WO2018181465A1 - Lithium composite metal oxide production method - Google Patents

Abstract

This lithium composite metal oxide production method is for producing a lithium composite metal oxide containing at least nickel, and has: a first washing step for washing a lithium composite metal oxide with a first washing liquid; and a second washing step for washing the washed product obtained in the first washing step, with a second washing liquid, wherein the first washing liquid is an alkaline washing liquid containing an alkali metal-containing compound, the second washing liquid is an alkaline washing liquid containing an alkali metal-containing compound and/or an alkaline compound not containing an alkali metal, and the concentration of alkali metals in the first washing liquid with respect to the total mass of the first washing liquid is higher than the concentration of alkali metals in the second washing liquid with respect to the total mass of the second washing liquid.

Description

Method for producing lithium composite metal oxide

The present invention relates to a method for producing a lithium composite metal oxide.
This application claims priority on March 31, 2017 based on Japanese Patent Application No. 2017-072870 filed in Japan, the contents of which are incorporated herein by reference.

The lithium composite metal oxide is used as a positive electrode active material for a lithium secondary battery. Lithium secondary batteries have already been put into practical use not only for small power sources for mobile phones and notebook computers, but also for medium and large power sources for automobiles and power storage.

The method for producing a lithium composite metal oxide generally includes a raw material mixing step, a firing step, and a cleaning step. Water is used as the cleaning liquid used in the cleaning process. For example, Patent Document 1 discloses a process in which a lithium composite metal oxide having a specific composition is baked and then washed with water stirring at a ratio of 50 to 200 parts by weight of water with respect to 100 parts by weight of the lithium composite metal oxide. The manufacturing method of the positive electrode active material for non-aqueous electrolyte secondary batteries which has this is described.

JP 2007-242288 A

As the application field of lithium secondary batteries continues to expand, lithium secondary batteries are required to have further improved battery characteristics such as high initial charge / discharge efficiency, and positive electrode active materials suitable for them.
This invention is made | formed in view of the said situation, Comprising: It aims at providing the manufacturing method of the lithium composite metal oxide suitable for a lithium secondary battery with high initial stage charge / discharge efficiency.

As a result of intensive studies by the present inventors, it has been found that when the washing step is carried out with water, lithium in the lithium composite metal oxide is eluted and the battery characteristics are deteriorated. As a result of intensive studies by the present inventors, the above-mentioned problems have been solved by performing the cleaning process of the lithium composite metal oxide stepwise and using a specific cleaning solution.
That is, the present invention includes the following [1] to [5].
[1] A method for producing a lithium composite metal oxide containing at least nickel, the first cleaning step of cleaning the lithium composite metal oxide with a first cleaning liquid, and the washed product obtained in the first cleaning step. A second cleaning step for cleaning with a second cleaning liquid, wherein the first cleaning liquid is an alkaline cleaning liquid containing a compound containing an alkali metal, and the second cleaning liquid contains an alkali metal. An alkaline cleaning liquid comprising at least one of a compound and an alkaline compound not containing an alkali metal, wherein an alkali metal concentration relative to a total mass of the first cleaning liquid in the first cleaning liquid is the second cleaning liquid The method for producing a lithium composite metal oxide, wherein the concentration of the alkali metal is higher than the total mass of the second cleaning liquid.
[2] The method for producing a lithium composite metal oxide according to [1], wherein the lithium composite metal oxide after the second cleaning step is represented by the following composition formula (I).
Li [Li _x (Ni _(1-yzw) Co _y Mn _z M _w ) _1-x ] O ₂ (I)
(However, M is one or more metal elements selected from the group consisting of Fe, Cu, Ti, Mg, Al, W, B, Mo, Nb, Zn, Sn, Zr, Ga and V, and 0 ≦ x ≦ 0.2, 0 <y ≦ 0.4, 0 ≦ z ≦ 0.4, and 0 ≦ w ≦ 0.1.] [3] In the composition formula (I), y + z + w ≦ 0.3. The method for producing a lithium composite metal oxide according to [2].
[4] The method for producing a lithium composite metal oxide according to any one of [1] to [3], wherein the second cleaning liquid is an aqueous lithium hydroxide solution.
[5] The method for producing a lithium composite metal oxide according to any one of [1] to [4], wherein the concentration of lithium hydroxide in the second cleaning liquid is 1% by mass or more and 30% by mass or less.
[6] The method for producing a lithium composite metal oxide according to any one of [1] to [5], wherein the second cleaning liquid contains ammonia.

According to the present invention, a method for producing a lithium composite metal oxide suitable for a lithium secondary battery having high initial charge / discharge efficiency can be provided.

It is a schematic block diagram which shows an example of a lithium ion secondary battery. It is a schematic block diagram which shows an example of a lithium ion secondary battery.

<Method for producing lithium composite metal oxide>
In the method for producing a lithium composite metal oxide according to the present invention, the production process of the metal composite compound and the production process of the lithium composite metal oxide are optional steps, and the subsequent first cleaning step and second cleaning step are essential. Prepare as a process.
Hereinafter, each step will be described.

In the method for producing a lithium composite metal oxide of the present invention, first, a metal other than lithium, that is, an essential metal composed of Ni, Co, and Mn is included, and optionally Fe, Cu, Ti, Mg, Al, Preparing a metal composite compound containing any one or more of W, B, Mo, Nb, Zn, Sn, Zr, Ga and V, and firing the metal composite compound with an appropriate lithium salt. preferable. As a metal complex compound, a metal complex hydroxide or a metal complex oxide is preferable. Below, an example of the manufacturing method of a positive electrode active material is divided and demonstrated to the manufacturing process of a metal composite compound, and the manufacturing process of a lithium composite metal oxide.

(Production process of metal composite compounds)
The metal complex compound can be produced by a generally known batch coprecipitation method or continuous coprecipitation method. Hereinafter, the manufacturing method will be described in detail by taking a metal composite hydroxide containing nickel, cobalt, and manganese as an example.

The metal complex hydroxide is co-precipitation, in particular by a continuous method described in 2002-201028 JP-nickel salt solution, cobalt salt solution, is reacted manganese salt solution and a complexing agent, Ni _{( 1-yz)} produced by precipitating a composite metal hydroxide represented by Co _y Mn _z (OH) ₂ (where 0 <y ≦ 0.4, 0 ≦ z ≦ 0.4) be able to.

Although it does not specifically limit as nickel salt which is the solute of the said nickel salt solution, For example, any one of nickel sulfate, nickel nitrate, nickel chloride, and nickel acetate can be used. As the cobalt salt that is a solute of the cobalt salt solution, for example, any one of cobalt sulfate, cobalt nitrate, and cobalt chloride can be used. As the manganese salt that is a solute of the manganese salt solution, for example, any one of manganese sulfate, manganese nitrate, and manganese chloride can be used. The above metal salt is used in a proportion corresponding to the composition ratio of Ni _(1-yz) Co _y Mn _z (OH) ₂ . That is, each of the molar ratios of nickel, cobalt, and manganese in the mixed solution containing the metal salt corresponds to (1-yz): y: z in the composition formula (I) of the lithium composite metal compound. Define the amount of metal salt.
Moreover, water is used as a solvent.

The complexing agent is capable of forming a complex with nickel, cobalt, and manganese ions in an aqueous solution. For example, an ammonium ion supplier (ammonium sulfate, ammonium chloride, ammonium carbonate, ammonium fluoride, etc.), hydrazine, Examples include ethylenediaminetetraacetic acid, nitrilotriacetic acid, uracil diacetic acid, and glycine. The complexing agent may not be included if desired. When the complexing agent is included, the amount of the complexing agent contained in the mixed solution containing the nickel salt solution, the cobalt salt solution, the manganese salt solution and the complexing agent. For example, the molar ratio with respect to the total number of moles of the metal salt is greater than 0 and 2.0 or less.

During precipitation, an alkali metal hydroxide (for example, sodium hydroxide or potassium hydroxide) is added if necessary to adjust the pH value of the aqueous solution.

In addition to the nickel salt solution, cobalt salt solution, and manganese salt solution, when a complexing agent is continuously supplied to the reaction vessel, nickel, cobalt, and manganese react to form Ni _(1-yz) Co _y. Mn _z (OH) ₂ is produced. During the reaction, the temperature of the reaction vessel is controlled within a range of, for example, 20 ° C. or more and 80 ° C. or less, preferably 30 ° C. or more and 70 ° C. or less. Hereinafter, it is preferably controlled within a range of pH 11 or more and pH 13 or less, and the substance in the reaction vessel is appropriately stirred. The reaction vessel is of a type that causes the formed reaction precipitate to overflow for separation.

By appropriately controlling the concentration of metal salt to be supplied to the reaction tank, the stirring speed, the reaction temperature, the reaction pH, and the firing conditions described later, the finally obtained lithium composite metal oxide is controlled to have desired physical properties. Can do.

After the above reaction, the obtained reaction precipitate is washed with water and then dried to isolate the nickel cobalt manganese metal composite hydroxide as the nickel cobalt manganese metal composite compound. Moreover, you may wash | clean with the alkaline solution containing weak acid water, sodium hydroxide, or potassium hydroxide as needed.
In the above example, nickel cobalt manganese metal composite hydroxide is manufactured, but nickel cobalt manganese metal composite oxide may be prepared.

In addition, although the example which prepares the metal composite hydroxide containing nickel, cobalt, and manganese was demonstrated, this invention is not limited to this. For example, a metal composite hydroxide containing nickel, cobalt, manganese and tungsten may be prepared. In this case, a metal composite hydroxide containing nickel, cobalt and manganese other than tungsten is prepared by the above method, and then the aqueous solution containing tungsten oxide is dried and deposited on the metal composite hydroxide containing nickel, cobalt and manganese. Thus, a metal composite hydroxide containing nickel, cobalt, manganese and tungsten can be prepared.

As a method of depositing an aqueous solution containing tungsten oxide on a dried metal composite hydroxide containing nickel, cobalt and manganese, the dried metal composite hydroxide containing nickel, cobalt and manganese is 100 ° C. to 200 ° C. For example, a method of spraying an aqueous solution containing tungsten oxide while heating at a temperature may be used.

The concentration of tungsten oxide contained in the aqueous solution containing tungsten oxide is, for example, 1% by mass or more and 10% by mass or less.

The aqueous solution containing tungsten oxide may contain a lithium salt such as lithium hydroxide. The concentration of lithium hydroxide contained in the aqueous solution containing tungsten oxide is 1% by mass or more and 10% by mass or less.

The metal composite hydroxide containing nickel, cobalt, manganese, and tungsten may contain a metal element other than tungsten as the optional metal.

(Lithium composite metal oxide manufacturing process)
The metal composite oxide or hydroxide is dried and then mixed with a lithium salt. The drying conditions are not particularly limited, but, for example, conditions in which the metal composite oxide or hydroxide is not oxidized and reduced (that is, the oxide is maintained as an oxide, the hydroxide is maintained as a hydroxide). Conditions), conditions under which the metal composite hydroxide is oxidized (ie, conditions under which the hydroxide is oxidized into oxide), conditions under which the metal composite oxide is reduced (ie under conditions under which the oxide is reduced into hydroxide) Any of the above conditions may be used. An inert gas such as nitrogen, helium and argon may be used for conditions where oxidation and reduction are not performed. Under conditions where the metal composite hydroxide is oxidized, oxygen or air is used in the atmosphere. Just do it. As a condition for reducing the metal composite oxide, a reducing agent such as hydrazine and sodium sulfite may be used in an inert gas atmosphere. As lithium salt, any one of lithium carbonate, lithium nitrate, lithium sulfate, lithium acetate, lithium hydroxide, lithium hydroxide hydrate, lithium oxide and lithium fluoride, or a mixture of two or more Can be used. In these, any one or both of lithium hydroxide and lithium carbonate are preferable.
Classification may be appropriately performed after the metal composite oxide or hydroxide is dried. The above lithium salt and metal composite metal hydroxide are used in consideration of the composition ratio of the final object. For example, when nickel cobalt manganese composite hydroxide is used, the lithium salt and the composite metal hydroxide are Li _x Ni _(1-yz) Co _y Mn _z O ₂ (where 0 ≦ x ≦ 0. 2, 0 <y ≦ 0.4, 0 ≦ z ≦ 0.4). A lithium-nickel cobalt manganese composite oxide is obtained by firing a mixture of a nickel cobalt manganese metal composite hydroxide and a lithium salt. For the firing, dry air, an oxygen atmosphere, an inert atmosphere, or the like is used according to a desired composition, and a plurality of heating steps are performed if necessary.

The firing temperature of the metal composite oxide or hydroxide and lithium salt such as lithium hydroxide and lithium carbonate is not particularly limited, but is preferably 600 ° C. or higher and 1100 ° C. or lower, and preferably 750 ° C. or higher and 1050 ° C. More preferably, it is 800 ° C. or lower and more preferably 800 ° C. or higher and 1025 ° C. or lower.

The firing time is preferably 3 hours or more and 50 hours or less. When the firing time exceeds 50 hours, the battery performance tends to be substantially inferior due to volatilization of lithium. That is, if the firing time is within 50 hours, the volatilization of lithium can be suppressed. If the firing time is less than 3 hours, the crystal growth is poor and the battery performance tends to be poor. When the firing time is 3 hours or more, the crystal development is good and the battery performance tends to be good.
The firing time is preferably 1 hour or more and 30 hours or less for the total time from the start of raising the temperature to the end of temperature holding. When the total time is 30 hours or less, the volatilization of Li can be prevented and the battery performance can be prevented from deteriorating. When the total time is 1 hour or more, the development of crystals proceeds well, and the battery performance can be improved.
The time from the start of the temperature rise to the firing temperature is preferably 0.5 hours or more and 20 hours or less. When the time from the start of temperature rise to the firing temperature is within this range, a more uniform lithium composite metal oxide can be obtained.
In addition, it is also effective to perform temporary baking before the above baking. The temperature for such preliminary firing is preferably in the range of 300 ° C. to 850 ° C. for 1 hour to 10 hours.

(Washing process)
The present embodiment includes a first cleaning process and a second cleaning process for cleaning the cleaning product obtained in the first cleaning process. The first cleaning step is a step of cleaning and removing the remaining lithium carbonate derived from the raw material. In other words, the first cleaning step is a step of cleaning the lithium composite metal compound and removing residual lithium carbonate derived from the raw material. The second cleaning step is a step of cleaning and removing residual components of the cleaning liquid used in the first cleaning step. In other words, the second cleaning step is a step of cleaning the lithium composite metal compound and removing the cleaning liquid used in the first cleaning step remaining in the lithium composite metal oxide.

In addition, in this specification, “removing” does not mean only when the object is completely removed, but is interpreted to include the case where the object remains partially. For example, the amount of lithium carbonate contained in the lithium composite metal oxide after the first cleaning step should be less than the amount of lithium carbonate contained in the lithium composite metal oxide before the first cleaning step, Lithium carbonate may remain in the lithium composite metal oxide.

-1st washing | cleaning process The 1st washing | cleaning process which wash | cleans lithium composite metal oxide with a 1st washing | cleaning liquid is performed after baking.

The first cleaning liquid is an alkaline cleaning liquid containing a compound containing an alkali metal.
Examples of the compound containing an alkali metal contained in the alkaline cleaning liquid include LiOH (lithium hydroxide), NaOH (sodium hydroxide), KOH (potassium hydroxide), Li ₂ CO ₃ (lithium carbonate), Na ₂ CO _3. Examples thereof include one or more anhydrides selected from the group consisting of (sodium carbonate) and K ₂ CO ₃ (potassium carbonate), and hydrates thereof. From the viewpoint of further suppressing elution of lithium from the lithium composite metal oxide, lithium hydroxide or lithium carbonate is preferable, and lithium hydroxide is more preferable.

The first cleaning liquid can be prepared by dissolving the alkali metal-containing compound in water. The concentration of the compound containing an alkali metal is preferably 1% by mass or more, more preferably 5% by mass or more, and particularly preferably 10% by mass or more with respect to the total mass of the first cleaning liquid. Moreover, 30 mass% or less is preferable, 25 mass% or less is more preferable, and 20 mass% or less is especially preferable. The upper limit and the lower limit of the concentration of the compound containing an alkali metal can be arbitrarily combined. For example, the concentration of the compound containing an alkali metal is preferably 1% by mass to 30% by mass, more preferably 5% by mass to 25% by mass, and more preferably 10% by mass to 20% by mass with respect to the total mass of the first cleaning liquid. A mass% or less is particularly preferred.
When the density | concentration of a 1st washing | cleaning liquid is more than the said lower limit, the elution of lithium from a lithium composite metal oxide can be suppressed more.
It can suppress that the compound containing an alkali metal remains in the lithium complex metal oxide manufactured because the density | concentration of a 1st washing | cleaning liquid is below the said upper limit.

In the present embodiment, the alkali metal concentration relative to the total mass of the first cleaning liquid in the first cleaning liquid is greater than the alkali metal concentration relative to the total mass of the second cleaning liquid in the second cleaning liquid described later. It is also characterized by high. In other words, the concentration of the compound containing an alkali metal with respect to the total mass of the first cleaning liquid in the first cleaning liquid is a compound containing the alkali metal with respect to the total mass of the second cleaning liquid in the second cleaning liquid. Higher than the concentration of.

The ratio of the lithium composite metal oxide after firing to the total mass of the first cleaning liquid in the first cleaning step is preferably 30 to 100% by mass, and more preferably 40 to 60% by mass. When the ratio of the lithium composite metal oxide after firing to the total mass of the first cleaning liquid is 30 to 100% by mass, elution of lithium from the lithium composite metal oxide can be further suppressed, and the manufactured lithium composite metal It can suppress that the compound containing an alkali metal remains in an oxide.

It is surmised that the elution of the lithium component in the lithium composite metal oxide can be suppressed in the cleaning liquid by performing the cleaning process using the first cleaning liquid. For this reason, the concentration gradient of the lithium component on the particle surface of the lithium composite metal oxide to be produced is small, and the remaining lithium carbonate derived from the raw material can be removed while maintaining the lithium component concentration on the particle surface high. Conceivable. In other words, while maintaining a state where the concentration gradient of the lithium component from the inside of the lithium composite metal oxide toward the particle surface is small and the decrease in the lithium component concentration on the particle surface is suppressed, Can be removed. Thereby, the lithium composite metal oxide suitable for a lithium secondary battery with high initial charge / discharge efficiency can be manufactured.

Second cleaning step After the first cleaning step, the second cleaning step includes a second step of cleaning the lithium composite metal oxide with the second cleaning liquid. The second cleaning liquid is an alkaline cleaning liquid. The second cleaning liquid is an alkaline cleaning liquid containing at least one of a compound containing an alkali metal as an alkali component and an alkaline compound not containing an alkali metal.
Examples of the compound containing an alkali metal contained in the second cleaning liquid include LiOH (lithium hydroxide), NaOH (sodium hydroxide), KOH (potassium hydroxide), Li ₂ CO ₃ (lithium carbonate), Na _2. Examples thereof include one or more anhydrides selected from the group consisting of CO ₃ (sodium carbonate) and K ₂ CO ₃ (potassium carbonate), and hydrates thereof. Examples of the alkaline compound not containing an alkali metal include one or more anhydrides selected from the group consisting of (NH ₄ ) ₂ CO ₃ (ammonium carbonate) and NH ₃ (ammonia) and hydrates thereof. The second cleaning liquid is preferably a lithium hydroxide aqueous solution. As described above, ammonia water can also be used as the second cleaning liquid.

The alkaline cleaning liquid as the second cleaning liquid may be a cleaning liquid containing an alkali metal as an alkali component, or may use at least one of ammonia water and ammonium carbonate water as a cleaning liquid without containing an alkali metal as an alkali component. Alternatively, a cleaning liquid containing an alkali metal as an alkali component and further containing at least one of ammonia water and ammonium carbonate water may be used. In the present embodiment, when the second alkali cleaning liquid contains an alkali metal as an alkali component, the alkali metal concentration in the first cleaning liquid is higher than the alkali metal concentration in the second cleaning liquid. Features.
In the case where at least one of ammonia water and ammonium carbonate water is used as the second alkaline cleaning liquid without containing an alkali metal as an alkaline component, the ammonia and ammonium ion concentrations in the second alkaline cleaning liquid are as follows. It may be higher than the concentration of alkali metal in the cleaning liquid.
The concentration of the alkali metal with respect to the total mass of the first cleaning liquid in the first cleaning liquid is preferably twice or more as compared with the concentration of the alkali metal with respect to the total mass of the second cleaning liquid in the second cleaning liquid. .

The second cleaning liquid can be prepared by dissolving the alkali component in water. The concentration of the alkali component in the second cleaning liquid with respect to the total mass of the second cleaning liquid is preferably 0.1% by mass or more, more preferably 1.0% by mass or more, and particularly preferably 2.0% by mass or more. Moreover, the upper limit of the concentration of the aqueous solution of the alkali component only needs to be lower than the concentration of the alkaline component in the first cleaning liquid, and is preferably 30% by mass or less, for example, 20% by mass with respect to the total mass of the second cleaning liquid. % Or less is more preferable, and 10% by mass or less is particularly preferable. The upper limit value and the lower limit value of the concentration of the alkali component in the second cleaning liquid can be arbitrarily combined. For example, the concentration of the alkali component in the second cleaning liquid is preferably 0.1% by mass or more and 30% by mass or less, more preferably 1.0% by mass or more and 20% by mass or less, with respect to the total mass of the second cleaning liquid. 2.0 mass% or more and 10 mass% or less are especially preferable.
When the second cleaning liquid contains both a compound containing an alkali metal and an alkaline compound not containing an alkali metal, the concentration of the alkali component in the second cleaning liquid is the alkali metal relative to the total mass of the second cleaning liquid. Is defined as the ratio of the total of the mass of the compound containing no and the alkali compound containing no alkali metal.
When the concentration of the second cleaning liquid is equal to or higher than the lower limit, the remaining components of the first cleaning liquid are washed by suppressing the elution of the lithium component contained in the manufactured lithium composite metal oxide. Can be removed.
When the concentration of the second cleaning liquid is equal to or lower than the above upper limit value, the remaining components of the first cleaning liquid are removed by cleaning while suppressing the remaining alkali metal-containing compound contained in the second cleaning liquid. it can.

The ratio of the lithium composite metal oxide after firing to the total mass of the second cleaning liquid in the second cleaning step is preferably 3 to 30% by mass, and more preferably 5 to 20% by mass. When the ratio of the lithium composite metal oxide after firing to the total mass of the second cleaning liquid in the second cleaning step is 3 to 30% by mass, the lithium component contained in the manufactured lithium composite metal oxide is eluted. The residual component of the first cleaning liquid can be removed by cleaning while suppressing this. In addition, the residual component of the first cleaning liquid can be removed by cleaning while suppressing the remaining alkali metal-containing compound contained in the second cleaning liquid.

In the first cleaning step and the second cleaning step, as a method of bringing the first or second cleaning liquid into contact with the lithium composite metal oxide, the lithium composite metal oxide is put into an aqueous solution of each cleaning liquid and stirred. The method, a method in which an aqueous solution of each cleaning solution is used as shower water, and the lithium composite metal oxide is washed with the first cleaning solution, and then the wet cake of the lithium composite metal oxide separated from the first cleaning solution The method (reslurry or repulp) which is put into the washing liquid and stirred.
As a preferred embodiment, after the lithium composite metal oxide is added to the first cleaning liquid and stirred, the lithium composite metal oxide is separated from the first cleaning liquid, and then the second cleaning liquid is used as shower water. Examples include a method of applying to the lithium composite metal oxide after separation.

(Drying process)
After the washing step, the lithium composite metal oxide is separated from the washing solution by filtration or the like. Thereafter, it is dried, pulverized as necessary, classified as appropriate, and used as a positive electrode active material applicable to a lithium secondary battery.

(Other processes)
After the drying step, if desired, a step of depositing Al ₂ O ₃ on the surface of the obtained lithium composite metal oxide and baking it may be performed. As firing conditions, an oxygen atmosphere is preferable. The firing temperature is preferably 300 to 850 ° C, more preferably 400 to 780 ° C. The firing time is preferably 1 to 30 hours, and more preferably 3 to 10 hours. By having such a firing step, an Al-containing compound coating layer can be formed on the surface of the lithium composite metal oxide.

In the present embodiment, the produced lithium composite metal oxide is preferably represented by the following composition formula (I).
Li [Li _x (Ni _(1-yzw) Co _y Mn _z M _w ) _1-x ] O ₂ (I)
(However, M is one or more metal elements selected from the group consisting of Fe, Cu, Ti, Mg, Al, W, B, Mo, Nb, Zn, Sn, Zr, Ga and V, and 0 ≦ x ≦ 0.2, 0 <y ≦ 0.4, 0 ≦ z ≦ 0.4, and 0 ≦ w ≦ 0.1 are satisfied.)

From the viewpoint of obtaining a lithium secondary battery having high cycle characteristics, x in the composition formula (I) is preferably more than 0, more preferably 0.01 or more, and particularly preferably 0.02 or more. . Further, from the viewpoint of obtaining a lithium secondary battery having higher initial Coulomb efficiency, x in the composition formula (I) is preferably 0.1 or less, more preferably 0.08 or less, and 0.06. It is particularly preferred that
The upper limit value and the lower limit value of x can be arbitrarily combined. For example, x exceeds 0 and is preferably 0.1 or less, more preferably 0.01 or more and 0.08 or less, and particularly preferably 0.02 or more and 0.06 or less.

Further, from the viewpoint of obtaining a lithium secondary battery with low battery resistance, y in the composition formula (I) is preferably 0.005 or more, more preferably 0.01 or more, and 0.05 or more. It is particularly preferred. Further, from the viewpoint of obtaining a lithium secondary battery having high thermal stability, y in the composition formula (I) is more preferably 0.35 or less, and particularly preferably 0.33 or less.
The upper limit value and the lower limit value of y can be arbitrarily combined. For example, y is preferably 0.005 or more and 0.35 or less, more preferably 0.01 or more and 0.33 or less, and particularly preferably 0.05 or more and 0.33 or less.

Further, from the viewpoint of obtaining a lithium secondary battery having high cycle characteristics, z in the composition formula (I) is preferably 0.01 or more, more preferably 0.03 or more, and 0.1 or more. It is particularly preferred. Further, from the viewpoint of obtaining a lithium secondary battery having high storage characteristics at a high temperature (for example, in an environment of 60 ° C.), z in the composition formula (I) is preferably 0.4 or less, and is 0.38 or less. Is more preferable, and it is especially preferable that it is 0.35 or less.
The upper limit value and lower limit value of z can be arbitrarily combined. For example, z is preferably 0.01 or more and 0.4 or less, more preferably 0.03 or more and 0.38 or less, and particularly preferably 0.1 or more and 0.35 or less.

Further, from the viewpoint of obtaining a lithium secondary battery with low battery resistance, w in the composition formula (I) is preferably more than 0, more preferably 0.0005 or more, and 0.001 or more. Particularly preferred. Further, from the viewpoint of obtaining a lithium secondary battery having a high discharge capacity at a high current rate, w in the composition formula (I) is preferably 0.09 or less, more preferably 0.08 or less, and 0 0.07 or less is particularly preferable.
The upper limit value and the lower limit value of w can be arbitrarily combined. For example, w exceeds 0 and is preferably 0.09 or less, more preferably 0.0005 or more and 0.08 or less, and particularly preferably 0.001 or more and 0.07 or less.

M in the composition formula (I) is one or more metals selected from the group consisting of Fe, Cu, Ti, Mg, Al, W, B, Mo, Nb, Zn, Sn, Zr, Ga, and V. To express.

Further, from the viewpoint of obtaining a lithium secondary battery with high cycle characteristics, M in the composition formula (I) is one or more metals selected from the group consisting of Ti, Mg, Al, W, B, and Zr. From the viewpoint of obtaining a lithium secondary battery with high thermal stability, it is more preferably one or more metals selected from the group consisting of Al, W, B, and Zr.

(Layered structure)
The crystal structure of the lithium nickel composite oxide is a layered structure, and more preferably a hexagonal crystal structure or a monoclinic crystal structure.

The hexagonal crystal structures are P3, P3 ₁ , P3 ₂ , R3, P-3, R-3, P312, P321, P3 ₁ 12, P3 ₁ 21, P3 ₂ 12, P3 ₂ 21, R32, P3m1, P31m, P3c1, P31c, R3m, R3c, P-31m, P-31c, P-3m1, P-3c1, R-3m, R-3c, P6, P6 ₁ , P6 ₅ , P6 ₂ , P6 ₄ , P6 ₃ , P-6, P6 / m, P6 ₃ / m, P622, P6 ₁ 22, P6 ₅ 22, P6 ₂ 22, P6 ₄ 22, P6 ₃ 22, P6 mm, P6 cc, P6 ₃ cm, P6 ₃ mc, P- It belongs to any one space group selected from the group consisting of 6m2, P-6c2, P-62m, P-62c, P6 / mmm, P6 / mcc, P6 ₃ / mcm, and P6 ₃ / mmc.

Monoclinic crystal structures are P2, P2 ₁ , C2, Pm, Pc, Cm, Cc, P2 / m, P2 ₁ / m, C2 / m, P2 / c, P2 ₁ / c, and C2. It belongs to any one space group selected from the group consisting of / c.

Among these, from the viewpoint of obtaining a lithium secondary battery having a high discharge capacity, the crystal structure is a hexagonal crystal structure belonging to the space group R-3m or a monoclinic crystal belonging to C2 / m. A crystal structure is particularly preferred.

The lithium salt used in the present invention is any one of lithium carbonate, lithium nitrate, lithium sulfate, lithium acetate, lithium hydroxide, lithium oxide, lithium chloride, lithium fluoride, or a mixture of two or more. can do. In these, any one or both of lithium hydroxide and lithium carbonate are preferable.
From the viewpoint of improving the handleability of the positive electrode active material for a lithium secondary battery, the lithium carbonate component contained in the lithium composite metal oxide is preferably 0.4% by mass or less based on the total mass of the lithium composite metal oxide. More preferably, it is 0.39 mass% or less, and it is especially preferable that it is 0.38 mass% or less.
In addition, from the viewpoint of improving the handling property of the positive electrode active material for a lithium secondary battery, the lithium hydroxide component contained in the lithium composite metal oxide is 0.35% by mass or less based on the total mass of the lithium composite metal oxide. The content is preferably 0.25% by mass or less, and particularly preferably 0.2% by mass or less.

The general formula (I) does not include H and C derived from lithium carbonate and lithium hydroxide. This is because lithium carbonate and lithium hydroxide contained in the lithium composite metal oxide are not contained in the crystal structure of the lithium composite metal oxide.

<Lithium secondary battery>
Next, while explaining the configuration of the lithium secondary battery, a positive electrode using the positive electrode active material for a lithium secondary battery of the present invention as a positive electrode active material of the lithium secondary battery, and a lithium secondary battery having the positive electrode will be described. To do.

An example of the lithium secondary battery of the present embodiment includes a positive electrode and a negative electrode, a separator sandwiched between the positive electrode and the negative electrode, and an electrolytic solution disposed between the positive electrode and the negative electrode.

1A and 1B are schematic views showing an example of the lithium secondary battery of the present embodiment. The cylindrical lithium secondary battery 10 of this embodiment is manufactured as follows.

First, as shown in FIG. 1A, a pair of separators 1 having a strip shape, a strip-like positive electrode 2 having a positive electrode lead 21 at one end, and a strip-like negative electrode 3 having a negative electrode lead 31 at one end, a separator 1, a positive electrode 2, and a separator 1 and negative electrode 3 are laminated in this order and wound to form electrode group 4.

Next, as shown in FIG. 1B, after the electrode group 4 and an insulator (not shown) are accommodated in the battery can 5, the bottom of the can is sealed, the electrode group 4 is impregnated with the electrolytic solution 6, the positive electrode 2, the negative electrode 3, An electrolyte is placed between the two. Furthermore, the lithium secondary battery 10 can be manufactured by sealing the upper part of the battery can 5 with the top insulator 7 and the sealing body 8.

As the shape of the electrode group 4, for example, a columnar shape in which the cross-sectional shape when the electrode group 4 is cut in a direction perpendicular to the winding axis is a circle, an ellipse, a rectangle, or a rectangle with rounded corners. Can be mentioned.

Moreover, as a shape of the lithium secondary battery having such an electrode group 4, a shape defined by IEC 60086 or JIS C 8500 which is a standard for a battery defined by the International Electrotechnical Commission (IEC) can be adopted. . For example, cylindrical shape, square shape, etc. can be mentioned.

Further, the lithium secondary battery is not limited to the above-described wound type configuration, and may have a stacked type configuration in which a stacked structure of a positive electrode, a separator, a negative electrode, and a separator is repeatedly stacked. Examples of the stacked lithium secondary battery include so-called coin-type batteries, button-type batteries, and paper-type (or sheet-type) batteries.

Hereafter, each structure is demonstrated in order.
(Positive electrode)
The positive electrode of this embodiment can be manufactured by first adjusting a positive electrode mixture containing a positive electrode active material, a conductive material and a binder, and supporting the positive electrode mixture on a positive electrode current collector.

(Conductive material)
As the conductive material included in the positive electrode of the present embodiment, a carbon material can be used. Examples of the carbon material include graphite powder, carbon black (for example, acetylene black), and a fibrous carbon material. Since carbon black is fine and has a large surface area, by adding a small amount to the positive electrode mixture, the conductivity inside the positive electrode can be improved and the charge / discharge efficiency and output characteristics can be improved. Both the binding force between the positive electrode mixture and the positive electrode current collector and the binding force inside the positive electrode mixture are reduced, which causes an increase in internal resistance.

The proportion of the conductive material in the positive electrode mixture is preferably 5 parts by mass or more and 20 parts by mass or less with respect to 100 parts by mass of the positive electrode active material. When a fibrous carbon material such as graphitized carbon fiber or carbon nanotube is used as the conductive material, this ratio can be lowered.

(binder)
As the binder included in the positive electrode of the present embodiment, a thermoplastic resin can be used.
Examples of the thermoplastic resin include polyvinylidene fluoride (hereinafter sometimes referred to as PVdF), polytetrafluoroethylene (hereinafter sometimes referred to as PTFE), tetrafluoroethylene, hexafluoropropylene, and vinylidene fluoride. And fluororesins such as copolymers, propylene hexafluoride / vinylidene fluoride copolymers, tetrafluoroethylene / perfluorovinyl ether copolymers; polyolefin resins such as polyethylene and polypropylene.

These thermoplastic resins may be used as a mixture of two or more. By using a fluororesin and a polyolefin resin as a binder, the ratio of the fluororesin to the total positive electrode mixture is 1% by mass or more and 10% by mass or less, and the ratio of the polyolefin resin is 0.1% by mass or more and 2% by mass or less. A positive electrode mixture having both high adhesion to the current collector and high bonding strength inside the positive electrode mixture can be obtained.

(Positive electrode current collector)
As the positive electrode current collector included in the positive electrode of the present embodiment, a band-shaped member made of a metal material such as Al, Ni, and stainless steel can be used. Among these, a material that is made of Al and formed into a thin film is preferable because it is easy to process and inexpensive.

Examples of the method of supporting the positive electrode mixture on the positive electrode current collector include a method of pressure-molding the positive electrode mixture on the positive electrode current collector. Also, the positive electrode mixture is made into a paste using an organic solvent, and the resulting positive electrode mixture paste is applied to at least one surface side of the positive electrode current collector, dried, pressed and fixed, whereby the positive electrode current collector is bonded to the positive electrode current collector. A mixture may be supported.

When the positive electrode mixture is made into a paste, usable organic solvents include amine solvents such as N, N-dimethylaminopropylamine and diethylenetriamine; ether solvents such as tetrahydrofuran; ketone solvents such as methyl ethyl ketone; methyl acetate And amide solvents such as dimethylacetamide and N-methyl-2-pyrrolidone (hereinafter sometimes referred to as NMP).

Examples of the method of applying the positive electrode mixture paste to the positive electrode current collector include a slit die coating method, a screen coating method, a curtain coating method, a knife coating method, a gravure coating method, and an electrostatic spray method.

A positive electrode can be manufactured by the method mentioned above.
(Negative electrode)
The negative electrode included in the lithium secondary battery of this embodiment is only required to be able to dope and dedope lithium ions at a lower potential than the positive electrode, and the negative electrode mixture containing the negative electrode active material is supported on the negative electrode current collector. And an electrode composed of the negative electrode active material alone.

(Negative electrode active material)
Examples of the negative electrode active material possessed by the negative electrode include carbon materials, chalcogen compounds (oxides, sulfides, etc.), nitrides, metals, and alloys that can be doped and dedoped with lithium ions at a lower potential than the positive electrode. It is done.

Examples of carbon materials that can be used as the negative electrode active material include graphite such as natural graphite and artificial graphite, cokes, carbon black, pyrolytic carbons, carbon fibers, and organic polymer compound fired bodies.

The oxide can be used as an anode active _material, (wherein, x represents a positive real number) SiO 2, SiO, etc. formula SiO _x oxides of silicon represented _by; TiO 2, TiO, etc. formula TiO _x (wherein , X is a positive real number); oxide of titanium represented by formula VO _x (where x is a positive real number) such as V ₂ O ₅ and VO ₂ ; Fe ₃ O ₄ , Fe ₂ O ₃ , FeO, etc. Iron oxide represented by the formula FeO _x (where x is a positive real number); SnO ₂ , SnO, etc. represented by the formula SnO _x (where x is a positive real number) Oxide of tin; tungsten oxide represented by general formula WO _x (where x is a positive real number) such as WO ₃ and WO ₂ ; lithium and titanium such as Li ₄ Ti ₅ O ₁₂ and LiVO ₂ Or a composite metal oxide containing vanadium; It is possible.

Examples of sulfides that can be used as the negative electrode active material include titanium sulfides represented by the formula TiS _x (where x is a positive real number) such as Ti ₂ S ₃ , TiS ₂ , and TiS; V ₃ S ₄ , VS _2, VS and other vanadium sulfides represented by the formula VS _x (where x is a positive real number); Fe ₃ S ₄ , FeS ₂ , FeS and other formulas FeS _x (where x is a positive real number) Iron sulfide represented; Mo ₂ S ₃ , MoS _{2 and the} like MoS _x (where x is a positive real number) Molybdenum sulfide; SnS _2, SnS and other formula SnS _x (where, a sulfide of tin represented by x is a positive real number; a sulfide of tungsten represented by a formula WS _x (where x is a positive real number) such as WS ₂ ; a formula SbS _x such as Sb ₂ S ₃ (here And x is a positive real number) antimony sulfide; Se ₅ S ₃ , selenium sulfide represented by the formula SeS _x (where x is a positive real number) such as SeS ₂ and SeS.

Examples of the nitride that can be used as the negative electrode active material include Li ₃ N and Li _3-x A _x N (where A is one or both of Ni and Co, and 0 <x <3). And lithium-containing nitrides.

These carbon materials, oxides, sulfides and nitrides may be used alone or in combination of two or more. These carbon materials, oxides, sulfides and nitrides may be crystalline or amorphous.

Further, examples of the metal that can be used as the negative electrode active material include lithium metal, silicon metal, and tin metal.

Alloys that can be used as the negative electrode active material include lithium alloys such as Li—Al, Li—Ni, Li—Si, Li—Sn, and Li—Sn—Ni; silicon alloys such as Si—Zn; Sn—Mn, Sn -Tin alloys such as Co, Sn-Ni, Sn-Cu, Sn-La; alloys such as Cu ₂ Sb, La ₃ Ni ₂ Sn ₇ ;

These metals and alloys are mainly used alone as electrodes after being processed into a foil shape, for example.

Among the negative electrode active materials, the potential of the negative electrode hardly changes from the uncharged state to the fully charged state at the time of charging (potential flatness is good), the average discharge potential is low, and the capacity retention rate when repeatedly charged and discharged is For reasons such as high (good cycle characteristics), carbon materials containing graphite as a main component, such as natural graphite and artificial graphite, are preferably used. The shape of the carbon material may be any of a flake shape such as natural graphite, a spherical shape such as mesocarbon microbeads, a fibrous shape such as graphitized carbon fiber, or an aggregate of fine powder.

The negative electrode mixture may contain a binder as necessary. Examples of the binder include thermoplastic resins, and specific examples include PVdF, thermoplastic polyimide, carboxymethyl cellulose, polyethylene, and polypropylene.

(Negative electrode current collector)
Examples of the negative electrode current collector included in the negative electrode include a band-shaped member made of a metal material such as Cu, Ni, and stainless steel. In particular, it is preferable to use Cu as a forming material and process it into a thin film from the viewpoint that it is difficult to make an alloy with lithium and it is easy to process.

As a method of supporting the negative electrode mixture on such a negative electrode current collector, as in the case of the positive electrode, a method using pressure molding, pasting with a solvent, etc., applying to the negative electrode current collector, drying and pressing. The method of crimping is mentioned.

(Separator)
Examples of the separator included in the lithium secondary battery of the present embodiment include porous films, nonwoven fabrics, and woven fabrics made of materials such as polyolefin resins such as polyethylene and polypropylene, fluororesins, and nitrogen-containing aromatic polymers. A material having the following form can be used. Moreover, a separator may be formed by using two or more of these materials, or a separator may be formed by laminating these materials.

In the present embodiment, the separator allows the electrolyte to permeate well when the battery is used (during charging / discharging). Therefore, the air resistance according to the Gurley method defined in JIS P 8117 is 50 seconds / 100 cc or more, 300 seconds / 100 cc. Or less, more preferably 50 seconds / 100 cc or more and 200 seconds / 100 cc or less.

Further, the porosity of the separator is preferably 30% by volume or more and 80% by volume or less, more preferably 40% by volume or more and 70% by volume or less with respect to the volume of the separator. The separator may be a laminate of separators having different porosity.

(Electrolyte)
The electrolyte solution included in the lithium secondary battery of this embodiment contains an electrolyte and an organic solvent.

The electrolyte contained in the electrolyte includes LiClO ₄ , LiPF ₆ , LiAsF ₆ , LiSbF ₆ , LiBF ₄ , LiCF ₃ SO ₃ , LiN (SO ₂ CF ₃ ) ₂ , LiN (SO ₂ C ₂ F ₅ ) ₂ , LiN (SO ₂ CF ₃ ) (COCF ₃ ), Li (C ₄ F ₉ SO ₃ ), LiC (SO ₂ CF ₃ ) ₃ , Li ₂ B ₁₀ Cl ₁₀ , LiBOB (where BOB is bis (oxalato) borate LiFSI (where FSI is bis (fluorosulfonyl) imide), lower aliphatic carboxylic acid lithium salts, and lithium salts such as LiAlCl ₄ , and two or more of these Mixtures may be used. Among them, as the electrolyte, at least selected from the group consisting of LiPF ₆ , LiAsF ₆ , LiSbF ₆ , LiBF ₄ , LiCF ₃ SO ₃ , LiN (SO ₂ CF ₃ ) ₂ and LiC (SO ₂ CF ₃ ) ₃ containing fluorine. It is preferable to use one containing one kind.

Examples of the organic solvent contained in the electrolyte include propylene carbonate, ethylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, 4-trifluoromethyl-1,3-dioxolan-2-one, and 1,2-di- Carbonates such as (methoxycarbonyloxy) ethane; 1,2-dimethoxyethane, 1,3-dimethoxypropane, pentafluoropropyl methyl ether, 2,2,3,3-tetrafluoropropyl difluoromethyl ether, tetrahydrofuran, 2- Ethers such as methyltetrahydrofuran; Esters such as methyl formate, methyl acetate and γ-butyrolactone; Nitriles such as acetonitrile and butyronitrile; N, N-dimethylformamide, N, N-dimethyla Amides such as toamide; Carbamates such as 3-methyl-2-oxazolidone; Sulfur-containing compounds such as sulfolane, dimethyl sulfoxide, 1,3-propane sultone, or those obtained by further introducing a fluoro group ( One obtained by substituting one or more hydrogen atoms in the organic solvent with fluorine atoms can be used.

It is preferable to use a mixture of two or more of these as the organic solvent. Of these, a mixed solvent containing carbonates is preferable, and a mixed solvent of cyclic carbonate and acyclic carbonate and a mixed solvent of cyclic carbonate and ethers are more preferable. As a mixed solvent of a cyclic carbonate and an acyclic carbonate, a mixed solvent containing ethylene carbonate, dimethyl carbonate and ethyl methyl carbonate is preferable. The electrolyte using such a mixed solvent has a wide operating temperature range, hardly deteriorates even when charged and discharged at a high current rate, hardly deteriorates even when used for a long time, and natural graphite as an active material of the negative electrode. Even when a graphite material such as artificial graphite is used, it has many features that it is hardly decomposable.

Further, as the electrolytic solution, it is preferable to use an electrolytic solution containing a lithium salt containing fluorine such as LiPF ₆ and an organic solvent having a fluorine substituent because the safety of the obtained lithium secondary battery is increased. A mixed solvent containing ethers having fluorine substituents such as pentafluoropropyl methyl ether and 2,2,3,3-tetrafluoropropyl difluoromethyl ether and dimethyl carbonate is capable of capacity even when charging / discharging at a high current rate. Since the maintenance rate is high, it is more preferable.

A solid electrolyte may be used instead of the above electrolytic solution. As the solid electrolyte, for example, an organic polymer electrolyte such as a polyethylene oxide polymer compound, a polymer compound containing at least one of a polyorganosiloxane chain or a polyoxyalkylene chain can be used. Moreover, what is called a gel type which hold | maintained the non-aqueous electrolyte in the high molecular compound can also be used. Also Li ₂ S—SiS ₂ , Li ₂ S—GeS ₂ , Li ₂ S—P ₂ S ₅ , Li ₂ S—B ₂ S ₃ , Li ₂ S—SiS ₂ —Li ₃ PO ₄ , Li ₂ S—SiS ₂ -Li ₂ SO _4, and an inorganic solid electrolyte can be mentioned include a sulfide such as _{Li 2 S-GeS 2 -P 2} S 5, it may be used a mixture of two or more thereof. By using these solid electrolytes, the safety of the lithium secondary battery may be further improved.

In the lithium secondary battery of this embodiment, when a solid electrolyte is used, the solid electrolyte may serve as a separator, and in that case, the separator may not be required.

Since the positive electrode active material having the above-described configuration uses the above-described lithium-containing composite metal oxide of the present embodiment, the first charge / discharge efficiency of the lithium secondary battery using the positive electrode active material can be improved. .

Moreover, since the positive electrode having the above-described configuration has the above-described positive electrode active material for a lithium secondary battery according to the present embodiment, the initial charge / discharge efficiency of the lithium secondary battery can be improved.

Furthermore, since the lithium secondary battery having the above-described configuration has the positive electrode described above, it becomes a secondary battery with higher initial charge / discharge efficiency than before.

Another aspect of the present invention is a method for producing a lithium composite metal oxide containing at least nickel, the first cleaning step of cleaning the lithium composite metal oxide with a first cleaning liquid, and the first cleaning step. A second washing step of washing the washed product with a second washing liquid, wherein the first washing liquid and the second washing liquid are alkaline washing liquids each containing a compound containing an alkali metal, The concentration of the alkali metal in the first cleaning liquid with respect to the total mass of the first cleaning liquid is 10% by mass to 20% by mass, and the alkali metal in the second cleaning liquid with respect to the total mass of the second cleaning liquid The concentration is 2% by mass or more and 10% by mass or less, and the concentration of the alkali metal in the first cleaning liquid with respect to the total mass of the first cleaning liquid is the second cleaning with respect to the total mass of the second cleaning liquid. Higher than the concentration of the alkali metal in a method for producing a lithium mixed metal oxide.

In the method for producing a lithium composite metal oxide, at least one of the alkali metal-containing compounds contained in the first cleaning liquid and the second cleaning liquid is lithium hydroxide.

In the method for producing a lithium composite metal oxide, the alkali metal-containing compound contained in the first cleaning liquid and the second cleaning liquid is lithium hydroxide.

Another aspect of the present invention is a method for producing a lithium composite metal oxide containing at least nickel, the first cleaning step of cleaning the lithium composite metal oxide with a first cleaning liquid, and the first cleaning step. A second washing step of washing the washed product with a second washing liquid, wherein the first washing liquid and the second washing liquid are alkaline washing liquids each containing a compound containing an alkali metal, The concentration of alkali metal in the first cleaning liquid with respect to the total mass of the first cleaning liquid is 2.5 to 20 times the concentration of alkali metal in the second cleaning liquid with respect to the total mass of the second cleaning liquid. And a method for producing a lithium composite metal oxide.

In the method for producing a lithium composite metal oxide, at least one of the alkali metal-containing compounds contained in the first cleaning liquid and the second cleaning liquid is lithium hydroxide.

In the method for producing a lithium composite metal oxide, the alkali metal-containing compound contained in the first cleaning liquid and the second cleaning liquid is lithium hydroxide.

Another aspect of the present invention is a lithium secondary battery positive electrode containing a lithium composite metal oxide as a positive electrode active material, a separator on the lithium secondary battery positive electrode, and a lithium secondary battery negative electrode on the separator. When an R2032 type lithium secondary battery containing at least the electrolyte solution injected into the separator is manufactured and the initial charge / discharge efficiency is measured (by the method described in this specification), the initial charge / discharge is 87 to 89%. It is a lithium composite metal oxide having characteristics indicating efficiency.

Next, the present invention will be described in more detail with reference to examples.

In this example, evaluation of the lithium composite metal oxide and production evaluation of the positive electrode for the lithium secondary battery and the lithium secondary battery were performed as follows.

<Composition analysis>
The composition analysis of the lithium composite metal oxide powder produced by the method described below is carried out by dissolving the obtained lithium composite metal oxide powder in hydrochloric acid and then using an inductively coupled plasma emission spectrometer (SII Nanotechnology Co., Ltd.). Manufactured by SPS3000).

<Preparation of positive electrode for lithium secondary battery>
A lithium composite metal oxide obtained by a production method described later is used as a positive electrode active material, and the positive electrode active material, a conductive material (acetylene black), and a binder (PVdF) are combined into a positive electrode active material for a lithium secondary battery: a conductive material: a binder. = 92: 5: 3 (mass ratio) was added and kneaded to prepare a paste-like positive electrode mixture. In preparing the positive electrode mixture, N-methyl-2-pyrrolidone was used as the organic solvent.

The obtained positive electrode mixture was applied to an Al foil having a thickness of 40 μm serving as a current collector and vacuum-dried at 150 ° C. for 8 hours to obtain a positive electrode for a lithium secondary battery. The electrode area of the positive electrode for the lithium secondary battery was 1.65 cm ² .

<Preparation of negative electrode for lithium secondary battery>
Next, artificial graphite (manufactured by Hitachi Chemical Co., Ltd., MAGD) as the negative electrode active material, CMC (manufactured by Daiichi Kogyo Co., Ltd.) and SBR (manufactured by Nippon A & L Co., Ltd.) as the binder, and negative electrode active material: CMC: A paste-like negative electrode mixture was prepared by adding and kneading so as to have a composition of SRR = 98: 1: 1 (mass ratio). During the preparation of the negative electrode mixture, ion-exchanged water was used as a solvent.

The obtained negative electrode mixture was applied to a 12 μm thick Cu foil serving as a current collector and vacuum dried at 60 ° C. for 8 hours to obtain a negative electrode for a lithium secondary battery. The electrode area of the negative electrode for a lithium secondary battery was 1.77 cm ² .

<Production of lithium secondary battery (coin type half cell)>
The following operations were performed in a glove box with an argon atmosphere.
Place the positive electrode for the lithium secondary battery prepared in <Preparation of Lithium Secondary Battery Positive Electrode> on the lower lid of the parts for Coin Type Battery R2032 (manufactured by Hosen Co., Ltd.) with the aluminum foil surface facing downward. A laminated film separator (laminated heat-resistant porous layer (thickness: 16 μm) on a polyethylene porous film) was placed thereon. 300 μl of electrolyte was injected here. The electrolytic solution was ethylene carbonate (hereinafter sometimes referred to as EC), dimethyl carbonate (hereinafter sometimes referred to as DMC), and ethyl methyl carbonate (hereinafter sometimes referred to as EMC) 30:35. : 35 (volume ratio) a mixture of LiPF ₆ dissolved to 1.0 mol / l (hereinafter sometimes referred to as LiPF ₆ / EC + DMC + EMC) was used.
Next, using lithium metal as the negative electrode, the negative electrode is placed on the upper side of the laminated film separator, covered with a gasket, and then caulked with a caulking machine to form a lithium secondary battery (coin type half cell R2032, hereinafter "half cell"). Was prepared.

<Discharge test>
Using the half cell produced in <Preparation of lithium secondary battery (coin-type half cell)>, an initial charge / discharge test was performed under the following conditions.

<Charge / discharge test conditions>
Test temperature: 25 ° C
Maximum charging voltage 4.3V, charging time 6 hours, charging current 0.2CA, constant current constant voltage charging Minimum discharging voltage 2.5V, discharging time 5 hours, discharging current 0.2CA, constant current discharging

The initial charge / discharge efficiency is obtained from the following equation.
<First charge / discharge efficiency (%)>
(Initial discharge capacity [mAh / g]) ÷ (Initial charge capacity [mAh / g]) × 100

Example 1
1. Production of Lithium Composite Metal Oxide 1 After water was placed in a reaction vessel equipped with a stirrer and an overflow pipe, an aqueous sodium hydroxide solution was added to keep the liquid temperature at 50 ° C.

A nickel sulfate aqueous solution, a cobalt sulfate aqueous solution, a manganese sulfate aqueous solution, and an aluminum sulfate aqueous solution have an atomic ratio of nickel atom, cobalt atom, manganese atom, and aluminum atom of 87.5: 9.5: 2.0: 1.0. It mixed so that the mixed raw material liquid might be prepared.

Next, with stirring, the mixed raw material solution and the aqueous ammonium sulfate solution were continuously added as a complexing agent to the reaction vessel, and nitrogen gas was continuously passed through. A sodium hydroxide aqueous solution was dropped in a timely manner so that the pH of the solution in the reaction vessel measured at 40 ° C. was 11.0 to obtain a nickel cobalt manganese aluminum composite hydroxide, washed with the sodium hydroxide aqueous solution, and then centrifuged. By dehydrating and isolating with a separator, and drying at 105 ° C., nickel cobalt manganese aluminum composite hydroxide was obtained.
A lithium hydroxide aqueous solution in which tungsten oxide was dissolved was prepared. The concentration of tungsten oxide in the prepared tungsten-dissolved lithium hydroxide aqueous solution was 61 g / L. The concentration of lithium hydroxide in the tungsten-dissolved lithium hydroxide aqueous solution was 66.6 g / L. A tungsten-dissolved lithium hydroxide aqueous solution was deposited on the nickel cobalt manganese aluminum composite hydroxide so that W / (Ni + Co + Mn + W) = 0.004 (molar ratio) to obtain nickel cobalt manganese aluminum tungsten composite hydroxide 1. It was.

The nickel-cobalt-manganese-aluminum-tungsten composite hydroxide 1 and lithium hydroxide powder obtained as described above were weighed and mixed so that Li / (Ni + Co + Mn + Al + W) = 1.10 (molar ratio), and then mixed with oxygen. Firing product 1 was obtained by firing at 760 ° C. for 5 hours in an atmosphere.

[First cleaning step]
200 g of the fired product 1 was added to 467 g of a 15% by mass lithium hydroxide aqueous solution to prepare a slurry-like liquid, and the slurry-like liquid was stirred for 10 minutes to perform the first washing step.

[Second cleaning step]
The slurry-like liquid obtained in the first washing step is subjected to suction filtration, and 2000 g of 1.0% by mass lithium hydroxide aqueous solution is further added to the obtained wet cake, followed by suction filtration. The process was performed. Then, it was dried in an air atmosphere at 150 ° C. for 12 hours.
The obtained dried powder was coated with alumina nanopowder and fired at 760 ° C. for 10 hours in an oxygen atmosphere to obtain the target lithium composite metal oxide 1.

2. Evaluation of Lithium Composite Metal Oxide 1 The composition analysis of the obtained lithium composite metal oxide 1 was performed, and when it was made to correspond to the composition formula (I), x = 0.02, y = 0.092, z = 0. 020, w = 0.024, M = W, Al.

(Example 2)
1. Production of lithium composite metal oxide 2 Lithium composite metal oxide 2 was prepared in the same manner as in Example 1 except that the first cleaning step and the second cleaning step were performed using the cleaning liquid shown in Table 1 below. Manufactured.

2. Evaluation of Lithium Composite Metal Oxide 2 The composition analysis of the obtained lithium composite metal oxide 2 was performed, and when it was made to correspond to the composition formula (I), x = 0.02, y = 0.092, z = 0. 020, w = 0.023, M = W, Al.

(Comparative Example 1)
1. Production of lithium composite metal oxide 3 Lithium composite metal oxide 3 was prepared in the same manner as in Example 1 except that the first cleaning step and the second cleaning step were performed using the cleaning liquid shown in Table 1 below. Manufactured.

2. Evaluation of Lithium Composite Metal Oxide 3 The composition analysis of the obtained lithium composite metal oxide 3 was conducted and made to correspond to the composition formula (I). As a result, x = −0.02, y = 0.093, z = 0 0.021, w = 0.024, M = W, Al.

(Comparative Example 2)
1. Production of lithium composite metal oxide 4 Lithium composite metal oxide 4 was produced in the same manner as in Example 1 except that the first cleaning step and the second cleaning step were performed using the cleaning liquid shown in Table 1 below. Manufactured.

2. Evaluation of Lithium Composite Metal Oxide 4 The composition analysis of the obtained lithium composite metal oxide 4 was performed and made to correspond to the composition formula (I). As a result, x = −0.01, y = 0.092, z = 0. .018, w = 0.023, M = W, Al.

(Comparative Example 3)
1. Production of lithium composite metal oxide 5 Lithium composite metal oxide 5 was prepared in the same manner as in Example 1 except that the first cleaning step and the second cleaning step were performed using the cleaning liquid shown in Table 1 below. Manufactured.

2. Evaluation of Lithium Composite Metal Oxide 5 The composition analysis of the obtained lithium composite metal oxide 5 was performed, and when it was made to correspond to the composition formula (I), x = −0.02, y = 0.092, z = 0. .018, w = 0.023, M = W, Al.

As shown in the above results, Examples 1 and 2 in which the cleaning process to which the present invention was applied were performed had higher initial charge / discharge efficiency than Comparative Examples 1 to 3 to which the present invention was not applied. This is because when the present invention is applied, the elution of lithium from the lithium composite metal oxide is small and the concentration gradient of lithium on the surface of the lithium composite metal oxide is small compared to the case of washing with pure water. Can be considered.

According to the present invention, a method for producing a lithium composite metal oxide having high initial charge / discharge efficiency can be provided.

DESCRIPTION OF SYMBOLS 1 ... Separator, 2 ... Positive electrode, 3 ... Negative electrode, 4 ... Electrode group, 5 ... Battery can, 6 ... Electrolyte solution, 7 ... Top insulator, 8 ... Sealing body, 10 ... Lithium secondary battery, 21 ... Positive electrode lead, 31 ... Negative electrode lead

Claims (6)

1. A method for producing a lithium composite metal oxide containing at least nickel,
   A first cleaning step of cleaning the lithium composite metal oxide with a first cleaning liquid;
   A second washing step of washing the washed product obtained in the first washing step with a second washing liquid,
   The first cleaning liquid is an alkaline cleaning liquid containing a compound containing an alkali metal,
   The second cleaning liquid is an alkaline cleaning liquid containing at least one of a compound containing an alkali metal and an alkaline compound not containing an alkali metal,
   Lithium composite metal oxidation wherein the concentration of alkali metal in the first cleaning liquid relative to the total mass of the first cleaning liquid is higher than the concentration of alkali metal in the second cleaning liquid relative to the total mass of the second cleaning liquid Manufacturing method.
2. The method for producing a lithium composite metal oxide according to claim 1, wherein the lithium composite metal oxide after the second cleaning step is represented by the following composition formula (I).
   Li [Li _x (Ni _(1-yzw) Co _y Mn _z M _w ) _1-x ] O ₂ (I)
   (However, M is one or more metal elements selected from the group consisting of Fe, Cu, Ti, Mg, Al, W, B, Mo, Nb, Zn, Sn, Zr, Ga and V, and 0 ≦ x ≦ 0.2, 0 <y ≦ 0.4, 0 ≦ z ≦ 0.4, and 0 ≦ w ≦ 0.1 are satisfied.)
3. The method for producing a lithium composite metal oxide according to claim 2, wherein y + z + w ≦ 0.3 in the composition formula (I).
4. The method for producing a lithium composite metal oxide according to any one of claims 1 to 3, wherein the second cleaning liquid is an aqueous lithium hydroxide solution.
5. The lithium mixed metal oxide according to any one of claims 1 to 4, wherein a concentration of lithium hydroxide in the second cleaning liquid is 1% by mass or more and 30% by mass or less based on a total mass of the second cleaning liquid. Manufacturing method.
6. The method for producing a lithium composite metal oxide according to any one of claims 1 to 5, wherein the second cleaning liquid is aqueous ammonia.

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