Oxidative pressure acid leaching method for processing purified waste residue in zinc hydrometallurgy process
A hydrometallurgy and oxygen pressure acid leaching technology is applied in the field of heavy metal smelting waste slag, nickel cobalt slag, copper and cadmium slag produced in the dissolution and recovery of zinc hydrometallurgy, and dissolving heavy metal-containing electronic waste, which can solve the cobalt recovery rate. It can improve the metal recovery rate, reduce pollution, and simplify the treatment process.
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Embodiment 1
[0020] Example 1: Copper-cadmium slag produced in zinc hydrometallurgical purification process, containing 10% copper, 15% cadmium, 20% zinc, 0.1% cobalt, and 6% iron.
[0021] Crush the massive slag, grind it to -100 mesh, add water to adjust the slurry, put it into a 2L titanium-lined autoclave, add 300g / L sulfuric acid, and seal it; introduce industrial oxygen until the gauge pressure is 0.4MPa, stir and heat up to 120°C, and keep warm React for 120min.
[0022] The leaching rates of copper, zinc and cadmium are all over 99.5%, the residual copper content in the slag is less than 0.2%, and the iron content in the leaching solution is less than 0.1g / L. It is possible to directly separate and extract valuable metals without iron removal.
Embodiment 2
[0023] Example 2: The nickel-cobalt slag produced in the hydrometallurgical purification process contains 40% zinc, 0.1% cadmium and cobalt, and 6% iron.
[0024] Crush the slag, grind it to -100 mesh, add water to adjust the slurry, put it into a 2L titanium-lined autoclave, add 300g / L sulfuric acid, and seal it; introduce industrial oxygen to a gauge pressure of 0.4MPa, stir and heat up to 120°C, and keep warm for reaction 120min.
[0025] The leaching rates of zinc, cadmium and cobalt are all over 99.9%, the total content of residual zinc, cadmium and cobalt heavy metals in the slag is less than 0.1%, and the iron content in the leaching solution is less than 0.1g / L. It is possible to directly separate and extract valuable metals without iron removal.
Embodiment 3
[0026] Example 3: Copper-cadmium slag produced in zinc hydrometallurgical purification process, containing 11% copper, 12% cadmium, 26% zinc and 7% iron.
[0027] Crush the massive slag, grind it to -100 mesh, add water to adjust the slurry, put it into a 2L titanium-lined autoclave, add 300g / L sulfuric acid, and seal it; introduce industrial oxygen until the gauge pressure is 0.2MPa, stir and heat up to 130°C, and keep warm React for 150min.
[0028] The leaching rates of copper, zinc and cadmium are all above 99.5%, the residual copper content in the slag is less than 0.1%, and the iron content in the leaching solution is less than 0.1g / L.
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