Comprehensive recovery method for zinc, nickel and cobalt-containing purification slag
A recovery method and sodium hydroxide technology are applied in the direction of improving process efficiency, photographic technology, instruments, etc., and can solve the problems of difficult separation and extraction, complicated separation of nickel and cobalt, etc.
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Embodiment 1
[0017] Example 1: An enterprise's high-temperature zinc powder replacement nickel and cobalt purification slag in hydro-zinc smelting contains 30-40% zinc, 0.8-2.5% nickel, and 0.5-1.5% cobalt. After washing with hot water at 60-70℃ for 3 times, the last washing solution contains 0.85g / L sulfate, and then the liquid-solid mass ratio is 4:1, the leaching temperature is 90-95℃, and the sodium hydroxide concentration is 165- Leach 2 times under 170g / L condition. The one-time leaching solution contains zinc 37.5-43.5g / L, cobalt 0.8-1.3g / L, and sodium hydroxide concentration 152g / L; twice zinc-containing 18-25g / L, cobalt 0.3-0.5g / L, sodium hydroxide The concentration is 160g / L. The alkali leaching residue contains 5-12% nickel, the total leaching rate of zinc is 95.2%, and the total leaching rate of cobalt is 86.3%. The primary alkaline immersion solution is placed in a magnetic field for electrolysis. The condition is that two permanent magnets are installed on both sides of the ...
Embodiment 2
[0018] Example 2: According to the leaching conditions of Example 1, use the raw materials of Example 1 and the second leaching solution for one leaching. The electrolytic residue is used for the second leaching. The first leaching solution contains 46-52g / L zinc and 1.2 cobalt. -1.8g / L, the concentration of sodium hydroxide is 158g / L. The second leaching solution contains 20-25g / L zinc, 0.7-0.8g / L cobalt, and 15.82% nickel in the leaching residue. The total leaching rate of zinc is 96.8%, and the total leaching rate of cobalt is 90.5%. Electromagnets are installed on both sides of the electrolytic cell, the magnetic field intensity H is 100A / m, and the anode is a permanent magnet, and the magnetic field intensity H generated by it is 20A / m. The remaining electrolysis conditions were the same as in Example 1. The electrolysis 36h collected cathode metal zinc powder, total zinc 99.1%, metal zinc 99.54%, 120h collected anode slime cobalt slag, containing 26.5% cobalt. The curre...
Embodiment 3
[0019] Example 3: Use nitroso β-naphthol to remove cobalt agent to purify nickel and cobalt in zinc sulfate solution to obtain organic nickel and cobalt slag. Nickel and cobalt cannot be leached with sodium hydroxide solution, and it is obtained by calcination above 500°C for 2 hours The calcined slag containing 30-40% nickel and 15-20% cobalt is leached with 160-200g / L sodium hydroxide solution to obtain a primary leachate containing 15-22g / L cobalt, and the leaching residue contains 52.5% nickel. Co(OH) was performed under the electromagnetic field conditions of Example 2 4 2- The electrochemical anodic oxidation, the cobalt slag obtained from the anode slime contains 35-45% cobalt, and the nickel and cobalt are separated and enriched.
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