Method for preparing high pure gold and enriching silver, platinum and palladium from silver anode mud
A silver anode slime and pure gold technology, applied in the direction of improving process efficiency, can solve the problems of low recovery rate, many equipment, long process flow, etc., and achieve the effect of increased gold content, high removal rate and simple operation
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Embodiment 1
[0031] In this example, Au62%, Ag27.4%, Pt0.09%, and Pd0.64% in copper-silver anode slime are treated, and the treatment process and treatment effect are as follows:
[0032] (1) Put the silver anode slime in the reaction kettle for nitric acid leaching to separate silver, control the mass concentration of nitric acid solution to 25%, the liquid-solid ratio according to the volume and mass ratio L:Kg is 5:1, the temperature is 90°C, the time is 7h, leaching After filtration, obtain silver-separating liquid and silver-separating slag, Au95.8%, Ag2.4%, Pt0.04%, Pd0.03% in the silver-separating slag;
[0033] (2) Add sodium chloride to the silver separation solution obtained in step (1) for silver precipitation, the temperature is 50-65°C, the time is 0.3-1h, no white precipitate is the reaction end point, and silver chloride precipitation and precipitation are obtained after filtration. Silver liquid;
[0034] (3) Add iron powder to the silver chloride precipitate obtained in s...
Embodiment 2
[0040] Au55.1%, Ag29.8%, Pt0.13%, Pd1.0% in the copper-silver anode slime treated in this example, the treatment process and effect are as follows:
[0041] (1) Put the silver anode slime in the reaction kettle for nitric acid leaching and silver separation, control the mass concentration of nitric acid solution to 25%, the liquid-solid ratio according to the volume and mass ratio L:Kg is 4:1, the temperature is 85°C, the time is 6h, and the leaching After filtration, obtain the silver separation liquid and the silver separation slag, in the silver separation slag, Au90.5%, Ag4.3%, Pt0.05%, Pd0.13%;
[0042] (2) Add sodium chloride to the silver separation solution obtained in step (1) for silver precipitation, the temperature is 50-65°C, the time is 0.3-1h, no white precipitate is the reaction end point, and silver chloride precipitation and precipitation are obtained after filtration. silver liquid;
[0043] (3), the silver chloride precipitate obtained in step (2) is repla...
Embodiment 3
[0049] Au59.3%, Ag29.1%, Pt0.09%, Pd0.69% in the copper-silver anode slime treated in this example, the treatment process and effect are as follows:
[0050] (1) Put the silver anode slime in the reaction kettle for nitric acid leaching to separate silver, control the mass concentration of nitric acid solution to 25%, the liquid-solid ratio according to the volume and mass ratio L:Kg is 3:1, the temperature is 85°C, the time is 6h, and the leaching After filtration, obtain silver-separating liquid and silver-separating slag, Au90.8%, Ag4.3%, Pt0.08%, Pd0.17% in the silver-separating slag;
[0051] (2) Add sodium chloride to the silver separation solution obtained in step (1) for silver precipitation, the temperature is 50-65°C, the time is 0.3-1h, no white precipitate is the reaction end point, and silver chloride precipitation and precipitation are obtained after filtration. silver liquid;
[0052] (3) The silver chloride precipitate obtained in step (2) is replaced by addin...
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