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Natural Gas Sweetening Process with DEA || Aspen HYSYS 

Chemiopedia
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This video is about the simulation of the Natural Gas Sweetening Process with diethanolamine (DEA) in Aspen DEA. The major units of the process are:
1. Absorber
2. Distillation Column (Stripper)
3. Shell and tube heat exchanger
4. Set
@ 00:12 Component list and property package
@ 00:54 Natural gas feed stream
@ 02:12 Amine stream and absorber setup
@ 06:39 Amine regenrator column
@ 08:36 Lean amine recyle
To read about the amine sweetening process please visit. www.chemiopedia.com/post/amin...
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Опубликовано:

 

17 ноя 2021

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Комментарии : 22   
@GeniusEnima
@GeniusEnima 2 года назад
Great Tutorial, Thanks again for your work sir ! Keep it Up as always.
@Chemiopedia
@Chemiopedia 2 года назад
Thanks again!
@omarmahmoud1989
@omarmahmoud1989 2 года назад
Thanks for these valuable information
@Chemiopedia
@Chemiopedia 2 года назад
Thank you
@mohammadghaziasgar3160
@mohammadghaziasgar3160 8 месяцев назад
Hello Thanks for your tutorial. I do the same as you show, but my absorber does not converge , it gives the error named : ' Fatal Error : Zero Diagonal in Column Matrix" , do you have any suggestions ? Thanks
@shoaibarshad4606
@shoaibarshad4606 Год назад
How do you calculate absorber and stripper stages?
@abdulhameedidakwoji1807
@abdulhameedidakwoji1807 2 года назад
Hi, pls are you familiar with DWSIM process software? Serves similar purpose as Aspen. However, I am running into challenges with the Absorption column pressure. There’s only room for a single operating pressure as opposed to Aspen where we have the top and bottom pressure. Pls any help?
@Chemiopedia
@Chemiopedia 2 года назад
Sorry I am not familiar with DWSIM
@user-lb7xu2ph2g
@user-lb7xu2ph2g Год назад
The tutorial is straight forward and nice. But i am having issue with my overhead product at the stripping section. Methane and water compositions are higher than CO2. What can i do to resolve the issue please?
@Chemiopedia
@Chemiopedia Год назад
In that case, you should adjust tray efficiencies to get your desired compositions.
@uswatunkhasanah8817
@uswatunkhasanah8817 2 года назад
can you make a video explaining the process, I got an assignment from my lecturer. please 🙏
@Chemiopedia
@Chemiopedia 2 года назад
see if this can help: chemiopedia.com/amine-sweetening-process/
@uswatunkhasanah8817
@uswatunkhasanah8817 2 года назад
@@Chemiopedia thank you very much sir🙏
@laxmareddy8309
@laxmareddy8309 2 года назад
I have done this simulation as a part of my project, can you please tell me from where is the simulation data collected from.
@Chemiopedia
@Chemiopedia 2 года назад
Hi, Glad it helped. The data for this simulation is not collected specifically from any source. This simulation is based on the professional experience. Don't forget to subscribe.
@laxmareddy8309
@laxmareddy8309 2 года назад
@@Chemiopedia thank you very much
@laxmareddy8309
@laxmareddy8309 2 года назад
What is the purpose of the saturator before absorbtion?
@Chemiopedia
@Chemiopedia 2 года назад
Natural gas streams are saturated with water while the composition I used was on a dry basis. To incorporate the water content, a saturator is used.
@laxmareddy8309
@laxmareddy8309 2 года назад
@@Chemiopedia thankyou very much
@nasirkhan3711
@nasirkhan3711 2 года назад
I don't know why but the DC didn't nucleate. Followed your procedure but it is taking unnecsessary long to solve.
@Chemiopedia
@Chemiopedia 2 года назад
Try to add some guess value in the profile section.
@Chemiopedia
@Chemiopedia 2 года назад
Try to add some guess value in the profile section.
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