Method for lixiviating anode materials of lithium nickel waste batteries
A lithium nickel oxide waste battery and positive electrode material technology, applied in the direction of improving process efficiency, can solve the problems of large nitrogen oxides, polluting the environment, large consumption of nitric acid, etc., achieve obvious economic and environmental benefits, and save pollution Treatment costs, the effect of avoiding the generation of pollutant nitrogen oxides
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Embodiment 1
[0023] Example 1: Add 100g of lithium nickelate waste battery positive electrode material (containing nickel 54.3%, lithium 5.5%, copper 7.8%, aluminum 3.1%) into a titanium-lined autoclave with a volume of 1L, add 3.5mol / L of Sulfuric acid 880ml, add nitric acid 13g (with HNO 3 meter), introduce 0.2MPa industrial pure oxygen, stir at 50~60℃ (stirring speed 80r / min) and leaching for 2.0 hours, carry out liquid-solid separation after leaching to obtain 840ml leaching solution (without leaching residue washing water) . The reaction tail gas is about 0.36L (converted to the volume of absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 2.4mg / m 3 . The leaching rates of nickel, lithium and copper were 98.2%, 98.3% and 97.1%, respectively (calculated based on the nickel, lithium and copper entering the leaching solution and the leaching residue washing solution).
Embodiment 2
[0024] Example 2: Add 400g of lithium nickelate waste battery positive electrode material (containing 54.3% nickel, 5.5% lithium, 7.8% copper, and 3.1% aluminum) into a titanium-lined autoclave with a volume of 5L, add 3.0mol / L sulfuric acid 4.1% L, add nitric acid 60g (with HNO 3 0.1MPa industrial pure oxygen was introduced, and the reaction was stirred at 60-70°C for 3 hours. After the reaction, liquid-solid separation was performed to obtain 3.9L of leaching solution (excluding leaching residue washing water), and the reaction tail gas was about 1.8L. (Converted to the volume of absolute pressure of 0.1MPa), the concentration of nitrogen oxides is 2.1mg / m 3 . The leaching rates of nickel, lithium and copper were 98.3%, 98.6% and 97.3%, respectively (calculated based on the nickel, lithium and copper entering the leaching solution and the leaching residue washing solution).
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