Method for recovering valuable metals from waste copper indium gallium selenide battery chips
A technology of copper indium gallium selenide and valuable metals, which is applied in the field of secondary utilization of resources, can solve problems such as low comprehensive recovery rate, complicated and dangerous operation, and large environmental pollution, and achieve high recovery rate, environmental friendliness, and complete separation effect
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Embodiment 1
[0044] Such as figure 1 As shown, the implementation steps of this embodiment include: taking 50g of CIGS waste battery chips and peeling off the substrate; after the peeled valuable metal layer is sulfuric acid of 500kg / t-waste, carry out sulfuration roasting, the roasting temperature is 200 ° C, The roasting time is 3 hours to obtain crude selenium and slag; the slag is soaked in water, the water immersion temperature is 95°C, the leaching time is 5h, the liquid-solid ratio is 10:1ml / g, the stirring speed is 400rpm, and the water immersion solution is obtained after water immersion and filtration and water leaching slag; water leaching liquid first removes impurities / separation, filters out slag containing zinc, cadmium, aluminum, and the filtrate is recrystallized to obtain copper sulfate; water leaching slag uses a mass concentration of 80% NaOH solution as the leaching agent at normal pressure Under the conditions of alkaline leaching, the leaching temperature of the alka...
Embodiment 2
[0046]The implementation steps of this embodiment include: taking 100g of CIGS waste battery chips and peeling off the substrate; adding 700kg / t-scrap sulfuric acid to the peeled valuable metal layer, and then performing sulfuration roasting, the roasting temperature is 700°C, and the roasting time is 700°C. 0.5h to obtain crude selenium and slag; the slag is soaked in water, the water immersion temperature is 20 ℃, the leaching time is 5h, the liquid-solid ratio is 1:1ml / g, the stirring speed is 200rpm, and the water immersion liquid and Water leaching slag; the water leaching liquid is firstly cleaned of impurities / separation, and the slag containing zinc, cadmium, and aluminum is filtered out, and the filtrate is recrystallized to obtain copper sulfate; The leaching temperature during the leaching process is 30°C, the leaching time is 4.5 hours, and the solid-to-liquid ratio before leaching is 1:5g / mL. After leaching, the alkali leaching solution and alkali leaching residue ...
Embodiment 3
[0048] The implementation steps of this embodiment include: taking 50g of CIGS waste battery chips and peeling off the substrate; adding 100kg / t-scrap of sulfuric acid to the peeled valuable metal layer, and then carrying out sulfuration roasting, the roasting temperature is 500°C, and the roasting time is 500°C. for 3.5h to obtain crude selenium and slag; the slag was soaked in water at a temperature of 70°C for 0.5h, the liquid-solid ratio was 5:1ml / g, and the stirring speed was 600rpm. and water leaching slag; water leaching liquid first removes impurities / separation, filters out slag containing zinc, cadmium, aluminum, and the filtrate is recrystallized to obtain copper sulfate; water leaching slag uses a mass concentration of 50% NaOH solution as the leaching agent at normal pressure Under the conditions of alkaline leaching, the leaching temperature of the alkaline leaching process is 90°C, the leaching time is 3 hours, the solid-liquid ratio before leaching is 1:5g / mL, a...
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