Dangers of too rapid pressure increase in the hydrogen production desulfurization reactor alone
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If the desulfurizing agent is replaced in one of the two desulfurization reactors, what are the requirements regarding the pressure increase rate for that reactor after the replacement? What are the risks if the voltage is increased too quickly? Also, why can the compressor reach a very high pressure so quickly just by being pressed? I hope everyone can help me answer this!
Do you mean that after replacing desulfurization agent A online, it is necessary to incorporate this into the system’s pressure increase control mechanism? I checked the design manual, but there are no specific requirements regarding pressure increase. The manual mentions two points: first, nitrogen must be used to heat this reactor to 300°C; second, the replaced reactor needs to be connected to the subsequent reactors in the process. I’m not sure if my answer satisfies you; if you have any questions, let’s discuss further.