Method for increasing copper recovery rate in zinc hydrometallurgy process
A technology for hydrometallurgical zinc smelting and recovery rate, applied in the field of metal smelting, can solve the problems of copper easily sinking into leaching slag and low recovery rate, and achieve the effects of increasing waste residue, improving recovery rate, and simple process operation procedures
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Embodiment 1
[0032] a) Oxidative leaching of zinc concentrate by using electroplating waste solution.
[0033] The weight percentage content of the zinc concentrate is: Zn50%, S32%, Fe10%, Cu2.8%.
[0034] The chemical composition of the waste liquid is: H 2 SO 4 210g / L, Zn 2+ 58g / L, Mn 2+ 6g / L, when mixed with pre-neutralized reflux underflow, H 2 SO 4 The concentration is controlled at 100g / L, and the amount of zinc concentrate is 70g / L.
[0035] The leaching temperature is 95 ℃ ~ 102 ℃, and the 120Nm 3 / t zinc concentrate, the volume percentage is 98% oxygen, and the leaching time is 30h.
[0036] The composition of the leachate obtained is: Zn 2+ 133g / L, H 2 SO 4 24g / L, Cu 2+ 1.8g / L, Fe 3+ 10.3g / L, Fe 2+ 4.2g / L.
[0037] b) performing reduction treatment on the leaching solution, the leaching temperature is 80° C., and the leaching time is 4 hours. The solution contains H during pre-neutralization 2 SO 4 24g / L, time 2.5h, end point pH value 2.3. The chemical compositi...
Embodiment 2
[0042] a) Oxidative leaching of zinc concentrate by using electroplating waste solution.
[0043] The weight percent content of the zinc concentrate is: Zn41%, S32%, Fe8%, Cu1.2%.
[0044] The chemical composition of the waste liquid is: H 2 SO 4 210g / L, Zn 2+ 58g / L, Mn 2+ 6g / L, when mixed with pre-neutralized reflux underflow, H 2 SO 4 The concentration is controlled at 90g / L, and the amount of zinc concentrate is 120g / L.
[0045] The leaching temperature is 95 ℃ ~ 102 ℃, and the 110Nm 3 / t zinc concentrate, the volume percentage is 98% oxygen, and the leaching time is 28h.
[0046] The composition of the leachate obtained is: Zn 2+ 130g / L, H 2 SO 4 18g / L, Cu 2+ 1.3g / L, Fe 3+ 11g / L, Fe 2+ 5.1g / L.
[0047] b) Perform reduction treatment on the leaching solution, the leaching temperature is 90°C, and the leaching time is 3.5h. The solution contains H during pre-neutralization 2 SO 4 18g / L, time 3h, end point pH value 2.5. The chemical composition of the soluti...
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