Regarding the pressure of the pipes associated with the reaction vessel
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When compiling pipeline data recently, I’m not confident enough to determine the pipeline pressure; I would appreciate some guidance from experts. As shown in the diagram, the nitrogen seal pressure in the reactor is 0.3 MPa, while the pressure in the vacuum line is -0.098 MPa. What are the pressures in the gas lift column (PG) and the material pipes (PL001–003) under different operating conditions of the reactor? For example, during reduced-pressure distillation, atmospheric distillation, and reflux – I would like to know how to determine these pressures
The process determines the most demanding road conditions!
The pressures in the air lift tube and the return tube must be the same as the pressure inside the reaction vessel
With a nitrogen sealing pressure of 3 kilograms, that storage tank or vessel is already considered a pressure vessel; ignore everything else and use the highest value