What is the effect of the re-pressurization device on the product distribution of the pre-pressurized dry gas in the reaction riser?
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This post was last edited by 37927 on 2016-10-14 at 14:32. I would like to ask the experts in catalysis: increasing the flow rate of the dry gas fed to the bottom of the reaction riser in the catalyst regeneration unit from the current level of 1800 cubic meters per hour to the design value of 3500 cubic meters per hour – what effects will this have on the product distribution and the light ends? What is the reaction mechanism behind this increase (with the reaction temperature around 510°C)?
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