We have a Condensate Splitter Unit in our plant.
There is a first tower that separates the Naphtha- out.
In the next tower, function is to fractionate Kero, Diesel and Residue.
At the flash zone, the liquid from the tray above the flash zone exits the tower and passes through a flowmeter to allow us to measure Overflash.
However the flow is never stable. And it fluctuates quite wildly. We try as much as possible to maintain the overflash flow at 3-5% of tower charge as per convention. But the swing is wilder than this. Currently the Diesel colour is still not affected even though this sometimes goes to zero (suspect the reason is because Condensate does not discolour the Diesel as much as the Residue from Crude).
But in order to have stability, it is better to have this stable.
Could it be flowmeter is not appropriate? Or we are misoperating?
Edited by colt16, 13 December 2016 - 09:50 AM.