Method for recovering copper and nickel from electroplating sludge
A technology for electroplating sludge and copper recovery, applied in the direction of improving process efficiency, can solve problems such as environmental pollution and waste of non-ferrous metal resources, and achieve the effects of reducing production costs, reducing acid and alkali consumption, and overcoming complex processes
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Embodiment 1
[0018] Mix the electroplating sludge with ammonia nitrogen concentration of 8mol / L and the leaching agent with the ammonia ammonium ratio of 1:2 according to the solid-to-liquid ratio of 1:4 and put them into a flat-bottomed flask. Put the flask in, adjust the stirring speed, set the leaching time to 4h, and collect the leaching solution after the reaction is completed. The collected leachate was adjusted to pH 9.5, then mixed with Lix984 and shaken for 5 minutes. Its recovery rate of copper is 69.3%, and the recovery rate of nickel is 0.18%.
Embodiment 2
[0020] Mix the leaching agent with the concentration of electroplating sludge and ammonia nitrogen at 9mol / L and the ratio of ammonia to ammonium at 1:2 and put it into a flat-bottomed flask at a solid-to-liquid ratio of 1:4. After the water bath magnetic stirrer reaches the preset temperature of 70°C Put the flask in, adjust the stirring speed, set the leaching time to 4h, and collect the leaching solution after the reaction is completed. Adjust the pH value of the collected leachate to 9.5, then mix it with Lix984, shake it for 5 minutes, and then carry out the second-stage extraction. Its copper recovery rate is 89.3% and nickel recovery rate is 5.2%.
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