RJB32482
Chemical
- Jan 19, 2005
- 271
Hello,
We are having troubles with our of our condensing units on a polystyrene batch reactor. This unit condenses styrene vapors while charging the reactor with styrene and also venting at 90C when sampling. Shell side is a 50/50 glycol/water solution and tube side is the process vapor (styrene). Currently, we are having issues with a high temperature on the outlet of the glycol shell. The flow through the shell is good, but temperature is not. So I am not thinking any issues with the shell side of the condenser.
But my thought is that if the tubes were plugged, that your temperature in the glycol would decrease (less heat transfer area = less heat transfered to shell side = less temperature change). Any thoughts on that?
Glycol chiller unit also supplies 11 other reactors and no issues with those temperatures while venting to those condensers. Same process in those reactors as with this problem child.
Thanks in advance.
We are having troubles with our of our condensing units on a polystyrene batch reactor. This unit condenses styrene vapors while charging the reactor with styrene and also venting at 90C when sampling. Shell side is a 50/50 glycol/water solution and tube side is the process vapor (styrene). Currently, we are having issues with a high temperature on the outlet of the glycol shell. The flow through the shell is good, but temperature is not. So I am not thinking any issues with the shell side of the condenser.
But my thought is that if the tubes were plugged, that your temperature in the glycol would decrease (less heat transfer area = less heat transfered to shell side = less temperature change). Any thoughts on that?
Glycol chiller unit also supplies 11 other reactors and no issues with those temperatures while venting to those condensers. Same process in those reactors as with this problem child.
Thanks in advance.