Method for preparing nickel-cobalt-manganese ternary precursor material by fractional reaction
A graded reaction, nickel-cobalt-manganese technology, applied to electrical components, nickel oxide/nickel hydroxide, manganese oxide/manganese hydroxide, etc., can solve the problems of increasing the difficulty of controlling the reactor, reducing production capacity, and not being suitable for industrial production. Achieve industrial production, reduce production costs, and achieve excellent product performance
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Embodiment 1
[0029] Nickel sulfate, cobalt sulfate and manganese sulfate are made into mixed solution, and the total molar mass of mixed solution is 2mol / L, wherein Ni 2+ 、Co 2+ , Mn 2+ The concentration ratio is 5:3:2, 23% aqueous ammonia solution, sodium hydroxide solution with a concentration of 4mol / L and the mixed solution are respectively added to the primary reaction kettle at the same time at 500L / h, 150L / h and 300L / h , control the pH value of the first-stage reactor to 11, control the temperature of the reactor to 55°C, control the ammonia value to 14g / L, control the material to stay in the reactor for 12h, and the stirring speed of the reactor to 200rpm, and the reactor adopts an upper port natural Flashing, the whole reaction process is completed under nitrogen protection;
[0030] The material liquid overflowing from the first-stage reaction kettle is transported to the solid-liquid separation device through pipelines, and then dried and screened to collect solid particles la...
Embodiment 2
[0034] Nickel sulfate, cobalt sulfate and manganese sulfate are made into mixed solution, and the total molar mass of mixed solution is 1mol / L, wherein Ni 2+ 、Co 2+ , Mn 2+ The concentration ratio is 5:3:2, add 23% aqueous ammonia solution, sodium hydroxide solution with a concentration of 1mol / L and the mixed solution at 500L / h, 150L / h, and 300L / h at the same time into the primary reactor , control the pH value of the primary reactor to be 10, control the temperature of the reactor to 45°C, control the ammonia value to 9g / L, control the material to stay in the reactor for 10h, and the stirring speed of the reactor to be 300rpm, and the reactor adopts an upper port natural Flashing, the whole reaction process is completed under nitrogen protection;
[0035] The material liquid overflowing from the first-stage reaction kettle is transported to the solid-liquid separation device through pipelines, and then dried and screened to collect solid particles larger than 7 μm, which a...
Embodiment 3
[0039] Nickel sulfate, cobalt sulfate and manganese sulfate are made into mixed solution, and the total molar mass of mixed solution is 4mol / L, wherein Ni 2+ 、Co 2+ , Mn 2+ The concentration ratio is 5:3:2, and the mixed solution, sodium hydroxide solution with a concentration of 6mol / L, and 23% ammonia aqueous solution are respectively added to the primary reactor at the same time at 500L / h, 300L / h, and 150L / h. Among them, the pH value of the first-stage reactor is controlled to be 13, the temperature of the reactor is controlled to be 65°C, the ammonia value is controlled at 20g / L, the material is controlled to stay in the reactor for 18 hours, the stirring speed of the reactor is 200rpm, and the reactor adopts an upper port Natural overflow, the whole reaction process is completed under nitrogen protection;
[0040] The material liquid overflowing from the first-stage reaction kettle is transported to the solid-liquid separation device through pipelines, and then dried an...
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Abstract
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