A method for purifying and removing copper from zinc sulfate leaching solution
A technology of leachate and zinc sulfate, applied in the direction of improving process efficiency, can solve the problems of long process route, high energy consumption, isolated method and process, etc., and achieve the effect of simple process flow and low consumption
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Embodiment 1
[0040] Pass the zinc sulfate leaching solution with chemical composition Zn150.70g / L, Cu0.95g / L, Fe0.15g / L, As0.25g / L, Sb0.71g / L with excess tinned copper scrap figure 1 After the process flow is purified, the copper-removing zinc sulfate leaching solution (Cu0.32g / L, As0.05 g / L, Sb0.03g / L, Fe0.04g / L) is obtained. There is no residual tin on the surface of the detinned copper scrap, the sponge copper contains less than 0.3% tin, the purification slag contains Sn18.72%, As1.57%, Fe1.4%, and the Cu content in the purification slag is less than 0.2%;
[0041] Wherein, each percentage represents the mass percentage content.
Embodiment 2
[0043]Take the zinc sulfate leaching solution whose chemical composition is Zn140.57g / L, Cu1.17g / L, As1.8g / L, Sb1.27g / L, Fe1.3g / L, use excessive tin-plated waste copper electronic feet, pass figure 1 After purification of the process flow, a copper-removing zinc sulfate leaching solution (Cu0.08g / L, As0.07g / L, Sb0.03g / L, Fe0.01g / L) was obtained. Detinning waste copper electronic pins are completely detinned, the sponge copper contains tin<0.3%, the purification slag contains Sn13.77%, As1.0%, Sb0.83%, and the purification slag Cu content is less than 0.2%;
[0044] Wherein, each percentage represents the mass percentage content.
Embodiment 3
[0046] Get the zinc sulfate leaching solution that the chemical composition is Zn137.07g / L, Cu1.03g / L, Sb0.97g / L, As1.12g / L, Fe1.12 g / L, with excessive tinning waste copper wire, through Fig. 1 After purification of the technological process, the copper-removing zinc sulfate leaching solution (Cu0.11g / L, As0.009 g / L, Sb0.27g / L, Fe0.51g / L) is obtained, and the detinning waste copper wire has no apparent residual tin, and the sponge Copper contains tin<0.3%, purification slag contains Sn17.78%, As0.98%, Sb0.57%, Fe1.7%, and purification slag Cu content is less than 0.3%;
[0047] Wherein, each percentage represents the mass percentage content.
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