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 .
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
Sir if i have to add more units in this model like hydrocracker or cyt cracker can i do that? If yes were the changes i need to do except the obvious ones plz help me🙏🏻🙏🏻
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.
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.
I watched the entire playlist, well done mate.
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 .
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
Can you please make a video on sizing the Fired Heaters i.e., the sizing of Radiant, Convection and Stack sections
Thanks for making amazing videos ! Well done 👍🏻
Try to also do simulation of FCC DHDT Naphtha Complex CCR Isomerization Delyed coker Visbreaking on same file
Amazing video. Thanks
Sir if i have to add more units in this model like hydrocracker or cyt cracker can i do that? If yes were the changes i need to do except the obvious ones plz help me🙏🏻🙏🏻
simulation of gas processing plant, sweetening, recovery sulfur and etc
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.
I tried to remove 180 deg D from spec, but it still doesn't converge to me(
V.GOOD, dear sir had you made video at safety and energy analysis of crude oil in aspen.
Hi Naseer. At the moment I don’t have videos on safety and energy analysis
Good iffrts
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 ...
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.