Hello,
I'm a new process engineer and I'm considering a emergency venting for a storage tank (200ft diameter). The tanks have open vents that are okay for normal venting (guided by API 2000). However, in case of fire or emergency venting, the open vents will not be enough. Then I proceed to...
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...