A kind of copper soot roasting strengthened leaching method
A technology for strengthening leaching and copper soot, applied in the field of non-ferrous metal metallurgy, can solve the problems of complex composition, difficulty in effectively leaching soot, and little research on soot treatment methods, and achieves low production cost, prevention of sintering phenomenon, and low labor intensity.
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Embodiment 1
[0026] The main components of the soot produced during the smelting process of the copper concentrate Osmelt furnace melting pool of a domestic enterprise are (%): Pb28.69, Cu3.37, Zn15.54, As2.61, Bi3.72 and S14.72. The mass percentage of industrial grade sulfuric acid is not less than 98.0%.
[0027]Copper smelting soot is mixed with sulfuric acid solution to adjust the slurry, the liquid-solid ratio (the ratio of liquid volume L to solid weight kg) is controlled to be 3:1, the pH value of the mixed slurry is controlled to be 2.0, and the temperature of the mixed slurry is kept at 80°C. After reacting for 90 minutes at a stirring speed of 300r / min, liquid-solid separation was achieved by means of plate-and-frame filter press. The slag rate obtained in one-stage leaching process was 64.06%, and the contents of copper and zinc were 3.88% and 8.37%, the leaching rates of zinc and copper are 65.50% and 26.25% respectively; after drying, the sulfuric acid primary leaching residu...
Embodiment 2
[0029] The main components of the soot produced during the smelting process of a copper concentrate oxygen-enriched bottom blowing furnace molten pool in a domestic enterprise are (%): Pb24.73, Cu15.68, Zn4.13, As10.14, Bi2.63 and S10.71. The mass percentage of industrial grade sulfuric acid is not less than 98.0%.
[0030] Bottom-blowing furnace soot and sulfuric acid solution are mixed to adjust the slurry, the liquid-solid ratio (the ratio of liquid volume L to solid weight kg) is controlled to be 3:1, the pH value of the mixed slurry is controlled to 2.0, and the temperature of the mixed slurry is kept at 80°C. After reacting for 90 minutes at a stirring speed of 300r / min, liquid-solid separation was achieved by means of plate and frame filtration. The slag rate obtained in the primary sulfuric acid leaching process was 48.64%, and the contents of copper and zinc after the primary leaching slag were dried were 10.52%. and 2.85%, the leaching rates of copper and zinc were ...
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