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Method for recycling selenium in electrolytic manganese anolyte

An anolyte and electrolytic manganese technology, applied in the field of electrolytic manganese, can solve the problems of insufficient economic feasibility of selenium recovery technology, no reports on the production of recovered selenium, and difficult recovery.

Inactive Publication Date: 2019-03-12
DAXIN MANGANESE MINE BRANCH OF CITIC DAMENG MINING IND
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Problems solved by technology

[0004] Due to the low selenium content in the electrolytic manganese anolyte (~0.01g / L), the recovery is difficult, and there are still obvious deficiencies in many aspects such as the economic feasibility of the existing selenium recovery technology, and there is no recovery of the electrolytic manganese anolyte at present. Production report of selenium

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  • Method for recycling selenium in electrolytic manganese anolyte
  • Method for recycling selenium in electrolytic manganese anolyte
  • Method for recycling selenium in electrolytic manganese anolyte

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Embodiment Construction

[0023] The present invention will be further described below in conjunction with specific examples, but the protection scope of the present invention is not limited to the following examples.

[0024] About the process study of step S1:

[0025] S1-1. Effect of Stirring Speed.

[0026] The fixed temperature was 30°C, and the amount of iron powder was 100mg L-1. The recovery rate of selenium at different stirring speeds (including 100r / min, 200r / min, 300r / min, 400r / min, 500r / min, and 600r / min) was studied. And the impact of the change of sulfuric acid concentration in the anolyte, the results are shown in Figure 1.

[0027] As can be seen from the figure, with the increase of stirring speed, the recovery rate of selenium is constantly increasing, when the stirring speed is at 300r min -1 ~600r·min -1 , the changes between the two are not obvious. Analyzing the reason, increasing the stirring speed can promote the dispersion of iron powder, reduce the possibility of agglomer...

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Abstract

The invention discloses a method for recycling selenium in electrolytic manganese anolyte. The method comprises the following steps of: S1, adding iron powder into the electrolytic manganese anolyte with the amount of the iron powder of 100-400mg.L<-1>, stirring at the stirring speed of 300-600r / min<-1>, reacting at the reaction temperature of 30-90 DEG C for 50-120 min, filtering and taking filter residue; and S2, drying the filter residue at 40-100 DEG C, then putting the filter residue into a container, adding hydrogen peroxide with the amount of 3.5-6 L per kilograms of selenium slag, adding sulfuric acid with the amount of 0-1.5 L per kilograms of selenium slag, reacting at the reaction temperature of 70-90 DEG C for 80-130 min, filtering after completing reaction, and enabling filtrate to return for the production of electrolytic manganese. The selenium in the anolyte can be recycled relatively well, the emission of the selenium in electrolytic manganese waste residue can be greatly reduced while economic benefits are gained, and the environment pollution caused by the selenium is reduced.

Description

technical field [0001] The invention relates to the technical field of electrolytic manganese, in particular to a method for recovering selenium from electrolytic manganese anolyte. Background technique [0002] As an important metallurgical and chemical raw material, electrolytic manganese has a very important strategic position in the national economy. At present, my country's annual output of electrolytic manganese metal is about 1.2 million tons, ranking first in the world in production and sales. The production process of electrolytic manganese metal mainly includes: manganese ore leaching → impurity removal → filter pressing → electrolysispassivation → stripping → drying and other processes. About 45 tons of anolyte are produced in the electrolysis process for every ton of electrolytic manganese metal product produced. Since the anolyte contains a certain concentration of sulfuric acid and manganese ions, the anolyte is usually sent back to the manganese ore leach...

Claims

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Application Information

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IPC IPC(8): C01B19/02C01G49/14C25C1/10
CPCC01B19/02C01G49/14C25C1/10Y02P10/20
Inventor 黄冠汉刘春明明宪权陈南雄吴晓丹陈发明杨勇李春霞谢彦韦婷婷覃燕玲黄海岛
Owner DAXIN MANGANESE MINE BRANCH OF CITIC DAMENG MINING IND