Method for leaching lead by wet method through copper anode slime silver-extracted sediment
A copper anode slime and silver slag separation technology, applied in the field of hydrometallurgy, can solve the problems of easy generation of nitrogen-containing gas, high equipment requirements, poor working environment, etc., achieve efficient and rapid leaching, comprehensive recovery benefits, and processing time short effect
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Embodiment 1
[0014] In the present embodiment, the percentage by weight of lead in the silver slag is 35.3%. Adding concentration to the silver slag is 100g / L of sodium hydroxide solution for slurry mixing. The weight concentration of the slurry is controlled at 10%. In a microwave reaction furnace, the microwave power and frequency are 600kW·MHz·h per kilogram of slurry, and the leaching reaction is carried out under normal pressure for 5 minutes, and then the material is discharged for solid-liquid separation to obtain a lead-containing leaching solution.
[0015] Among them, the leaching rate of lead is 98%.
Embodiment 2
[0017] In the present embodiment, the percentage by weight of lead in the silver-separating slag is 36.2%. Adding concentration to the silver-separating slag is 150g / L sodium hydroxide solution for pulping, and the weight concentration of the control slurry is at 15%. In a microwave reaction furnace, the microwave power and frequency are 650kW·MHz·h per kilogram of slurry, and the leaching reaction is carried out under normal pressure for 10 minutes, and then the material is discharged for solid-liquid separation to obtain a lead-containing leaching solution.
[0018] Among them, the leaching rate of lead is 96%.
Embodiment 3
[0020] In the present embodiment, the percentage by weight of lead in the silver-separating slag is 37.3%. Adding concentration to the silver-separating slag is 200g / L sodium hydroxide solution for pulping, and the weight concentration of the control slurry is at 20%. In a microwave reaction furnace, the microwave power and frequency are 450kW·MHz·h per kilogram of slurry, and the leaching reaction is carried out under normal pressure for 15 minutes, and then the material is discharged for solid-liquid separation to obtain a lead-containing leachate.
[0021] Among them, the leaching rate of lead is 95%.
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