Unotec
Chemical
- Jun 13, 2006
- 593
Good day,
We have a problem with a crude oil cooler.
The oil comes from a high (80ºC) process at a relatively low viscosity (1.38cP). It is cooled down by water to about 40ºC, where the viscosity increases to about 7.33cP.
The problem is that, as the viscosity increases the differential pressure between the hot oil and cold water sides varies throughout the unit. Plate and frame, usually, allow for up to 6kPa pressure differential, which is very minimal.
We have busted couple plates.
In theory, the pressure drop throughout the unit should remain constant and minimal, but apparently it isn't.
Has anybody experienced similar problems to this scenario?
Cheers!
<<A good friend will bail you out of jail, but a true friend
will be sitting beside you saying ” Damn that was fun!” - Unknown>>
We have a problem with a crude oil cooler.
The oil comes from a high (80ºC) process at a relatively low viscosity (1.38cP). It is cooled down by water to about 40ºC, where the viscosity increases to about 7.33cP.
The problem is that, as the viscosity increases the differential pressure between the hot oil and cold water sides varies throughout the unit. Plate and frame, usually, allow for up to 6kPa pressure differential, which is very minimal.
We have busted couple plates.
In theory, the pressure drop throughout the unit should remain constant and minimal, but apparently it isn't.
Has anybody experienced similar problems to this scenario?
Cheers!
<<A good friend will bail you out of jail, but a true friend
will be sitting beside you saying ” Damn that was fun!” - Unknown>>