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Pyrite-to-sulfuric acid flue gas defluorination equipment and pyrite-to-sulfuric acid flue gas defluorination process method

A process method and technology made from iron ore, applied in the field of flue gas defluorination, can solve the problems of small footprint fluoride removal equipment, reduced catalyst pulverization activity, collapse of ceramic rings in drying towers, etc. Convenience and compact layout

Inactive Publication Date: 2020-04-21
洛阳丰瑞氟业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Sulfuric acid plant has serious corrosion on dry suction facilities due to excessive fluoride in the gas phase, such as corrosion and perforation of dry suction pump, corrosion of first suction and second suction fiber demisters, resulting in reduced catalyst powdering activity, and even collapse of the ceramic ring of the drying tower; therefore, it must be purified The defluoridation treatment is carried out in the workshop section to ensure the normal operation of subsequent equipment
However, there is still a lack of a defluoridation equipment suitable for the improvement of old plants, with small footprint, high treatment efficiency, convenient maintenance and reasonable structure layout.

Method used

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Experimental program
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Effect test

Embodiment 1

[0044] The furnace gas generated from the reaction furnace is guided into the high-efficiency scrubber. Add the first fluoride removal material in the high-efficiency scrubber, wherein the first fluoride removal material is a mixed agent of 6wt% polyferric sulfate solution, 80mg / L PAC coagulant, and 5mg / L PAM flocculant, and adjust the pH to 6.0, stirring for 1 min. Add the second fluoride removal material in the intermediate scrubber, wherein the second fluoride removal material is milk of lime, CaCl 2 , 80mg / L PAC coagulant, and 5mg / L PAM flocculant, adjust the pH to 11.0, and let it stand for 20min. The furnace gas treated by the intermediate scrubber is discharged.

Embodiment 2

[0046] The furnace gas generated from the reaction furnace is guided into the high-efficiency scrubber. Add the first fluoride removal material in the high-efficiency scrubber, wherein the first fluoride removal material is a mixed agent of 9wt% polyferric sulfate solution, 80mg / L PAC coagulant, and 5mg / L PAM flocculant, and adjust the pH to 7.5, stirring for 2min. Add the second fluoride removal material in the intermediate scrubber, wherein the second fluoride removal material is milk of lime, CaCl 2 , 80mg / L PAC coagulant, and 5mg / L PAM flocculant, adjust the pH to 10.5, and let it stand for 25 minutes. The furnace gas treated by the intermediate scrubber is discharged.

Embodiment 3

[0048] The furnace gas generated from the reaction furnace is guided into the high-efficiency scrubber. Add the first fluorine removal material in the high-efficiency scrubber, wherein the first fluoride removal material is a mixed agent of 7wt% polyferric sulfate solution, 80mg / L PAC coagulant, and 5mg / L PAM flocculant, and adjust the pH to 7. Stir for 1.5 minutes. Add the second fluoride removal material in the intermediate scrubber, wherein the second fluoride removal material is milk of lime, CaCl 2 , 80mg / L PAC coagulant, and 5mg / L PAM flocculant, adjust the pH to 11, and let it stand for 20min. The furnace gas treated by the intermediate scrubber is discharged.

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Abstract

The invention relates to pyrite-to-sulfuric acid flue gas defluorination equipment, which comprises a reaction furnace, an efficient washing tower and a middle washing tower, wherein the efficient washing tower comprises a first defluorination material inlet, and the middle washing tower comprises a second defluorination material inlet formed in the side wall. According to the invention, a two-stage washing tower with defluorination gradient is arranged to treat so as to improve the defluorination efficiency, and different defluorination materials can be added to achieve efficient defluorination treatment; the equipment is small in occupied area and high in defluorination efficiency, and is suitable for transformation and upgrading of old factories; the process method of the pyrite-to-sulfuric acid flue gas defluorination equipment comprises the following steps: S1, introducing furnace gas into the efficient washing tower; S2, adding a first defluorination material into the efficient washing tower; S3, adding a second defluorination material into the middle washing tower; and S4, discharging the treated furnace gas; and the process method has the advantages of high defluorination efficiency and convenience in raw material obtaining of pyrite-to-sulfuric acid preparation plants, and is suitable for transformation and upgrading of old plants.

Description

technical field [0001] The invention relates to the technical field of flue gas defluorination, and more specifically, relates to a flue gas defluorination equipment and a process method of sulfuric acid produced from pyrite. Background technique [0002] Usually, most manufacturers of sulfuric acid produced from pyrite do not take into account that the fluorine content of the gas phase in the purification section will increase significantly due to the change of raw material fluorine content in the initial stage of design, resulting in severe corrosion, which makes it difficult to add washing devices or defluorination towers in the later stage. Moreover, because fluorine is difficult to remove during the roasting process, the prevention of fluorine hazards in the industry is also concentrated in the purification system. By increasing the amount of dilute acid discharge and using fluorine-resistant materials to remove and prevent fluorine, reduce the impact on purification equ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/18B01D53/68B01D53/75B01D53/79C01B17/74
CPCB01D53/1406B01D53/1456B01D53/1493B01D53/185B01D53/68B01D53/75B01D53/79B01D2257/2047B01D2258/0283C01B17/74
Inventor 李海强谷若谷李毅王田田
Owner 洛阳丰瑞氟业有限公司
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