A method for removing arsenic by leaching materials containing germanium and gallium
A leaching and material technology, applied in the field of arsenic-containing materials, can solve the problems of high content, affecting the quality of germanium and gallium enrichment, and low leaching rate of germanium
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Embodiment 1
[0032] 1) Atmospheric pressure oxidation leaching reaction
[0033] Add arsenic-containing materials: cobalt-copper-iron alloy materials containing germanium and gallium (containing germanium 3625g / t, gallium 763g / t, arsenic 1923g / t), sulfuric acid and compressed air into the stirring tank, atmospheric pressure oxidation leaching conditions: temperature 85 °C, react for 24 hours, and end-point sulfuric acid concentration of 10g / L, and obtain the first leaching liquid and the first leaching residue through solid-liquid separation.
[0034] Adjust the pH value of the above-mentioned first leaching solution to 1.5 with magnesium oxide, and perform conventional copper extraction to recover copper to obtain the extract and stripping solution. The stripping solution is subjected to the first electrowinning to recover the first copper. After electrowinning at this time The liquid is not taken out to continue the first electrowinning; the aforementioned extract is partially returned t...
Embodiment 2
[0044] 1) Atmospheric pressure oxidation leaching reaction
[0045] Add arsenic-containing materials: including germanium-gallium-containing cobalt-copper-iron alloy materials (containing germanium 2300g / t, gallium 450g / t, arsenic 1450g / t), sulfuric acid, and compressed air into the stirring tank, atmospheric pressure oxidation leaching conditions: The temperature was 75°C, the reaction was 32 hours, the final sulfuric acid concentration was 15g / L, and the first leaching solution and the first leaching residue were obtained through solid-liquid separation.
[0046] Adjust the pH value of the above first leaching solution to 1.5 with magnesium oxide, perform copper extraction to recover copper, obtain the extract and raffinate, and recover the first copper by electrowinning the extract. The first electrowinning; part of the aforementioned extract returns to participate in normal pressure oxidation leaching, and the initial solid-liquid mass ratio is adjusted to 1:8.
[0047] 2...
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