sir in case which the stages that we don't know, how you determine the stages of the absorber/stripper in HYSYS? since we know if the distilation we can use shortcut column but not with absorber/stripper
Most of the times, while adding comp fraction in monitor tab. My Wt. Error diiferes from yours although i followed the same steps as your and same values. Why this happen? Does it have concequences on the calculations?
It will depend on the specification. If any particular value is required from a particular stage, then this spec will be used. However, mostly the specifications presented in the video are used.
In refinery there is use only one stripper but in coke oven industry there is use double stripper coloumn sir...pls send ur email id sir...and thanks for ur nice video...
Gr8....i hv simulated using ur ideas. Thanks Dr.
Good to hear that
Can you provide the calculation
sir in case which the stages that we don't know, how you determine the stages of the absorber/stripper in HYSYS? since we know if the distilation we can use shortcut column but not with absorber/stripper
Most of the times, while adding comp fraction in monitor tab. My Wt. Error diiferes from yours although i followed the same steps as your and same values. Why this happen? Does it have concequences on the calculations?
Very good presentation
Thanks a lot
Can you tell when to select stream/stage when adding a spec in distillation column?
It will depend on the specification. If any particular value is required from a particular stage, then this spec will be used. However, mostly the specifications presented in the video are used.
Thank you very much sir
Sir ❤❤❤
Thanks Mohsin.
In refinery there is use only one stripper but in coke oven industry there is use double stripper coloumn sir...pls send ur email id sir...and thanks for ur nice video...
Yes, I agree. I will send shortly. As I want to have correspondence on different email address :-)