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Method for improving cadmium recovery through acid dissolution of cadmium sponge

A cadmium cotton and acid-soluble technology, which is applied in the field of improving cadmium recovery from cadmium cotton acid dissolution, can solve the problems of reducing the purity of recovered metal cadmium, hindering the cadmium ion replacement reaction, and reducing the economic benefits of enterprises. It is not easy to reduce the zinc content exceeding the standard. The effect of compaction, reduction of replacement and scrapping rate, and good social benefits

Pending Publication Date: 2021-06-01
BAIYIN NONFERROUS GROUP
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  • Summary
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] In the hydrometallurgical electrolytic zinc industry, a large amount of purified slag is produced in the pre-electrolyte electrolytic liquid preparation section, especially the pressure filtration of multiple purification processes. The purified slag contains high-grade cadmium. The purified slag has undergone pulping, chemical leaching and Impurity removal and purification to make a high-cadmium solution; at present, most electrolytic zinc enterprises adopt the mixed-phase replacement reaction mode. During the replacement reaction, a large amount of reducing agent zinc powder is wrapped by sponge cadmium, which cannot be completely reacted, resulting in zinc powder consumption during the replacement reaction. Too high, the product sponge cadmium purity is low, the product quality is reduced, and the economic benefit of the enterprise is reduced
[0003] At present, the traditional cadmium recovery method mainly uses zinc powder as the reducing agent, and the reducing agent is added to the high-cadmium solution that is constantly stirred to recover the metal cadmium. The research shows that as the reaction progresses, the pH value of the solution rises, and the zinc powder A passivation film is formed on the surface, which hinders the further progress of the replacement reaction between metal zinc and cadmium ions in the solution, resulting in the incomplete reaction of some zinc powders with large particles, and the residual metal zinc is wrapped by the generated metal cadmium, and finally sinks to the bottom of the reaction tank Mixed into the product metal cadmium, the consumption of zinc powder is large and the purity of recovered metal cadmium is reduced. How to quickly and efficiently replace the cadmium ions in the solution has important environmental and economic significance

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] This embodiment is a method for recycling zinc and cadmium from copper-cadmium slag. The main components in copper-cadmium slag are: Zn: 37.6%, Cu: 6.4%, and Cd: 17.2%.

[0024] After the copper cadmium slag is pulped by ball milling, it is transported to the thickener for liquid-solid separation. After the liquid-solid separation, 20m 3 (liquid-solid ratio 2:1) pump into the leaching tank, add copper cadmium slag pickling pulp filtrate to 30m3; turn on steam to heat to 90 ° C, and slowly add concentrated sulfuric acid, when the pH of the pulp is ≤ 2.5, stop adding acid, the reaction process When the pH value rises to 3.5, add concentrated sulfuric acid until the pH value is 2.5, stop adding acid, repeat the above adding process of concentrated sulfuric acid, when the pH value of the pulp is stable between 2.5-3.5 for 30 minutes, the copper cadmium slag is ended For leaching operation, the final pH value of the pulp is 3.0, and the whole leaching process lasts for 7 hou...

Embodiment 2

[0029] In this embodiment, the method for recycling copper and cadmium from copper cadmium slag, the main components in the copper wool are: Zn: 36.8%, Cu: 6.3%, Cd: 14.8%.

[0030] After the copper cadmium slag is pulped by ball milling, it is transported to the thickener for liquid-solid separation. After the liquid-solid separation, 20m 3(liquid-solid ratio 2:1) pump into the leaching tank, add copper cadmium slag pickling pulp filtrate to 35m3; open steam to heat to 85°C, and slowly add concentrated sulfuric acid, when the pH of the pulp is ≤ 2.5, stop adding acid, the reaction process When the pH value rises to 3.5, add concentrated sulfuric acid until the pH value is 2.5, stop adding acid, repeat the above process of adding concentrated sulfuric acid, when the pH value of the pulp is stable between 2.5-3.5 for 40 minutes, the copper cadmium slag is ended For leaching operation, the final pH value of the slurry is 2.5, and the whole leaching process lasts for 6 hours to o...

Embodiment 3

[0035] This embodiment is a method for recycling copper and cadmium from copper-cadmium slag. The main components in copper-cadmium slag are: Zn: 36.3%, Cu: 6.2%, and Cd: 16.5%.

[0036] After the copper cadmium slag is pulped by ball milling, it is transported to the thickener for liquid-solid separation. After the liquid-solid separation, 20m 3 (liquid-solid ratio 2:1) pumped into the leaching tank, add copper cadmium slag pickling pulp filtrate to 40m 3 Turn on steam and heat to 80°C, and slowly add concentrated sulfuric acid at the same time, when the pH of the pulp is ≤ 2.5, stop adding acid, when the pH value rises to 3.5 during the reaction, add concentrated sulfuric acid until the pH value is 2.5, stop adding acid, Repeat the above process of adding concentrated sulfuric acid. When the pH value of the pulp is stable between 2.5-3.5 for 40 minutes, the copper-cadmium slag leaching operation is ended. The final pH value of the pulp is 3.5. The entire leaching process las...

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Abstract

The invention belongs to the technical field of recycling of by-products of smelting engineering, and particularly relates to a method for improving cadmium recovery through acid dissolution of cadmium sponge. In the method for improving cadmium recovery through acid dissolution of the cadmium sponge, a copper and cadmium slag system is a system for mainly producing crude cadmium, copper slag and a lean cadmium solution with copper and cadmium slag generated from first-stage purification and second-stage purification of a purification system as a main raw material, wherein main components of the copper and cadmium slag are zinc, copper and cadmium, by adopting the principles that zinc, cadmium and compounds of zinc and cadmium are soluble in sulfuric acid, copper is not soluble in sulfuric acid, cadmium is substituted with zinc powder, and the like, the zinc, the copper and the cadmium in the copper and cadmium slag are recovered, the cadmium is substituted with the zinc powder, and is subjected to crude smelting in a metal form to produce the crude cadmium for sale, while the copper is enriched in the slag in a metal form, and is transferred to a copper company for recovery, and the produced lean cadmium solution is reacted with nickel and cobalt slag. By means of the method for improving cadmium recovery through acid dissolution of the cadmium sponge, loss of the metal cadmium in the cadmium sponge is reduced, a scrap rate of substitution of the cadmium sponge is reduced, the problems that during crude smelting of cadmium briquettes, briquetting is hard due to standard exceeding of a zinc content, material consumption is large during crude smelting, and the like are solved, and the copper and cadmium slag is recycled, so that stacking and storage of the copper and cadmium slag are reduced.

Description

technical field [0001] The invention belongs to the technical field of recovery and utilization of smelting engineering by-products, and in particular relates to a method for improving recovery of cadmium from cadmium acid solution. Background technique [0002] In the hydrometallurgical electrolytic zinc industry, a large amount of purified slag is produced in the pre-electrolyte electrolytic liquid preparation section, especially the pressure filtration of multiple purification processes. The purified slag contains high-grade cadmium. The purified slag has undergone pulping, chemical leaching and Impurity removal and purification to make a high-cadmium solution; at present, most electrolytic zinc enterprises adopt the mixed-phase replacement reaction mode. During the replacement reaction, a large amount of reducing agent zinc powder is wrapped by sponge cadmium, which cannot be completely reacted, resulting in zinc powder consumption during the replacement reaction. If it ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B17/00C22B3/46C22B3/08
CPCC22B7/007C22B17/04C22B3/46Y02P10/20
Inventor 冶玉花王普公苟有强焦晓斌马菲菲段小维赵贵俊崔耀
Owner BAIYIN NONFERROUS GROUP
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