hello. Do you have a simulation with piperazine activator (a-mdea)?
@Chemiopedia Жыл бұрын
No, I am afraid not. I haven't prepared MDEA-PZ simulation yet.
@aparnaam32503 жыл бұрын
can u plz explain on converging the stream after connecting the recycle stream
@Chemiopedia3 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.
@manishakarim33972 жыл бұрын
Can i use this simulation with presence of H2S in the feed? I noticed your feed does not have H2S.
@Chemiopedia2 жыл бұрын
Yes, we can add H2S in feed as well. There will be no complications.
@uswatunkhasanah88173 жыл бұрын
is this a simulation of the factory sir? may I know what is the name of the factory, sir?
@idrishammed95242 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 ?
@Chemiopedia2 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
@inaraamatullah44493 жыл бұрын
also the flash drum is a three phase separator, for removing hydrocarbon
@Chemiopedia3 жыл бұрын
You can replace the two phase with three phase.
@inaraamatullah44493 жыл бұрын
what is the meaning of shell in series ?
@Chemiopedia3 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.
@inaraamatullah44493 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
@Chemiopedia3 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.
@filippopirontilubrano77383 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?
@Chemiopedia3 жыл бұрын
Which version of HYSYS do you have?
@filippopirontilubrano77383 жыл бұрын
@@Chemiopedia It is an older version, that is why I do not have it. Thanks any way
@inaraamatullah44493 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 ?
@Chemiopedia3 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.
@rahmounikhouloud47993 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.
@Chemiopedia3 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.
@rahmounikhouloud47993 жыл бұрын
@@Chemiopedia thanks a lot
@shoaibarshad4606 Жыл бұрын
thanks a lot for the video, how do you calculate absorber and stripper stages for amine simulations.
@LPdweller2 жыл бұрын
Thank you! Maybe a silly question but is this a rate-based model or an equilibrium-based model?
@Chemiopedia2 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!
@harveenagill38743 жыл бұрын
Hi, can this simulation be used with DEA?
@Chemiopedia3 жыл бұрын
The process for DEA is same however you have to adjust the operating parameters.
@harveenagill38743 жыл бұрын
@@Chemiopedia would you by chance have the operating parameters? 😅
@Chemiopedia3 жыл бұрын
Not sure. But you can find easily on google.
@talhakhayyam448611 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
@uswatunkhasanah88173 жыл бұрын
sir, which factory is this from ?
@inaraamatullah44493 жыл бұрын
what is the meaning, inlet stage 1_Main Tower ? in regenerator
@Chemiopedia3 жыл бұрын
In stripper, the feed enters at the top stage. 1_Main Tower means the feed is at the top most tray.
@hannahmichaelareyes61723 жыл бұрын
Hello, Sir. Can I have a copy of the simulation just to check how it’s done? :)
@Chemiopedia3 жыл бұрын
Please write to us: support@chemiopedia.com
@abdulwasi74112 жыл бұрын
how much the final CO2 mole% after sweetened? (in this simulation)
@hashirmoghal4 жыл бұрын
Well thats a good one.
@inaraamatullah44493 жыл бұрын
can you explain the SET on booster pump to MDEA for temperature control
@Chemiopedia3 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.
@wenwen90413 жыл бұрын
This is very helpful. Great taste on the bgm. What is the name of this music?
@hast663 жыл бұрын
sounds like a gnossienne of Satie but?
@sayakneogi5403 Жыл бұрын
I am having a severe error regarding pressure but everything is same as the video
@inaraamatullah44493 жыл бұрын
it was too fast , cant follow, and no explanation either :(
@Chemiopedia3 жыл бұрын
If you need any help. You can write us on support@chemiopedia.com