Process for performing ammonium sulfite pulping by using sulfur-containing flue gas absorber
A technology of ammonium method and absorbent, applied in the field of recycling technology, can solve the problems of low economic added value, waste pollutants, low absorption rate, etc., achieve high economic value, reduce degradation, and increase pulping yield
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Embodiment 1
[0048] The flue gas is firstly dedusted by the electrostatic precipitator, and after the dedusted flue gas is pressurized by the induced draft fan, the amount of flue gas entering the induced draft fan is 310800m 3 / h, the flue gas enters the liquid collection tank at the bottom of the desulfurization tower, sprays excess ammonia water and reacts with sulfur dioxide to form ammonium sulfite and ammonium bisulfite. A mixture of ammonium bisulfite and ammonium sulfite ammonia is formed in the liquid collection tank. The mixture is pumped to the height of the tower and sprayed downward through the three-layer spray device in the middle of the tower. The gas is evenly mixed to absorb the residual sulfur dioxide in the flue gas. Ammonium bisulfite in the mixture reacts with sulfur dioxide to obtain ammonium sulfite and returns to the liquid collection tank. Such repeated cycles will completely absorb the sulfur dioxide in the flue gas. The temperature in the desulfurization tower...
Embodiment 2
[0062] The flue gas first passes through the filter and dust removal equipment for dust removal. After the dust removal flue gas is pressurized by the induced draft fan, the amount of flue gas entering the induced draft fan is 200,000~400,000m 3 / h, into the liquid collection tank at the bottom of the desulfurization tower, spraying excess ammonia water with a concentration of 0.8-11% to react with ammonium bisulfite to generate ammonium sulfite. A mixture of ammonium bisulfite and ammonium sulfite ammonia is formed in the liquid collection tank, and the mixture is pumped to the height of the tower, and sprayed downward through the second-layer spray device in the middle of the tower, and the upward smoke The gas is evenly mixed to absorb the residual sulfur dioxide in the flue gas. Ammonium bisulfite in the mixture reacts with sulfur dioxide to obtain ammonium sulfite and returns to the liquid collection tank. The temperature in the desulfurization tower is 90-120°C; the pre...
Embodiment 3
[0076] The flue gas is firstly dedusted by the electrostatic precipitator, and after the dedusted flue gas is pressurized by the induced draft fan, the intake volume of the induced draft fan is 305,000-400,000m 3 / h, the flue gas enters the liquid collection tank at the bottom of the desulfurization tower, sprays excess ammonia water and reacts with sulfur dioxide to form ammonium sulfite and ammonium bisulfite. A mixture of ammonium bisulfite and ammonium sulfite ammonia is formed in the liquid collection tank. The mixture is pumped to the height of the tower and sprayed downward through the three-layer spray device in the middle of the tower. The gas is evenly mixed to absorb the residual sulfur dioxide in the flue gas. Ammonium bisulfite in the mixture reacts with sulfur dioxide to obtain ammonium sulfite and returns to the liquid collection tank. Such repeated cycles will completely absorb the sulfur dioxide in the flue gas. The temperature in the desulfurization tower is...
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