A comprehensive recovery method for preferentially extracting copper in hydrometallurgy of copper-bismuth-containing materials
A technology of hydrometallurgy and recovery method is applied in the direction of improving process efficiency, etc., to achieve high copper leaching rate, good leaching effect, and better copper-bismuth separation effect.
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Embodiment 1
[0022] (1) Crushing and grinding the copper-bismuth-containing materials produced in the lead anode slime pyrometallurgy process, and then sieving to below 100 mesh.
[0023] (2) Weigh 160g of the sieved material, add 800ml of sulfuric acid solution with a NaCl concentration of 20g / L, and the initial sulfuric acid concentration is 100g / L; heat to 70°C for leaching reaction for 2h, detect the change of pH value during the leaching process, and pass periodic Dilute sulfuric acid solution is added to adjust the pH value of the leaching end point to about 3.0; after leaching is completed, solid-liquid separation is carried out to obtain leaching liquid and leaching residue.
[0024] After testing: the copper content of the leaching slag is 0.75%, and the copper leaching rate is 98.13%; the bismuth content of the leaching solution is lower than 1g / L.
[0025] (3) The leaching solution obtained in step (2) is tested for copper content and replaced with iron powder to recover copper,...
Embodiment 2
[0031] (1) Crushing and grinding the copper-bismuth-containing materials produced in the lead anode slime pyrometallurgy process, and then sieving to below 100 mesh.
[0032] (2) Weigh 160g of the sieved material, add 700ml of sulfuric acid solution with a NaCl concentration of 25g / L, and the initial sulfuric acid concentration is 100g / L; heat to 80°C for leaching reaction for 2h, detect the change of pH value during the leaching process, and pass periodic Supplement dilute sulfuric acid solution to adjust the pH value of the leaching end point to about 4.0; perform solid-liquid separation after leaching to obtain leaching liquid and leaching residue.
[0033] After testing: the copper content of the leaching slag is 0.66%, and the copper leaching rate is 98.81%; the bismuth content of the leaching solution is lower than 1g / L.
[0034] (3) The leaching solution obtained in step (2) is replaced with excess iron powder to recover copper.
[0035] (4), The leaching residue obtai...
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