Okanv
Mechanical
- Oct 11, 2004
- 2
My question is related with the safety relief valve capacity assessment of a submarine LPG pipeline.
The system is consisted of 14" SCH XS (Mix LPG) and 10" SCH 40 (Propane) seamless steel piping with a length of 1.450 meters; both isolated with HDPE for 2.2 mm. These pipes are mostly buried under the seabed, going to a maximum depth of 40 meters. Maximum operation pressure will be 17.5 bars, the latest to be valid for the safety valves's discharging setpoint.
I have looked to find anything related other than the bulk storage tanks but related with the piping, especially for the submarine piping, but unfortunately I wasn't lucky enough to find it out.
So, could anyone enlighten me with this issue? Any info including, formulas, related standards etc. will be welcomed.. Thanks before
The system is consisted of 14" SCH XS (Mix LPG) and 10" SCH 40 (Propane) seamless steel piping with a length of 1.450 meters; both isolated with HDPE for 2.2 mm. These pipes are mostly buried under the seabed, going to a maximum depth of 40 meters. Maximum operation pressure will be 17.5 bars, the latest to be valid for the safety valves's discharging setpoint.
I have looked to find anything related other than the bulk storage tanks but related with the piping, especially for the submarine piping, but unfortunately I wasn't lucky enough to find it out.
So, could anyone enlighten me with this issue? Any info including, formulas, related standards etc. will be welcomed.. Thanks before