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