A method for optimizing particle size distribution during the preparation of nickel-cobalt-manganese precursor materials
A preparation process and particle size distribution technology, applied in electrochemical generators, electrical components, battery electrodes, etc., can solve problems not mentioned, unsuitable for industrial production, complicated operation, etc.
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Embodiment 1
[0034] Nickel-cobalt-manganese precursor material Ni of the present invention x co y mn 1-x-y (OH) 2 Prepared in the following preparation device: the used preparation device includes two reactors connected in series by overflow pipe 7: reactor I 1 and reactor II 2. The reactor I is provided with a feeding pipe I3 and a stirring device I4; the reactor II is provided with a feeding pipe II5 and a stirring device II6.
[0035] The preparation device also includes an aging tank 9, and the reaction tank II is connected to the aging tank 9 through a draft tube 8.
Embodiment 2
[0037] 1) prepare the first solution, the first solution contains nickel sulfate 0.3mol / L, cobalt sulfate 0.3mol / L, manganese sulfate 0.3mol / L, glycine 5g / L;
[0038] 2) prepare the second solution, the second solution contains 10mol / L sodium hydroxide;
[0039] 3) The first solution and the second solution are passed into the reactor I having adjusted the stirring speed and the reaction temperature from the feed pipe 1 through a parallel flow mode; meanwhile, the first solution and the second solution are Feed into the reaction kettle II that has adjusted the stirring speed and the reaction temperature from the feed pipe II through the parallel flow mode;
[0040] Control the following parameters:
[0041] The feed rate of the first solution in reactor I is 30L / h, the stirring speed is 600rpm, the reaction temperature is 50°C, and the pH range is between 12.00-12.10. After continuous reaction for a period of time, the result of sampling and testing particle size in reactor I...
Embodiment 3
[0043] 1) prepare the first solution, the first solution contains nickel sulfate 0.5mol / L, cobalt sulfate 0.5mol / L, manganese sulfate 0.5mol / L, glycine 5g / L;
[0044] 2) prepare the second solution, the second solution contains 10mol / L sodium hydroxide;
[0045] 3) The first solution and the second solution are passed into the reactor I having adjusted the stirring speed and the reaction temperature from the feed pipe 1 through a parallel flow mode; meanwhile, the first solution and the second solution are Feed into the reaction kettle II that has adjusted the stirring speed and the reaction temperature from the feed pipe II through the parallel flow mode;
[0046] Control the following parameters:
[0047] The feed rate of Reactor I is 200L / h, the stirring speed is 300rpm, the reaction temperature is 55°C, and the pH range is between 11.85-11.95. After continuous reaction for a period of time, the result of sampling and testing particle size in Reactor I is D0.1=0.22 um, D1...
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