carol2005
Chemical
- May 24, 2005
- 21
I was asked to check the adequacy of a relief valve on some pipelines of supplying natural gas fuel to steam boilers (the steam boilers are to generate 270 pounds of steam for a chemical plant which is located in a place where ASME codes apply).
Thesse relief valves all located downstream of pressure regulators which reduce the Natural Gas pressure to about 15 to 20 PSIG. These relief valves have set pressure of 30 PSIG for regulator failure scenario.
Although I haven't talk to the relief valve suppliers yet, I pretty sure these relief valves are not compliant with ASME Section I because these valves:
One of them has model as Fisher Easy Joe Type 399A-6365 pilot-operated pressure relief valve. This type of valve requires buidup of 5 PSI over Set pressure 30 PSIG to fully open
Another model is Fisher 399A-6358 backpressure regulator which is not even a pressure relief valve.
My question: are these relief valve adequate for this application (on natural gas line to high pressure steam boilers)? Don't they have to be ASME Section I stamped? Thank you very much for your advice.
Thesse relief valves all located downstream of pressure regulators which reduce the Natural Gas pressure to about 15 to 20 PSIG. These relief valves have set pressure of 30 PSIG for regulator failure scenario.
Although I haven't talk to the relief valve suppliers yet, I pretty sure these relief valves are not compliant with ASME Section I because these valves:
One of them has model as Fisher Easy Joe Type 399A-6365 pilot-operated pressure relief valve. This type of valve requires buidup of 5 PSI over Set pressure 30 PSIG to fully open
Another model is Fisher 399A-6358 backpressure regulator which is not even a pressure relief valve.
My question: are these relief valve adequate for this application (on natural gas line to high pressure steam boilers)? Don't they have to be ASME Section I stamped? Thank you very much for your advice.