Operation mode of the desulfurization absorption tower circulation pump
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During wet limestone flue gas desulfurization, the circulation pump should be adjusted or shut down based on the volume of flue gas being treated and the SO2 content in the flue gas, in order to make the desulfurization process more economical. Are there specific plans? How is it operated or handled?
Desulfurization is generally a loss-making operation; the desulfurization circulation pump can only be stopped when production is halted. The economic efficiency of desulfurization is adjusted based on the SO2 content in the flue gas, with the actual operations being coordinated with the previous processes
Desulfurization is a loss-making business, but if there are no losses, where else can one make a profit? Should the circulation pump be adjusted based on previous data or based on smoke exhaust parameters? It seems that the latter approach is safer