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
US2020161653A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020161653-A1 |
| Application number | US-202016749208-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 22, 2020 |
| Priority date | Oct 30, 2014 |
| Publication date | May 21, 2020 |
| Grant date | — |
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Provided is a nickel-containing composite hydroxide that is a precursor of a positive-electrode active material with which a nonaqueous-electrolyte secondary battery having a low irreversible capacity and a high energy density can be configured. An aqueous alkaline aqueous solution and a complexing agent are added to an mixed aqueous solution including at least nickel and cobalt to regulate the pH (measured at a reference liquid temperature of 25° C.) of this mixed aqueous solution to 11.0 to 13.0, the ammonium concentration to 4 to 15 g/L, and the reaction temperature to 20° C. to 45° C. Using stirring blades having an inclination angle of 20° to 60° with respect to a horizontal plane, the mixture is stirred to conduct a crystallization reaction under such conditions that when the nickel-containing composite hydroxide to be obtained is roasted in air at 800° C. for 2 hours, the roasted composite hydroxide has a BET value of 12 to 50 m2/g. Thus a nickel-containing composite hydroxide expressed by Ni1-x-yCoxAlyMt(OH)2+α (where, 0<x≤0.20, 0<y≤0.15, 0≤t≤0.10, 0≤α 0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y), or the general formula: Ni1-x-zCoxMnzMt(OH)2+α (where 0<x≤0.50, 0<z≤0.50, x+z≤0.70, 0≤t≤0.10, 0≤α≤0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y) is obtained.
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What is claimed is: 1 . A nickel-containing composite hydroxide that is expressed by the general formula: Ni 1-x-y Co x Al y M t (OH) 2+α (where, 0<x≤0.20, 0<y≤0.15, 0≤t≤0.10, 0≤α 0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y), or the general formula: Ni 1-x-z Co x Mn z M t (OH) 2+α (where 0<x≤0.50, 0<z≤0.50, x+z≤0.70, 0≤t≤0.10, 0≤α≤0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y), and includes secondary particles that are formed from an aggregation of plural primary particles, with the average particle size of the secondary particles being 20 μm to 50 μm, and the average particle size of the primary particles being 0.01 μm to 0.40 μm, and when roasted in air for 2 hours at 800° C., the BET value of the nickel-containing composite oxide that is obtained is 12 m 2 /g to 50 m 2 /g. 2 . The nickel-containing composite hydroxide according to claim 1 , wherein the shape of the secondary particles is spherical or ellipsoidal. 3 . A production method for a nickel-containing composite hydroxide is a method for producing a nickel-containing composite hydroxide that is expressed by the general formula: Ni 1-x-y Co x Al y M t (OH) 2+α (where, 0<x≤0.20, 0<y≤0.15, 0≤t≤0.10, 0≤α 0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y), or the general formula: Ni 1-x-z Co x Mn z M t (OH) 2+α (where 0<x≤0.50, 0<z≤0.50, x+z≤0.70, 0≤t≤0.10, 0≤α≤0.50, and M is one or more kind of element selected from among Mg, Ca, Ba, Nb, Mo, V, Ti, Zr and Y) by a crystallization reaction; and when performing the crystallization reaction adds an alkaline aqueous solution to a mixed aqueous solution that includes at least nickel and cobalt to make the pH value of that mixed aqueous solution that is measured at a reference liquid temperature of 25° C. 11.0 to 13.0; makes the reaction temperature of the mixed aqueous solution 20° C. to 45° C.; adds a complexing agent to the mixed aqueous solution to make the ammonium ion concentration of that mixed aqueous solution 4 g/L to 15 g/L; and using stirring blades that have an inclination angle with respect to a horizontal plane of no less than 20° and no greater than 60°, stirs the mixed solution according to stirring conditions so that the BET value of nickel-containing composite oxide that is obtained by roasting the nickel-containing composite hydroxide in air for 2 hours at 800° C. becomes 12 m 2 /g to 50 m 2 /g. 4 . The production method for nickel-containing composite hydroxide according to claim 3 , further comprising a process of covering the nickel-containing composite hydroxide that is obtained by the crystallization reaction with Al or Mn, or with Al or Mn and added elements M.
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