Transform catalyst with steam
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Gentlemen! In the process of producing synthetic ammonia via water-coal slurry gasification, the carbon monoxide content at the outlet of the first stage is designed to be 10%, but it is currently 12.5%; the carbon monoxide content at the outlet of the second stage is designed to be 4%, but it is currently 2.7%. Are there any cases of adding steam at the inlet of the second stage?
Hello, teacher. I would like to ask: the current operating condition is set at 4%, while it is currently at 2.7%, which is lower than the designed value. Then why is steam needed? Moreover, I suggest that even if steam is to be added, it is better to add it at the inlet – that will yield better results