Valuable metal leaching system and leaching method in a kind of waste lithium battery
A technology for waste lithium batteries and valuable metals, which is applied in battery recycling, waste collector recycling, and process efficiency improvement, to achieve innovative and outstanding advantages, less equipment corrosion, and good application prospects.
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Embodiment 1
[0032] Embodiment 1: the leaching of lithium, cobalt in the waste lithium cobalt oxide battery
[0033] After pretreatment such as dismantling and crushing of waste lithium cobalt oxide batteries, the positive electrode powder is separated. The positive electrode powder contains 5.37% Li and 57.73% Co, mainly LiCoO 2 Morphological existence ( figure 1 ). Prepare 100mL sulfamic acid-glucose mixed solution (sulfamic acid concentration 1.5mol / L, glucose 50g / L) and pour it into a 250mL Erlenmeyer flask. After the leaching solution was preheated to 80° C., 5 g of positive electrode powder (solid-to-liquid ratio 50 g / L) was added, and the leaching reaction was carried out under the condition of magnetic stirring (600 rpm). Under different leaching time conditions, the leaching rate of lithium and cobalt in the positive electrode powder of waste lithium cobalt oxide battery changes as follows: figure 2 shown.
Embodiment 2
[0034] Embodiment 2: the leaching of lithium, cobalt, nickel, manganese in the waste ternary lithium battery
[0035] After the waste ternary lithium battery is disassembled, crushed and other pretreatments, the positive electrode powder is separated. The positive electrode powder contains Li 7.38%, Co14.52%, Ni 35.03%, and Mn 18.63%, mainly in the form of lithium-cobalt-nickel-manganese-oxygen complex ( image 3). Prepare 100mL sulfamic acid-glucose mixed solution (sulfamic acid concentration 1.5mol / L, glucose 40g / L), and pour it into a 250mL Erlenmeyer flask. After the leaching solution was preheated to 80°C, 4g of positive electrode powder (solid-to-liquid ratio: 40g / L) was added, and the leaching reaction was carried out under the condition of magnetic stirring (500rpm). Under different leaching time conditions, the leaching rates of lithium, cobalt, nickel, and manganese in the positive electrode powder of waste ternary lithium batteries change as follows: Figure 4 sh...
Embodiment 3
[0036] Embodiment 3: the leaching of lithium, cobalt, nickel, manganese in the waste ternary lithium battery
[0037] After the waste ternary lithium battery is disassembled, crushed and other pretreatments, the positive electrode powder is separated. The positive electrode powder contains 7.38% Li, 14.52% Co, 35.03% Ni, and 18.63% Mn. Prepare 100mL sulfamic acid-glucose mixed solution (sulfamic acid concentration 1.2mol / L, glucose 50g / L) and pour it into a 250mL Erlenmeyer flask. After the leaching solution was preheated to 85°C, 5g of positive electrode powder (solid-to-liquid ratio: 50g / L) was added, and the leaching reaction was carried out under the condition of magnetic stirring (500rpm). After leaching for 2 hours, the leaching rates of lithium, cobalt, nickel, and manganese in the positive electrode powder of waste ternary lithium batteries were 97.18%, 95.41%, 95.83%, and 95.29%, respectively.
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