Method for preparing positive electrode active material precursor and positive electrode material for lithium secondary battery having concentration-gradient layer using batch reactor, and positive electrode active material precursor and positive electrode material for lithium secondary battery prepared by the method

Patent metadata

Field	Value
Publication number	US-9923190-B2
Application number	US-201113521974-A
Country	US
Kind code	B2
Filing date	Jan 14, 2011
Priority date	Jan 14, 2010
Publication date	Mar 20, 2018
Grant date	Mar 20, 2018

Abstract

The present invention relates to a method for preparing a positive electrode active material precursor and a positive electrode material for a lithium secondary battery having a concentration-gradient layer using a batch reactor, and to a positive electrode active material precursor and a positive electrode material for a lithium secondary battery prepared by the method. The method for preparing a positive electrode active material precursor and a positive electrode active material for a lithium secondary battery having a concentration-gradient layer using a batch reactor involves supplying a predetermined amount of a chelating agent into the batch reactor, and simultaneously supplying transition metals while continuously adjusting the concentration of the transition metals such that the concentration-gradient layer can be formed from a core to a shell of the positive electrode active material in a more economically advantageous and stable manner, and at the same time a positive electrode active material having an elongated lifespan and improved thermal stability can be provided.

First claim

What is claimed is:

1. A method for preparing a positive electrode active material precursor for a lithium secondary battery having a concentration-gradient layer using a batch reactor, which comprises:
1) supplying a first chelating agent aqueous solution into the batch reactor; then
2) simultaneously supplying a first precursor aqueous solution, a second chelating agent aqueous solution and a first basic aqueous solution into the reactor continuously to obtain a spherical precipitate forming a core layer; then
3) simultaneously supplying a second precursor aqueous solution, a third chelating agent aqueous solution and a second basic aqueous solution into the reactor continuously to obtain a precipitate forming the concentration-gradient layer, where the concentrations of nickel (Ni), manganese (Mn) and cobalt (Co) are relatively and gradually changed, on the surface of the core layer; then
4) simultaneously supplying a third precursor aqueous solution, a fourth chelating agent aqueous solution and a third basic aqueous solution into the reactor continuously to obtain a precipitate forming a shell layer on the surface of the concentration-gradient layer; and then
5) drying or heat-treating the precipitate to prepare a positive electrode active material precursor for a lithium secondary battery,
wherein, in the step 1), the concentration of the first chelating agent aqueous solution is 2 to 3 mol/L, and the first chelating agent aqueous solution is supplied into the reactor to 25 to 35% of the total reactor volume, and
wherein, in the step 2), the molar concentration ratio of the metal salts in the first precursor aqueous solution to the chelating agent in the second chelating agent aqueous solution is 0.1 to 0.5; the first precursor aqueous solution, the second chelating agent aqueous solution and the first basic aqueous solution are simultaneously supplied into the reactor continuously to 30 to 60% of the total reactor volume; the concentration of the chelating agent in the reactor is reduced as the reaction progresses, and
wherein, in the step 3), the molar concentration ratio of the metal salts in the second precursor aqueous solution to the chelating agent in the third chelating agent aqueous solution is 0.2 to 0.4, and the second precursor aqueous solution, the third chelating agent aqueous solution and the second basic aqueous solution are simultaneously supplied into the reactor continuously up to 10 to 30% of the total reactor volume, and
wherein, in the step 3), the second precursor aqueous solution is prepared by mixing the first precursor aqueous solution and an aqueous solution in a separate reactor for forming a concentration-gradient at a predetermined ratio, and is supplied into the reactor continuously at the same time, and
wherein, in the step 4), the molar concentration ratio of the metal salts in the third precursor aqueous solution to the chelating agent in the fourth chelating agent aqueous solution is 0.05 to 0.2; and the third precursor aqueous solution, the fourth chelating agent aqueous solution and the third basic aqueous solution are simultaneously supplied into the reactor continuously up to 5 to 10% of the total reactor volume.

2. The method of claim 1 ,
wherein, in step 2), a molar ratio of Ni:Co:Mn in the first precursor aqueous solution is a:b:1−(a+b) (0.7≤a≤0.9, 0≤b≤0.2).

3. The method of claim 1 , wherein in the step 3), the molar ratio of Ni:Co:Mn in the aqueous solution for forming a concentration-gradient is a:b:1−(a+b) (0≤a≤0.2, 0.1≤b≤0.4).

4. The method of claim 1 , wherein the second precursor aqueous solution of step 3) is prepared by mixing the first precursor aqueous solution and an aqueous solution for forming a concentration until the molar ratio of Ni:Co:Mn in the mixture becomes a:b:1−(a+b) (0≤a≤0.5, 0≤b≤0.4) and is supplied into the reactor continuously at the same time.

5. The method of claim 1 , wherein, in the step 4), the molar ratio of Ni:Co:Mn in the third precursor aqueous solution is a:b:1−(a+b) (0≤a≤0.5, 0≤b≤0.4).

6. A method for preparing a positive electrode active material for a lithium secondary battery having a concentration-gradient layer using a batch reactor, which further comprises:
1) mixing the positive electrode active material precursor for a lithium secondary battery having a concentration-gradient layer prepared according to according to claim 1 with lithium (Li) compound; and
2) heat-treating the mixture at 750° C. to 1000° C. under oxidative atmosphere containing air or oxygen for 10 to 25 hours.

Assignees

• Yu Jong Ryeol
• Choi Moon Ho
• Ecopro Bm Co Ltd

Inventors

• Yu Jong-Ryeol
• Choi Moon-Ho

Classifications

• C01P2006/11

  Powder tap density · CPC title

• H01M4/1391

  of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx · CPC title

• H01M4/131 Primary

  Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx · CPC title

• C01P2004/03

  obtained by SEM · CPC title

• 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