silvz71
Chemical
- Jun 13, 2007
- 13
Hello, I am trying to size a relief valve for a "minimum flow/sample" loop. I have a pump operating at around 600psi feeding boilers. There is a small loop just off the discharge of the pump that is regulated to 50psi, and then ties back into the suction of the pump. The idea is to protect the 50psi side since the pipe spec is different from the 600psi side. The fluid is boiler feed water, coming off a deaerator and feeding the boilers. An additional point of concern is that the desired discharge point of the relief is an atmospheric blowdown tank, that is nearly 200ft away.
Any tips on what to consider for this case? I've sized several relief valves in the past, but they have all been more "conventional" applications (i.e. PSV on a vessel where the fire case is governing, etc).
Any help is much appreciated! Thanks!
-David
Any tips on what to consider for this case? I've sized several relief valves in the past, but they have all been more "conventional" applications (i.e. PSV on a vessel where the fire case is governing, etc).
Any help is much appreciated! Thanks!
-David