Technology for preparing ammonium sulfate by high-efficiency ammonia desulphurization and crystallization
A technology of ammonia desulfurization and ammonium sulfate, which is applied in the field of flue gas desulfurization and dust removal, can solve the problems of increased operating costs, high liquid level in the oxidation tank, unfavorable safety production, etc., and achieves improved production efficiency, high yield, reduced equipment investment and The effect of production energy consumption
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Embodiment 1
[0030] A. Desulfurization: The flue gas to be desulfurized and the atomized ammonia water are respectively passed into the desulfurization section of the desulfurization tower at a volume ratio of 400:1, and the slurry containing ammonium bisulfite and ammonium sulfite generated after reaction desulfurization enters the regeneration storage tank.
[0031] B. Oxidation: Pass the ammonia water into the regeneration storage tank, control the pH of the slurry in the regeneration storage tank to 6.0, after the ammonia water reacts with ammonium bisulfite to generate ammonium sulfite, then pass the atomized ammonium sulfite solution into In the oxidation section of the desulfurization tower, the volume ratio of the atomized ammonium sulfite solution to the oxygen-enriched flue gas is 1:400, and the oxidation is 150 minutes. The ammonium sulfate-containing slurry produced by the reaction of ammonium sulfite and oxygen-rich flue gas enters the concentration storage tank.
[0032] C. Concen...
Embodiment 2
[0034] A. Desulfurization: The flue gas to be desulfurized and the atomized ammonia water are respectively passed into the desulfurization section of the desulfurization tower at a volume ratio of 380:1, and the slurry containing ammonium bisulfite and ammonium sulfite generated after reaction desulfurization enters the regeneration storage tank.
[0035] B. Oxidation: Pass the ammonia water into the regeneration tank and control the pH of the slurry in the regeneration tank to 6.5. After the ammonia water reacts with ammonium bisulfite to generate ammonium sulfite, then the atomized ammonium sulfite solution is passed into In the oxidation section of the desulfurization tower, the volume ratio of the atomized ammonium sulfite solution to the oxygen-enriched flue gas is 1:380, and the oxidation is 120 minutes. The ammonium sulfate-containing slurry produced by the reaction of ammonium sulfite and oxygen-rich flue gas enters the concentration storage tank.
[0036] C. Concentration:...
Embodiment 3
[0038] A. Desulfurization: The flue gas to be desulfurized and the atomized ammonia water are respectively introduced into the desulfurization section of the desulfurization tower at a volume ratio of 420:1, and the slurry containing ammonium bisulfite and ammonium sulfite generated after reaction desulfurization enters the regeneration storage tank.
[0039] B. Oxidation: Pass the ammonia water into the regeneration tank and control the pH of the slurry in the regeneration tank to 5.5. After the ammonia water reacts with ammonium bisulfite to generate ammonium sulfite, then the atomized ammonium sulfite solution is passed into In the oxidation section of the desulfurization tower, the volume ratio of the atomized ammonium sulfite solution to the oxygen-rich flue gas is 1:420, and the oxidation is 180min. The ammonium sulfate-containing slurry produced by the reaction of ammonium sulfite and oxygen-rich flue gas enters the concentration storage tank.
[0040] C. Concentration: The ...
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