JP5830842B2 - Method for producing lithium titanate particle powder and non-aqueous electrolyte secondary battery - Google Patents

Description

  The present invention provides an inexpensive and simple method for producing lithium titanate particles having an excellent initial discharge capacity and a high high rate discharge capacity retention rate as an active material for a non-aqueous electrolyte secondary battery.

  In recent years, electronic devices such as AV devices and personal computers are rapidly becoming portable and cordless, and there is an increasing demand for secondary batteries having a small size, light weight, and high energy density as power sources for driving these devices. Under such circumstances, a lithium ion secondary battery having advantages such as a high charge / discharge voltage and a large charge / discharge capacity has attracted attention.

  Conventionally, in this lithium ion secondary battery, it is known to use lithium titanate as a negative electrode active material (Patent Document 1).

Lithium titanate Li ₄ Ti ₅ O ₁₂ is known as a highly reliable negative electrode active material having high structural stability because the crystal structure change in the lithium ion insertion / extraction reaction due to charge / discharge is very small.

Conventionally, a manufacturing method for obtaining lithium titanate Li ₄ Ti ₅ O ₁₂ is a mixed powder obtained by dry or wet mixing lithium salt and titanium oxide so that Li / Ti = 0.80. A so-called solid phase reaction method is known in which Li ₄ Ti ₅ O ₁₂ is obtained by heating and baking a mixture of lithium salt and titanium oxide. (Patent Documents 1 to 4)

  Further, as a method similar to the above solid-phase reaction method, a production method in which a slurry containing a titanium oxide, a titanic acid compound (metatitanic acid, orthotitanic acid or a mixture thereof) and a lithium salt is dried and granulated and then heated and fired. Is also known. (Patent Documents 5 and 6)

On the other hand, a step of reacting a titanium compound and an ammonium compound in water to obtain a titanate compound, a step of reacting the titanate compound and a lithium compound in water to obtain a lithium titanate hydrate, the lithium titanate hydration A method for producing lithium titanate Li ₄ Ti ₅ O ₁₂ comprising a step of heat-dehydrating an object is known. (Patent Document 7)

JP-A-6-275263 JP 2001-192208 A Japanese Patent Laid-Open No. 2001-240498 JP 2003-137547 A JP-A-2005-239460 JP 2005-239461 A JP-A-9-309727

  As an active material for a non-aqueous electrolyte secondary battery, an inexpensive and simple production method for obtaining lithium titanate particles having an excellent initial discharge capacity and a high high discharge capacity retention rate is currently most demanded. Although it is, it has not been obtained yet.

That is, Patent Documents 1 to 4 are mixed powders obtained by dry or wet mixing lithium salt and titanium oxide so that Li / Ti = 0.80 (these are simply a mixture of lithium salt and titanium oxide. ) To obtain Li ₄ Ti ₅ O ₁₂ . These are production methods generally known as solid phase reaction methods, but in order to obtain a Li ₄ Ti ₅ O ₁₂ type spinel type single phase, firing at a high temperature, or firing and pulverization at least twice. Often it is necessary to repeat the method. Therefore, it is difficult to obtain a compositionally uniform spinel type structure single phase lithium titanate Li ₄ Ti ₅ O ₁₂ fine particles, and when this is used as a negative electrode active material of a lithium ion secondary battery, an excellent initial It is difficult to say that the discharge capacity and the high rate discharge capacity maintenance ratio are high.

  In addition, in the production methods of Patent Documents 5 and 6, a slurry containing a titanium compound and a lithium compound (lithium salt) is dried and granulated, and then heated and fired to produce lithium titanate. A titanium compound containing at least a titanic acid compound (orthotitanic acid, metatitanic acid, etc.) is added to the lithium salt solution to form the slurry. The purpose of this production method is to obtain large particles of lithium titanate having a high tap density by heating and firing the dried and granulated precursor. If the tap density is high, the particle packing property is improved, and the effect of improving the electrode density is expected. On the other hand, it is difficult to ensure the conductivity between the primary particles inside the granulated secondary particles. Therefore, it is very difficult to increase the high rate discharge capacity maintenance rate. Therefore, it is difficult to say that the manufacturing method is sufficient for improving the initial discharge capacity and the high-rate discharge capacity retention rate, which are the objects of the present invention.

In Patent Document 7, a step of reacting a titanium compound and an ammonium compound in water to obtain a titanate compound, a step of reacting the titanate compound and a lithium compound in water to obtain a lithium titanate hydrate, In the step of heat dehydrating lithium titanate hydrate, fine particles of flaky or plate-like lithium titanate Li ₄ Ti ₅ O ₁₂ are obtained. The lithium titanate particles obtained by this synthesis method are characterized by being extremely thin plate-shaped and porous.
On the other hand, when producing an electrode of a lithium ion secondary battery, it is common to disperse and paint a lithium titanate particle as an active material in an organic solvent and apply it in a sheet form. The fine particles characterized by the above-mentioned extremely thin plate-like shape and porosity are remarkably disadvantageous for coating dispersion. Therefore, it is difficult and not preferable to fully exhibit the original charge / discharge performance of the active material.
Moreover, since the reaction process in water is required twice as a manufacturing process, it is difficult to say that it is an advantageous manufacturing method even in consideration of both cost and productivity.

  Therefore, the present invention provides a lithium titanate particle powder that exhibits an excellent initial discharge capacity and a high high rate discharge capacity maintenance rate as an active material for a non-aqueous electrolyte secondary battery by using an inexpensive and simple process. Is a technical issue.

  The technical problem can be achieved by the present invention as follows.

In the present invention, a water-soluble lithium solution is added to and mixed with an aqueous suspension of titanium oxide having a BET specific surface area value of 40 to 400 m ² / g and a primary particle size of 5 to 50 nm, and the mixed suspension is added to an autoclave. A step of aging reaction at 50 to 100 ° C. (excluding 100 ° C.) without using a solution, a step of filtering, drying and pulverizing the obtained reaction product, and heating and baking the obtained dry powder at 550 to 800 ° C. It is a manufacturing method of the lithium titanate particle powder characterized by including the process to process. (Invention 1)

  In addition, the present invention is a nonaqueous electrolyte secondary battery using an electrode containing, as an active material, lithium titanate particle powder obtained by the production method of the present invention 1. (Invention 2)

  By using the lithium titanate particle powder obtained by the production method according to the present invention, a nonaqueous electrolyte secondary battery exhibiting excellent initial discharge capacity as a secondary battery and having a high high-rate discharge capacity retention rate is obtained. Can do.

  The configuration of the present invention will be described in more detail as follows.

  A method for producing lithium titanate particles according to the present invention will be described.

In the method for producing lithium titanate particles according to the present invention, an aqueous lithium solution is placed in an aqueous suspension of titanium oxide having a BET specific surface area value of 40 to 400 m ² / g and a primary particle size of 5 to 50 nm. A fixed amount was added and mixed, the mixed suspension was aged at 50 to 100 ° C., the obtained reaction product was filtered, dried and pulverized, and the obtained dry powder was heated and fired at 550 to 800 ° C. A lithium titanate particle powder is obtained.

  Examples of the titanium oxide include titanium oxide (anatase) and titanium oxide (rutile), and titanium oxide (anatase) is preferable. Examples of the water-soluble lithium include lithium hydroxide, lithium carbonate, lithium sulfate and the like, and lithium hydroxide is preferable.

The BET specific surface area of the titanium oxide is 40 to 400 m ² / g. A more preferable BET specific surface area is 50 to 400 m ² / g. When the BET specific surface area is less than 40 m ² / g, the reactivity in the aging reaction under an aqueous suspension is poor, and the titanium oxide and the water-soluble lithium solution do not sufficiently react. -Even if it is dried, pulverized, and fired, a Li ₄ Ti ₅ O ₁₂ type spinel structure single phase cannot be obtained, which is not preferable. If it exceeds 400 m ² / g, it is difficult to handle as a powder, and generally it is expensive as a raw material, which is not preferable for the purpose of the present invention.

The primary particle diameter of the titanium oxide is 5 to 50 nm. A more preferable primary particle diameter is 5 to 45 nm. Particles of less than 5 nm are not preferable from the object of the present invention because they are difficult to handle as powders and generally expensive as raw materials. If it exceeds 50 nm, the reactivity in the aging reaction under an aqueous suspension is poor, and the titanium oxide and the water-soluble lithium solution do not react sufficiently, so the obtained reaction product is filtered, dried, ground, Even if baked, a single phase of a spinel structure of Li ₄ Ti ₅ O ₁₂ type cannot be obtained, which is not preferable.

The addition amount of lithium is 0.80 to 2.0 as Li / Ti (mol ratio) with respect to titanium. Preferably it is 0.85-1.7. When the addition amount of lithium is less than 0.80 with respect to titanium, a single phase of a spinel structure of Li ₄ Ti ₅ O ₁₂ type cannot be obtained. If it exceeds 2.0, there is no effect even if it is added, and the raw material cost also increases, so there is no point in adding excessively.

The reaction temperature of the aging reaction is preferably 50 to 100 ° C. When the temperature is lower than 50 ° C., the titanium oxide and the water-soluble lithium solution do not sufficiently react in the aging reaction under an aqueous suspension, and thus the obtained reaction product is filtered, dried, pulverized, and calcined. However, it is not preferable because a single phase having a spinel structure of Li ₄ Ti ₅ O ₁₂ type cannot be obtained. Further, even if the aging reaction is performed at a temperature exceeding 100 ° C., a substantial effect is not seen, and an expensive pressure vessel such as an autoclave is required, which is not preferable. More preferably, it is 60-100 degreeC. The reaction time is preferably 4 to 10 hours.

  The dry powder obtained by filtering and drying the aging reaction product is preferably a mixture containing at least titanium oxide and a lithium-titanium composite oxide having a rock salt structure.

The heat treatment temperature is preferably 550 ° C to 800 ° C. When the temperature is lower than 550 ° C., a single phase having a spinel structure of Li ₄ Ti ₅ O ₁₂ type cannot be obtained. When the temperature exceeds 800 ° C., interparticle sintering is promoted, and electrochemical characteristics (battery performance) are deteriorated. Air is preferable as the atmosphere for the baking treatment. The firing time is preferably 2 to 10 hours.

The BET specific surface area value of the lithium titanate particle powder obtained by the production method according to the present invention is preferably 5.0 to 30 m ² / g. When the BET specific surface area value is less than 5 m ² / g, the high rate discharge capacity retention rate decreases, and when it exceeds 30 m ² / g, a single phase of a spinel structure of Li ₄ Ti ₅ O ₁₂ type is obtained. This is not preferable because the performance as a secondary battery active material is significantly reduced. A more preferable BET specific surface area value is 5.0 to 25 m ² / g, and even more preferably 5.0 to ²⁰ m ² / g.

  The crystal structure of the lithium titanate particle powder obtained by the production method according to the present invention is a spinel type single phase. The presence of an impurity phase is not preferable because the initial discharge capacity is reduced.

  Next, the nonaqueous electrolyte secondary battery according to the present invention will be described.

  The nonaqueous electrolyte secondary battery according to the present invention is characterized in that lithium titanate particle powder obtained by the production method described in the present invention 1 is used as an electrode active material. The electrode for a secondary battery is obtained by adding a conductive material such as carbon black and a binder such as a fluororesin to lithium titanate particle powder, and molding or applying the material appropriately.

The non-aqueous electrolyte secondary battery is composed of the above electrode, counter electrode and electrolyte, and when lithium titanate particle powder is used as the positive electrode active material, the counter electrode (negative electrode) is metal lithium, lithium alloy, graphite, coke, etc. These carbon-based materials are used. Moreover, when using lithium titanate particle powder as a negative electrode active material, lithium-containing manganese oxide, lithium manganate, lithium cobaltate, lithium nickelate, lithium iron phosphate, vanadium pentoxide, and these One kind or two or more kinds of compounds obtained by substituting a part of the compounds with other elements are used. The electrolyte includes a lithium salt such as LiPF ₆ , LiClO ₄ , LiCF ₃ SO ₃ , LiN (CF ₃ SO ₂ ) ₂ , LiBF _{4 in} a solvent such as propylene carbonate, ethylene carbonate, diethyl carbonate, 1,2-dimethoxyethane. What dissolved is used.

<Action>
In the present invention, the most important point is that by using the lithium titanate particle powder obtained by the production method according to the present invention, an excellent initial discharge capacity as a secondary battery is exhibited, and a high rate discharge capacity maintenance rate is high. This is that a non-aqueous electrolyte secondary battery can be obtained.

In the present invention, the excellent initial discharge capacity is obtained because the crystal structure of the lithium titanate particle powder obtained by the production method according to the present invention is a single phase of spinel structure of Li ₄ Ti ₅ O ₁₂ type. .

In addition, a predetermined amount of a water-soluble lithium solution is added to and mixed with an aqueous suspension of titanium oxide, the mixed suspension is aged at 50 to 100 ° C., and the dried and filtered powder is at least titanium oxide and It is a mixture containing a lithium-titanium composite oxide having a rock salt structure. That is, since a portion of titanium oxide reacts with lithium to form a lithium-titanium composite oxide having a rock salt structure at the stage of the dry powder before firing, the spinel structure single-phase fine particles are formed by firing at a relatively low temperature. can get. Furthermore, in the ripening reaction at 100 ° C. or lower, the Li / Ti feed ratio is set to a low value (less Li surplus from Li ₄ Ti ₅ O ₁₂ stoichiometric composition 0.80), Li segregation during the ripening reaction product during filtration and drying is suppressed, and the obtained dry powder is fired at 550 to 800 ° C. to obtain a Li ₄ Ti ₅ O ₁₂ fine particle powder having a uniform composition. Is possible.

In other words, due to the effect of producing a spinel-type single-phase and uniform composition Li ₄ Ti ₅ O ₁₂ fine particle powder, it exhibits excellent initial discharge capacity as an active material for a non-aqueous electrolyte secondary battery, and high rate discharge The present inventor estimates that a lithium titanate particle powder having a high capacity retention rate can be obtained.

  In the production method according to the present invention, a predetermined amount of a water-soluble lithium solution is added to and mixed with an aqueous suspension of titanium oxide, and the mixed suspension is subjected to an aging reaction. The aging temperature is 100 ° C. or less. Therefore, an expensive pressure vessel such as an autoclave is not required. Furthermore, it can be said that it is an inexpensive and simple manufacturing method in consideration of the various processes up to the filtration, drying and pulverization described above.

  A typical embodiment of the present invention is as follows.

  For identification of lithium titanate particle powder, powder X-ray diffraction (RIGAKU RINT2500 (tube ball: Cu, tube voltage: 40 kV, tube current: 300 mA) was used.

  The battery characteristics of the lithium titanate particle powder were evaluated by preparing a positive electrode, a negative electrode, and an electrolytic solution by the following production method to produce a coin-type battery cell.

<Preparation of positive electrode>
The lithium titanate particle powder, the conductive agent acetylene black and the binder polyvinylidene fluoride were precisely weighed so as to have a weight ratio of 90: 5: 5, and thoroughly mixed in a mortar, and then N-methyl-2 A positive electrode mixture slurry was prepared by dispersing in -pyrrolidone. Next, this slurry was applied to an aluminum foil as a current collector with a film thickness of 40 μm, vacuum-dried at 110 ° C., and then punched into a disk shape of φ16 mm to obtain a positive electrode plate.

<Production of negative electrode>
A metal lithium foil was punched into a disk shape of φ16 mm to produce a negative electrode.

<Preparation of electrolyte>
An electrolyte solution was prepared by mixing 1 mol / liter of lithium hexafluorophosphate (LiPF ₆ ) as an electrolyte in a mixed solution of ethylene carbonate and diethyl carbonate in a volume ratio of 50:50.

<Assembly of coin-type battery cells>
Using a case made of SUS316 in a glove box in an argon atmosphere, a CR2032-type coin battery was manufactured by injecting an electrolyte solution through a polypropylene separator between the positive electrode and the negative electrode.

<Battery evaluation>
A charge / discharge test of a secondary battery was performed using the coin-type battery. As measurement conditions, the current density with respect to the positive electrode was 0.2 mA / cm ^2, and charge / discharge was repeated while the cut-off voltage was between 1.1 V and 3.0 V. The initial discharge capacity was measured at a rate of 0.1C. Moreover, the high rate discharge capacity maintenance rate was expressed as a ratio (percentage) of the discharge capacity value at a rate of 5 C to the initial discharge capacity value.

Example 1
<Manufacture of lithium titanate particle powder>
A suspension in which 72.77 g of titanium oxide (anatase) having a specific surface area of 300 m ² / g and a primary particle diameter of 6 nm is dispersed in 500 ml of ion-exchanged water is placed in a 1500 ml stainless steel container and gently stirred. To this, an aqueous solution in which 41.08 g of lithium hydroxide is dissolved in 200 ml of ion exchange water is added to adjust the total amount of the reaction suspension to 800 ml. At this time, Li / Ti (mol / mol) = 1.075. This mixed suspension is immediately heated to 95 ° C. and subjected to aging reaction for 6 hours. After completion of the aging reaction, the reaction suspension is cooled to room temperature, filtered by Nutsche, and then the filter cake is dried at 120 ° C. and then pulverized. As a result of X-ray diffraction of the obtained dry powder, it was confirmed that it was a mixture containing at least titanium oxide (anatase type structure oxide) and lithium salt composite oxide having a rock salt type structure. The dry powder was put in an alumina crucible and baked in a muffle furnace at a temperature of 670 ° C. for 3 hours in an air atmosphere to obtain lithium titanate particle powder.

As a result of X-ray diffraction of the obtained lithium titanate particle powder, it was a single phase of spinel structure of Li ₄ Ti ₅ O ₁₂ type, and no impurity phase was present. Further, the BET specific surface area value was 7.5 m ² / g.

  The coin-type battery produced using the lithium titanate particle powder as the positive electrode active material had an initial discharge capacity of 166 mAh / g and a high rate discharge capacity retention rate of 76.7%.

Examples 2-5
Lithium titanate particle powder was obtained in the same manner as in Example 1 except that the type of titanium oxide, the Li / Ti charging ratio during the aging reaction, the aging temperature, the heat treatment temperature, and the like were variously changed.

  In Comparative Example 1, titanium oxide (anatase) powder, lithium carbonate powder and magnesium hydroxide powder were blended in a charging composition such that Li / Ti (mol / mol) = 0.80, and thoroughly mixed in a mortar, The obtained mixed powder was put into an alumina crucible and fired in a muffle furnace at a temperature of 820 ° C. for 3 hours in an air atmosphere to obtain lithium titanate particle powder.

In Comparative Example 2, lithium titanate particle powder was obtained in exactly the same manner as in Example 1 except that titanium oxide (anatase) powder having a specific surface area of 10 m ² / g and a primary particle diameter of 180 nm was used. However, as a result of X-ray diffraction of the obtained lithium titanate particle powder, a large amount of impurity phase of titanium oxide (anatase type) is contained in addition to the Li ₄ Ti ₅ O ₁₂ type spinel structure, and the spinel structure single unit No phase was produced.

Comparative Examples 3 and 4
Lithium titanate particle powder was obtained in the same manner as in Example 1 except that the reaction temperature of the ripening reaction and the heat treatment temperature were variously changed.

In Comparative Example 3, an aging reaction was performed under the same conditions as in Example 1 except that the aging temperature was 45 ° C. After completion of the aging, the reaction suspension was cooled to room temperature, filtered by Nutsche, and then filtered. Was dried and pulverized at 120 ° C. to obtain a dry powder. As a result of X-ray diffraction of the obtained dry powder, only the presence of titanium oxide (anatase type structure oxide) was confirmed, and no diffraction peak attributed to the lithium titanium composite oxide having a rock salt type structure was observed. The dry powder was put in an alumina crucible and baked in a muffle furnace at a temperature of 670 ° C. for 3 hours in an air atmosphere to obtain lithium titanate particle powder. As a result of X-ray diffraction of the obtained lithium titanate particle powder, a slight amount of spinel structure of Li ₄ Ti ₅ O ₁₂ type was observed, but most was titanium oxide (anatase type structure oxide).

  Table 1 shows the production conditions and characteristics of the obtained lithium titanate particles.

  As shown in the examples, the lithium titanate particle powder according to the present invention has a high initial discharge capacity and a high discharge capacity maintenance rate, and is therefore suitable as an active material for a non-aqueous electrolyte secondary battery. is there.

  In addition, in the said Example, although the example which used the lithium titanate particle powder which concerns on this invention as a positive electrode active material is shown, also when the lithium titanate particle powder which concerns on this invention is used as a negative electrode active material, As an active material of a nonaqueous electrolyte secondary battery, it can exhibit excellent characteristics.

Claims (2)

A water-soluble lithium solution is added to and mixed with an aqueous suspension of titanium oxide having a BET specific surface area value of 40 to 400 m ² / g and a primary particle size of 5 to 50 nm, and the mixed suspension is used with an autoclave. Without aging reaction at 50 to 100 ° C. (excluding 100 ° C.) , step of filtering, drying and pulverizing the obtained reaction product, step of heating and baking the obtained dry powder at 550 to 800 ° C. A process for producing a lithium titanate particle powder comprising: Preparation of non-aqueous electrolyte secondary battery characterized in that Ru using the electrode which contains lithium titanate particles obtained by the claims 1 Process according as the active material.