Preparation method of lithium-titanium complex oxide according to particle size control of slurry through wet-milling

Abstract

The present invention relates to a lithium-titanium complex oxide used in an electrode active material. A preparation method of a lithium-titanium complex oxide according to the present invention comprises the steps of: preparing a slurry mixture in which a titanium oxide, lithium and zirconium are mixed; wet-milling the mixture using beads having a size of 0.30 mm or less to obtain a wet-milled mixture; spray drying the wet-milled mixture to obtain a spray dried mixture; and calcining the spray dried mixture.

Claims

1. A preparation method of a lithium-titanium complex oxide, the preparation method comprising the steps of: preparing a slurry mixture in which a titanium oxide, lithium, and zirconium are mixed; wet-milling the slurry mixture for 2 to 7 hours using beads having a size of 0.10 to 0.30 mm to obtain a wet-milled mixture such that a particle size (D.sub.50) of the slurry mixture is controlled to be 0.22 μm or less; spray drying the wet-milled mixture to obtain a spray dried mixture; and calcining the spray dried mixture.

2. The preparation method of claim 1, wherein the wet-milling process is performed at a milling speed of 4,200 rpm.

3. The preparation method of claim 1, wherein the wet-milling step comprises wet-milling the slurry mixture such that the particle size (D.sub.50) is 0.10 μm.

4. The preparation method of claim 1, wherein the slurry mixture has a Li/Ti ratio of 0.81.

5. The preparation method of claim 1, wherein the slurry mixture has a zirconium element contained therein in an amount of 0.01 to 0.10 mol %.

6. The preparation method of claim 1, wherein the spray dried mixture has a particle size (D.sub.50) of 7 to 20 μm.

7. The preparation method of claim 1, wherein the calcination step comprises performing a calcination process at a temperature of 700 to 800° C. in an inert gas atmosphere for 10 to 20 hours.

8. The preparation method of claim 1, further comprising the step of classifying the calcined mixture using a sieve having a sieve size corresponding to 200 to 400 meshes.

9. The preparation method of claim 1, further comprising the step of finely milling the calcined mixture to obtain a finely milled mixture.

10. The preparation method of claim 9, wherein the finely milled mixture has a particle size (D.sub.50) of 0.5 to 2.0 μm.

11. A lithium-titanium complex oxide prepared by preparation method of claim 1, in which Rutile-TiO.sub.2 is contained in an amount of about 1.2 to 1.6%, and Anatase-TiO.sub.2 is contained in an amount of 0%.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIGS. 1A to 1E illustrate Scanning Electron Microscope (SEM) images having primary particle shapes of precursors according to particle sizes of wet-milled slurries of the present invention.

(2) FIGS. 2A to 2E illustrate SEM images having primary particle shapes of calcined products of the present invention.

(3) FIGS. 3A to 3D illustrate SEM images having primary particle cross-sectional shapes of the calcined products of the present invention.

(4) FIG. 4 illustrates results of observing arrival times of an average particle diameter D.sub.50 at which is intended to be arrived according to bead sizes in the wet-milling step of the present invention.

(5) FIG. 5 illustrates a relationship between slurry particles and primary particles of active materials of the present invention.

(6) FIGS. 6A to 6E illustrate expanded SEM images of lithium-titanium complex oxides after finely milling the calcined products according to the present invention.

DESCRIPTION OF EXEMPLARY EMBODIMENTS

(7) Hereinafter, the present invention is described in detail.

(8) A preparation method of a lithium-titanium complex oxide according to an embodiment of the present invention comprises the steps of: preparing a slurry mixture in which a titanium oxide, lithium and zirconium are mixed; wet-milling the mixture using beads having a size of 0.30 mm or less to obtain a wet-milled mixture; spray drying the wet-milled mixture to obtain a spray dried mixture; and calcining the spray dried mixture.

(9) The wet-milling is preferably performed by using a method of performing a wet-milling process using a medium stirring type milling pillar after dispersing the slurry mixture in a dispersion medium. The dispersion medium used for wet-milling of the slurry mixture may include various organic solvents or aqueous solvents, and may preferably include water.

(10) The wet-milling step may comprise performing a wet-milling process for 2 to 7 hours, the wet-milling process may be performed at a milling speed of 4,200 rpm, and a pump may have a rotational speed of 110 to 120 rpm during the milling process.

(11) The wet-milling step preferably comprises wet-milling the slurry mixture to a particle size D.sub.50 of 0.10 μm, and the slurry mixture may be milled to D.sub.max≤1.5 μm. When an average particle diameter of solid particles in the slurry is too large, a final powder packing density tends to be lowered since reactivity is deteriorated in the calcination process, and sphericity of the solid particles is lowered.

(12) A zirconium element may be contained in the slurry mixture in an amount of 0.01 to 0.10 mol %, the slurry mixture may preferably have a Li/Ti ratio of 0.81. When the zirconium element is contained in the slurry mixture in an amount of more than 0.10 mol %, capacity is lowered, and resistance is increased. Therefore, when the zirconium element is contained in the slurry mixture in an amount of less than 0.01 mol %, growth of the primary particles is increased, and deterioration of rate properties is caused.

(13) Gases supplied during the spray drying process may include air, nitrogen and others, and may preferably include air. It is preferable to use pressurized gases obtained after pressurizing the gases. The spray dried mixture may have a particle size D.sub.50 of 7 to 20 μm, and a tap density of 0.68 to 0.79 g/cm.sup.2.

(14) A sprayer used during spray drying may be a rotary disc type sprayer or a nozzle type sprayer, and the nozzle type sprayer may be a pressure nozzle type sprayer or a two-fluid nozzle type sprayer. In addition, the sprayer may include all of means well known in the art such as a rotary sprayer, a pressure nozzle, a pneumatic nozzle, a sonic nozzle, and the like.

(15) In the calcination step, although calcination conditions also depend on a raw material composition, the primary particles are excessively grown if a calcination temperature is too high while a volume density is small, and specific surface area is excessively increased if the calcination temperature is too low. Therefore, an atmosphere during the calcination process in the calcination step may be an oxygen-containing gas atmosphere such as air or the like, or an inert gas atmosphere such as nitrogen, argon or the like, the calcination temperature may be a temperature of 700 to 800° C., and a calcination time may be 10 to 20 hours.

(16) The preparation method of the present invention may further comprise the step of classifying the calcined mixture using a sieve having a sieve size corresponding to 200 to 400 meshes or the step of finely milling the calcined mixture to obtain a finely milled mixture.

(17) In the fine milling step, the calcined mixture may be finely milled using a classifier having a rotational speed of 5,000 to 7,000 rpm at an air pressure of 6.0 to 6.5 bar.

(18) The finely milled mixture may have a particle size D.sub.50 of 0.5 to 2.0 μm.

(19) An intensity of Rutile-TiO.sub.2 compared to a main peak of a lithium-titanium complex oxide of the present invention is about 2%, and an intensity of Anatase-TiO.sub.2 compared to the main peak of the lithium-titanium complex oxide of the present invention is about 1%.

(20) Hereinafter, the present invention will be described in more detail through Examples. These Examples are only for illustrating the present invention, and it is apparent to those skilled in the art that the scope of the present invention is not to be construed as limited to these Examples.

Example 1. Wet-Milling

(21) TiO.sub.2 (COSMO Chemical Co., Ltd, purity≥98%), Li.sub.2CO.sub.3 (SQM, purity≥95%), and Zr(OH).sub.4 (NAOH, purity≥40%) were mixed by designing a Li/Me ratio as 0.81. After mixing the materials, a wet-milling process was performed under conditions including a bead size of 0.30 mm, a milling speed of 4,200 rpm, a rotational speed of a pump of 110 to 120 rpm for 7 hours by using a wet mill. The wet-milling process was performed under conditions (particle sizes and chemical compositions) of the following Table 1 to obtain wet-milled slurry mixtures.

(22) TABLE-US-00001 TABLE 1 Example Example Example Example Example Unit 1-1 1-2 1-3 1-4 1-5 Particle size D.sub.min μm 0.147 0.040 0.040 0.040 0.040 Distribution D.sub.10 0.287 0.101 0.089 0.078 0.057 (slurry) D.sub.50 0.536 0.394 0.304 0.219 0.104 D.sub.90 1.006 0.900 0.795 0.640 0.229 D.sub.max 1.622 1.660 1.445 1.445 1.413 Chemical Li/Ti 0.81 0.81 0.81 0.81 0.81 composition ratio Zr % 0.01 0.01 0.01 0.01 0.01

Comparative Example 1

(23) The wet-milling process was performed in the same manner as in Example 1 except that the bead size was 0.65 mm.

Example 2. Calcination Step

(24) Spray dried slurries were obtained by performing spray drying process on the wet-milled slurry mixtures obtained in Example 1 through a spray dryer under conditions of an inlet temperature of 250° C. and an outlet temperature of 110° C. After performing the spray drying process, calcined products were obtained by performing a calcination process on the spray dried slurries under conditions including a calcination temperature of 700 to 800° C. and a calcination time of 10 to 20 hours by using a firing furnace such as a box furnace or a RHK (Roller Hearth Kiln).

Measurement Example 1. Photographing of SEM Images

(25) After photographing SEM images for particles having particle sizes of slurries that had been wet-milled in Example 1, the photographed SEM images for the particles are illustrated in FIG. 1, and after photographing SEM images for primary particles of active materials that had been calcined in Example 2, the photographed SEM images for the primary particles are illustrated in FIGS. 2A to 2E and FIGS. 3A to 3D.

Measurement Example 2

(26) A graph of comparing average slurry particle diameters D.sub.50 according to wet-milling time variations due to a difference between bead sizes in Example 1 and Comparative Example 1 is illustrated in FIG. 4, and a relationship between sizes of the average slurry particle diameters D.sub.50 of Example 1 and primary particle sizes of the active materials calcined in Example 1 is shown in Table 2 and FIG. 5.

(27) TABLE-US-00002 TABLE 2 Example Example Example Example Example 1-1 1-2 1-3 1-4 1-5 Slurry 0.54 μm 0.39 μm 0.30 μm 0.22 μm 0.10 μm particle size (D.sub.50) Primary 0.55 μm 0.47 μm 0.35 μm 0.23 μm 0.12 μm particle size

Example 3-1. Large Particle Diameter Process (D.SUB.50.: 1.2 to 20 μm)

(28) After classifying calcined products obtained by performing the calcination process in Example 2 using a standard sieve having a sieve size corresponding to 200 to 400 meshes, lithium-titanium complex oxides were finally obtained.

Example 3-2. Small Particle Diameter Process (D.SUB.50.: 0.5 to 2.0 μm)

(29) After finely milling the calcined products obtained by performing the calcination process in Example 2 under conditions including an air pressure of 6.0 to 6.5 bar and a classifier's rotational speed of 5,000 to 7,000 rpm by using a jet air mill, lithium-titanium complex oxides were finally obtained.

Measurement Example 2

(30) After measuring diameters of primary particles from enlarged images obtained by photographing finely milled lithium-titanium complex oxides according to Example 3-2 using a scanning electron microscope, measurement results are illustrated in FIGS. 6A to 6E.

Measurement Example 3. Changes in Characteristics According to Slurry Particle Sizes

(31) After measuring particle sizes, chemical compositions, impurity concentrations, tap densities, Brunauer-Emmett-Teller (BET) surface areas, pH values, electrochemical characteristics, and phase distributions of the spray dried slurries obtained by performing the spray drying process in Example 2, measurement results are shown in Table 3, and after measuring particle sizes, chemical compositions, impurity concentrations, tap densities, BET surface areas, pH values, electrochemical characteristics, and phase distributions of the finely milled slurries obtained by performing a fine milling process on the spray dried slurries, measurement results are shown in Table 4. The phase distributions were calculated using the following Expression 1 and Expression 2.
Rutile-TiO.sub.2 intensity (%)=main peak intensity value of Rutile-TiO.sub.2/main peak intensity value of lithium-titanium complex oxide  Expression 1:
Anatase-TiO.sub.2 intensity (%)=main peak intensity value of Anatase-TiO.sub.2/main peak intensity value of lithium-titanium complex oxide  Expression 2:

(32) TABLE-US-00003 TABLE 3 Example Example Example Example Example Unit 1-1 1-2 1-3 1-4 1-5 Particle size D.sub.min μm 3.90 3.90 3.90 2.60 2.60 distribution D.sub.10 8.78 7.29 7.33 7.89 7.69 D.sub.50 13.70 13.16 13.23 14.15 13.85 D.sub.90 20.27 21.80 21.77 23.34 22.95 D.sub.max 39.23 39.23 34.26 51.47 51.47 Impurities Residual ppm 81 77 127 92 179 LiOH Residual 1,923 1,850 1,557 2,131 2,106 Li.sub.2CO.sub.3 Tap density g/ml 0.79 0.75 0.74 0.71 0.68 BET surface area m.sup.2/g 4.8 5.2 5.8 6.4 7.0 pH — 10.5 10.5 10.5 10.6 10.6 Electro- 0.1 C mAh/g 168.7 169.1 169.5 170.3 170.9 chemical test Discharge 10 C/0.1 C % 78 83 86 89 92 Phase A-TiO.sub.2 % 0.0 0.0 0.0 0.0 0.0 R-TiO.sub.2 1.6 1.5 1.4 1.2 1.2

(33) TABLE-US-00004 TABLE 4 Example Example Example Example Example Unit 1-1 1-2 1-3 1-4 1-5 Particle size D.sub.min μm 0.23 0.23 0.23 0.20 0.20 distribution D.sub.10 0.64 0.62 0.56 0.53 0.54 D.sub.50 1.73 1.69 1.65 1.52 1.36 D.sub.90 4.41 4.36 4.57 4.13 3.32 D.sub.max 11.56 11.56 13.24 11.56 10.10 Impurities Residual ppm 145 195 227 228 279 LiOH Residual 2,528 2,783 2,707 2,899 2,396 Li.sub.2CO.sub.3 Tap density g/ml 0.68 0.63 0.59 0.52 0.45 BET surface area m.sup.2/g 5.5 5.9 6.3 6.9 7.4 pH — 10.5 10.5 10.5 10.6 10.6 Electro- 0.1 C mAh/g 168.7 169.9 170.1 170.4 171.1 chemical test Discharge 10 C/0.1 C % 82 85 87 90 94 Phase A-TiO.sub.2 % 0.0 0.0 0.0 0.0 0.0 R-TiO.sub.2 1.6 1.5 1.4 1.2 1.2

(34) Hereinabove, preferred embodiments of the present invention have been described in detail. However, the scope of the right of the present invention is not limited thereto. The above-disclosed subject matter is to be considered illustrative, and not restrictive, and the appended claims are intended to cover all such modifications, enhancements, and other embodiments, which fall within the true spirit and scope of the present invention. Thus, to the maximum extent allowed by law, the scope of the present invention is to be determined by the broadest permissible interpretation of the following claims and their equivalents, and shall not be restricted or limited by the foregoing detailed description.

(35) According to the present invention, there is an effect that the particle sizes can be adjusted through the milling process by controlling particle sizes of the precursor slurry through wet-milling.

(36) Further, there is an effect of improving tap density, specific surface area and electrochemical characteristics of the lithium-titanium complex oxide that is finally prepared.

(37) The preparation method according to the present invention has an effect that the particle sizes can be adjusted through the milling process by controlling particle sizes of the precursor slurry through wet-milling.

(38) Further, the preparation method according to the present invention has an effect of improving tap density, specific surface area and electrochemical characteristics of the lithium-titanium complex oxide that is finally prepared.