Roasting-free evaporation-free method for producing cupric sulfate from zinc hydrometallurgy acid-wash copper dross
A technology for hydro-smelting zinc and copper sulfate, which is applied in the direction of copper sulfate and the improvement of process efficiency, can solve the problems of increased production cost, rising raw material cost, complicated operation, etc., and achieves water consumption saving, fast production speed, and utilization rate. high effect
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Embodiment 1
[0026] (1) Store 1.82t of pickling copper slag for 1 day, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of zinc hydrometallurgy solution, and the copper content The phase is elemental metal copper or copper metal compound, containing more than 38.71wt% copper (total copper);
[0027] (2) Using a sulfuric acid solution with a concentration of 250g / L as a leaching agent, the pickling copper slag oxidized in step (1) was leached for 2.5 hours at 100°C with a solid-to-liquid ratio of 1:6 to obtain a slurry;
[0028] (3) Filter the leached slurry obtained in step (2) at 100°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching 5 times until Copper (total copper) in leaching slag is less than 1wt%;
[0029] (4) The leaching solution obtained in step (...
Embodiment 2
[0032] (1) Store 2.75 tons of pickling copper slag for 3 days, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of the zinc hydrometallurgy solution, and the copper content The phase is simple metal copper or copper metal compound, containing 33.52wt% copper (total copper);
[0033] (2) Using a sulfuric acid solution with a concentration of 150g / L as a leaching agent, leaching the acid-washed copper slag oxidized in step (1) for 0.5 hours at 92°C with a solid-to-liquid ratio of 1:5 to obtain a slurry;
[0034] (3) Filter the leached slurry obtained in step (2) at 92°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching three times until leaching Copper (total copper) in slag is less than 1wt%;
[0035](4) The leaching solution obtained in step (3) ...
Embodiment 3
[0038] (1) Store 2.79 tons of pickling copper slag for 5 days, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of the zinc hydrometallurgy solution, and the copper content The phase is elemental metal copper or copper metal compound, containing more than 34.06wt% copper (total copper);
[0039] (2) Using a sulfuric acid solution with a concentration of 250g / L as a leaching agent, leaching the acid-washed copper slag oxidized in step (1) for 1 hour at 80°C with a solid-to-liquid ratio of 1:4 to obtain a slurry;
[0040] (3) Filter the leached slurry obtained in step (2) at 80°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching three times until leaching Copper (total copper) in slag is less than 1wt%;
[0041] (4) The leaching solution obtained i...
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