The issue of stopping the feed pump during accident handling
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This post was last edited by aini*yi on 2010-2-22 14:02. In a gasoline hydrogenation unit, when the fuel gas supply is stopped, why is it necessary to wait until the temperature of the reactor drops below 200 degrees before stopping the reaction feed pump? Maintain the operation of the circulating hydrogen compressor. By the way, I have a question: in our installation, the fuel gas volume for the main burner of the reactor was previously indicated by pressure, but it was later changed to being indicated by flow rate. What is the difference between the two?
Lift it up. . . I hope someone can help me answer it