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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[0042] Example 1: 100g of mixed materials for the positive and negative electrodes of waste nickel-cobalt manganese batteries (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, and 12.9% manganese) and ground pyrolusite (Particle size 200 mesh, MnO 2 The content is 55%, and the amount added is 105% of the theoretical amount.) Put it into a 2L titanium-lined pressure reactor, add 4.0mol / L sulfuric acid 1800ml, add 10g nitric acid (in HNO 3 Calculate), leaching for 3.5 hours with stirring at 50-60°C (stirring speed 80r / min), after leaching, liquid-solid separation is performed to obtain 1650ml leaching solution (without leaching residue 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 respectively 98.7%, 98.9%, 99.4%, 98.6%, 99.6% and 98.2% (according to the nickel, cobalt, and lithium in the leaching solutio...
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[0043] Example 2: 300g of mixed materials for positive and negative electrodes of waste nickel-cobalt manganese batteries (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese, and ground pyrolusite ( 180 mesh, MnO 2 The content is 45%, and the amount added is 103% of the theoretical amount.) Put into a 5L titanium-lined pressure reactor, add 4.8L of 3.5mol / L sulfuric acid, and add 50g of nitric acid (with HNO 3 Calculate), stir for 2.5 hours at 60~70℃ (stirring speed is 70r / min), and carry out liquid-solid separation after leaching, to obtain 4.7L leaching solution (excluding leaching residue washing water), reaction tail gas is about 0.2L, The nitrogen oxide concentration is 2.1 mg / m 3 . The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are respectively 98.9%, 99.0%, 99.6%, 98.5%, 99.4% and 99.2% (according to the nickel, cobalt, and lithium in the leaching solution and the washing solution of the lea...
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