A method for recycling copper and cadmium from copper cadmium slag
A technology of copper cadmium slag and copper slag, which is applied in the field of recycling of smelting engineering by-products, can solve the problems of resource waste, environmental protection burden, etc., and achieve the effects of reducing costs, reducing stacking and storage, and good economic benefits
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Embodiment 1
[0019] This embodiment is a method for recycling copper and cadmium from copper-cadmium slag. The main components in copper-cadmium slag are: Zn: 37.6%, Cu: 5.8%, and Cd: 15.3%.
[0020] (1) Copper and cadmium slag is ball milled and transported to the thickener for liquid-solid separation. After liquid-solid separation, 20m of thickener bottom flow slag is 3 (Liquid to solid volume ratio 2:1) pump into the leaching tank, add copper cadmium slag pickling pulp filtrate to 27m 3 Turn on the steam and heat to 90°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 at 2.5-3.5 for 30 minutes, the copper cadmium slag leaching operation is ended. The final pH value of the pulp is 3.0. The whole l...
Embodiment 2
[0025] This embodiment is a method for recycling copper and cadmium from copper-cadmium slag. The main components in copper-cadmium slag are: Zn: 36.8%, Cu: 6.3%, and Cd: 14.8%.
[0026] (1) Copper and cadmium slag is ball milled and transported to the thickener for liquid-solid separation. After liquid-solid separation, 20m of thickener bottom flow slag is 3 (Liquid to solid volume ratio 2:1) pump into the leaching tank, add copper cadmium slag pickling pulp filtrate to 33m 3 Turn on the steam and heat to 85°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 2.5. The en...
Embodiment 3
[0031] This embodiment is a method for recycling copper and cadmium from copper-cadmium slag. The main components in copper-cadmium slag are: Zn: Zn: 38.1%, Cu: 5.6%, and Cd: 15.6%.
[0032] (1) Copper and cadmium slag is ball milled and transported to the thickener for liquid-solid separation. After liquid-solid separation, 20m of thickener bottom flow slag is 3 (Liquid to solid volume ratio 2:1) pump 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 en...
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