Dear Forum members,
attached is existing crude oil storage tank skecth, tank venting is big problem because of heavy smoke in LP flare. staff resident camp is very close to production facility hardly 500 meters away. the design of blankiting and venting is different from today crude oil storage and handling.
balnkit gas is coming from dehydrator outlet and from de-gassing boot directly with out controlling and LP gas going to flare from is controlled by PCV on 20'' dia line. tank pressure is only 0.2 psig.
Maximum crude inlet flow is 25000BOPD to de-gassing boot. I think, if we can modify the de-gassing boot vapour outlet line and divert to flare and regulate the dehydrator gas by installing the PRV this problem can be solved but i need some more input in this regards.
Thanks
Toor