WO2010137582A1 - チタン酸リチウム及びその製造方法並びにそれを用いた電極活物質及び蓄電デバイス - Google Patents
チタン酸リチウム及びその製造方法並びにそれを用いた電極活物質及び蓄電デバイス Download PDFInfo
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- WO2010137582A1 WO2010137582A1 PCT/JP2010/058815 JP2010058815W WO2010137582A1 WO 2010137582 A1 WO2010137582 A1 WO 2010137582A1 JP 2010058815 W JP2010058815 W JP 2010058815W WO 2010137582 A1 WO2010137582 A1 WO 2010137582A1
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- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
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- H01M4/00—Electrodes
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- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
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- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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Definitions
- the present invention relates to lithium titanate excellent in battery characteristics, particularly rate characteristics, and a method for producing the same.
- the present invention also relates to an electrode active material containing the lithium titanate and an electricity storage device using the electrode containing the electrode active material.
- lithium secondary batteries have high energy density and excellent cycle characteristics, in recent years, they have rapidly spread to small batteries such as power supplies for portable devices. On the other hand, large batteries for the power industry and automobiles are used. Development is also desired. Electrode active materials for these large lithium secondary batteries are required to have long-term reliability and high input / output characteristics. In particular, lithium negative electrode active materials are promising for lithium titanate, which has excellent safety, long life, and excellent rate characteristics.
- Various lithium titanates have been proposed for electrode active materials.
- lithium titanate is known in which spherical secondary particles are granulated to improve filling properties and battery characteristics (Patent Documents 1 and 2). Such lithium titanate secondary particles are produced by drying and granulating a titanium compound and a lithium compound, followed by firing.
- crystalline titanium In a method in which a slurry containing a titanic acid compound and a lithium compound is dried, granulated, and then heated and fired, a crystalline titanium oxide and a titanic acid compound are added to a lithium compound solution preheated to 50 ° C. or more to prepare the slurry. (Patent Document 3), a method of preparing the slurry at a temperature lower than 45 ° C. (Patent Document 4), and the like are also used.
- Patent Document 5 there is also a technology to improve the large current characteristics and cycle characteristics by crushing and refiring lithium titanate to give pores with an average pore diameter in the range of 50 to 500 mm on the surface of lithium titanate particles.
- the present invention provides a lithium titanate excellent in battery characteristics, particularly rate characteristics, and a method for producing the same.
- lithium titanate secondary particles having at least macropores on the surface are more excellent in rate characteristics, and such lithium titanate has the above-described crystalline titanium and titanium.
- a slurry containing an acid compound and a lithium compound is dried and granulated and then fired to obtain secondary particles of lithium titanate, two or more kinds of particles are used as the crystalline titanium oxide, or crystalline titanium oxide and It has been found that the titanic acid compound can be obtained at a specific blending ratio, and the present invention has been completed.
- the present invention is a lithium titanate containing secondary particles in which primary particles of lithium titanate are aggregated and having at least macropores on the surface of the secondary particles, and a slurry containing crystalline titanium oxide, titanate compound and lithium compound
- a method for producing lithium titanate in which crystalline titanium oxide is used in an amount more than four times the weight ratio in terms of TiO 2 with respect to the titanate compound.
- An electricity storage device using the lithium titanate of the present invention as an electrode active material has excellent battery characteristics, particularly rate characteristics.
- FIG. 1 is an adsorption / desorption isotherm of Example 1 (Sample A).
- the present invention is lithium titanate, including secondary particles in which primary particles of lithium titanate are aggregated, and has at least a macropore on the surface of the secondary particles.
- lithium titanate since lithium titanate is used as the secondary particles, irregularities and voids between the primary particles are formed on the particle surface, the contact area with the electrolytic solution is increased, and the amount of lithium ion adsorption / desorption is increased. it can.
- the pore diameter of the powder is generally determined by analyzing the nitrogen adsorption / desorption isotherm obtained by the nitrogen adsorption method using the HK method, the BJH method, etc. to obtain the pore distribution, and calculating the total pore volume calculated from the pore distribution. And the measured specific surface area.
- cm 3 (STP) / g is a value obtained by converting the nitrogen adsorption / desorption amount into a volume in a standard state (temperature 0 ° C., atmospheric pressure 101.3 KPa).
- V a (0.99) is more preferably at least 55 cm 3 (STP) / g.
- the nitrogen adsorption amount (V a (0.50)) at a relative pressure of 0.50 is 10 cm 3 (STP) / g or less, and ⁇ V d ⁇ a is continuously, That is, if each of the two or more consecutive measurement points does not take a value of 5 cm 3 (STP) / g or more, it is assumed that no micropore or mesopore is present.
- V a (0.50) is more preferably 8 cm 3 (STP) / g or less, and ⁇ V d ⁇ a is further preferably not continuously taking a value of 3 cm 3 (STP) / g or more.
- the average particle diameter of secondary particles is preferably in the range of 0.5 to 100 ⁇ m from the viewpoint of packing properties.
- the particle shape of the secondary particles is preferably isotropic from the viewpoint of battery characteristics, and more preferably spherical or polyhedral.
- the primary particles constituting the secondary particles are not particularly limited, but if the average particle diameter (50% median diameter by electron microscopy) is in the range of 0.01 to 2.0 ⁇ m, secondary particles in the above range are used. It is preferable because the diameter can be easily obtained, and isotropic shapes such as a spherical shape and a polyhedral shape are preferable because secondary particles having an isotropic shape are easily obtained.
- These secondary particles are in a state in which the primary particles are firmly bonded to each other, and are not aggregated or mechanically consolidated by interaction between particles such as van der Waals force, but are used industrially. It is not easily disintegrated by ordinary mechanical pulverization, and most remains as secondary particles.
- the lithium titanate of the present invention is preferably represented by the composition formula Li x Ti y O 4 , and more preferably a single phase of lithium titanate. However, some titanium oxide may be mixed as long as the effect of the present invention is not impaired.
- the values of x and y in the general formula are preferably in the range of 0.5 to 2 in terms of x / y values, and those of the spinel type represented by the composition formula Li 4 Ti 5 O 12 are particularly preferable.
- the surface of the secondary particles may be coated with at least one selected from inorganic compounds such as silica and alumina, and organic compounds such as surfactants and coupling agents.
- inorganic compounds such as silica and alumina
- organic compounds such as surfactants and coupling agents.
- These coating species can carry 1 type, can laminate 2 or more types as a plurality of carrying layers, and can carry 2 or more types as a mixture and a compound.
- carbon can be included in the interior or surface of the lithium titanate secondary particles.
- Inclusion of carbon is preferable because electric conductivity is improved, and the amount of carbon is preferably in the range of 0.05 to 30% by weight in terms of C. If it is less than this range, the desired electrical conductivity cannot be obtained, and if it is more, the inactive material component in the electrode increases, which is not preferable because the battery capacity decreases.
- a more preferable carbon amount is in the range of 0.1 to 15% by weight.
- the amount of carbon can be analyzed by a CHN analysis method, a high frequency combustion method, or the like.
- different metal elements other than titanium and lithium can be included in the secondary particles.
- the different metal element is preferably magnesium, aluminum, zirconium or the like, and one or more of these can be used.
- the amount of different metal elements is preferably in the range of 0.05 to 15% by weight in terms of Mg, Al, and Zr. More preferably, Al and Mg are in the range of 0.05 to 10% by weight, and Zr is in the range of 0.1 to 10% by weight. For Al and Mg, the range of 0.1 to 5% by weight is more preferable.
- the amount of the different metal element can be analyzed by, for example, an inductively coupled plasma (ICP) method.
- ICP inductively coupled plasma
- the present invention is a method for producing lithium titanate, wherein a slurry containing crystalline titanium oxide, a titanate compound and a lithium compound is dried and granulated, and then fired to obtain lithium titanate secondary particles.
- a slurry containing crystalline titanium oxide, a titanate compound and a lithium compound is dried and granulated, and then fired to obtain lithium titanate secondary particles.
- (1) Crystalline titanium oxide containing at least two types of crystalline titanium oxide particles having different average particle diameters is used (hereinafter sometimes referred to as (1) production method) and / or (2) crystalline oxidation Titanium is used in an amount more than four times as much as the TiO 2 weight ratio with respect to the titanic acid compound (hereinafter sometimes referred to as (2) production method).
- starting materials such as crystalline titanium oxide, a titanic acid compound, and a lithium compound are added to a liquid medium, and a slurry containing them is prepared.
- concentration of the titanium component in the slurry is industrially advantageous when it is in the range of 120 to 300 g / liter in terms of TiO 2 , and more preferably in the range of 150 to 250 g / liter.
- the medium water, an organic solvent such as alcohol, or a mixture thereof can be used, and industrially, it is preferable to use water or an aqueous medium mainly composed of water.
- the temperature of the liquid medium containing the lithium compound is preferably in the range of 25 to 100 ° C. because the reaction between the titanate compound and the lithium compound proceeds in the slurry preparation stage, and lithium titanate is easily obtained during firing. A range of 50 to 100 ° C. is more preferable.
- the crystalline titanium oxide and the titanic acid compound may be added to the liquid medium containing the lithium compound separately, in parallel, or in a mixture.
- lithium compound when the reaction is performed in water or an aqueous medium containing water as a main component, it is preferable to use a water-soluble lithium compound such as lithium hydroxide, lithium carbonate, lithium nitrate, or lithium sulfate. Among them, lithium hydroxide having high reactivity is preferable.
- the titanate compound TiO (OH) 2 or metatitanic acid represented by TiO 2 ⁇ H 2 O, Ti (OH) 4 or orthotitanate represented by TiO 2 ⁇ 2H 2 O, or a mixture thereof
- the titanic acid compound is obtained by heat hydrolysis or neutralization hydrolysis of a hydrolyzable titanium compound.
- metatitanic acid is heat hydrolysis of titanyl sulfate (TiOSO 4 ), neutralization hydrolysis of titanium chloride at a high temperature, etc.
- Orthotitanic acid is a neutralized hydrolysis of titanium sulfate (Ti (SO 4 ) 2 ) and titanium chloride (TiCl 4 ) at a low temperature, and a mixture of metatitanic acid and orthotitanic acid is a neutralized titanium chloride. It can be obtained by appropriately controlling the hydrolysis temperature. If an ammonium compound such as ammonia, ammonium carbonate, ammonium sulfate, or ammonium nitrate is used as the neutralizing agent for neutralization hydrolysis, it can be decomposed and volatilized during firing.
- the titanium compound in addition to the inorganic compounds such as titanium sulfate, titanyl sulfate, and titanium chloride, organic compounds such as titanium alkoxide may be used.
- titanium dioxide represented by the composition formula TiO 2 is preferably used.
- the crystal form of titanium dioxide anatase type, rutile type, brookite type and the like can be used without limitation.
- the crystalline titanium oxide may have a single crystal form, a mixed crystal containing two or more crystal forms, or a part of amorphous. If the average particle diameter of the crystalline titanium oxide particles contained in the crystalline titanium oxide is in the range of 0.01 to 0.4 ⁇ m, the viscosity of the slurry is hardly increased even at a high concentration, which is preferable.
- Crystalline titanium oxide can be obtained by a known method for producing a titanium dioxide pigment, for example, a so-called sulfuric acid method in which titanyl sulfate is hydrolyzed and calcined by heating, a so-called chlorine method in which titanium tetrachloride is oxidized in a gas phase, and the like.
- two or more kinds of crystalline titanium oxide particles having different average particle diameters can be used.
- other crystals can be used.
- the titanium oxide particles are 1.3 times or more, preferably 1.3 times or more and 40 times or less, more preferably 1.3 times or more and 10 times or less, still more preferably 1.3 times or more and 3.5 times or less. It is preferable that the average particle diameter is as follows.
- the crystal form of each particle may be the same or different.
- the average particle diameter is 50% median diameter by electron microscopy, and the preferred average particle diameter of the crystalline titanium oxide particles having the smallest average particle diameter is 0.01 to 0.20 ⁇ m.
- the average particle diameter of the other crystalline titanium oxide particles can be adjusted as appropriate by granulating into secondary particles according to the average particle diameter of the smallest one. Alternatively, if primary particles of crystalline titanium oxide are used, the average particle diameter is preferably in the range of 0.05 to 0.40 ⁇ m.
- the weight of the crystalline titanium oxide having an average particle diameter of 1.3 times or more with respect to the weight of the crystalline titanium oxide having the smallest average particle diameter is in the range of 0.1 to 5 times. When there are a plurality of crystalline titanium oxides having an average particle size of 1.3 times or more, the total weight is used as a reference. If the total amount of the crystalline titanium oxide particles is in the range of 1 to 10 times the weight ratio in terms of TiO 2 with respect to the titanate compound, lithium titanate is advantageously produced industrially. It is preferable because it is possible.
- the amount of crystalline titanium oxide used is more than 4 times the amount of titanic acid compound, preferably 4.2 times or more, but there is no particular upper limit.
- the following is preferable because the slurry viscosity is suitable for dry granulation.
- the crystalline titanium oxide may be one kind of crystalline titanium oxide particles, or two or more kinds of crystalline titanium oxide particles having different average particle diameters and crystal shapes.
- the dry granulation method For example, (A) a method of spray-drying the slurry and granulating it into secondary particles, and (B) a solid-liquid separation of the solid content contained in the slurry. And a method of pulverizing and granulating into secondary particles of a desired size.
- the method (A) is preferable because the particle diameter can be easily controlled and spherical secondary particles can be easily obtained.
- the spray dryer used for spray drying can be appropriately selected according to the properties and processing capacity of the slurry, such as a disk type, a pressure nozzle type, a two-fluid nozzle type, and a four-fluid nozzle type.
- the secondary particle size can be controlled by, for example, adjusting the solid content concentration in the slurry, or if the disk type is the above, the rotational speed of the disk is a pressure nozzle type, a two-fluid nozzle type, a four-fluid nozzle type, etc.
- the size of the sprayed droplets can be controlled by adjusting the spray pressure, the nozzle diameter, the flow rate of each fluid, and the like. Properties such as the concentration and viscosity of the slurry are appropriately set according to the ability of the spray dryer.
- An organic binder may be used when the viscosity of the slurry is low and granulation is difficult, or in order to further facilitate control of the particle diameter.
- the organic binder used include (1) vinyl compounds (polyvinyl alcohol, polyvinyl pyrrolidone, etc.), (2) cellulose compounds (hydroxyethyl cellulose, carboxymethyl cellulose, methyl cellulose, ethyl cellulose, etc.), and (3) protein compounds ( Gelatin, gum arabic, casein, sodium caseinate, ammonium caseinate, etc.), (4) acrylic acid compounds (sodium polyacrylate, ammonium polyacrylate, etc.), (5) natural polymer compounds (starch, dextrin, agar) , Sodium alginate, etc.), (6) synthetic polymer compounds (polyethylene glycol, etc.), etc., and at least one selected from these can be used. Especially, what does not contain inorganic components, such as soda, is more preferable because it is easily decomposed and volatilized by firing.
- the firing temperature varies depending on the firing atmosphere and the like, but in order to produce lithium titanate, it may be about 550 ° C. or higher, and preferably 1000 ° C. or lower to prevent sintering between secondary particles. From the viewpoint of promoting the production of Li 4 Ti 5 O 12 and improving the rate characteristics, a more preferable firing temperature is in the range of 550 to 850 ° C., and more preferably in the range of 650 to 850 ° C. As the firing atmosphere, a non-oxidizing atmosphere or the like can be selected as appropriate.
- the obtained lithium titanate secondary particles are sintered and agglomerated after firing, they may be pulverized using a flake crusher, a hammer mill, a pin mill, a bantam mill, a jet mill or the like, if necessary.
- the lithium titanate secondary particles may further include a step of containing carbon.
- a step of containing carbon As a specific method for containing carbon, (A) a slurry containing crystalline titanium oxide, a titanic acid compound and a lithium compound is dried and granulated and fired, and the obtained fired product is subjected to the presence of a carbon-containing substance. And (B) a method of drying and granulating a slurry containing crystalline titanium oxide, a titanic acid compound, a lithium compound and a carbon-containing substance, and firing.
- the calcination temperature of the carbon-containing material is preferably in the range of 150 to 1000 ° C.
- the calcination temperature is preferably in the range of 550 to 1000 ° C., where lithium titanate is easily generated.
- a non-oxidizing atmosphere or the like can be appropriately selected in the air, but it is preferably performed in a non-oxidizing atmosphere.
- Examples of the carbon-containing substance include carbon black, acetylene black, ketjen black, and organic compounds.
- the organic compounds may be used after being heated and decomposed in advance.
- a hydrocarbon compound and / or an oxygen-containing hydrocarbon compound in which components other than carbon hardly remain is preferable.
- Examples of the hydrocarbon compounds include (a) alkane compounds (methane, ethane, propane, etc.), (b) alkene compounds (ethylene, propylene, etc.), (c) alkyne compounds (acetylene, etc.), (d) And cycloalkane compounds (cyclohexane, etc.) and (e) aromatic compounds (benzene, toluene, xylene, etc.).
- oxygen-containing hydrocarbon compounds include (a) alcohol compounds ((a) monohydric alcohols (methanol, ethanol, propanol, etc.), (b) dihydric alcohols (ethylene glycol, etc.), and (c) trihydric alcohols. (Trimethylolethane, trimethylolpropane, etc.), (d) polyalcohol (polyvinyl alcohol, etc.), (b) ether compounds ((a) ether monomers (diethyl ether, ethyl methyl ether, etc.), (b) poly Ethers (polyethylene glycol, polyethylene oxide, polypropylene ether, etc.), etc.
- alcohol compounds ((a) monohydric alcohols (methanol, ethanol, propanol, etc.), (b) dihydric alcohols (ethylene glycol, etc.), and (c) trihydric alcohols. (Trimethylolethane, trimethylolpropane, etc.), (d) polyalcohol (polyvinyl alcohol, etc.
- carboxylic acid compounds ((a) oxycarboxylic acids (citric acid, malic acid, etc.), (b) monocarboxylic acids (acetic acid, formic acid, etc.), (c) Dicarboxylic acid (oxalic acid, malonic acid, etc.), (d) Aromatic carboxylic acid (benzoic acid, etc.), etc.
- Products formaldehyde, acetaldehyde, etc.), (e) phenolic compounds (phenol, catechol, pyrogallol, etc.), (he) sugars (glucose, sucrose, cellulose, etc.), etc.
- a compound serving as a binder such as polyalcohol or polyether can be selected.
- a step of incorporating different metal elements other than titanium and lithium into the lithium titanate secondary particles can be provided.
- a specific method of including the different metal element in the secondary particles (A) a method of adding a compound of a different metal element to a slurry containing crystalline titanium oxide, a titanate compound and a lithium compound, and (B) a different metal Examples thereof include a method of drying and granulating a slurry containing crystalline titanium oxide containing an element, a titanic acid compound and a lithium compound, and firing.
- the compound of the dissimilar metal element can be mixed in advance with crystalline titanium oxide or a titanic acid compound, and if it is crystalline titanium oxide, the compound of the dissimilar metal element is formed on the particle surface.
- the hydrolyzable titanium compound may be hydrolyzed in the presence of a compound of a different metal element to obtain a mixture.
- the crystalline titanium oxide containing the different metal element used in the method (B) can be obtained by mixing and baking a titanium compound and a compound of a different metal element.
- the compound of the different metal element an oxide, hydrated oxide, chloride, carbonate, nitrate, sulfate, or the like of the different metal element is appropriately selected according to the methods (A) and (B).
- this invention is an electrode active material, Comprising:
- the said lithium titanate is characterized by the above-mentioned.
- the present invention is an electricity storage device, wherein an electrode including the electrode active material is used.
- the electricity storage device include a lithium battery, a lithium capacitor, and the like, which are composed of an electrode, a counter electrode, a separator, and an electrolytic solution.
- the electrode is appropriately added with a conductive material and a binder in the electrode active material. It is obtained by molding or applying to the electrode plate.
- the conductive material include carbon-containing materials such as carbon black, acetylene black, and ketjen black.
- the binder examples include fluorine resins such as polytetrafluoroethylene, polyvinylidene fluoride, and fluorine rubber, and styrene butadiene rubber. And water-soluble resins such as carboxymethyl cellulose and polyacrylic acid.
- the electrode active material can be used as a positive electrode, and a lithium-containing metal, lithium alloy, or a carbon-containing material such as graphite can be used as a counter electrode.
- the electrode active material is used as a negative electrode, and a lithium / transition metal composite oxide such as a lithium / manganese composite oxide, a lithium / cobalt composite oxide, a lithium / nickel composite oxide, a lithium / vanadine composite oxide, Olivine type compounds such as lithium, iron, and complex phosphate compounds can be used.
- a lithium / transition metal composite oxide such as a lithium / manganese composite oxide, a lithium / cobalt composite oxide, a lithium / nickel composite oxide, a lithium / vanadine composite oxide, Olivine type compounds such as lithium, iron, and complex phosphate compounds
- a capacitor an asymmetric capacitor using the electrode active material and a carbon-containing material such as graphite or activated carbon can be used.
- a porous polyethylene film or the like is used, and for the electrolyte, propylene carbonate, ethylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, ⁇ -butyl lactone, 1,2-dimethoxyethane, etc.
- Conventional materials such as those obtained by dissolving lithium salts such as LiPF 6 , LiClO 4 , LiCF 3 SO 3 , LiN (CF 3 SO 2 ) 2 , and LiBF 4 in the above solvent can be used.
- the present invention is another power storage device, characterized in that an electrode including the electrode active material and not including a conductive material is used. Since lithium titanate has insulating properties, conventionally, it has been difficult to obtain charge / discharge capacity unless a conductive material such as a carbon-containing material such as carbon black, acetylene black, or ketjen black is used in combination. In the electricity storage device of the invention, a practically sufficient charge / discharge capacity can be obtained without using a conductive material. Moreover, this electricity storage device has excellent rate characteristics.
- the term “electrode does not contain a conductive material” means not only that the conductive material is not blended with the electrode, but also that lithium titanate does not contain a conductive material such as carbon inside or on the surface. Also includes states.
- the above-mentioned materials can be used as the electrode active material, binder, electrolyte solution and the like used for the counter electrode of this electrode.
- Example 1 (Production method of (1)) To 340 ml of 4.5 mol / liter lithium hydroxide aqueous solution, crystalline titanium dioxide particles (a) (anatase type) having an average particle diameter of 0.10 ⁇ m and crystalline titanium dioxide particles having an average particle diameter of 0.07 ⁇ m ( b) 50 g of (anatase type and rutile type mixed crystal) was added and dispersed.
- the liquid temperature was kept at 80 ° C., and 650 ml of an aqueous slurry in which 50 g of titanic acid compound (orthotitanic acid) was dispersed in terms of TiO 2 was added, and crystalline titanium oxide, titanic acid compound and A slurry containing a lithium compound was obtained.
- This slurry was spray dried using a GB210-B type spray dryer (manufactured by Yamato Kagaku Co., Ltd.) under the conditions of an inlet temperature of 190 ° C. and an outlet temperature of 80 ° C. to obtain a dried granulated product. Firing was performed in the atmosphere at a temperature of 700 ° C.
- lithium titanate (sample A) of the present invention represented by the composition formula Li 4 Ti 5 O 12 .
- a transmission electron microscope H-7000 type and an image diffraction apparatus Luzex IIIU type both manufactured by Hitachi, Ltd. were used.
- Example 2 (Production method of (1)) In 340 ml of 4.5 mol / liter lithium hydroxide aqueous solution, 85.7 g of crystalline titanium dioxide particles (b) (anatase type and rutile type mixed crystal) having an average particle size of 0.07 ⁇ m, and an average particle size of 21.5 g of 0.13 ⁇ m crystalline titanium dioxide particles (c) (anatase type and rutile type mixed crystal) were added and dispersed.
- b crystalline titanium dioxide particles
- c anatase type and rutile type mixed crystal
- Example B lithium titanate (sample B) of the present invention represented by the composition formula Li 4 Ti 5 O 12 .
- Example 3 (Production method of (1)) 50 g of lithium titanate (sample A) obtained in Example 1 and 2.5 g of polyethylene glycol were uniformly mixed, and the mixture was calcined at a temperature of 500 ° C. for 2 hours in a nitrogen atmosphere to obtain titanic acid of the present invention. Lithium (Sample C) was obtained. Analysis using a CHN elemental analyzer Vario ELIII type (manufactured by Elementar) revealed that sample C contained 0.80% by weight of carbon in terms of C.
- Example 4 (Production method of (1))
- the amount of crystalline titanium dioxide particles (a), (b) and titanic acid compound used was 53.2 g in terms of TiO 2
- the amount of titanic acid compound aqueous slurry added was 680 ml.
- the lithium titanate of the present invention (sample D) containing 2.1% by weight of magnesium in terms of Mg in the same manner as in Example 1 except that 8.8 g of magnesium hydroxide (containing 3.5 g as Mg) was added.
- An ICP emission analyzer SPS-3100 type manufactured by Seiko Instruments Inc. was used for the measurement of the amount of magnesium.
- Example 5 (Production method of (1))
- the amount of crystalline titanium dioxide particles (a), (b) and titanic acid compound used was 54.5 g in terms of TiO 2
- the amount of titanic acid compound aqueous slurry added was 690 ml.
- lithium titanate (sample E) of the present invention containing aluminum was obtained in the same manner as in Example 1 except that 12.3 g of aluminum hydroxide (containing 4.1 g of Al) was added.
- the aluminum content of Sample E was measured in the same manner as in Example 4, it was 2.3% by weight in terms of Al.
- Example 6 (Production method of (1))
- the amount of crystalline titanium dioxide particles (a), (b) and titanic acid compound used was 53.2 g in terms of TiO 2
- the amount of titanic acid compound aqueous slurry added was 680 ml.
- the lithium titanate of the present invention (sample F) containing 8.4 wt% of zirconium in terms of Zr in the same manner as in Example 1 except that 9.3 g of zirconium oxide (including 6.9 g of Zr) was added.
- Example 7 (Production method of (2)) 125 g of crystalline titanium dioxide particles (b) having an average particle diameter of 0.07 ⁇ m were added to and dispersed in 340 ml of a 4.5 mol / liter lithium hydroxide aqueous solution. While stirring this slurry, the liquid temperature was kept at 80 ° C., and 250 ml of an aqueous slurry in which 25 g of titanic acid compound (ortho titanic acid) was dispersed in terms of TiO 2 was added, and crystalline titanium oxide, titanic acid compound and A slurry containing a lithium compound was obtained. Thereafter, the dry granulated product was prepared and fired in the same manner as in Example 1 to obtain a lithium titanate of the present invention (sample G) represented by the composition formula Li 4 Ti 5 O 12 .
- Comparative Example 1 75 g of crystalline titanium dioxide particles (b) having an average particle size of 0.07 ⁇ m were added to and dispersed in 340 ml of a 4.5 mol / liter lithium hydroxide aqueous solution. While stirring this slurry, the liquid temperature was kept at 80 ° C., and 720 ml of an aqueous slurry in which 75 g of titanic acid compound (orthotitanic acid) was dispersed in terms of TiO 2 was added, and crystalline titanium oxide, titanic acid compound and A slurry containing a lithium compound was obtained. The subsequent preparation and firing of the dried granulated product were carried out in the same manner as in Example 1 to obtain a comparative target lithium titanate (sample H) represented by the composition formula Li 4 Ti 5 O 12 .
- Comparative Example 2 In Comparative Example 1, the amount of crystalline titanium dioxide particles (b) used was 111.5 g, the amount of titanic acid compound (ortho titanic acid) was 38.5 g in terms of TiO 2 , and a 375 milliliter aqueous slurry was used. In the same manner as in Comparative Example 1, a comparative lithium titanate (sample I) represented by the composition formula Li 4 Ti 5 O 12 was obtained.
- Comparative Example 3 1500 ml of an aqueous slurry in which 150 g of titanic acid compound (ortho titanic acid) is dispersed in terms of TiO 2 is added to 340 ml of 4.5 mol / liter lithium hydroxide aqueous solution, and the liquid temperature is kept at 80 ° C. while stirring. Thereby, the slurry containing a titanic acid compound and a lithium compound was obtained.
- the subsequent dry granulated material preparation and firing were carried out in the same manner as in Example 1 to obtain a comparative target lithium titanate (sample J) represented by the composition formula Li 4 Ti 5 O 12 .
- Examples 8-14 Lithium titanate (samples A to G) obtained in Examples 1 to 7, acetylene black powder as a conductive agent, and polyvinylidene fluoride resin as a binder were mixed at a weight ratio of 100: 5: 7. And paste in a mortar to prepare a paste. This paste was applied on an aluminum foil, dried at a temperature of 120 ° C. for 10 minutes, punched into a circle having a diameter of 12 mm, and pressed at 17 MPa to obtain a working electrode. The amount of active material contained in the electrode was 3 mg.
- This working electrode was vacuum-dried at 120 ° C. for 4 hours, and then incorporated as a positive electrode in a sealable coin-type cell in a glove box having a dew point of ⁇ 70 ° C. or lower.
- As the negative electrode a metal lithium having a thickness of 0.5 mm formed into a circle having a diameter of 12 mm was used.
- As the non-aqueous electrolyte a mixed solution of ethylene carbonate and dimethyl carbonate (mixed in a volume ratio of 1: 2) in which LiPF 6 was dissolved at a concentration of 1 mol / liter was used.
- the working electrode was placed in a lower can of a coin-type cell, a porous polypropylene film was placed thereon as a separator, and a nonaqueous electrolyte was dropped from above. Further, a negative electrode, a 0.5 mm thick spacer for adjusting the thickness, and a spring (both made of SUS316) are put thereon, and an upper can with a propylene gasket is put on the outer peripheral edge to seal and sealed.
- An electricity storage device was obtained (samples K to Q). Each is designated as Examples 8-14.
- Example 15 the electricity storage device of the present invention was prepared in the same manner as in Example 8 except that the paste A was prepared by mixing sample A and polyvinylidene fluoride resin at a weight ratio of 100: 7 without using acetylene black. (Sample R) was obtained.
- Comparative Examples 4-6 In Example 8, except that the samples H to J obtained in Comparative Examples 1 to 3 were used in place of the sample A, in the same manner as in Example 8, the power storage devices (samples S to U) to be compared were used. Obtained. These are referred to as Comparative Examples 4 to 6, respectively.
- Example 16 Lithium titanate obtained in Example 1 (sample A), acetylene black powder as a conductive agent, and polyvinylidene fluoride resin as a binder were mixed at a weight ratio of 100: 3: 10 and kneaded in a mortar. A paste was prepared. This paste was applied on an aluminum foil, dried at a temperature of 120 ° C. for 10 minutes, punched into a circle having a diameter of 12 mm, and pressed at 17 MPa to obtain a working electrode. The amount of active material contained in the electrode was 4 mg.
- lithium manganate M01Y01: manufactured by Mitsui Kinzoku Co., Ltd.
- acetylene black as a conductive additive
- polyvinylidene fluoride resin as a binder at a weight ratio of 100: 10: 10
- Application and drying were performed at a temperature of 120 ° C. for 10 minutes, cut into a circle having a diameter of 12 mm, and pressed at 17 MPa to obtain a positive electrode.
- the amount of active material contained in the electrode was 8 mg.
- Each of these electrodes was vacuum-dried at a temperature of 120 ° C. for 5 hours, and then incorporated into a sealable coin-type test cell in a glove box having a dew point of ⁇ 70 ° C. or less.
- the cell for evaluation was made of stainless steel (SUS316) having an outer diameter of 20 mm and a height of 3.2 mm.
- the lithium manganate electrode is placed in the lower can of the evaluation cell as a positive electrode, a porous polypropylene film is placed thereon as a separator, a working electrode as a negative electrode, a 1.0 mm thick spacer for adjusting the thickness, and a spring.
- Comparative Example 7 In Example 16, a comparative power storage device (Sample W) was obtained in the same manner as in Example 16 except that Sample J obtained in Comparative Example 3 was used instead of Sample A. This is referred to as Comparative Example 7.
- Evaluation 1 Measurement of nitrogen adsorption / desorption amount
- the nitrogen adsorption / desorption amount of the lithium titanates (samples A to G, J) obtained in Examples 1 to 7 and Comparative Example 3 was determined using a highly accurate fully automatic gas adsorption amount (BELSORP). -MiniII type: manufactured by Nippon Bell Co., Ltd.). About 1 g of the sample was taken in a measurement cell that had been vacuum degassed for about one day, and subjected to vacuum degassing for 3 hours at a temperature of 150 ° C.
- FIG. 1 The adsorption / desorption isotherm of Sample A is shown in FIG. 1
- ADS is an adsorption isotherm
- DES is a desorption isotherm
- p / p0 is a relative pressure
- V a is an adsorption amount
- V d is a desorption amount.
- Respective nitrogen adsorption amounts (V a (0.99) , V a (0.50) ) at relative pressures of 0.99 and 0.50, with a relative pressure of 0.05 interval, a range of 0.45 to 0.90
- Table 1 shows the difference ( ⁇ V d ⁇ a (p) ) between the nitrogen desorption amount and the nitrogen adsorption amount when measured by the above method. It can be seen that all of the lithium titanates of the present invention have V a (0.99) of 50 cm 3 (STP) / g or more and have macropores on the secondary particle surfaces.
- V a (0.50) is 10 cm 3 (STP) / g or less, and ⁇ V d ⁇ a (p) does not continuously take a value of 5 cm 3 (STP) / g or more, resulting in hysteresis. It can be seen that it has almost no mesopores or micropores.
- Evaluation 2 Evaluation of rate characteristics of power storage device using lithium titanate as positive electrode active material
- the power storage devices (samples K to U) obtained in Examples 8 to 15 and Comparative Examples 4 to 6 were subjected to various current amounts.
- the discharge capacity was measured and the capacity retention rate (%) was calculated.
- the measurement was performed by setting the voltage range to 1 to 3 V, the charging current to 0.25 C, and the discharging current to 0.25 C to 30 C.
- the environmental temperature was 25 ° C.
- the capacity retention rate is (X n / X 0.25 ) ⁇ 100, where X 0.25 is the measured value of the discharge capacity at 0.25 C and X n is the measured value in the range of 0.5 C to 30 C. Calculated by the formula.
- 1 C means a current value that can be fully charged in one hour
- 0.48 mA corresponds to 1 C in this evaluation.
- Table 2 The results are shown in Table 2. It can be seen that all of the electricity storage devices of the present invention have a capacity retention rate of 30% or more at 30 C and excellent rate characteristics.
- the electricity storage device of the present invention that does not contain a conductive material has excellent rate characteristics equivalent to those of an electricity storage device containing a conductive material.
- Evaluation 3 Evaluation of rate characteristics of an electricity storage device using lithium titanate as a negative electrode active material
- the discharge capacity was varied with various charge current amounts.
- the capacity retention rate (%) was calculated by measurement. The measurement was performed after aging for 3 hours after producing the electricity storage device, and after charging and discharging at 0.25 C for 2 cycles and conditioning, the voltage range was 1.5 to 2.8 V, and the discharge current was 0.25 C.
- the charging current was set in the range of 0.25 C to 10 C.
- the environmental temperature was 25 ° C.
- the capacity retention rate is (X n / X 0.25 ) ⁇ 100, where X 0.25 is the measured value of discharge capacity at 0.25 C charge, and X n is the measured value in the range of 0.5 C to 10 C. It was calculated by the following formula. Here, 1C means a current value that can be fully charged in 1 hour, and 0.64 mA corresponds to 1C in this evaluation. The results are shown in Table 3. It can be seen that the electricity storage device of the present invention has a capacity retention rate of 10% or more at 10 C and is excellent in rate characteristics even when used as a negative electrode active material.
- the lithium titanate of the present invention has excellent battery characteristics, particularly rate characteristics, and is useful for power storage devices.
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Abstract
Description
4.5モル/リットルの水酸化リチウム水溶液340ミリリットルに、平均粒子径が0.10μmの結晶性二酸化チタン粒子(a)(アナターゼ型)及び平均粒子径が0.07μmの結晶性二酸化チタン粒子(b)(アナターゼ型とルチル型の混晶)を、それぞれ50gを添加し分散させた。このスラリーを撹拌しながら液温を80℃に保ち、チタン酸化合物(オルトチタン酸)を、TiO2換算で50g分散させた水性スラリー650ミリリットルを添加して、結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを得た。このスラリーをGB210-B型噴霧乾燥機(ヤマト科学社製)を用いて、入口温度190℃、出口温度80℃の条件で噴霧乾燥を行い乾燥造粒物を得た後、乾燥造粒物を大気中700℃の温度で3時間焼成を行い、組成式Li4Ti5O12で表される、本発明のチタン酸リチウム(試料A)を得た。尚、結晶性二酸化チタン粒子の平均粒子径の測定には、透過電子顕微鏡H-7000型及び画像回折装置ルーゼックスIIIU型(いずれも日立製作所製)を用いた。
4.5モル/リットルの水酸化リチウム水溶液340ミリリットルに、平均粒子径が0.07μmの結晶性二酸化チタン粒子(b)(アナターゼ型とルチル型の混晶)85.7gと、平均粒子径が0.13μmの結晶性二酸化チタン粒子(c)(アナターゼ型とルチル型の混晶)21.5gを添加し分散させた。このスラリーを撹拌しながら液温を80℃に保ち、チタン酸化合物(オルトチタン酸)を、TiO2換算で42.9g分散させた水性スラリー420ミリリットルを添加して、結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを得た。その後の乾燥造粒物の調製及び焼成は、実施例1と同様にして、組成式Li4Ti5O12で表される、本発明のチタン酸リチウム(試料B)を得た。
実施例1で得られたチタン酸リチウム(試料A)50gとポリエチレングリコール2.5gを均一に混合し、窒素雰囲気下で、混合物を500℃の温度で2時間焼成して、本発明のチタン酸リチウム(試料C)を得た。CHN元素分析装置Vario ELIII型(Elementar社製)で分析したところ、試料Cには、C換算で炭素が0.80重量%含まれていることが判った。
実施例1において、結晶性二酸化チタン粒子(a)、(b)及びチタン酸化合物の使用量を、TiO2換算でそれぞれ53.2gとし、チタン酸化合物の水性スラリーの添加量を680ミリリットルとして、更に、水酸化マグネシウム8.8g(Mgとして3.5g含む)を添加した以外は実施例1と同様にして、マグネシウムをMg換算で2.1重量%含む、本発明のチタン酸リチウム(試料D)を得た。マグネシウム量の測定には、ICP発光分析装置SPS-3100型(セイコーインスツル社製)を用いた。
実施例1において、結晶性二酸化チタン粒子(a)、(b)及びチタン酸化合物の使用量を、TiO2換算でそれぞれ54.5gとし、チタン酸化合物の水性スラリーの添加量を690ミリリットルとして、更に、水酸化アルミニウム12.3g(Alとし4.1g含む)を添加した以外は実施例1と同様にして、アルミニウムを含む、本発明のチタン酸リチウム(試料E)を得た。試料Eのアルミニウムの含有量を、実施例4と同様に測定したところ、Al換算で2.3重量%であった。
実施例1において、結晶性二酸化チタン粒子(a)、(b)及びチタン酸化合物の使用量を、TiO2換算でそれぞれ53.2gとし、チタン酸化合物の水性スラリーの添加量を680ミリリットルとして、更に、酸化ジルコニウム9.3g(Zrとし6.9g含む)を添加した以外は実施例1と同様にして、ジルコニウムをZr換算で8.4重量%含む、本発明のチタン酸リチウム(試料F)を得た。
4.5モル/リットルの水酸化リチウム水溶液340ミリリットルに、平均粒子径が0.07μmの結晶性二酸化チタン粒子(b)125gを添加し分散させた。このスラリーを撹拌しながら液温を80℃に保ち、チタン酸化合物(オルトチタン酸)を、TiO2換算で25g分散させた水性スラリー250ミリリットルを添加して、結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを得た。その後の乾燥造粒物の調製及び焼成は、実施例1と同様にして、組成式Li4Ti5O12で表される、本発明のチタン酸リチウム(試料G)を得た。
4.5モル/リットルの水酸化リチウム水溶液340ミリリットルに、平均粒子径が0.07μmの結晶性二酸化チタン粒子(b)75gを添加し分散させた。このスラリーを撹拌しながら液温を80℃に保ち、チタン酸化合物(オルトチタン酸)を、TiO2換算で75g分散させた水性スラリー720ミリリットルを添加して、結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを得た。その後の乾燥造粒物の調製及び焼成は、実施例1と同様にして、組成式Li4Ti5O12で表される、比較対象のチタン酸リチウム(試料H)を得た。
比較例1において、結晶性二酸化チタン粒子(b)の使用量を111.5g、チタン酸化合物(オルトチタン酸)の使用量をTiO2換算で38.5gとして、375ミリリッの水性スラリーとした以外は、比較例1と同様にして、組成式Li4Ti5O12で表される、比較対象のチタン酸リチウム(試料I)を得た。
4.5モル/リットルの水酸化リチウム水溶液340ミリリットルに、チタン酸化合物(オルトチタン酸)を、TiO2換算で150g分散させた水性スラリー1500ミリリットル添加し、撹拌しながら液温を80℃に保つことで、チタン酸化合物及びリチウム化合物を含むスラリーを得た。その後の乾燥造粒物の調製及び焼成は、実施例1と同様にして、組成式Li4Ti5O12で表される、比較対象のチタン酸リチウム(試料J)を得た。
実施例1~7で得られたチタン酸リチウム(試料A~G)と、導電剤としてのアセチレンブラック粉末、及び結着剤としてのポリフッ化ビニリデン樹脂を重量比で100:5:7で混合し、乳鉢で練り合わせ、ペーストを調製した。このペーストをアルミ箔上に塗布し、120℃の温度で10分乾燥した後、直径12mmの円形に打ち抜き、17MPaでプレスして作用極とした。電極中に含まれる活物質量は、3mgであった。
実施例8おいて、アセチレンブラックを用いずに、試料Aとポリフッ化ビニリデン樹脂を重量比で100:7で混合し、ペーストを調製した以外は実施例8と同様にして、本発明の蓄電デバイス(試料R)を得た。
実施例8おいて、試料Aに替えて比較例1~3で得られた試料H~Jを用いたこと以外は実施例8と同様にして、比較対象の蓄電デバイス(試料S~U)を得た。それぞれを、比較例4~6とする。
実施例1で得られたチタン酸リチウム(試料A)と、導電剤としてのアセチレンブラック粉末、及び結着剤としてのポリフッ化ビニリデン樹脂を重量比で100:3:10で混合し、乳鉢で練り合わせ、ペーストを調製した。このペーストをアルミ箔上に塗布し、120℃の温度で10分乾燥した後、直径12mmの円形に打ち抜き、17MPaでプレスして作用極とした。電極中に含まれる活物質量は、4mgであった。
実施例16において、試料Aにかえて比較例3で得られた試料Jを用いたこと以外は実施例16と同様にして、比較対象の蓄電デバイス(試料W)を得た。これを、比較例7とする。
実施例1~7及び比較例3で得られたチタン酸リチウム(試料A~G、J)の窒素の吸脱着量を、高精度全自動ガス吸着量(BELSORP‐miniII型:日本ベル株式会社製)を使用して測定した。試料約1gを、約一日真空脱気した測定セルに採り、前処理装置(BELLPREP‐vacII型:日本ベル株式会社製)で150℃の温度で3時間の真空脱ガス処理を行った後、液体窒素温度下(77K)で高純度窒素ガスを吸脱着させて、吸脱着等温線を得た。試料Aの吸脱着等温線を、図1に示す。図1において、「ADS」は吸着等温線であり、「DES」は脱着等温線であり、「p/p0」は相対圧を、「Va」は吸着量を、「Vd」は脱着量を表す。相対圧0.99及び0.50におけるそれぞれの窒素吸着量(Va(0.99)、Va(0.50))、相対圧を0.05間隔とし0.45~0.90の範囲で測定した際の窒素脱着量と窒素吸着量との差(ΔVd-a(p))を表1に示す。本発明のチタン酸リチウムは、いずれもVa(0.99)が50cm3(STP)/g以上であり、二次粒子表面にマクロポアを有していること判る。また、Va(0.50)が10cm3(STP)/g以下あり、しかも、ΔVd-a(p)が連続して5cm3(STP)/g以上の値を取らず、ヒステリシスが生じていないので、メソポアやマイクロポアをほとんど有していないことが判る。
実施例8~15、比較例4~6で得られた蓄電デバイス(試料K~U)について、種々の電流量で放電容量を測定して容量維持率(%)を算出した。測定は、電圧範囲を1~3Vに、充電電流は0.25Cに、放電電流は0.25C~30Cの範囲に設定して行った。環境温度は25℃とした。容量維持率は、0.25Cでの放電容量の測定値をX0.25、0.5C~30Cの範囲での測定値をXnとすると、(Xn/X0.25)×100の式で算出した。尚、ここで1Cとは、1時間で満充電できる電流値を言い、本評価では、0.48mAが1Cに相当する。容量維持率が高いほうが、レート特性が優れている。結果を、表2に示す。本発明の蓄電デバイスは、いずれも、30Cでの容量維持率が70%以上であり、レート特性に優れていることが判る。また、導電材を含まない本発明の蓄電デバイスは、導電材を配合した蓄電デバイスと同等の優れたレート特性を有している。
実施例16、比較例7で得られた蓄電デバイス(試料V、W)について、種々の充電電流量で放電容量を測定して容量維持率(%)を算出した。測定は、蓄電デバイスを作製した後3時間熟成してから、0.25Cで2サイクル充放電してコンディショニングを行った後、電圧範囲を1.5~2.8Vに、放電電流は0.25Cに、充電電流は0.25C~10Cの範囲に設定して行った。環境温度は25℃とした。容量維持率は、0.25C充電での放電容量の測定値をX0.25、0.5C~10Cの範囲での測定値をXnとすると、(Xn/X0.25)×100の式で算出した。尚、ここで1Cとは、1時間で満充電できる電流値を言い、本評価では、0.64mAが1Cに相当する。結果を、表3に示す。本発明の蓄電デバイスは、10Cでの容量維持率が70%以上であり、負極活物質に用いても、レート特性に優れていることが判る。
Claims (16)
- チタン酸リチウムの一次粒子が集合した二次粒子を含み、二次粒子表面に少なくともマクロポアを有するチタン酸リチウム。
- 窒素の吸脱着等温線における相対圧0.99での窒素吸着量が50cm3(STP)/g以上にある請求項1記載のチタン酸リチウム。
- 窒素の吸脱着等温線における相対圧0.50での窒素吸着量が10cm3(STP)/g以下にあり、且つ、相対圧を0.05間隔とし0.45~0.90の範囲で測定した際の窒素脱着量と窒素吸着量との差が、連続的に5cm3(STP)/g以上の値を取らない請求項1記載のチタン酸リチウム。
- 組成式Li4Ti5O12で表される請求項1記載のチタン酸リチウム。
- 炭素を含む請求項1記載のチタン酸リチウム。
- 異種金属元素を含む請求項1記載のチタン酸リチウム。
- 異種金属元素がマグネシウム、アルミニウム、ジルコニウムから選ばれる少なくとも1種である請求項6記載のチタン酸リチウム。
- 結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを乾燥造粒した後、焼成してチタン酸リチウム二次粒子を得る方法において、(1)平均粒子径の異なる少なくとも2種の結晶性酸化チタン粒子を含む結晶性酸化チタンを用いる、及び/又は(2)結晶性酸化チタンをチタン酸化合物に対しTiO2換算の重量比で4倍より多い量で用いる、チタン酸リチウムの製造方法。
- 前記(1)の方法において、平均粒子径が最小である結晶性酸化チタン粒子に対し、他の結晶性酸化チタン粒子が1.3倍以上の平均粒子径を有する請求項8記載のチタン酸リチウムの製造方法。
- 更にチタン酸リチウム二次粒子に炭素を含ませる工程を含む請求項8記載のチタン酸リチウムの製造方法。
- (A)結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを乾燥造粒して焼成した後、得られた焼成物を炭素含有物質の存在下で再焼成するか、又は(B)結晶性酸化チタン、チタン酸化合物、リチウム化合物及び炭素含有物質を含むスラリーを乾燥造粒して焼成する請求項10記載のチタン酸リチウムの製造方法。
- 更にチタン酸リチウム二次粒子に異種金属元素を含ませる工程を含む請求項8記載のチタン酸リチウムの製造方法。
- (A)結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーに異種金属元素の化合物を添加するか、又は(B)異種金属元素を含む結晶性酸化チタン、チタン酸化合物及びリチウム化合物を含むスラリーを乾燥造粒して焼成する請求項12記載のチタン酸リチウムの製造方法。
- 請求項1記載のチタン酸リチウムを含む電極活物質。
- 請求項14記載の電極活物質を含む電極を用いた蓄電デバイス。
- 請求項14記載の電極活物質を含み、且つ導電剤を含まない電極を用いた蓄電デバイス。
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CA2760985A CA2760985A1 (en) | 2009-05-26 | 2010-05-25 | Lithium titanate comprising secondary particles |
KR1020117028185A KR101761428B1 (ko) | 2009-05-26 | 2010-05-25 | 티탄산 리튬, 그 제조 프로세스 및 그를 각각 포함하는 전극 활물질 및 축전 디바이스 |
CN201080021706.6A CN102428031B (zh) | 2009-05-26 | 2010-05-25 | 钛酸锂、生产钛酸锂的方法以及各自包含钛酸锂的电极活性材料和蓄电装置 |
JP2011516021A JP5726074B2 (ja) | 2009-05-26 | 2010-05-25 | チタン酸リチウム及びその製造方法並びにそれを用いた電極活物質及び蓄電デバイス |
US13/321,973 US9126847B2 (en) | 2009-05-26 | 2010-05-25 | Lithium titanate, electrode active material and electricity storage device each comprising the same |
KR1020177005974A KR101829177B1 (ko) | 2009-05-26 | 2010-05-25 | 티탄산 리튬, 그 제조 프로세스 및 그를 각각 포함하는 전극 활물질 및 축전 디바이스 |
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US14/812,125 US9452940B2 (en) | 2009-05-26 | 2015-07-29 | Lithium titanate, electrode active material and electricity storage device each comprising the same |
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- 2010-05-25 CA CA2760985A patent/CA2760985A1/en not_active Abandoned
- 2010-05-25 EP EP10780537.6A patent/EP2436650B1/en not_active Not-in-force
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Also Published As
Publication number | Publication date |
---|---|
CN104319383A (zh) | 2015-01-28 |
EP2436650A4 (en) | 2012-11-14 |
CN102428031A (zh) | 2012-04-25 |
EP2436650B1 (en) | 2016-11-02 |
US9452940B2 (en) | 2016-09-27 |
US20120070744A1 (en) | 2012-03-22 |
CN104319383B (zh) | 2018-04-17 |
KR20170028455A (ko) | 2017-03-13 |
HK1202707A1 (en) | 2015-10-02 |
KR20120023021A (ko) | 2012-03-12 |
HK1169822A1 (zh) | 2013-02-08 |
JP5726074B2 (ja) | 2015-05-27 |
EP2436650A1 (en) | 2012-04-04 |
US9126847B2 (en) | 2015-09-08 |
KR101761428B1 (ko) | 2017-07-25 |
TW201111285A (en) | 2011-04-01 |
JPWO2010137582A1 (ja) | 2012-11-15 |
CA2760985A1 (en) | 2010-12-02 |
TWI471270B (zh) | 2015-02-01 |
CN102428031B (zh) | 2016-08-10 |
KR101829177B1 (ko) | 2018-02-13 |
US20160009567A1 (en) | 2016-01-14 |
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