Preparation method of ternary positive electrode material precursor and lithium carbonate
A cathode material and precursor technology, which is applied in the field of preparation of ternary cathode material precursors and lithium carbonate, can solve the problems of serious environmental pollution, consumption, and environmental pollution, and achieves simplified process flow, high process added value, and high technological progress. short process effect
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Embodiment 1
[0050] The preparation method of ternary cathode material precursor and lithium carbonate, such as figure 1 shown, including the following steps:
[0051] (1) Recycling waste LiNi 1 / 3 co 1 / 3 mn 1 / 3 o 2 After the battery is discharged, crushed and calcined, the battery material and the current collector are screened and separated;
[0052] (2) Take 1kg of battery material that has passed through a 200-mesh sieve, first add 45L of ammonia water with a mass fraction of 10%, and 9kg of ammonium chloride, stir for 0.5h, then add 2kg of sodium sulfite and carry out pressure leaching, and control the reaction leaching temperature to 70°C, The reaction leaching time is 5h, the control pressure is 0.3Mpa, and the stirring speed is 200r / min. After three leachings are analyzed by inductively coupled plasma atomic emission spectrometry, a section of leaching solution is obtained by filtering and washing. The leaching rate of nickel is measured to be 99.8%. The leaching rate of cobalt...
Embodiment 2
[0056] The preparation method of ternary cathode material precursor and lithium carbonate, such as figure 1 shown, including the following steps:
[0057] (1) Recycling waste LiNi 0.5 co 0.2 mn 0.3 o 2 Battery discharge, crushing, calcination, screening and separation of battery materials and current collectors;
[0058] (2) Take 1kg of material passed through a 200-mesh sieve; first add 38L of ammonia water with a mass fraction of 10%, 7kg of ammonium chloride, stir for 0.5h, add 1.7kg of sodium sulfite, and then carry out pressure leaching. Control the reaction leaching temperature to 90°C. The leaching time is 9h, the control pressure is 0.5Mpa, and the stirring speed is 300r / min. After the secondary leaching is analyzed by inductively coupled plasma atomic emission spectrometry, a section of leaching solution is obtained by filtering and washing. The leaching rate of nickel is measured to be 99.8%. The leaching rate of cobalt is 99.9%, the leaching rate of manganese i...
Embodiment 3
[0062] The preparation method of ternary cathode material precursor and lithium carbonate, such as figure 1 shown, including the following steps:
[0063] (1) Recycling waste LiNi 0.8 co 0.1 mn 0.1 o 2 Battery discharge, crushing, calcination, screening and separation of battery materials and current collectors;
[0064] (2) Take 1kg of material passed through a 200-mesh sieve; first add 27L of ammonia water with a mass fraction of 10%, 5kg of ammonium chloride, stir for 0.5h, add 1.4kg of ammonium sulfite, and then carry out pressure leaching, and control the reaction leaching temperature to 50°C , The reaction leaching time is 1h, the control pressure is 0.1Mpa, and the stirring speed is 100r / min. After one leaching is analyzed by inductively coupled plasma atomic emission spectrometry, a section of leaching solution is obtained by filtering and washing, and the leaching rate of nickel is measured to be 98.5%. , the leaching rate of cobalt is 97.0%, the leaching rate of...
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