jcme7212
Chemical
- Dec 10, 2003
- 7
Dear coleagues.
In accordance to API Recomended Practice 521, the criteria of dimensioning the discharge piping of a gas safety valve is do not exceed the permissible backpressure, however this code doesn't state clearly the restriction about the Mach Number, Is it possible to have a choked flow at the discharge piping without affect the performance of the safety valve?. Is it feasible to have supersonic flow i.e, Mach > 1.?
I know a common criteria for main header should no exceed 0.8 Mach, but what about the lateral segments of discharge valves piping.
If someone can help me i would appreciate a lot.
thanks in advance.
In accordance to API Recomended Practice 521, the criteria of dimensioning the discharge piping of a gas safety valve is do not exceed the permissible backpressure, however this code doesn't state clearly the restriction about the Mach Number, Is it possible to have a choked flow at the discharge piping without affect the performance of the safety valve?. Is it feasible to have supersonic flow i.e, Mach > 1.?
I know a common criteria for main header should no exceed 0.8 Mach, but what about the lateral segments of discharge valves piping.
If someone can help me i would appreciate a lot.
thanks in advance.