Method for recycling copper from copper-steel back bimetal waste through wet process
A metal scrap and bimetallic technology, which is applied to the improvement of process efficiency, photographic technology, instruments, etc., can solve the problems of serious loss of steel materials, environmental pollution, etc., and achieve the effect of short process, environmental friendliness and low operating cost
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Embodiment 1
[0021] (1) Use a degreasing agent to remove the residual oil stains on the surface of the copper-steel back bimetal scrap;
[0022] (2) Dissolve a certain amount of copper sulfate in water, and then 2+ : NH 3 = 1:7 ratio of ammonia water was added to make cuproammonia solution, and then a certain amount of ammonium sulfate was added to obtain Cu 2+ Concentration is 1.2mol / L, (NH 4 ) 2 SO 4 Leaching solution with a concentration of 1.0mol / L;
[0023] (3) Put the degreased metal scraps in the leaching solution. During the leaching process, an appropriate amount of air is introduced, and the leaching temperature is 40°C. After the leaching is completed, the remaining scrap steel is taken out, and the leaching solution is properly treated as the electrolyte for the next process;
[0024] (4) Add gelatin to the above leaching solution at a concentration of 20mg / L, mix well and place it in the electrolytic cell as an electrolyte, adjust the pH value of the solution to be betwe...
Embodiment 2
[0029] (1) Use a degreasing agent to remove the residual oil stains on the surface of the metal scrap;
[0030] (2) According to Cu 2+ : NH 3 = 1:6 ratio of ammonia water was added to the copper sulfate solution, and then a certain amount of ammonium sulfate was added to obtain Cu 2+ The concentration is 1.0mol / L, (NH 4 ) 2 SO 4 Leaching solution with a concentration of 0.8mol / L;
[0031] (3) Put the degreased metal scrap in the leaching solution. During the leaching process, an appropriate amount of air is introduced, and the leaching temperature is 50°C. After the leaching is completed, the remaining scrap steel is taken out, and the leaching solution is properly treated as the electrolyte for the next process;
[0032] (4) Add thiourea with a content of 50 mg / L to the above leaching solution, mix well and place it in the electrolytic cell as an electrolyte, adjust the pH value of the solution to be between 9 and 11, use stainless steel as the cathode, and graphite as t...
Embodiment 3
[0037] (1) Use a degreasing agent to remove the residual oil stains on the surface of the metal scrap;
[0038] (2) According to Cu 2+ : NH 3 = 1:5 ratio of ammonia water is added to the copper sulfate solution, and then a certain amount of ammonium sulfate is added to obtain Cu 2+ The concentration is 0.8mol / L, (NH 4 ) 2 SO 4 Leaching solution with a concentration of 0.5mol / L;
[0039] (3) Put the degreased metal scraps in the leaching solution. During the leaching process, an appropriate amount of air is introduced, and the leaching temperature is 60°C. After the leaching is completed, the remaining scrap steel is taken out, and the leaching solution is properly treated as the electrolyte for the next process;
[0040] (4) Add β-naphthol with a content of 30mg / L to the above leaching solution, mix well and place it in the electrolytic cell as an electrolyte, adjust the pH value of the solution between 9 and 11, use stainless steel as the cathode, and graphite as the ano...
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