Nice video.Would like to highlight one point :While defining TBP distillation data ,data as per presentation beyond 70%(450 Deg C),76%(490 Deg C) ,80%(516 Deg C) is not covered correctly in Aspen Hysys. This will help in maintaining consistency in future upcoming videos.
Thank you very much for highlighting this oversight. Since the next lecture is a continuation of this one, I'll start by correcting the data before proceeding. Thanks.
Nice video.Would like to highlight one point :While defining TBP distillation data ,data as per presentation beyond 70%(450 Deg C),76%(490 Deg C) ,80%(516 Deg C) is not covered correctly in Aspen Hysys. This will help in maintaining consistency in future upcoming videos.
Thank you very much for highlighting this oversight.
Since the next lecture is a continuation of this one, I'll start by correcting the data before proceeding.
Thanks.
How can you introduce Refinery properties into the crude assay? like Sulfur content, Nitrogen content, TAN, smoke point, etc?
Thank you so much! Your videos helped me a lot!:)
thanks for the video, am having issues with the oil cut specification on Hysys
Thanks , please I have question If they didn't give us the component list with there light ends what we can do in this case
Hello..
I have been having issue sourcing simulation data, and i dont want to make unrealistic guesses. How do you come about thia datas? Kindly
I just want to create a straight run Naphtha cut as the feed for a hydrotreater unit, how can i achieve this please
Sir, could you please show in the next lecture on how to convert oil manager assay to petroleum assay and vice versa? Thanks a lot