Collins, can you also show how to model conversion reactors where the feed is an assay like naphtha or crude but the products will be a mix of pure gases(like LPG) as well as liquids with BP cuts
Thanks for this lesson but I want to ask u sir that the composition in light ends wasn't clear in screen...can you write it please ... Big thank for u sir
Collins is definitely a force to reckon with in this field. Keep up the good work, sir! Thanks for this highly informative video.
Thanks a lot for watching and subscribing too. More videos will be coming up soon. Stay tuned
Thanks a lot sir for all such valuable videos. Kindly upload more :)
that was really helpful, thanks
Great explanation!
Thank you very much!
Thank you for all your support Sir
Super useful. Thanks, man :)
Thanks for the video, sir. It was really helpful. Please can I get the fractions of the other paraffins; C6 to C17.
Collins, can you also show how to model conversion reactors where the feed is an assay like naphtha or crude but the products will be a mix of pure gases(like LPG) as well as liquids with BP cuts
Thanks a lot sir! Could you please type the values for paraffinic componentes? because my distribution plot is totally different to yours!
please share sir
Sir how to find the properties of kerosene oil i.e molecular weight, density ect from the crude oil characterization in Aspen HYSYS
excuse me sir, how to solve light end section composition doesn't appear? thx
Is it possible to make an assay of ordinary oil from the fatty acid profile that has compositions?
No sir it's not possible, the assay in Aspen Hysys is for oil and gas
Thanks for this lesson but I want to ask u sir that the composition in light ends wasn't clear in screen...can you write it please
... Big thank for u sir
Good day Imosh,
Below is the composition in mole percent
N2 0.48
H2S 0.00
CO2 0.87
C1 41.83
C2 8.87
C3 7.11
i-C4 1.47
n-C4 3.75
i-C5 1.25
n-C5 1.63
n-C6 0.00
H2O 0.00
Hi Sir. May I know for my case, the data I have are only TBP (by volume %) and density. What should I input in the components list?
Hi i have the same data as u, have u found a solution?
still confusing why selecting user points? kindly clear why using cut ranges
Hello, good knight
I need to know about petroleum process
Please could you send me some simulation about this and bibliography.
Thanks a lot
sir please share the paraffinic fraction file.