Our fluid Catalytic Cracking unit, commissioned an year ago, is constrained with high stripper/absorber pressure drop problems. When stripper feed temp was 42 deg, stripper exhibited high del pr even at 80% loads. After failure of HPS inlet condensers cooling water exchangers, the stripper feed...
We have a three separator (HC, HC-Water vapor, Water). We are facing difficulties in separation of water and hydrocarbon. There is carryover of HC with water. Is there is any effect of gas velocity on separation of water and hydrocarbon in liquid phase.
