Olidin
Chemical
- Oct 16, 2012
- 3
Hello,
I have a question about some set-ups that use relief devices as minimum bypass valves. On PD pumps, I understand why this is necessary since PD can overpressure the line or itself if blocked in. However, for centrifugal pump, it's unlikely pump will overpressure itself during shut-in (if that was possible then every start-up would be very scary for the operators).
So what are the benefit of using relief valves for minimum bypass? How would you determine the valve set pressure? On the other hand, what are the advantage for using a minimum bypass line instead of a relief valve?
If the current set-up uses relief valves, what are the incentives to use a minimum bypass line?
Thanks for your help.
I have a question about some set-ups that use relief devices as minimum bypass valves. On PD pumps, I understand why this is necessary since PD can overpressure the line or itself if blocked in. However, for centrifugal pump, it's unlikely pump will overpressure itself during shut-in (if that was possible then every start-up would be very scary for the operators).
So what are the benefit of using relief valves for minimum bypass? How would you determine the valve set pressure? On the other hand, what are the advantage for using a minimum bypass line instead of a relief valve?
If the current set-up uses relief valves, what are the incentives to use a minimum bypass line?
Thanks for your help.