almostbroken
Petroleum
- Sep 15, 2004
- 12
If I size a blowdown valve to depressure a sour gas plant from 1000 psig to 100 psi in 15 minutes I end up with a large flare system that is not warranted for other failures.
My question is does anyone know if I can stage the depressuring with a smaller valve that restricts the max flow to 12mmscfd for the first minute or so until the peak pressure is lost, then open a larger valve to keep near the 12 mmscfd with the lower pressure?
Almost Broken
My question is does anyone know if I can stage the depressuring with a smaller valve that restricts the max flow to 12mmscfd for the first minute or so until the peak pressure is lost, then open a larger valve to keep near the 12 mmscfd with the lower pressure?
Almost Broken