Method of Preparing Cathode Material for Secondary Battery

Patent metadata

Field	Value
Publication number	US-2020185760-A1
Application number	US-201716313978-A
Country	US
Kind code	A1
Filing date	Dec 8, 2017
Priority date	Dec 19, 2016
Publication date	Jun 11, 2020
Grant date	—

Abstract

Provided herein is a method for preparing a ternary cathode material for lithium-ion battery by a static mixer, wherein the cathode material comprises a lithium multi-metal composite oxide represented by xLi 2 MnO 3 . (1-x) LiNi a Mn b Co c Al (1-a-b-e) O 2 , where 0≤a<1, 0≤b<1, 0≤c<1, a+b+c≤1, and 0≤x<1. The cathode material disclosed herein exhibits a high initial specific capacity, possesses good safety characteristics and shows excellent capacity retention.

First claim

What is claimed is:

1 . A method of preparing a cathode material for a lithium-ion battery cell, comprising the steps of:
1) dissolving a combination of at least three of a salt of nickel, a salt of manganese, a salt of cobalt, and a salt of aluminium in water to obtain a first solution, wherein a total molar concentration of the metal elements in the first solution is from about 0.1 mol/L to about 3 mol/L; 2) dissolving a precipitating agent in water to form a second solution, wherein a concentration of the precipitating agent in the second solution is from about 0.5 mol/L to about 6 mol./L; 3) pre-heating the first solution and the second solution to the same temperature from about 30° C. to about 80° C. to obtain a pre-heated first solution and a pre-heated second solution respectively; 4) feeding the pre-heated first solution and the pre-heated second solution to a first inlet and a second inlet of a static mixer respectively to obtain a co-precipitating solution; 5) filtering a suspension eluted from an outlet of the static mixer to obtain a cathode material precursor, wherein the outlet of the static mixer is coupled to a pH controller for controlling the flow rate of the pre-heated first and second solutions; 6) washing the cathode material precursor with water; 7) drying the cathode material precursor at a temperature from about 60° C. to about 105° C. for a time period from about 4 hours to about 24 hours to obtain a dried cathode material precursor; 8) mixing the dried cathode material precursor with one or more lithium salts to obtain a solid mixture, wherein a molar ratio of the metal element lithium of the one or more lithium salts to the total amount of the metal elements selected from a combination of at least three of nickel, manganese, cobalt, and aluminium is from about 1.5:1 to about 1:1, or from about L03:1 to about 1:1; and 9) calcinating the solid mixture in two stages to obtain the cathode material, wherein the first stage is conducted at a temperature from about 350° C. to about 550° C. for a time period from about 2 hours to about 10 hours, and the second stage is conducted at a temperature from about 750° C. to about 950° C. for a time period from about 6 hours to about 15 hours, and wherein the cathode material comprises a lithium multi-metal composite oxide represented by xLi 2 MnO 3 .(1-x)LiNi a Mn b Co c Al ( 1-a-b-c) O 2 , wherein 0≤a<1, 0≤b<1, 0≤c<1, a+b+c≤1, and 0≤x<1; and the cathode material has a D90/D10 ratio from about 1.4 to about 1.9.

2 . The method of claim 1 , wherein the cathode material precursor is [Ni a Mn b Co c Al (1-a-b-c) ](OH) 2 or [Ni a Mn b Co c Al (1-a-b-c) ]CO 3, wherein 0≤a<1, 0≤b<1, 0≤c<1, and a+b+c≤1.

3 . The method of claim 1 , wherein the cathode material precursor is selected from the group consisting of [Ni 0.33 Mn 0.33 Co 0.33 ](OH) 2 , [Ni 0.4 Mn 0.4 Co 0.2 ](OH) 2 , [Ni 0.5 Mn 0.3 Co 0.2 ](OH) 2 , [Ni 0.6 Mn 0.2 Co 0.2 ](OH) 2 , [Ni 0.7 Mn 0.15 Co 0.15 ](OH) 2 , [Ni 0.8 Mn 0.1 Co 0.1 ](OH) 2 , [Ni 0.92 Mn 0.04 Co 0.04 ](OH) 2 , [Ni 0.8 Mn 0.15 Co 0.05 ](OH) 2 , [Ni 0.33 Mn 0.33 Co 0.33 ]CO 3 ,[Ni 0.4 Mn 0.4 Co 0.2 ]CO 3 , [Ni 0.5 Mn 0.2 Co 0.2 ]CO 3 ,[Ni 0.6 Mn 0.2 Co0.2]CO 3 , [Ni 0.7 Mn 0.15 Co 0.15 ]CO 3 ,[Ni 0.8 Mn 0.1 Co 0.1 ]CO 3 , [Ni 0.92 Mn 0.04 Co 0.04 ]CO 3 , and [Ni 0.8 Co 0.15 Al 0.05 ]CO 3 .

4 . The method of claim 1 , wherein each of the salt of nickel, the salt of manganese, the salt of cobalt, and the salt of the aluminium independently comprise an anion selected from the group consisting of sulfate, nitrate, acetate, chloride, and combinations thereof.

5 . The method of claim 1 , wherein the salt of the aluminium is sodium aluminate.

6 . The method of claim 1 , wherein the precipitating agent is selected from the group consisting of sodium hydroxide, potassium hydroxide, calcium hydroxide, ammonium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogencarbonate, potassium hydrogencarbonate, calcium hydrogencarbonate, ammonium carbonate, and combinations thereof.

7 . The method of claim 1 , wherein the static mixer has a length from about 30 cm to about 100 cm and a diameter from about 5 mm to about 20 cm, and wherein the ratio of the length of the static mixer to the diameter of the static mixer is from about 2:1 to about 20:1.

8 . The method of claim 1 , wherein the static mixer is made of plastic selected from the group consisting of polypropylene, polytetrafluoroethylene, polyvinyl chloride, copolymers thereof, and combinations thereof.

9 . The method of claim 1 , wherein the static mixer is coupled to a heating element, and wherein the heating element is a heating jacket surrounding at least a portion of the length of the static mixer.

10 . The method of claim 1 , wherein the temperature of the heating jacket and the pre-heated first and second solutions are the same.

11 . The method of claim 1 , wherein the static mixer is sonicated by an ultrasonicator.

12 . The method of claim 11 , wherein the ultrasonicator is operated at a power from about 60 W to about 600 W.

13 . The method of claim 1 , wherein the pH value of the co-precipitating solution in the static mixer is maintained at a range from about 8 to about 12.

14 . The method of claim 1 , wherein the co-precipitating solution is mixed in the static mixer for a time period less than 2 minutes.

15 . The method of claim 1 , wherein the method does not comprise a step of adding ammonia solution to the pre-heated second solution or the co-precipitating solution.

16 . The method of claim 1 , wherein the suspension is washed with water for a time period from about 30 minutes to about 2 hours.

17 . The method of claim 1 , wherein the dried cathode material precursor and the one or more lithium salts are mixed for a time period from about 30 minutes to about 2 hours.

18 . The method of claim 1 , wherein the dried cathode material precursor has a particle size D50 in the range from about 1 μm to about 12 μm.

19 . The method of claim 1 , wherein the dried cathode material precursor has a D90/D10 ratio from about 1.3 to about 2.

20 . The method of claim 1 , wherein the lithium salt is selected from the group consisting of lithium hydroxide, lithium carbonate, lithium fluoride, lithium acetate, lithium oxalate, and combinations thereof.

Assignees

• Grst Int Ltd

Inventors

• Ho Kam Piu
• Wang Ranshi
• Shen Peihua
• Jiang Yingkai

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

• H01M4/505 Primary

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

• C01P2006/11

  Powder tap density · CPC title

• C01P2004/61

  Micrometer sized, i.e. from 1-100 micrometer · CPC title

• C01P2004/51

  Particles with a specific particle size distribution · CPC title