Vacuum Distillation unit in HYSYS | Part 4

[@DDDelgado]

I watched the entire playlist, well done mate.

[@ДамирИргалиев-й1ю]

Thank you so much. I followed all your video tutorials and it really helped me. Do you plan to continue? Please do so. Will be interesting to see SRU & TGTU plant simulation

[@silvioazevedo8213]

Very good , I have been following your video lessons and in a way it has helped me in my final work , so I would so much like you to do the simulation of the catalytic cracking unit including the fractionation tower .

[@AroojFatima-zz2yr]

Thanks for making amazing videos ! Well done 👍🏻

[@isaiaslopez1953]

Amazing video. Thanks

[@muhammadtalhafarooq6457]

Try to also do simulation of FCC DHDT Naphtha Complex CCR Isomerization Delyed coker Visbreaking on same file

[@KagakuCB250]

I've followed all of the Oil Refinery tutorials using Hysys 2006 (don't ask how) and it works correctly but the last part (Vacuum Distillation Unit) where the 180°F should be added and then, when it does not converge, removed and it will converge.

[@ДамирИргалиев-й1ю]

I tried to remove 180 deg D from spec, but it still doesn't converge to me(

[@naseerahmad739]

V.GOOD, dear sir had you made video at safety and energy analysis of crude oil in aspen.

[@eduXinsight]

Hi Naseer. At the moment I don’t have videos on safety and energy analysis

[@julioxvc6810]

simulation of gas processing plant, sweetening, recovery sulfur and etc

[@khadidjaressaf8111]

Thnx for the videos ... Btw it didn't converge for me in this last one 🙁 even though i tried to re do it a multiples times ...

[@KagakuCB250]

the point where it is supposed to be added an additional parameter, meaning, the top temperature of 180°F. Get rid of it. You'll have 0 DF with the top stage PA rate, LVGO rate, HVGO rate, Slop Wax rate, TopStage PA_TRet, HVGO PA Rate & HVGO PA Dt.

[@thisisbismay5681]

Good iffrts