KR101375704B1 - Precursor of cathode active material for lithium secondary battery and preparation method thereof - Google Patents

Abstract

A cathode active material precursor for a lithium secondary battery comprising nickel manganese cobalt hydroxide particles of Formula 1 prepared by adding an alkali solution to a mixed metal salt solution of nickel manganese cobalt and controlling a pH and stirring rpm and performing a coprecipitation reaction, has a short length. Since the average value of the sphericity, which is the ratio of the major axis length to, is 1.3 to 1.8, it can be used in a lithium secondary battery to improve electrical characteristics:
Formula 1
Ni _x Co _y Mn _(1-xy) (OH) ₂
Wherein 0.33 ≦ x ≦ 0.80 and 0 ≦ y ≦ 0.33, where 0 <x + y <1.

Description

Cathode active material precursor for lithium secondary battery and manufacturing method therefor {PRECURSOR OF CATHODE ACTIVE MATERIAL FOR LITHIUM SECONDARY BATTERY AND PREPARATION METHOD THEREOF}

The present invention relates to a precursor used in the production of a lithium secondary battery cathode active material and a method for producing the same.

As the technology development and demand for mobile devices have increased, the demand for secondary batteries has increased sharply as an energy source. Among such secondary batteries, lithium secondary batteries having high energy density and operating potential, long cycle life, Have been commercialized and widely used.

Lithium-containing cobalt oxide (LiCoO ₂ ) is mainly used as a positive electrode active material of a lithium secondary battery. In addition, lithium-containing manganese oxides such as LiMnO _{2 in a} layered crystal structure and LiMn ₂ O _{4 in a} spinel crystal structure, and lithium-containing nickel oxide (LiNiO ₂ ) and the use of LiNi _x Mn _y CO _(1-xy) O ₂ of the ternary system are also considered.

Generally, the positive electrode active material of a lithium secondary battery is manufactured by a solid state reaction at a high temperature of 700 ° C. or higher. However, when the cathode active material is manufactured by the solid phase reaction method, since the mixing and grinding are performed physically, the mixing state is uneven, and thus, the mixing and grinding process must be performed several times. Will rise.

Accordingly, a wet manufacturing method represented by the sol-gel process and co-precipitation, which consist of hydrolysis and condensation, has been developed. Among these, the coprecipitation method is a method of precipitating chloride, nitride, or sulfide containing a raw material with hydroxide in a basic coprecipitation solution and calcining it to prepare an oxide powder. Control of pH, temperature, and agitation conditions of the coprecipitation solution is necessary.

Conventional coprecipitation technology implementation is mainly carried out by a continuous stirred-tank reactor (CSTR). However, these methods have a problem in that all metal hydroxides finally obtained do not have an optimum sphericity, densification degree, etc. through a constant coprecipitation reaction time. For example, if the coprecipitation reaction time is too long, the final particle of the secondary particle is increased, and the amount of fines falling from the secondary borrowing increases. On the contrary, when the coprecipitation reaction time is insufficient, the completeness of the primary particle and the composition of the secondary particle are reduced. The amount of fines may increase and sphericity and density may decrease.

In addition, in order to improve the safety of the lithium secondary battery, it is necessary to control the particle distribution of less than 3㎛ excellent in electrochemical reactivity, the conventional method of manufacturing a metal hydroxide by a continuous reactor is a high spherical shape at the entire particle size through the coprecipitation reaction It is difficult to realize particle distribution that ensures degree and density. In other words, low growth fines can be partially solved through the introduction of additional processes, but require high additional costs, and low spherical particles do not inhibit the improvement of tap or electrode density in the final product, but additional fines during heat treatment The possibility of the occurrence of and the formation of high-density electrode is likely to intensify the secondary particle cracking phenomenon.

Accordingly, the present inventors have found that the sphericity of the particles can be controlled by appropriately changing the flow, pH value, reaction time, and the like of the solution in the reactor, and completed the present invention.

Accordingly, an object of the present invention is to provide a precursor of a cathode active material for producing a lithium secondary battery excellent in electrical characteristics and the like and a method of manufacturing the same.

In accordance with the above object, the present invention comprises a particle of the hydroxide of nickel manganese cobalt represented by the following formula (1), the spherical figure which is the ratio (l / w) of the long axis length (l) to the short axis length (w) of the particles It provides a cathode active material precursor for a lithium secondary battery, the average value of the (sphericity coefficient) is 1.3 to 1.8:

Formula 1

Ni _x Co _y Mn _(1-xy) (OH) ₂

Wherein 0.33 ≦ x ≦ 0.80 and 0 ≦ y ≦ 0.33, where 0 <x + y <1.

In addition, the present invention is adjusted to pH 10 to 13 by adding an alkaline solution to the mixed metal salt solution of nickel manganese cobalt and then stirred at 500 to 1,000 rpm to perform a coprecipitation reaction to the nickel manganese cobalt hydroxide particles of the formula (1) It provides a method for producing a cathode active material precursor for a lithium secondary battery, comprising the step of manufacturing.

The positive electrode active material precursor particles for a lithium secondary battery according to the present invention may be manufactured to have a specific range of sphericity through adjustment of pH, stirring RPM, etc. during the coprecipitation reaction, and when used as a positive electrode active material for the production of a lithium secondary battery The electrical characteristics of the battery can be improved.

1 and 2 are high and low magnification SEM images of the precursor particles obtained in Example 1, respectively.
3 is a high magnification SEM image of the precursor particles obtained in Example 2. FIG.
4 is a high magnification SEM image of the precursor particles obtained in Example 3. FIG.
5 and 6 are high and low magnification SEM images of the precursor particles obtained in Comparative Example 1, respectively.
7 is a high magnification SEM image of the precursor particles obtained in Comparative Example 2. FIG.
8 is a high magnification SEM image of the precursor particles obtained in Comparative Example 3. FIG.
9 is an XRD result of the precursor particles obtained in Example 1. FIG.
10 is a graph comparing the charge and discharge characteristics of the positive electrode active material obtained using the precursors obtained in Example 1 and Comparative Example 1.
11 is a graph comparing the charge and discharge characteristics of the positive electrode active material obtained using the precursors obtained in Example 2 and Comparative Example 2.

Hereinafter, the present invention will be described more specifically.

The present invention relates to a cathode active material precursor for a lithium secondary battery comprising particles of a hydroxide of nickel manganese cobalt represented by Formula 1 below:

Formula 1

Ni _x Co _y Mn _(1-xy) (OH) ₂

Wherein 0.33 ≦ x ≦ 0.80 and 0 ≦ y ≦ 0.33, where 0 <x + y <1.

The precursor particles according to the present invention have an average value of sphericity coefficient, which is the ratio (l / w) of the major axis length (l) to the minor axis length (w), of 1.3 to 1.8, more preferably 1.4 to 1.7. When the average value of the sphericity of the particles is within the above range, there is an advantage of high tap density, there is an advantage of high electrode density and high capacity and high output in the final lithium secondary battery.

The average particle diameter (D50) of the precursor particles according to the present invention is in the range of 5 to 20 µm, more preferably in the range of 6 to 12 µm. In addition, it is preferable that the SPAN value used as the prescribed index of the particle size distribution is in the range of 0.5 to 0.8.

Moreover, the tap density after baking of the precursor particle which concerns on this invention is 2 g / cc or more, for example, 2.0-2.6 g / cc, More preferably, it is 2.1 g / cc or more. When the tap density of the particles is within the above range, it is possible to implement a high electrode density, there is an advantage that it is easy to manufacture a high capacity battery.

In addition, the present invention includes the step of adding an alkaline solution to the mixed metal salt solution of nickel manganese cobalt, performing stirring and coprecipitation reaction to prepare the nickel manganese cobalt hydroxide particles of the formula (1), a cathode active material precursor for a lithium secondary battery It provides a method of manufacturing.

At this time, it is necessary to adjust the pH to 10 to 13 of the mixed metal salt solution of nickel manganese cobalt by the alkaline solution, more preferably to adjust to pH 10.5 to 12.0, most preferably pH 11.0 to 11.4 It is good. When the pH is in the above range, the precursor particles obtained by the coprecipitation reaction may have a range of uniformity and sphericity degree desired in the present invention, and the precursor particles may be prevented by re-dissolving a part of the precipitation of the resulting precursor particles. It can be made to have a desired composition ratio, and there is an advantage that can increase the tap density of the powder.

The stirring speed is preferably 500 to 1,000 rpm, more preferably 600 to 900 rpm. When the stirring speed is within the above range, the collision between particles is sufficient, while the aggregation efficiency between particles is high, but the collision recovery and collision strength between particles are appropriate, so that aggregation between particles for the production of precursor particles of a desired size can occur more efficiently.

In addition, the residence time (RT) in the reactor is preferably 1 to 6 hours in the case of the Kuet Taylor reactor, and 3 to 12 hours is preferable in the case of the continuous reactor (CSTR), the uniform precursor particles are stable in the above range Has the advantage of being manufactured.

The concentration of the metal salt solution is preferably 1.0 to 4.0 M, more preferably 1.5 to 2.5 M. The yield of precursor particles produced when the concentration of the metal salt solution is within the above range is further increased.

In addition, nickel salts that may be included in the mixed metal salt of nickel manganese cobalt may be nickel sulfate, nickel nitrate, nickel hydrochloride, and the like, and the cobalt salt may be cobalt sulfate, cobalt nitrate, and the like. Manganese nitrate, manganese hydrochloride, and the like are possible, of which nickel sulfate, cobalt sulfate, or manganese sulfate is most preferred.

The molar ratio of these raw metal salts is preferably mixed so that the molar ratio of Ni: Co: Mn in the nickel salt, cobalt salt, and manganese salt falls within the molar ratio range of the general formula (1).

On the other hand, the lithium transition metal composite oxide prepared using the precursor containing Ni, Co, and Mn as described above, when the charge and discharge in some high potential region, the lifespan characteristics may decrease due to the change in crystal structure Can be. In order to solve this problem, Fe, Ga, Ge, Al, Ti, V, Cu, Zn, Si, P, Nb, Ta, Zr, Zn, Sn, Sb, Pt, In, Ag, Au, Bi, By doping a metal selected from the group consisting of Pd, W and Nb, the cycle characteristics can be significantly improved in the high potential region, and the doping of the metal is performed in the step of introducing the mixed metal salt solution into the reactor, by using Fe, Ga, Ge Metal salts of metals selected from the group consisting of Al, Ti, V, Cu, Zn, Si, P, Nb, Ta, Zr, Zn, Sn, Sb, Pt, In, Ag, Au, Bi, Pd, W and Nb It can be made by adding additional solution.

The alkaline solution serves to control the pH of the metal salt solution introduced into the reactor as a coprecipitation agent to an appropriate range, and specific examples thereof may preferably use an aqueous sodium hydroxide solution or an aqueous ammonia solution. These alkali solutions can add 1 type (s) or 2 or more types together.

The temperature during the coprecipitation reaction is preferably from room temperature to 90 ℃, more preferably from 40 ℃ to 90 ℃.

In the present invention, the coprecipitation reaction may be carried out using a continuous reactor or a Kuet Taylor reactor.

For example, in a continuous reactor, the sphericity of the whole particles can be continuously controlled by controlling the RPM in an appropriate range, and in the Kuet Taylor reactor, the final metal hydroxides are produced sequentially in the order of the coprecipitation reaction, so that the continuous The sphericity of the particles can be controlled.

First, in the case of using a continuous reactor, it is important to keep the reaction residence time as similar as possible, and similar sphericity control at a certain range of residence time can be controlled by changing the RPM. That is, when the average retention time is 10 hours, the range of RPM forming the shape of similar particles in the range of 5 to 15 hours is obtained, and the RPM value is sequentially changed according to pH and reaction time within the range. By doing so, the degree of sphericity can be kept constant. For example, by rotating the stirrer at 800 to 1000 rpm until the initial stabilization of the coprecipitation reaction, the stirring speed is lowered to 600 to 700 rpm over 3 to 24 hours, and then raised to the original speed range again. The change of can be repeated continuously between the above ranges, to prepare a cathode active material precursor.

In the case of the Kuet Taylor reactor, it is possible to adjust the sphericity more easily than in the case of using a continuous reactor. In the case of the coprecipitation reaction involving the rotation of the particles, the growth direction of the particles is determined by the change of the pH value. The sphericity of the particles thus formed will depend on the pH value at the same composition and vortex rotation conditions.

The prepared cathode active material precursor may additionally undergo baking for 8 to 12 hours in an oxidation furnace at 800 to 1,300 ° C. When the firing process is performed, the cathode active material precursor particles may be stably grown while improving adhesion between crystals, thereby obtaining cathode particles having a more uniform particle size.

In addition, the present invention provides a cathode active material for a lithium secondary battery prepared by adding and sintering a lithium compound to the cathode active material precursor for a lithium secondary battery. The lithium compound may, for example, be Li ₂ CO ₃ .

When the cathode active material manufactured as described above is used in the production of a lithium secondary battery, there is an effect of improving the electrical characteristics such as initial capacity, output characteristics, cycle life, and volumetric energy density of the lithium secondary battery.

Hereinafter, the present invention will be described in more detail with reference to the following examples. The following examples are only examples of the present invention, but the scope of the present invention is not limited thereto.

Example 1 Preparation of Cathode Active Material Precursor (Using Queuth Taylor Reactor)

A metal salt solution having a total concentration of 2M by mixing NiSO ₄ 6H ₂ O, CoSO ₄ 7H ₂ O, and MnSO ₄ H ₂ O in a molar ratio of 1: 1 and adding distilled water after N ₂ purging. Was prepared. The prepared metal salt solution was introduced at a rate of 200 mL / h through a metal salt solution supply part of a reactor (manufacturer: Lamina, product name: CT reactor) using 1 L of Kuet Taylor vortex.

25% aqueous ammonia solution was introduced at a rate of 35 mL / h through the ammonia aqueous solution supply of the reactor, and 40% aqueous sodium hydroxide solution was automatically added at a rate of 85-100 mL / h through the aqueous sodium hydroxide solution of the reactor. The pH meter and control were used to maintain pH 11.2. The temperature of the reactor was 40 ℃, the residence time (RT) was adjusted to 3 hours, and stirred at 600 rpm.

The obtained reaction solution was filtered through a filter, purified with distilled water, and then dried to obtain a final cathode active material precursor particle.

Example 2: Preparation of Cathode Active Material Precursor (Using Queuth Taylor Reactor)

A cathode active material precursor was prepared in the same manner as in Example 1 except for mixing NiSO ₄ 6H ₂ O, CoSO ₄ 7H ₂ O, and MnSO ₄ H ₂ O in a molar ratio of 5: 2: 3. .

Example 3: Preparation of Cathode Active Material Precursor (Using Continuous Reactor)

NiSO ₄ and 6H ₂ O, CoSO ₄ and 7H ₂ O and the MnSO ₄ and H ₂ O molar ratio of 1: 1 were mixed in 1, adding the distilled water, subjected to N ₂ purge the total concentration to prepare a 2M of the metal salt solution . The prepared metal salt solution was added to a continuous reactor (CSTR, manufacturer: EMS Tech, product name: CSTR-L0) at a rate of 250 mL / h.

25% aqueous ammonia solution was introduced at a rate of 40 mL / h through the ammonia aqueous solution supply of the reactor, while 40% sodium hydroxide aqueous solution was automatically added at a rate of 105-120 mL / h through the aqueous sodium hydroxide solution of the reactor. pH 11.3 was maintained via a pH meter and controls. The temperature of the reactor was 40 ℃, the residence time (RT) was adjusted to 10 hours, and stirred at a speed of 800rpm.

The obtained reaction solution was filtered through a filter, purified with distilled water, and then dried to obtain a final cathode active material precursor particle.

Comparative Example 1: Preparation of Cathode Active Material Precursor (Using Continuous Reactor)

NiSO ₄ and 6H ₂ O, CoSO ₄ and 7H ₂ O and the MnSO ₄ and H ₂ O molar ratio of 1: 1 were mixed in 1, adding the distilled water, subjected to N ₂ purge the total concentration to prepare a 2M of the metal salt solution . The prepared metal salt solution was added to a continuous reactor (CSTR, manufacturer: EMS Tech, product name: CSTR-L0) at a rate of 250 mL / h.

25% aqueous ammonia solution was introduced at a rate of 40 mL / h through the ammonia aqueous solution supply of the reactor, while 40% sodium hydroxide aqueous solution was automatically added at a rate of 105-120 mL / h through the aqueous sodium hydroxide solution of the reactor. pH 11 was maintained via a pH meter and controls. The temperature of the reactor was 40 ℃, the residence time (RT) was adjusted to 10 hours, and stirred at a speed of 450rpm.

The obtained reaction solution was filtered through a filter, purified with distilled water, and then dried to obtain a final cathode active material precursor particle.

Comparative Example 2: Preparation of Cathode Active Material Precursor (Using Continuous Reactor)

A cathode active material precursor was prepared in the same manner as in Comparative Example 1 except for mixing NiSO ₄ 6H ₂ O, CoSO ₄ 7H ₂ O, and MnSO ₄ H ₂ O in a molar ratio of 5: 2: 3. .

Comparative Example 3: Preparation of Cathode Active Material Precursor (Using Continuous Reactor)

A pH active material was prepared in the same manner as in Comparative Example 1 except that the pH was maintained at 11.35 through a pH meter and a controller, and the stirring speed was 400 rpm.

Test Example 1: SEM Analysis

The positive electrode active material precursors obtained in Examples and Comparative Examples were observed using a scanning electron microscope (SEM).

1 and 2 are high and low magnification SEM images of the precursor particles obtained in Example 1, FIG. 3 is a high magnification SEM image of the precursor particles obtained in Example 2, and FIG. 4 is a high magnification SEM of the precursor particles obtained in Example 3 5 and 6 are high and low magnification SEM images of the precursor particles obtained in Comparative Example 1, FIG. 7 is a high magnification SEM image of the precursor particles obtained in Comparative Example 2, and FIG. 8 is a precursor particle obtained in Comparative Example 3 High magnification SEM image of.

As shown in Figures 1 to 8, it can be seen that the precursor particles obtained in Examples 1 to 3 have an elliptical shape on average, and the precursor particles obtained in Comparative Examples 1 to 2 have a shape almost close to a sphere. In addition, it can be seen that the precursor particles obtained in Comparative Example 3 have a more elliptical shape than those obtained in Examples 1 to 3.

Test Example 2: Measurement of Sphericality

After obtaining the length of the major axis (l) and the minor axis (w) of the representative particles in the positive electrode active material precursor obtained through an SEM image, the sphericity (l / w) was calculated. The results are shown in Table 1 below.

In order to measure the sphericity, samples of Examples 1 to 3 and Comparative Examples 1 to 3 were collected by 30, and the long and short axes of the particles were measured, and the average value was determined. That is, the length of the long axis and short axis of all 90 particles for each Example or Comparative Example was measured and the average value is shown in Table 1 below.

Test Example 3: SPAN Measurement

The SPAN value was measured with a SPAN meter (S3000, Microtrack, Inc.) and is shown in Table 1 below.

The SPAN value is used as the particle size distribution specification index and is defined as (D90-D10) / D50, where D90, D10 and D50 each represent 90%, 10% and 50% of the particles by volume in the size distribution. It means the diameter, and the closer to SPAN value, the more uniform.

Test Example 4 Measurement of Tap Density

The tap density was measured by a tap density meter (Auto Tap Analyzer, Quantachrome), and is shown in Table 1 below.

Test Example 5: XRD Measurement

X-ray diffraction was performed on the positive electrode active material precursor. Figure 9 shows the XRD results of the positive electrode active material precursor prepared in Example 1, it can be seen that the metal complex hydroxide was obtained normally.

division Long axis length
(l, ㎛) Short Length
(w, μm) Spherical diagram
(l / w) SPAN Tap density
(g / cc)
Example 1 Measurement 1 7.52 5.61 1.34 Average
1.48 0.59 2.15 Measurement 2 7.97 5.13 1.55 0.61 2.17 Measurement 3 6.23 4.00 1.56 0.62 2.17
Example 2 Measurement 1 8.32 4.65 1.79 Average
1.69 0.66 2.25 Measurement 2 7.71 4.77 1.61 0.63 2.18 Measurement 3 6.84 4.10 1.67 0.64 2.20
Example 3 Measurement 1 9.34 5.32 1.76 Average
1.56 0.67 2.14 Measurement 2 6.65 4.94 1.35 0.59 2.13 Measurement 3 10.22 6.52 1.57 0.62 2.16
Comparative Example 1 Measurement 1 5.16 4.13 1.25 Average
1.20 0.99 1.88 Measurement 2 5.45 4.65 1.17 0.95 1.91 Measurement 3 4.52 3.81 1.19 0.96 1.92
Comparative Example 2 Measurement 1 7.52 6.81 1.10 Average
1.19 0.82 2.03 Measurement 2 8.32 6.68 1.25 0.86 2.10 Measurement 3 8.84 7.32 1.21 0.85 2.08
Comparative Example 3 Measurement 1 2.93 1.54 1.90 Average
1.90 0.94 1.90 Measurement 2 2.70 1.36 1.99 1.01 1.76 Measurement 3 2.33 1.29 1.81 0.99 1.83

As shown in Table 1, the precursor particles of Examples 1 to 3 can be seen that the average value of the sphericity (l / w) is 1.3 to 1.8 is slightly out of the spherical shape, the SPAN value is small, the particles are uniform It can be seen that the tap density is excellent at 2.1g / cc or more. On the other hand, the precursor particles of Comparative Examples 1 and 2 can be seen that the spherical degree (l / w) average value is close to 1, the shape is almost spherical, the SPAN value is high, the particles are non-uniform, the tap density is low. have. In addition, the precursor particles of Comparative Example 3 were far from the spherical shape because the average value (l / w) of the spherical degree (l / w) was nearly 2, and the particles were uneven and the tap density was low due to the highest SPAN value. It can be seen.

Preparation of Cathode Active Material

Using the positive electrode active material precursors obtained in Examples and Comparative Examples, respectively, the positive electrode active material precursor and Li ₂ CO ₃ are mixed in a stoichiometric molar ratio (Li: M = 1.1: 1), and the mixture is 950-1000 in air. By calcining (calcination) for 10 hours at a temperature range of ℃, to prepare a positive electrode active material containing a lithium mixed transition metal oxide, respectively.

Manufacture of Lithium Secondary Battery

The obtained cathode active materials were mixed so that the ratio of the active material, the conductive material, and the binder were 95: 3: 2, thereby obtaining a slurry, and the slurry was coated on the Al foil by a doctor blade method to obtain respective electrodes. Li metal was used as the negative electrode, and electrolytic solution containing 1 M LiPF ₆ in EC: EMC (1: 2) was used as an electrolyte, and a lithium secondary battery was prepared by placing a separator between the positive electrode and the negative electrode.

Using the prepared lithium secondary battery, various characteristics were evaluated as follows, and the results are shown in Table 2 below.

Test Example 6: Evaluation of Charge and Discharge Capacity

Charging and discharging characteristics of the lithium secondary battery manufactured by using the cathode active materials prepared in Examples and Comparative Examples were evaluated. At this time, after the cutoff voltage range was 3.0 to 4.5V, 1C = 180mAh / g, and 0.1C initial charge and discharge. The test was performed at room temperature under the conditions of 0.2C-0.5C-1C-2C-5C. The results are shown in FIGS. 10 and 11.

Test Example 7 Evaluation of High Rate Discharge Characteristics

For lithium secondary batteries manufactured using the positive electrode active materials prepared in Examples and Comparative Examples, the battery discharge capacity was measured until the discharge voltage of the battery became 3.0 V by discharging currents of 1 C and 5 C. . The results are shown in Table 2 below.

1C capacity
(mAh / g) 5C capacity
(mAh / g) (5C capacity / 1C capacity) x 100
(%) Example 1 167.6 145.4 86.8 Example 2 171.4 149.7 87.3 Comparative Example 1 157.3 132.5 84.2 Comparative Example 2 166.1 134.4 80.9

From Table 2, it can be seen that the positive electrode active material prepared using the precursors obtained in Examples 1 and 2 shows high 1C capacity and excellent high output characteristics.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is clearly understood that the same is by way of illustration and example only and is not to be taken by way of limitation, It is to be understood that the invention may be practiced within the scope of the appended claims.

Claims (8)

An average value of a sphericity coefficient including particles of a hydroxide of nickel manganese cobalt represented by the following Chemical Formula 1 and a ratio (l / w) of the major axis length (l) to the minor axis length (w) of the particle is 1.3 To 1.8, a cathode active material precursor for a lithium secondary battery:
Formula 1
Ni _x Co _y Mn _(1-xy) (OH) ₂
Wherein 0.33 ≦ x ≦ 0.80 and 0 ≦ y ≦ 0.33, where 0 <x + y <1.
The method of claim 1,
The average value of the sphericity is 1.4 to 1.7, the cathode active material precursor for a lithium secondary battery.
The method of claim 1,
An average particle diameter of the particles is 5 to 20 ㎛, the tap density after firing is 2.0 to 2.6 g / cc, the cathode active material precursor for a lithium secondary battery.
Adding an alkaline solution to the mixed metal salt solution of nickel manganese cobalt to adjust the pH to 10 to 13, followed by stirring at 500 to 1,000 rpm, and performing a coprecipitation reaction to prepare nickel manganese cobalt hydroxide particles of Formula 1 below. Method for producing a cathode active material precursor for a lithium secondary battery according to claim 1:
Formula 1
Ni _x Co _y Mn _(1-xy) (OH) ₂
Wherein 0.33 ≦ x ≦ 0.80 and 0 ≦ y ≦ 0.33, where 0 <x + y <1.
5. The method of claim 4,
The coprecipitation reaction is performed by adding an alkaline solution to a mixed metal salt solution of nickel manganese cobalt to adjust the pH to 11.0 to 11.4 and stirring at 600 to 900 rpm, to prepare a cathode active material precursor for a lithium secondary battery. Way.
5. The method of claim 4,
The alkaline solution is a sodium hydroxide aqueous solution, ammonia aqueous solution or a mixture thereof, characterized in that the method for producing a cathode active material precursor for a lithium secondary battery.
5. The method of claim 4,
The coprecipitation reaction is characterized in that carried out using a continuous reactor (CSTR) or Kuet Taylor reactor, a method for producing a cathode active material precursor for a lithium secondary battery.
A cathode active material for a lithium secondary battery prepared by adding a lithium compound to the cathode active material precursor for a lithium secondary battery of claim 1 and sintering.

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