A method for controlling the crystalline products in a wet 
flue gas desulfurization 
slurry pool belongs to the technical field of 
flue gas desulfurization. The method comprises the following steps thaA method for controlling the crystalline products in a wet 
flue gas desulfurization 
slurry pool belongs to the technical field of 
flue gas desulfurization. The method comprises the following steps thaver high saturation of 
calcium sulfite in the 
liquid phase for 
synchronizing the yield and growth of 
gypsum crystal in the 
slurry, to prevent excessive production of 
gypsum fine 
crystal and to facilitver high saturation of 
calcium sulfite in the 
liquid phase for 
synchronizing the yield and growth of 
gypsum crystal in the slurry, to prevent excessive production of gypsum fine crystal and to facilitate the 
dehydration of the crystalline products.ate the 
dehydration of the crystalline products.t: for an absorber which has a 
flue gas purification channel on top, a raw 
flue gas inlet in the middle and a slurry 
pool at bottom, the saturation of 
calcium sulfite in a 
liquid phase in the slurry pt: for an absorber which has a flue gas purification channel on top, a raw flue gas inlet in the middle and a slurry pool at bottom, the saturation of 
calcium sulfite in a liquid phase in the slurry pool can be quickly reduced by controlling the required volume of injected 
oxygen in the slurry pool and the 
oxygen supply is kept constantly in a proper state to prevent semi-hydrated gypsum and crystool can be quickly reduced by controlling the required volume of injected 
oxygen in the slurry pool and the 
oxygen supply is kept constantly in a proper state to prevent semi-hydrated gypsum and crystal scale generated due to inadequate filling of oxygen in the slurry pool from causing scale to block the vessel wall and 
pipe wall of the slurry pool and to provent the crystalline products from dehyal scale generated due to inadequate filling of oxygen in the slurry pool from causing scale to block the vessel wall and 
pipe wall of the slurry pool and to provent the crystalline products from dehydrating difficultly; the injection amount of the limestone slurry in the slurry pool is controlled to control the fluctuation range of the pH value of the gypsum slurry in the slurry pool to prevent odrating difficultly; the injection amount of the limestone slurry in the slurry pool is controlled to control the fluctuation range of the pH value of the gypsum slurry in the slurry pool to prevent o