Leaching method of nickel cobalt lithium manganate waste battery positive-negative electrode mixed material
A technology of nickel-cobalt-lithium-manganese-manganate and mixed materials, which is applied in the field of leaching the positive and negative electrode mixed materials of nickel-cobalt-lithium-manganese-oxide waste batteries, can solve the problems of storage, transportation and use of industrial pure oxygen, and uneconomical use of industrial pure oxygen for self-use. The amount of industrial pure oxygen is not large, achieving obvious economic and environmental benefits, saving pollution control costs, and being easy to apply in engineering
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Embodiment 1
[0042] Example 1: 100g nickel-cobalt lithium manganate waste battery positive and negative mixed material (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese) and finely ground pyrolusite (particle size 200 mesh, MnO 2 content of 55%, and the amount added is 105% of the theoretical amount) into a titanium-lined pressure reactor with a volume of 2L, 1800ml of 4.0mol / L sulfuric acid, and 10g of nitric acid (in the form of HNO 3 ) and stirred at 50-60°C (stirring speed: 80r / min) for 3.5 hours. After the leaching, liquid-solid separation was carried out to obtain 1650ml leaching solution (excluding leaching slag washing water). The reaction tail gas is about 0.2L, and the nitrogen oxide concentration is 1.6 mg / m 3 . The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 98.7%, 98.9%, 99.4%, 98.6%, 99.6% and 98.2% respectively (according to the nickel, cobalt and lithium in the leaching solution and le...
Embodiment 2
[0043] Embodiment 2: 300g nickel-cobalt lithium manganese acid lithium waste battery positive and negative mixed material (containing nickel 14.5%, cobalt 20.3%, lithium 17.5%, aluminum 2.2%, copper 2.5%, manganese 12.9% and fine pyrolusite ( Particle size 180 mesh, MnO 2 content of 45%, and the addition amount is 103% of the theoretical amount) into a titanium-lined pressure reactor with a volume of 5L, add 4.8L of 3.5mol / L sulfuric acid, and add 50g of nitric acid (in the form of HNO 3 ) and stirred at 60-70°C (stirring speed: 70r / min) for 2.5 hours. After the leaching, liquid-solid separation was carried out to obtain 4.7L leaching solution (excluding leaching slag washing water), and the reaction tail gas was about 0.2L. The concentration of nitrogen oxides is 2.1 mg / m 3 . The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 98.9%, 99.0%, 99.6%, 98.5%, 99.4% and 99.2% respectively (according to the nickel, cobalt and lithium in the leachi...
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