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Do the colleagues from the design institute know about it? Is methanol methanation in ammonia synthesis plants considered a hydrogenation process? Is there a temperature and pressure interlock design? Is design needed? Have you ever thought about standards?
Do the colleagues from the design institute know about it? Is methanol methanation in ammonia synthesis plants considered a hydrogenation process? Is there a temperature and pressure interlock design? Is design needed? Have you ever thought about standards? Can you call this post a discussion? What do the colleagues from the design institute need to know? First, figure out whether it exists or not. The conversion of methanol into methane is a form of hydrogenation, and it is deep hydrogenation. This reaction process is a chemical equilibrium process on a large scale, rather than a rapid reaction under specific temperature and pressure conditions; generally, no interlock design is required. Of course, if one has extra money to spend, it’s not a problem to include additional interlocks. Any industrial facility, as long as it is obtained through legitimate means, requires design. Rules are not meant only for thinking about; they are to be strictly enforced.
I’m sorry, I didn’t write it clearly! During the ammonia synthesis process, trace amounts of CO and CO2 are purified through methanation. The design does not include any interlocks, but safety inspections indicate that since this is a hydrogenation reaction, temperature and pressure interlocks should be implemented. We are not sure how to make the necessary adjustments, so we have come here for help. Thank you everyone for your assistance
Methanol methanation in ammonia synthesis plants is a hydrogenation process. It features a temperature and pressure interlock design. Design is needed.
Thank you, big brother! ! ~~~~~! ! ! !
Where can I find these specifications to write them?