Method for recycling copper from basic waste etching liquid
A technology for recovering copper from waste etching solution, applied in the field of copper recovery, can solve the problems of low copper extraction rate, high copper content in mother liquor, low copper powder efficiency, etc., and achieves good separation effect, low oxygen content, and copper extraction rate. high effect
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Embodiment 1
[0013] A certain alkaline waste etching solution, wherein pH is 7.7, copper ion 6g / L and a large amount of chloride ion; 10%Lix84-I: 5%N235 extractant and: the organic phase of 85% kerosene and alkaline waste etching solution by volume The ratio is 2:1 three-stage extraction. After extraction, the concentration of copper in the waste water is 0.10mg / L, and the extraction rate of copper is calculated to be 99%. : 1 three-stage washing, after washing, compare the loaded organic phase with the copper sulfate solution containing 140g / L of sulfuric acid and 8g / L of copper ions in a volume ratio of 8:1 for secondary stripping, after stripping, the organic phase returns Repeated use, the water phase is copper sulfate solution, the current density is 105A / m 2 Electrolytic copper was obtained by electrodeposition on stainless steel 316 cathode, the purity of electrolytic copper was 99.95%, and the copper sulfate solution containing 140g / L sulfuric acid and 8g / L copper ions after electr...
Embodiment 2
[0015] A certain alkaline waste etching solution, wherein the pH is 8.7, copper ions 140g / L and a large amount of chloride ions; 5% Lix973: 15% N235 extractant and: 80% 200 # The organic phase of the solvent oil and the alkaline waste etching solution are first-stage extracted at a volume ratio of 25:1. After the extraction, the analysis shows that the copper concentration in the waste water is 3.50mg / L, and the copper extraction rate is calculated to reach 99%. Then the loaded organic Phase and [H + ]=1.5mol / L dilute sulfuric acid solution by volume ratio is 5:1 secondary washing, after washing, the load organic phase and copper sulfate solution containing sulfuric acid 235g / L, copper ion 20g / L are by volume ratio 6:1 Compared with secondary stripping, after stripping, the organic phase is returned for reuse, and the aqueous phase is copper sulfate solution, at a current density of 200A / m 2 Under the conditions, stainless steel 304 cathodic electrodeposition obtains electrol...
Embodiment 3
[0018] A certain alkaline waste etching solution, wherein pH is 9, copper ion 160g / L and a large amount of chloride ion; 5%Lix984 extractant: 5%N235 extractant and: the organic phase of 90% kerosene and alkaline waste etchant by volume Ratio is 25: 1 first stage extraction, after extraction analysis records the copper concentration in the waste water is 5.50mg / L, and copper extraction rate reaches 99% through calculation; Then load organic phase and [H + ]=0.3mol / L dilute sulfuric acid solution by volume ratio is 0.2:1 first stage washing, after washing, the load organic phase and copper sulfate solution containing sulfuric acid 200g / L, copper ion 30g / L by volume ratio are 4:1 Compared with secondary stripping, after stripping, the organic phase is returned for reuse, and the aqueous phase is a copper sulfate solution, at a current density of 300A / m 2 Under the following conditions, electrolytic copper is obtained by cathodic electrodeposition of metal titanium plates, and the...
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