello. Do you have a simulation with piperazine activator (a-mdea)?
@Chemiopedia
@Chemiopedia Жыл бұрын
No, I am afraid not. I haven't prepared MDEA-PZ simulation yet.
@aparnaam3250
@aparnaam3250 3 жыл бұрын
can u plz explain on converging the stream after connecting the recycle stream
@Chemiopedia
@Chemiopedia 3 жыл бұрын
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.
@manishakarim3397
@manishakarim3397 2 жыл бұрын
Can i use this simulation with presence of H2S in the feed? I noticed your feed does not have H2S.
@Chemiopedia
@Chemiopedia 2 жыл бұрын
Yes, we can add H2S in feed as well. There will be no complications.
@uswatunkhasanah8817
@uswatunkhasanah8817 3 жыл бұрын
is this a simulation of the factory sir? may I know what is the name of the factory, sir?
@idrishammed9524
@idrishammed9524 2 жыл бұрын
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 жыл бұрын
HYSYS adds reaction automatically when Acid Gas property package is used. You can see all the reactions in the properties section > reaction set
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
also the flash drum is a three phase separator, for removing hydrocarbon
@Chemiopedia
@Chemiopedia 3 жыл бұрын
You can replace the two phase with three phase.
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
what is the meaning of shell in series ?
@Chemiopedia
@Chemiopedia 3 жыл бұрын
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.
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
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 3 жыл бұрын
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.
@filippopirontilubrano7738
@filippopirontilubrano7738 3 жыл бұрын
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 жыл бұрын
Which version of HYSYS do you have?
@filippopirontilubrano7738
@filippopirontilubrano7738 3 жыл бұрын
@@Chemiopedia It is an older version, that is why I do not have it. Thanks any way
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
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 3 жыл бұрын
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.
@rahmounikhouloud4799
@rahmounikhouloud4799 3 жыл бұрын
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 жыл бұрын
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 жыл бұрын
@@Chemiopedia thanks a lot
@shoaibarshad4606
@shoaibarshad4606 Жыл бұрын
thanks a lot for the video, how do you calculate absorber and stripper stages for amine simulations.
@LPdweller
@LPdweller 2 жыл бұрын
Thank you! Maybe a silly question but is this a rate-based model or an equilibrium-based model?
@Chemiopedia
@Chemiopedia 2 жыл бұрын
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!
@harveenagill3874
@harveenagill3874 3 жыл бұрын
Hi, can this simulation be used with DEA?
@Chemiopedia
@Chemiopedia 3 жыл бұрын
The process for DEA is same however you have to adjust the operating parameters.
@harveenagill3874
@harveenagill3874 3 жыл бұрын
@@Chemiopedia would you by chance have the operating parameters? 😅
@Chemiopedia
@Chemiopedia 3 жыл бұрын
Not sure. But you can find easily on google.
@talhakhayyam4486
@talhakhayyam4486 11 ай бұрын
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
@uswatunkhasanah8817
@uswatunkhasanah8817 3 жыл бұрын
sir, which factory is this from ?
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
what is the meaning, inlet stage 1_Main Tower ? in regenerator
@Chemiopedia
@Chemiopedia 3 жыл бұрын
In stripper, the feed enters at the top stage. 1_Main Tower means the feed is at the top most tray.
@hannahmichaelareyes6172
@hannahmichaelareyes6172 3 жыл бұрын
Hello, Sir. Can I have a copy of the simulation just to check how it’s done? :)
@Chemiopedia
@Chemiopedia 3 жыл бұрын
Please write to us: support@chemiopedia.com
@abdulwasi7411
@abdulwasi7411 2 жыл бұрын
how much the final CO2 mole% after sweetened? (in this simulation)
@hashirmoghal
@hashirmoghal 4 жыл бұрын
Well thats a good one.
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
can you explain the SET on booster pump to MDEA for temperature control
@Chemiopedia
@Chemiopedia 3 жыл бұрын
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 жыл бұрын
This is very helpful. Great taste on the bgm. What is the name of this music?
@hast66
@hast66 3 жыл бұрын
sounds like a gnossienne of Satie but?
@sayakneogi5403
@sayakneogi5403 Жыл бұрын
I am having a severe error regarding pressure but everything is same as the video
@inaraamatullah4449
@inaraamatullah4449 3 жыл бұрын
it was too fast , cant follow, and no explanation either :(
@Chemiopedia
@Chemiopedia 3 жыл бұрын
If you need any help. You can write us on support@chemiopedia.com
@filippopirontilubrano7738
@filippopirontilubrano7738 3 жыл бұрын
Thanks, well explained and uptodate
@Chemiopedia
@Chemiopedia 3 жыл бұрын
Glad it was helpful! Don't forget to subscribe.
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