Aspen Plus: Simulation of H2S and CO2 Removal from Syngas by Cryogenic Distillation

[@sandilemhlaba3828]

thanks for the video, its really helpful

[@faroukmerouani5902]

can you a rate based model distillation for acid gas capture?

[@cricketsixes2656]

Can you upload simulation of PM2.5 and PM10 removal by Fabric filter?

[@rodrigop9714]

Does it make sense to use Cryogenic Distillation when your initial syngas flow is 2000 kg/hr instead of the 450000 from the video?

[@kgengineeringsolutions]

Try it😀

[@marinaaina8342]

Thanks. Can you help me by simulating a biogas cleaning system in biomethane to inject it into the natural gas network ?

[@kgengineeringsolutions]

Yes email me [e-mail]

[@吳聿倫]

what is your size of the distillation column

[@kgengineeringsolutions]

The calculation type is equilibrium --> The simulation cannot calculate a column size.

[@sandilemhlaba3828]

Can you assist in cryogenic aspen plus DE sublimation of co2 capture

[@kgengineeringsolutions]

Please write me the requirements. I'd be happy to make you an offer.

[@sandilemhlaba3828]

@@kgengineeringsolutions is there a way to connect maybe on LinkedIn

[@elgatomax7434]

Hello. The results are not equal with the ones that were obtained in the paper. Do you know why?
I need to design a process to remove H2S from syngas and this alternative doesnt work for now :(

[@kgengineeringsolutions]

Hello, which results exactly?

[@elgatomax7434]

@kgengineeringsolutions The ammount of H2S in current H2S. If the process works properly it need to recover a maximum of H2S

[@kgengineeringsolutions]

@@elgatomax7434 The reason is I simulated higher temperature. I don't know why I got higher temperature...