The invention claimed is:
1. A method for producing a nickel-manganese composite hydroxide represented by General Formula (1): Ni x Mn y M z (OH) 2+α in Formula (1), M is at least one element selected from Co, Ti, V, Cr, Zr, Nb, Mo, Hf, Ta, Fe, and W; and x, y, z, and a satisfy 0.1≤x≤0.9, 0.05≤y≤0.8, 0≤z≤0.8, x+y+z=1.0, and 0≤α≤0.4 and containing a secondary particle formed of a plurality of flocculated primary particles;
the method comprising a crystallization process of forming the nickel-manganese composite hydroxide by neutralizing a salt containing at least nickel and a salt containing at least manganese in a reaction aqueous solution; and
in the reaction aqueous solution in the crystallization process, a dissolved oxygen concentration is adjusted to fall within a range of at least 0.2 mg/L and up to 4.6 mg/L, and a dissolved nickel concentration is adjusted to fall within a range of at least 700 mg/L and up to 1,500 mg/L.
2. The method for producing a nickel-manganese composite hydroxide according to claim 1 , wherein a stirring power loaded to the reaction aqueous solution in the crystallization process is adjusted to fall within a range of at least 3 kW/m 3 and up to 15 kW/m 3 .
3. The method for producing a nickel-manganese composite hydroxide according to claim 1 , wherein a temperature of the reaction aqueous solution in the crystallization process is adjusted to fall within a range of at least 35° C. and up to 60° C.
4. The method for producing a nickel-manganese composite hydroxide according to claim 1 , wherein a pH value in the crystallization process measured based on a temperature of the reaction aqueous solution at 25° C. is adjusted to fall within a range of at least 10.0 and up to 13.0.
5. The method for producing a nickel-manganese composite hydroxide according to claim 1 , wherein the crystallization process includes continuously adding a mixed aqueous solution including nickel and manganese into a reaction vessel and overflowing slurry including nickel-manganese composite hydroxide particles formed by neutralization to recover the secondary particle.
6. A method for producing a positive electrode active material for a nonaqueous electrolyte secondary battery, the positive electrode active material comprising: a lithium-nickel-manganese composite oxide represented by General Formula (2): Li 1+t Ni x Mn y M z O 2+β in Formula (2), M is at least one additional element selected from Co, Ti, V, Cr, Zr, Nb, Mo, Hf, Ta, Fe, and W; and t, x, y, z, and β satisfy −0.05≤t≤0.5, 0.1≤x≤0.9, 0.05≤y≤0.8, 0≤z≤0.8, x+y+z=1.0, and 0≤β≤0.5 and contains a secondary particle formed of a plurality of flocculated primary particles,
the method comprising:
a process of providing a nickel-manganese composite hydroxide represented by General Formula (1): Ni x Mn y M z (OH) 2+α in Formula (1), M is at least one element selected from Co, Ti, V, Cr, Zr, Nb, Mo, Hf, Ta, Fe, and W; and x, y, z, and a satisfy 0.1≤x≤0.9, 0.05≤y≤0.8, 0≤z≤0.8, x+y+z=1.0, and 0≤α≤0.4 and containing a secondary particle formed of a plurality of flocculated primary particles, wherein the nickel-manganese composite hydroxide has a half width of a diffraction peak of a (001) plane obtained by X-ray diffraction measurement of at least 0.10° and up to 0.40° and has a degree of sparsity/density represented by [(void area within secondary particle/cross section of secondary particle)×100](%) of at least 0.5% and up to 10%;
a process of mixing the nickel-manganese composite hydroxide with a lithium compound to obtain a mixture; and
a process of firing the mixture to obtain the lithium-nickel-manganese composite oxide.
7. The method for producing a positive electrode active material for a nonaqueous electrolyte secondary battery according to claim 6 , wherein the nickel-manganese composite hydroxide is obtained by the method comprising a crystallization process of forming the nickel-manganese composite hydroxide by neutralizing a salt containing at least nickel and a salt containing at least manganese in a reaction aqueous solution; and
in the reaction aqueous solution in the crystallization process, a dissolved oxygen concentration is adjusted to fall within a range of at least 0.2 mg/L and up to 4.6 mg/L, and a dissolved nickel concentration is adjusted to fall within a range of at least 700 mg/L and up to 1,500 mg/L.