Considering the enormous amounts of thermal energy and stripping steam required for crude distillation unit (CDU) throughputs, are there any new crude oil processing schemes for reducing CDU operating costs?

What can be the possible reason for foaming in HP amine absorber in Hydrocracker unit? Though we have a centrifugal separator upstream of Amine absorber we face foaming & at same time level in HP centrifugal separator in upstream remain NIL.

We are experiencing frequent amine carry-over from our high pressure amine absorber. What are the possible causes and solutions?

We’re encountering fines build-up in the drum overhead into the fractionator of our delayed coker. Solutions please.