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
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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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