Method for recovering copper from acid waste etching solution
A waste etching solution and copper recovery technology, which is applied in the field of copper recovery, can solve the problems of environmental pollution, high copper content in mother liquor, and easy generation of chlorine gas, etc., and achieve good separation effect, low oxygen content, and simple process
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Embodiment 1
[0013] An acidic waste etching solution, in which H + Concentration is 0.012mol / L, copper ion 120g / L and a large amount of chloride ion; The organic phase of 15%Lix84-I-85% kerosene and acid waste etchant are 10: 1 three-stage extraction by volume ratio, after extraction analysis measures The concentration of copper in the waste water is 0.50mg / L, and the copper extraction rate reaches 99% through calculation; then the loaded organic phase and pure water are washed in three stages of 10:1 by volume. After washing, the loaded organic phase is mixed with 130g of sulfuric acid. / L, copper sulfate solution with copper ion 5g / L is 10:1 by volume ratio compared with the secondary stripping, after stripping, the organic phase is returned for reuse, the water phase is copper sulfate solution, and the current density is 55A / m 2 Electrolytic copper was obtained by electrodeposition on stainless steel 316 cathode. The purity of electrolytic copper was 99.95%. After electrodeposited coppe...
Embodiment 2
[0015] An acidic waste etching solution, in which H + The concentration is 1.0mol / L, the copper ion is 140g / L and a large amount of chloride ion; 20% Lix973-80%200 # The organic phase of the solvent oil and the acidic waste etching solution are extracted in a volume ratio of 30:1. After the extraction, the copper concentration in the waste water is measured to be 3.50mg / L, and the copper extraction rate is calculated to reach 99%. Then the loaded organic phase Secondary washing with purified water at a volume ratio of 5:1. After washing, compare the loaded organic phase with a copper sulfate solution containing 245 g / L of sulfuric acid and 10 g / L of copper ions at a volume ratio of 5:1 for 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 200A / m 2 Under the following conditions, stainless steel 304 cathode electrodeposited to obtain electrolytic copper, the purity of elec...
Embodiment 3
[0017] An acidic waste etching solution, in which H + The concentration is 2.9mol / L, the copper ion is 100g / L and a large amount of chloride ion; the organic phase of 5% Lix984 extractant-95% kerosene and the acidic waste etching solution are extracted in a volume ratio of 20:1, and the analysis and measurement after extraction The concentration of copper in the waste water is 5.50mg / L, and the extraction rate of copper is calculated to be 99%; then the loaded organic phase and pure water are washed in the first stage at a volume ratio of 0.2:1. After washing, the loaded organic phase is mixed with 200g of sulfuric acid. / L, copper sulfate solution with copper ion 30g / L is 5:1 by volume ratio compared with secondary stripping. After stripping, the organic phase is returned for reuse, and the water phase is copper sulfate solution. 2 Under the following conditions, electrolytic copper is obtained by cathodic electrodeposition of metal titanium plates, and the purity of electrol...
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