Nickel manganese composite hydroxide particles and manufacturing method thereof, cathode active material for a non-aqueous electrolyte secondary battery and manufacturing method thereof, and a non-aqueous electrolyte secondary battery

Patent metadata

Field	Value
Publication number	US-10669646-B2
Application number	US-201815989147-A
Country	US
Kind code	B2
Filing date	May 24, 2018
Priority date	Mar 28, 2011
Publication date	Jun 2, 2020
Grant date	Jun 2, 2020

Abstract

Provided are nickel manganese composite hydroxide particles having a small and uniform particle size and having a double structure which enables to obtain a cathode active material having a hollow structure, and a manufacturing method thereof. When obtaining the nickel manganese composite hydroxide by a reaction crystallization, using an aqueous solution for nucleation, which includes at least a metallic compound that contains nickel, a metallic compound that contains manganese and an ammonium ion donor and controlling the pH value that is measured at a standard solution temperature of 25° C. is 10.5 to 12.0, nucleation is performed in an oxidizing atmosphere in which the oxygen concentration is greater than 1% by volume, and then nuclei are grown by switching the atmosphere from the oxidizing atmosphere to a mixed atmosphere of oxygen and inert gas in which the oxygen concentration is 1% by volume or less.

First claim

What is claimed is:

1. A manufacturing method for manufacturing nickel manganese composite hydroxide particles using a reaction crystallization, the nickel manganese composite hydroxide particles being expressed by a general formula of Ni x Mn y Co z M t (OH) 2+a (where x+y+z+t=1, 0.3≤x≤0.7, 0.1≤y≤0.55, 0≤z≤0.4, 0≤t≤0.1, 0≤a≤0.5, and M is one or more added elements that are selected from among Mg, Ca, Al, Ti, V, Cr, Zr, Nb, Mo and W),
the manufacturing method using a batch reaction tank that does not collect the nickel manganese composite hydroxide particles until the reaction thereof is complete; and
the manufacturing method comprising:
a nucleation step of controlling an aqueous solution for nucleation, which includes at least a metallic compound that contains nickel, a metallic compound that contains manganese, and an ammonium ion donor, so that a pH value thereof that is measured at a standard solution temperature of 25° C. is 12.0 to 14.0, and causing nucleation in an oxidizing atmosphere having an oxygen concentration of greater than 1% by volume; and
a particle growth step of controlling an aqueous solution for particle growth, which includes nuclei formed in the nucleation step, so that a pH value that is measured at a standard solution temperature of 25° C. is 10.5 to 12.0, the pH value of the particle growth step being at least 0.5 less than the pH value of the nucleation step, and causing nuclear growth by switching from the oxidizing atmosphere to a mixed atmosphere of oxygen and inert gas having an oxygen concentration of 1% by volume or less within a range of 0 to 40% of the overall time of the particle growth step from the start of the particle growth step.

2. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein the oxygen concentration in the oxidizing atmosphere is 10% by volume or greater.

3. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein the oxygen concentration in the mixed atmosphere is 0.5% by volume or less.

4. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein switching in the particle growth step from the oxidizing atmosphere to the mixed atmosphere of oxygen and inert gas is performed within a range of 0 to 30% of the overall time of the particle growth step from the start of the particle growth step.

5. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein the aqueous solution for particle growth is obtained by adjusting the pH value of the aqueous solution for nucleation after the nucleation step has finished.

6. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein the aqueous solution for particle growth is obtained by adding the aqueous solution for nucleation, which contains the nuclei formed in the nucleation step, to a solution that is separate from the aqueous solution for nucleation with the formed nuclei.

7. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein, in the particle growth step, part of a liquid part of the aqueous solution for particle growth is excreted.

8. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein, in the nucleation step and the particle growth step, a temperature of the aqueous solution for nucleation and for particle growth is maintained at 20° C. or greater.

9. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 , wherein, in the nucleation step and the particle growth step, an ammonia concentration of the aqueous solution for nucleation and for particle growth is maintained within a range of 3 to 25 g/L.

10. The manufacturing method for manufacturing nickel manganese composite hydroxide particles according to claim 1 further comprising a step of coating the nickel manganese composite hydroxide particles obtained in the particle growth step with a compound containing the one or more added elements.

11. Nickel manganese composite hydroxide particles that are expressed by a general formula of Ni x Mn y Co z M t (OH) 2+a (where x+y+z+t=1, 0.3≤x≤0.7, 0.1≤y≤0.55, 0≤z≤0.4, 0≤t≤0.1, 0≤a≤0.5, and M is one or more added elements that are selected from among Mg, Ca, Al, Ti, V, Cr, Zr, Nb, Mo and W), and that are spherical shaped secondary particles that are formed by a plurality of aggregate primary particles, wherein the secondary particles have an average particle size of 3 to 7 μm, a value [(d90−d10)/average particle size], which is an index indicating an extent of particle size distribution thereof, of 0.55 or less, and wherein the secondary particles have a center section comprising fine primary particles, and an outer shell section on the outside of the center section comprising plate shaped primary particles that are larger than the fine primary particles.

12. The nickel manganese composite hydroxide particles according to claim 11 , wherein the fine primary particles have an average particle size of 0.01 to 0.3 μm, and the plate shaped primary particles that are larger than the fine primary particles have an average particle size of 0.3 to 3 μm.

13. The nickel manganese composite hydroxide particles according to claim 11 , wherein a ratio of the thickness of the outer shell section with respect to the particle size of the secondary particles is 5 to 45%.

14. The nickel manganese composite hydroxide particles according to claim 11 , wherein the one or more added elements are uniformly distributed inside the secondary particles and/or uniformly cote the surface of the secondary particles.

15. A manufacturing method for manufacturing a cathode active material for a non-aqueous electrolyte secondary battery comprising lithium nickel manganese composite oxide having a layered hexagonal crystal structure and expressed by a general formula of Li 1+u Ni x Mn y Co z M t O 2 (where −0.05≤u≤0.50, x+y+z+t=1, 0.3≤x≤0.7, 0.1≤y≤0.55, 0≤z≤0.4, 0≤t≤0.1, M is one or more added elements that are selected from among Mg, Ca, Al, Ti, V, Cr, Zr, Nb, Mo and W),
the manufacturing method comprising:
heat treatment of the nickel manganese composite hydroxide particles of claim 11 at a temperature of 105 to 750° C.,
a mixing step that mixes a lithium compound into the heat treated particles to form a lithium mixture; and
a calcination step that performs calcination of the mixture formed in the mixing step in an oxidizing atmosphere at a temperature of 800 to 980° C.

16. The manufacturing method for manufacturing cathode active material for a non-aqueous electrolyte secondary battery according to claim 15 , wherein the lithium mixture is adjusted so that a ratio between the sum of the number of metal atoms other than lithium included in the lithium mixture and the number of lithium atoms is 1:0.95 to 1.5.

17. The manufacturing method for manufacturing cathode active material for a non-aqueous electrolyte secondary battery according to claim 15 , wherein, in the calcination step, temporary calcination has already been performed before calcination at a temperature of 350 to 800° C.

18. The manufacturing method for manufacturing cathode active material for a non-aqueous electrolyte secondary battery according to claim 15 , wherein the oxidizing atmosphere during the calcination step is an atmosphere ha

Assignees

• Sumito Metal Mining Co Ltd
• Sumitomo Metal Mining Co

Inventors

• Toya Hiroyuki
• Mori Kensaku
• Imaizumi Shin
• Ikeuchi Kenji
• Osako Toshiyuki

Classifications

• H01M4/525

  of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy · CPC title

• C01G53/006

  Chemistry & Metallurgy · mapped topic

• H01M4/505

  of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy · CPC title

• H01M10/0525

  Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries · CPC title

• C01P2002/52

  containing elements as dopants · CPC title