Method of manufacturing cathode active material
A method of manufacturing a cathode active material is provided. The method includes the step of precipitating step for providing a solution of a deposition component onto composite oxide particles including lithium Li and nickel Ni, removing a solvent from the solution on the composite oxide particles within a short time period, and precipitating the deposition component on surfaces of the composite oxide particles; and heating step for heating under an oxidation atmosphere the composite oxide particles with the deposition component precipitated on the surfaces.
1. A method of manufacturing a cathode active material, the method comprising:
preheating composite oxide particles including lithium Li and nickel Ni;
providing a solution of a deposition component onto the preheated composite oxide particles;
precipitating the deposition component on surfaces of the composite oxide particles; and
heating under an oxidation atmosphere the composite oxide particles with the deposition component precipitated on the surfaces,
wherein the composite oxide particles are preheated to a temperature equal to or higher than a boiling point of the solution containing the deposition component, and
wherein a solvent in the solution is in contact with the composite oxide particles for 10 seconds or less.
2. The method according to claim 1 , wherein the composite oxide particles have an average composition represented by following Chemical Formula 1:
Li a Ni x Co y Al z O 2 [Chemical Formula 1]
where, nickel Ni may be substituted with one or more metal elements selected from a group consisting of manganese Mn, chrome Cr, iron Fe, vanadium V, magnesium Mg, titanium Ti, zirconium Zr, niobium Nb, molybdenum Mo, tungsten W, copper Cu, zinc Zn, gallium Ga, indium In, tin Sn, lanthanum La, and cerium Ce within a range of 0.1 or less of nickel Ni assuming that a total amount of nickel Ni is set to 1, and
where, in the Chemical Formula 1, coefficients a, x, y, and z are set to 0.3≦a≦1.05, 0.60<x<0.90, 0.10<y<0.40, and 0.01<z<0.20, respectively, and a relationship between x, y and z is set to x+y+z=1.
3. The method according to claim 1 , wherein the solution is provided on the preheated composite oxide particles to remove the solvent to precipitate the deposition component on surfaces of the composite oxide particles.
4. The method according to claim 1 , wherein the deposition component is made of oxoacid salt.
5. The method according to claim 4 , wherein the oxoacid salt is ammonium salt.
6. The method according to claim 4 , wherein an addition amount of the oxoacid salt is ranged between 0.01 parts by weight and 20 parts by weight with respect to 100 parts by weight of the composite oxide particles.
7. The method according to claim 1 , wherein the composite oxide particles with the deposition component are heated within a temperature range between 500° C. and 1200° C. in the heating step.
8. The method according to claim 1 , wherein an average particle diameter of the cathode active material is ranged between 2.0 μm and 50 μm.
9. The method according to claim 1 , wherein the deposition component is selected from the group consisting of ammonium sulfate and ammonium pentaborate.
10. The method according to claim 1 , wherein the composite oxide particles are preheated to a temperature of 120° C.
11. The method according to claim 1 , wherein the composite oxide particles have an average composition of Li 1.03 Ni 0.77 Co 0.20 Al 0.03 O 2 .
12. The method according to claim 1 , wherein the composite oxide particles are preheated before the deposition component is deposited on the composite oxide particles.
13. A method of manufacturing a cathode active material, the method comprising:
providing a solution of a deposition component onto composite oxide particles including lithium Li and nickel Ni;
removing a solvent from the solution on the composite oxide particles within about ten seconds;
precipitating the deposition component on surfaces of the composite oxide particles; and
heating under an oxidation atmosphere the composite oxide particles with the deposition component precipitated on the surfaces.
14. The method according to claim 13 , wherein the composite oxide particles have an average composition represented by following Chemical Formula 1:
Li a Ni x Co y Al z O 2 [Chemical Formula 1]
where, nickel Ni may be substituted with one or more metal elements selected from a group consisting of manganese Mn, chrome Cr, iron Fe, vanadium V, magnesium Mg, titanium Ti, zirconium Zr, niobium Nb, molybdenum Mo, tungsten W, copper Cu, zinc Zn, gallium Ga, indium In, tin Sn, lanthanum La, and cerium Ce within a range of 0.1 or less of nickel Ni assuming that a total amount of nickel Ni is set to 1, and
where, in the Chemical Formula 1, coefficients a, x, y, and z are set to 0.3≦a≦1.05, 0.60<x<0.90, 0.10<y<0.40, and 0.01<z<0.20, respectively, and a relationship between x, y and z is set to x+y+z=1.
15. The method according to claim 13 , wherein the deposition component is made of oxoacid salt.
16. The method according to claim 15 , wherein the oxoacid salt is ammonium salt.
17. The method according to claim 15 , wherein an addition amount of the oxoacid salt is ranged between 0.01 parts by weight and 20 parts by weight with respect to 100 parts by weight of the composite oxide particles.
18. The method according to claim 13 , wherein the composite oxide particles with the deposition component are heated within a temperature range between 500° C. and 1200° C. in the heating step.
19. The method according to claim 13 , wherein an average particle diameter of the cathode active material is ranged between 2.0 μm and 50 μm.
20. The method according to claim 13 , wherein the solvent is removed by adiabatically compressing a chamber containing the composite oxide particles having the deposited solution.
21. The method according to claim 13 , wherein the solvent is removed by drying the composite oxide particles having the deposited solution with a hot air blast.
22. The method according to claim 13 , wherein the deposition component is selected from the group consisting of ammonium sulfate and ammonium pentaborate.