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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

Active Publication Date: 2015-07-22
YUNNAN YONGXIN ALUMINUM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the use of pressurized aeration method to oxidize ammonium sulfite, the current technology undoubtedly increases the operating cost, and the liquid level of the oxidation tank required by this method is too high, which is not conducive to safe production.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention discloses a process for preparing ammonium sulfate through high-efficiency ammonia desulfurization and crystallization, and belongs to the technical field of flue gas desulfurization and dust removal. The process includes desulfurization, oxidation, and concentration steps. First, the flue gas and ammonia water are passed into the desulfurization section of the desulfurization tower, and the slurry containing ammonium bisulfite and ammonium sulfite generated after the reaction desulfurization enters the regeneration storage tank; the ammonia water is passed into the regeneration tank. The storage tank reacts with ammonium bisulfite to generate ammonium sulfite, and then the ammonium sulfite solution is passed into the oxidation section of the desulfurization tower, and the slurry containing ammonium sulfate generated by reaction and oxidation with flue gas enters the concentrated storage tank; the sulfuric acid in the concentrated storage tank is The ammonium solution is passed into the cooling section of the desulfurization tower to contact the flue gas for heat exchange. After the ammonium sulfate solution is concentrated, it enters the crystallization storage tank and is transported to the separator for solid-liquid separation. The process of the present invention utilizes the characteristics of high oxygen content in the flue gas itself, has high efficiency in oxidizing ammonium sulfite, improves the crystallization speed of ammonium sulfate, and effectively reduces equipment investment and production energy consumption, reduces production safety hazards, and improves economic benefits. significantly.

Description

technical field [0001] The invention belongs to the technical field of flue gas desulfurization and dust removal, and in particular relates to a process for preparing ammonium sulfate by high-efficiency ammonia desulfurization and crystallization. Background technique [0002] Flue gas desulfurization and dust removal can effectively reduce pollution and clean the production environment. At present, there are mainly two types of flue gas desulfurization: dry method and wet method. Compared with gypsum desulfurization and double-alkali desulfurization, ammonia desulfurization in wet desulfurization technology is a A more environmentally friendly and efficient process, its main product - ammonium sulfate, as an important fertilizer product, has higher economic value than products obtained by other desulfurization methods, so ammonia desulfurization technology has gained more and more attention in the field of flue gas dedusting Wide range of applications. The process of prepa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78C01C1/242B01D53/50
Inventor 杨叶伟赵群车立志赵瑞敏张川登王跃全白礼平文卫国卢栖
Owner YUNNAN YONGXIN ALUMINUM