Dry gas hydrogen production
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What is the maximum temperature that a medium-temperature reactor can withstand?
Different process designs are different, right? The design of our equipment is not more than 420
Our operating temperature is 412°C, with a design value of 444℃
It depends on the catalyst and conversion requirements. It’s usually around 350
Looking at the design temperature, the design temperature for equipment is generally higher than the maximum allowable temperature of the catalyst; as long as it’s below 400, there should be no problem
In the operation of a conventional medium-pressure reactor, the bed temperature is generally controlled at around 380°C; temperatures that are too high are actually unfavorable for the carbon monoxide conversion reaction
Could you give a general overview of the process flow?
Variable reactor in the steam reforming of light hydrocarbons to produce hydrogen
The PSA CO content won’t go down; I want to try taking action in this regard to see if it works
The temperature in our device shall not exceed 420°C, with the highest temperature at the bed layer being 380°C; the main focus is on controlling the inlet temperature to prevent overheating due to the heat released during the reaction