Hi friends from Cheresources,
In designing a crude oil -water separator vessel, some calculation procedures state the following:
A maximum droplet settling velocity of 10 inch/min is used regardless of the computed settling velocity.
The issue is: If we use a coalescer to increase the size of the liquid droplets ¿ Could we then use a droplet settling velocity higher than 10 inch/min to reduce the length of the separator?
If the computed setling velocity give say like 40 inch/min ¿ can we use let`s say 80% of 40 inch/min to calculate the lengh of the separator vessel?
I appreciate some lights on this subject please.