Positive electrode active material and preparation method thereof, positive electrode plate, secondary battery, battery module, battery pack, and electric apparatus
US-2024429384-A1 · Dec 26, 2024 · US
US10141571B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10141571-B2 |
| Application number | US-201314431995-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 27, 2013 |
| Priority date | Sep 28, 2012 |
| Publication date | Nov 27, 2018 |
| Grant date | Nov 27, 2018 |
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To improve cycling characteristics of a non-aqueous electrolyte secondary battery by obtaining a nickel-cobalt composite hydroxide having a sharp particle size distribution as a precursor, a slurry including a nickel-cobalt composite hydroxide obtained by continuously supplying an aqueous solution that includes at least nickel and cobalt, an ammonium ion donor aqueous solution and a caustic alkali aqueous solution to a reaction vessel and reacting, is continuously extracted and separated into a large particle size portion and s small particle size portion by classification, and the small particle size portion is continuously returned to the reaction vessel. As a result, a nickel-cobalt composite hydroxide is obtained that is expressed by the general formula: Ni 1-x-y Co x M y (OH) 2 (where, 0.05≤x≤0.50, 0≤y≤0.10, 0.05≤x+y≤0.50, and M is at least one kind of metal element selected from among Al, Mg, Mn, Ti, Fe, Cu, Zn and Ga, and that satisfies the relationships (D50−D10)/D50≤0.30, and (D90−D50)/D50≤0.30 among D10, D50 and D90 of this composite hydroxide.
Opening claim text (preview).
What is claimed is: 1. In combination, a nickel-cobalt composite hydroxide and a production device for producing the nickel-cobalt composite hydroxide, the combination comprising: the nickel-cobalt composite hydroxide comprising a general formula: Ni 1-x-y Co x M y (OH) 2 (where, 0.05≤x≤0.50, 0≤y≤0.10, 0.05≤x+y≤0.50, and M is at least one kind of metal element selected from among Al, Mg, Mn, Ti, Fe, Cu, Zn and Ga, an average particle size of within a range from 10 μm to 30 μm, and (D50−D10)/D50≤0.30, and (D90−D50)/D50≤0.30 among D10, D50 and D90 of the nickel-cobalt composite hydroxide; and the production device comprising a reaction vessel; a constant volume pump for continuously supplying an aqueous solution including nickel and cobalt, an aqueous solution including an ammonium ion donor, and a caustic alkali aqueous solution to the reaction vessel; a constant volume pump for with an extraction nozzle for continuously extracting nickel-cobalt composite hydroxide generated by a reaction inside the reaction vessel from the reaction vessel by way of the extraction nozzle; a separation apparatus separating the extracted nickel-cobalt composite hydroxide into a large particle size portion and a small particle size portion by classification; and a reflux apparatus continuously returning the small particle size portion separated out to the reaction vessel. 2. The combination of claim 1 , wherein the nickel-cobalt composite hydroxide has a tap density of 2.0 g/cm 3 or greater.
Compounds of nickel · CPC title
containing alkali metals, e.g. LiNiO2 · CPC title
Manufacturing of an active layer by chemical means · CPC title
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries · CPC title
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