Hi,
Im simulating a crude unit with heat exchanger network using chemcad. Can we actually extract the sub-stream from the crude column? For the purpose of accurate heat integration, I need to extract i.e. the pumparound stream from the column to integrate with the heat exchanger, however as far...
the content consists of crude oil ligthends ranging from lets say 1.5% wt Naphtha C5+ 10% C5 and rest <C4-1
the problem is it is a range of unspecified components
Currently im trying to get the simulation work by plotting an assay (TBP curve) which keeps giving me errors earlier on
But the...
I am currently using pipephase 9.1 to determine pressure & temperature profile and flow regime of a pipeline (120km). The pipeline consists of gas condensate which is fully vapour at 55 bar, 55C (from booster pump and cooled down by an air cooler).
My question is will the simulation take into...
Sry shud be more precise on my reply
A reboiler stripper will cost more than a steam stripper due to an additional fired heater.
I assume the price of a vacuum dryer is a lot cheaper than a fired heater.
Can anyone provide any information on vacuum drying for diesel? operating parameters, design specifications, simulator and estimate price ? Thank you.
Background:Designing a new diesel hydrotreater for a refinery. Using steam stripper which requires water removal for the ULSD product. Client...
Can anyone provide any information on vacuum drying for diesel? operating parameters, design specifications, pfd and estimate price ? Thank you.
Background:
Designing a new diesel hydrotreater for a refinery. Using steam stripper which requires water removal for the ULSD product. Client does...
