The gas storage tank is equipped with a safety valve outlet; however, the technical specifications state that the safety relief device should be installed within the piping system
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In this case, is it not necessary to calculate the discharge capacity and volume of the safety valve? When helping other departments obtain evidence, in such cases the evaluation experts asked for no further calculations; but a colleague said that if there are safety valve outlets, calculations are necessary. I need the answer!
Our company’s practice is that if there are safety valve ports indicated on the drawing, a safety discharge calculation sheet should be provided； If there is no safety valve port on the diagram, then indicate that \"the safety relief device should be installed on the nearest pipeline in accordance with the process requirements.\" Since the drawings from your company show both a safety valve outlet and a requirement for a safety relief device to be installed in the pipeline, I believe this is contradictory. It’s best to change the pattern and remove one of the items.
I have a device whose medium is bromine. There is no safety valve outlet pipe on the pipe connection table; the technical specifications state that the safety relief device shall be installed by the user within the system. In such a case, is it necessary to recommend specific models or provide calculations for the safety valves? Seeking advice
I have a device whose medium is bromine. There is no safety valve outlet pipe on the pipe connection table; the technical specifications state that the safety relief device shall be installed by the user within the system. In such a case, is it necessary to recommend specific models or provide calculations for the safety valves? Seeking advice
I have a device whose medium is bromine. There is no safety valve outlet pipe on the pipe connection table; the technical specifications state that the safety relief device shall be installed by the user within the system. In such a case, is it necessary to recommend specific models or provide calculations for the safety valves? Seeking advice
I have a device whose medium is bromine. There is no safety valve outlet pipe on the pipe connection table; the technical specifications state that the safety relief device shall be installed by the user within the system. In such a case, is it necessary to recommend specific models or provide calculations for the safety valves? Seeking advice
I have a device whose medium is bromine. There is no safety valve outlet pipe on the pipe connection table; the technical specifications state that the safety relief device shall be installed by the user within the system. In such a case, is it necessary to recommend specific models or provide calculations for the safety valves? Seeking advice
When encountering such ambiguously simulated situations, it is recommended to carry out the calculations yourself. For safety valves installed on external pipelines, you can specify in the technical requirements the size of the piping used for the safety valve’s discharge as well as any relevant precautions; there is no need to include this information in the calculation documents, nor should any details about the safety valves be written on the overall layout diagram.