Technological method for comprehensively recovering valued metal such as indium and germanium from lead-zinc smoke
A process method and valuable metal technology, applied in the field of hydrometallurgy, can solve the problems of low comprehensive recovery rate, low resource utilization rate and high recovery cost
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Embodiment 1
[0023] Embodiment 1: A kind of lead-zinc fume, its chemical composition is listed in the following table 1.
[0024] Table 1 :
[0025] chemical composition lead% Zinc % germanium% indium% Silver ug / g arsenic% content 42.14 32.04 1.275 0.36 327 4.65
[0026] (1) Weigh 200kg of lead-zinc dust, containing 42.14% lead, 32.04% zinc, 1.275% germanium, 0.36% indium, and 327g / t silver, and add 60kg of industrial Sulfuric acid, 200kg of water, start stirring, the rotating speed is 115 rev / min, after heating, stirring, aging and leaching for 1h, then add 300kg of water, under the condition of starting stirring, slowly add 200kg of hydrogen peroxide, after adding, heat up to 80-85°C, leaching for 4 hours, using a filter press to separate the solid-liquid residue from the liquid, and washing the leaching residue twice with a dilute sulfuric acid solution with a pH of 1.68. The second leaching was carried out under controlled conditions. After the t...
Embodiment 2
[0030] Embodiment 2: A kind of lead-zinc fume, its chemical composition is listed in the following table 1.
[0031] Table 1 :
[0032] chemical composition lead% Zinc % germanium% indium% Silver ug / g arsenic% content 38.70 21.85 0.47 0.58 187 3.26
[0033] (1) Weigh 200kg of lead-zinc dust, containing 38.70% lead, 21.85% zinc, 0.47% germanium, 0.58% indium, and 187g / t silver, and add 50kg of industrial Sulfuric acid, 200kg of water, start stirring, the rotating speed is 115 rev / min, after heating, stirring, aging and leaching for 1h, then add 400kg of water, under the condition of starting stirring, slowly add 100kg of hydrogen peroxide, after adding, heat up to 80-85°C, leaching for 3 hours, using a filter press to filter and separate the slag liquid, and washing the leaching residue twice with a dilute sulfuric acid solution with a pH of 1.56, transferring the leaching residue to the original leaching reactor, and proceeding according ...
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