WO2016151890A1 - Secondary battery positive electrode active material and method for producing same - Google Patents
Secondary battery positive electrode active material and method for producing same Download PDFInfo
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- WO2016151890A1 WO2016151890A1 PCT/JP2015/076385 JP2015076385W WO2016151890A1 WO 2016151890 A1 WO2016151890 A1 WO 2016151890A1 JP 2015076385 W JP2015076385 W JP 2015076385W WO 2016151890 A1 WO2016151890 A1 WO 2016151890A1
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- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive electrodes
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- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a positive electrode active material for a secondary battery in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide, and a method for producing the same.
- lithium ion secondary batteries are widely known as the most excellent secondary batteries that operate near room temperature.
- lithium-containing olivine-type phosphate metal salts such as Li (Fe, Mn) PO 4 and Li 2 (Fe, Mn) SiO 4 are more resource-constrained than lithium transition metal oxides such as LiCoO 2. Therefore, it is possible to exhibit high safety, and therefore, it is an optimum positive electrode material for obtaining a high-output and large-capacity lithium ion secondary battery.
- these compounds have the property that it is difficult to sufficiently increase the conductivity due to the crystal structure, and there is room for improvement in the diffusibility of lithium ions. Has been made.
- Patent Document 2 discloses that after the firing treatment of the raw material mixture containing the carbonaceous material precursor, the water content is reduced to a certain value or less by performing pulverization treatment and classification treatment in a dry atmosphere.
- Technology is disclosed.
- a predetermined lithium phosphate compound, lithium silicate compound, and the like and a conductive carbon material are mixed by a wet ball mill, and then a mechanochemical treatment is performed so that the conductive carbon material is uniformly applied to the surface.
- a technique for obtaining a composite oxide deposited is disclosed.
- Patent Document 4 discloses a sodium secondary battery active material using marisite-type NaMnPO 4
- Patent Document 5 discloses a positive electrode active material containing transition metal sodium phosphate having an olivine structure. Substances are disclosed, and any literature shows that a high-performance sodium ion secondary battery can be obtained.
- the surface of the positive electrode active material for secondary batteries is not sufficiently covered with the carbon source, and a part of the surface is exposed, so that moisture adsorption can be suppressed. Therefore, it has been found that it is difficult to obtain a positive electrode active material for a secondary battery having a sufficiently high moisture content and sufficiently high battery properties such as cycle characteristics.
- an object of the present invention is to provide a positive electrode active material for a secondary battery that can effectively suppress moisture adsorption and a method for manufacturing the same, in order to obtain a high-performance lithium ion secondary battery or a sodium ion secondary battery. It is to provide.
- the present inventors have made various studies, and as long as a positive electrode active material for a secondary battery in which conductive carbon powder and carbon obtained by carbonizing a water-soluble carbon material are supported on a specific oxide. Since the carbons derived from a plurality of carbon sources can effectively cover the oxide surface and effectively suppress the adsorption of moisture, lithium ions or sodium ions can effectively carry out electrical conduction. As a substance, it was found to be extremely useful, and the present invention was completed.
- the present invention includes at least the following formula (A), (B) or (C) containing iron or manganese: LiFe a Mn b M c PO 4 (A) (In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd.
- Li 2 Fe d Mn e N f SiO 4 (B) (In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr.
- D, e, and f are 0 ⁇ d ⁇ 1, 0 ⁇ e ⁇ 1, and 0 ⁇ f ⁇ 1, 2d + 2e +.
- a positive electrode active material for a secondary battery in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by:
- the present invention provides the following formula (A), (B) or (C) containing at least iron or manganese: LiFe a Mn b M c PO 4 (A) (In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd.
- Li 2 Fe d Mn e N f SiO 4 (B) (In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr.
- D, e, and f are 0 ⁇ d ⁇ 1, 0 ⁇ e ⁇ 1, and 0 ⁇ f ⁇ 1, 2d + 2e +.
- a method for producing a positive electrode active material for a secondary battery in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by: A step (I) of obtaining an oxide X by subjecting a slurry water containing a lithium compound or sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction; Step (II) in which a water-insoluble conductive carbon material is added to the obtained oxide X and dry-mixed to obtain a composite Y, and a water-soluble carbon material is added to the obtained composite Y and wet-mixed.
- the manufacturing method of the positive electrode active material for secondary batteries provided with the process (III) to bake is provided.
- a predetermined oxide effectively supports a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material, so that the oxide is partially supported on the oxide surface. Since the oxide is effectively suppressed from being exposed without the presence of carbon, a positive electrode active material for a secondary battery in which the exposed portion on the oxide surface is effectively reduced can be obtained. Therefore, since such a positive electrode active material can effectively suppress the adsorption of moisture, in a lithium ion secondary battery or a sodium ion secondary battery using the positive electrode active material, lithium ions or sodium ions effectively carry electric conduction, and various Excellent battery characteristics such as cycle characteristics can be stably exhibited even in a different use environment.
- the oxide used in the present invention contains at least iron or manganese and has the following formula (A), (B) or (C): LiFe a Mn b M c PO 4 (A) (In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd.
- Li 2 Fe d Mn e N f SiO 4 (B) (In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr.
- D, e, and f are 0 ⁇ d ⁇ 1, 0 ⁇ e ⁇ 1, 0 ⁇ f ⁇ 1, and 2d + 2e +.
- oxides all have an olivine structure and contain at least iron or manganese.
- oxide represented by the above formula (A) or (B) a positive electrode active material for a lithium ion battery is obtained, and when the oxide represented by the above formula (C) is used.
- a positive electrode active material for a sodium ion battery is obtained.
- the oxide represented by the above formula (A) is an olivine-type transition metal lithium compound containing at least iron (Fe) and manganese (Mn) as so-called transition metals.
- M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd, and is preferably Mg, Zr, Mo, or Co.
- a is 0 ⁇ a ⁇ 1, preferably 0.01 ⁇ a ⁇ 0.99, and more preferably 0.1 ⁇ a ⁇ 0.9.
- b is 0 ⁇ b ⁇ 1, preferably 0.01 ⁇ b ⁇ 0.99, and more preferably 0.1 ⁇ b ⁇ 0.9.
- olivine-type transition metal lithium compound represented by the above formula (A) include LiFe 0.2 Mn 0.8 PO 4 , LiFe 0.9 Mn 0.1 PO 4 , LiFe 0.15 Mn 0.75 Mg 0.1 PO 4 , LiFe Examples include 0.19 Mn 0.75 Zr 0.03 PO 4 , and among them, LiFe 0.2 Mn 0.8 PO 4 is preferable.
- the oxide represented by the above formula (B) is a so-called olivine-type transition metal lithium compound containing at least iron (Fe) and manganese (Mn) as transition metals.
- N represents Ni, Co, Al, Zn, V, or Zr, and is preferably Co, Al, Zn, V, or Zr.
- d is 0 ⁇ d ⁇ 1, preferably 0 ⁇ d ⁇ 1, and more preferably 0.1 ⁇ d ⁇ 0.6.
- e is 0 ⁇ d ⁇ 1, preferably 0 ⁇ e ⁇ 1, and more preferably 0.1 ⁇ e ⁇ 0.6.
- f is 0 ⁇ f ⁇ 1, preferably 0 ⁇ f ⁇ 1, and more preferably 0.05 ⁇ f ⁇ 0.4.
- olivine-type transition metal lithium compound represented by the above formula (B) include, for example, Li 2 Fe 0.45 Mn 0.45 Co 0.1 SiO 4 , Li 2 Fe 0.36 Mn 0.54 Al 0.066 SiO 4 , Li 2 Fe 0.45 Mn 0.45 Zn 0.1 SiO 4 , Li 2 Fe 0.36 Mn 0.54 V 0.066 SiO 4 , Li 2 Fe 0.282 Mn 0.658 Zr 0.02 SiO 4 and the like can be mentioned, among which Li 2 Fe 0.282 Mn 0.658 Zr 0.02 SiO 4 is preferable.
- the oxide represented by the formula (C) is an olivine-type transition metal sodium phosphate compound containing iron (Fe) and manganese (Mn) as at least transition metals.
- Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd, and is preferably Mg, Zr, Mo, or Co.
- g is 0 ⁇ g ⁇ 1, and preferably 0 ⁇ g ⁇ 1.
- h is 0 ⁇ h ⁇ 1, and preferably 0.5 ⁇ h ⁇ 1.
- i is 0 ⁇ i ⁇ 1, preferably 0 ⁇ i ⁇ 0.5, and more preferably 0 ⁇ i ⁇ 0.3.
- olivine-type transition metal sodium phosphate compound represented by the above formula (C) include, for example, NaFe 0.2 Mn 0.8 PO 4 , NaFe 0.9 Mn 0.1 PO 4 , NaFe 0.15 Mn 0.7 Mg 0.15 PO 4 , NaFe Examples include 0.19 Mn 0.75 Zr 0.03 PO 4 , NaFe 0.19 Mn 0.75 Mo 0.03 PO 4 , NaFe 0.15 Mn 0.7 Co 0.15 PO 4 , and NaFe 0.2 Mn 0.8 PO 4 is preferred.
- the positive electrode active material for a secondary battery according to the present invention is obtained by carbonizing a water-insoluble conductive carbon material and a water-soluble carbon material on the oxide represented by the above formula (A), (B), or (C). Carbon (carbon derived from a water-soluble carbon material) is supported. That is, a water-insoluble conductive carbon material and a water-soluble carbon material coexist as a carbon source, and the oxide surface is coated without the presence of such carbon while the oxide surface is coated with carbon derived from one carbon source. The carbon derived from the other carbon source is effectively supported on the exposed portion.
- the water-insoluble conductive carbon material and the carbon obtained by carbonizing the water-soluble carbon material are combined and firmly supported on the entire surface of the oxide while effectively suppressing the exposure of the oxide surface. Therefore, moisture adsorption in the positive electrode active material for a secondary battery of the present invention can be effectively prevented.
- the water-insoluble conductive carbon material supported on the oxide represented by the above formula (A), (B) or (C) means that the amount dissolved in 100 g of water at 25 ° C. is carbon of the water-insoluble conductive carbon material.
- Examples of the water-insoluble conductive carbon material include one or more selected from graphite, acetylene black, ketjen black, channel black, furnace black, lamp black, and thermal black. Of these, graphite is preferable from the viewpoint of reducing the amount of adsorbed moisture.
- the graphite may be any of artificial graphite (scaly, massive, earthy, graphene) or natural graphite.
- the BET specific surface area of the water-insoluble conductive carbon material that can be used is preferably 1 to 750 m 2 / g, more preferably 3 to 500 m 2 / g, from the viewpoint of effectively reducing the amount of adsorbed water. Further, from the same viewpoint, the average particle size of the water-insoluble conductive carbon material is preferably 0.5 to 20 ⁇ m, more preferably 1.0 to 15 ⁇ m.
- the water-soluble carbon material supported as carbon carbonized by the oxide represented by the formula (A), (B) or (C) is used in 100 g of water at 25 ° C.
- the water-soluble carbon material include one or more selected from saccharides, polyols, polyethers, and organic acids.
- monosaccharides such as glucose, fructose, galactose and mannose
- disaccharides such as maltose, sucrose and cellobiose
- polysaccharides such as starch and dextrin
- polyols and polyethers such as diol, propanediol, polyvinyl alcohol, and glycerin
- organic acids such as citric acid, tartaric acid, and ascorbic acid.
- glucose, fructose, sucrose, and dextrin are preferable, and glucose is more preferable from the viewpoint of improving the solubility and dispersibility in a solvent and effectively functioning as a carbon material.
- the carbon atom equivalent of the water-insoluble conductive carbon material and the water-soluble carbon material is the positive electrode for the secondary battery of the present invention as the carbon in which the water-insoluble conductive carbon material and the carbonized water-soluble carbon material are supported on the oxide. It will coexist in the active material.
- the carbon atom equivalent amount of the water-insoluble conductive carbon material and the water-soluble carbon material corresponds to the total supported amount of carbon obtained by carbonizing the water-insoluble conductive carbon material and the water-soluble carbon material.
- the total amount in the positive electrode active material for batteries is preferably 1.0 to 20.0% by mass, more preferably 2.0 to 17.5% by mass, and still more preferably 3.0 to 15.0%. % By mass.
- the carbon atom equivalent amount of the water-insoluble conductive carbon material and the water-soluble carbon material is preferably the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C). 1.0 to 15.0 mass%, more preferably 2.0 to 13.5 mass%, still more preferably 3.0 to 12.0 mass%, and the oxide is represented by the above formula (B). Is preferably 2.0 to 20.0% by mass, more preferably 3.0 to 17.5% by mass, and still more preferably 4.0 to 15%. 0.0% by mass. Further, the carbon atom equivalent amount of the water-soluble carbon material, that is, the supported amount of carbon obtained by carbonizing the water-soluble carbon material is preferably 0.5 to 17.0 in the positive electrode active material for secondary battery of the present invention.
- the carbon atom equivalent amount of the water-soluble carbon material is preferably 0.5 to 10.0 for the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C).
- the positive electrode active material for use it is preferably 0.75 to 17.0% by mass, more preferably 0.75 to 13.5% by mass, and further preferably 0.75 to 10.0% by mass.
- the total amount of carbon-atom equivalents of the water-insoluble conductive carbon material and the water-soluble carbon material present in the positive electrode active material for secondary batteries is confirmed as the total carbon amount measured using a carbon / sulfur analyzer. can do. Further, the carbon atom equivalent amount of the water-soluble carbon material can be confirmed by subtracting the addition amount of the water-insoluble conductive carbon material from the total carbon amount measured using a carbon / sulfur analyzer.
- the positive electrode active material for a secondary battery according to the present invention efficiently (A), (B) or (C) while the water-insoluble conductive carbon material and the carbon obtained by carbonizing the water-soluble carbon material complement each other.
- the composite containing the oxide and the water-insoluble conductive carbon material is supported as carbon obtained by carbonizing the water-soluble carbon material.
- a composite formed by supporting a water-insoluble conductive carbon material on an oxide is supported by carbon obtained by carbonizing a water-soluble carbon material.
- the water-insoluble conductive carbon material is preferably dry-mixed with an oxide obtained by a hydrothermal reaction and supported on the oxide, and is premixed with the oxide. It is more preferable that the mixture is mixed while applying a compressive force and a shearing force and is supported on an oxide. That is, the composite containing the oxide and the water-insoluble conductive carbon material is preferably a dry mixture of the water-insoluble conductive carbon material and an oxide that is a hydrothermal reaction product.
- supported by the oxide by baking a water-insoluble conductive carbon material is obtained as a composite_body
- a water-soluble carbon material may be supplementarily added as necessary, separately from the water-soluble carbon material added during the wet mixing described later.
- the composite obtained at this time contains a water-soluble carbon material together with an oxide and a water-insoluble conductive carbon material.
- a water-soluble carbon material supported as carbonized carbon on a composite containing the oxide and the water-insoluble conductive carbon material is obtained by using the oxide surface of the composite without the presence of the water-insoluble conductive carbon material. From the viewpoint of effectively supporting carbon on the exposed portion, it is preferable that it is supported on an oxide as carbon that is carbonized by being baked after being wet mixed with the composite. . That is, the positive electrode active material for a secondary battery of the present invention is preferably a fired product of a wet mixture of a water-soluble carbon material and a composite containing an oxide and a water-insoluble conductive carbon material.
- the water-soluble carbon material used when wet-mixing may be the same type as the water-soluble carbon material used as an auxiliary when necessary during the dry-mixing, or another type. There may be.
- the positive electrode active material for a secondary battery of the present invention is a slurry water containing a lithium compound or a sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound.
- a step (I) of obtaining an oxide X by subjecting to a thermal reaction Step (II) in which a water-insoluble conductive carbon material is added to the obtained oxide X and dry-mixed to obtain a composite Y, and a water-soluble carbon material is added to the obtained composite Y and wet-mixed. It is preferably obtained by a production method comprising the step (III) of firing.
- Step (I) is a step of obtaining an oxide X by subjecting a slurry water containing a lithium compound or sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction.
- a lithium compound or sodium compound that can be used include hydroxides (for example, LiOH.H 2 O, NaOH), carbonates, sulfates, and acetates. Of these, hydroxide is preferable.
- the content of the lithium compound or silicic acid compound in the slurry water is preferably 5 to 50 parts by mass, more preferably 7 to 45 parts by mass with respect to 100 parts by mass of water.
- the content of the lithium compound or sodium compound in the slurry water is preferably 5 to 50 parts by mass with respect to 100 parts by mass of water.
- the amount is preferably 10 to 45 parts by mass.
- the content of the silicate compound in the slurry water is preferably 5 to 40 parts by mass, more preferably 7 to 35 parts by mass with respect to 100 parts by mass of water.
- Step (I) is a mixture A containing a lithium compound or a sodium compound from the viewpoint of improving the dispersibility of each component contained in the slurry water and making the obtained positive electrode active material particles finer to improve battery physical properties.
- a mixture a 2 was mixed phosphoric acid compound or a silicic acid compound (Ia), to the mixture a 2 obtained as well, by adding a metal salt containing at least an iron compound or a manganese compound, and mixed
- step (I) or (Ia) prior to mixing the mixture A phosphoric acid compound to one or silicic acid compound, preferably it is allowed to stir in advance mixture A 1.
- the stirring time of the mixture A 1 is preferably 1 to 15 minutes, more preferably 3 to 10 minutes.
- the temperature of the mixture A 1 is preferably 20 to 90 ° C., more preferably 20 to 70 ° C.
- Examples of the phosphoric acid compound used in the step (I) or (Ia) include orthophosphoric acid (H 3 PO 4 , phosphoric acid), metaphosphoric acid, pyrophosphoric acid, triphosphoric acid, tetraphosphoric acid, ammonium phosphate, and ammonium hydrogen phosphate. Etc. Of these, phosphoric acid is preferably used, and an aqueous solution having a concentration of 70 to 90% by mass is preferably used.
- phosphoric acid is preferably used, and an aqueous solution having a concentration of 70 to 90% by mass is preferably used.
- the reaction proceeds well in the mixture A 1 , and the precursor of the oxide X represented by the above (A) to (C) is contained in the slurry. It is also possible to effectively prevent the oxide precursors from being agglomerated unnecessarily while being uniformly dispersed.
- the dropping rate of phosphoric acid into the mixture A 1 is preferably 15 to 50 mL / min, more preferably 20 to 45 mL / min, and further preferably 28 to 40 mL / min.
- the stirring time of the mixture A 1 while dropping phosphoric acid is preferably 0.5 to 24 hours, more preferably 3 to 12 hours.
- the stirring speed of the mixture A 1 while dropping phosphoric acid is preferably 200 to 700 rpm, more preferably 250 to 600 rpm, and further preferably 300 to 500 rpm. Note that when the mixture is stirred for A 1, preferred to further cool the mixture A in the following 1 the boiling point temperature. Specifically, cooling to 80 ° C. or lower is preferable, and cooling to 20 to 60 ° C. is more preferable.
- the silicic acid compound used in the step (I) or (Ia) is not particularly limited as long as it is a reactive silica compound.
- the mixture A 2 after mixing the phosphoric acid compound or the silicic acid compound preferably contains 2.0 to 4.0 mol of lithium or sodium with respect to 1 mol of phosphoric acid or silicic acid. It is more preferable to contain 1 mol, and the lithium compound or sodium compound and the phosphoric acid compound or silicic acid compound may be used so as to obtain such an amount. More specifically, when a phosphoric acid compound is used in step (I), the mixture A 2 after mixing the phosphoric acid compound has 2.7 to 3.3 of lithium or sodium per mol of phosphoric acid.
- the mixture A 2 after mixing the silicate compound is Lithium is preferably contained in an amount of 2.0 to 4.0 mol, more preferably 2.0 to 3.0, with respect to 1 mol.
- the reaction in the mixture A 2 is completed, and represented by the above (A) to (C) to produce a precursor of the oxides in the mixture a 2.
- the reaction can proceed in a state where the dissolved oxygen concentration in the mixture A 2 is reduced, and the dissolved oxygen concentration in the mixture containing the resulting oxide precursor is also effectively increased. Since it is reduced, oxidation of the iron compound or manganese compound added in the next step can be suppressed.
- the oxide precursors represented by the above (A) to (C) exist as fine dispersed particles. For example, in the case of the oxide represented by the above formula (A), such an oxide precursor is obtained as trilithium phosphate (Li 3 PO 4 ).
- the pressure for purging nitrogen is preferably 0.1 to 0.2 MPa, more preferably 0.1 to 0.15 MPa.
- the temperature of the mixture A 2 after mixing the phosphoric acid compound or the silicic acid compound is preferably 20 to 80 ° C., more preferably 20 to 60 ° C.
- the reaction time is preferably 5 to 60 minutes, more preferably 15 to 45 minutes.
- the stirring speed at this time is preferably 200 to 700 rpm, more preferably 250 to 600 rpm.
- dissolved oxygen in the mixture A 2 after mixing the phosphoric acid compound or the silicate compound is preferably 0.5 mg / L or less, and more preferably 0.2 mg / L or less.
- an oxide X is obtained by subjecting the obtained oxide precursor and slurry water containing a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction. . It is preferable to use the obtained oxide precursor as a mixture and add a metal salt containing at least an iron compound or a manganese compound to the slurry water X.
- the oxides represented by the above (A) to (C) can be obtained while simplifying the process, and it is possible to obtain extremely fine particles, which are very useful for secondary batteries.
- a positive electrode active material can be obtained.
- iron compounds examples include iron acetate, iron nitrate, and iron sulfate. These may be used alone or in combination of two or more. Among these, iron sulfate is preferable from the viewpoint of improving battery characteristics.
- manganese compounds examples include manganese acetate, manganese nitrate, and manganese sulfate. These may be used alone or in combination of two or more. Among these, manganese sulfate is preferable from the viewpoint of improving battery characteristics.
- the use molar ratio of these iron compound and manganese compound is preferably 99: 1 to 1:99, more preferably 90. : 10 to 10:90.
- the total addition amount of these iron compound and manganese compound is preferably 0.99 to 1.01 mol, more preferably 0.995 with respect to 1 mol of Li 3 PO 4 contained in the slurry water X. ⁇ 1.005 mol.
- metal (M, N, or Q) salts other than an iron compound and a manganese compound as a metal salt as needed.
- M, N, and Q in the metal (M, N, or Q) salt have the same meanings as M, N, and Q in the above formulas (A) to (C), and as the metal salt, sulfate, halogen compound, organic Acid salts and hydrates thereof can be used. These may be used alone or in combination of two or more. Among them, it is more preferable to use a sulfate from the viewpoint of improving battery physical properties.
- the total amount of iron compound, manganese compound, and metal (M, N, or Q) salt added is phosphoric acid in the mixture obtained in the above step (I).
- the amount is preferably 0.99 to 1.01 mole, more preferably 0.995 to 1.005 mole relative to 1 mole of silicic acid.
- the amount of water used for the hydrothermal reaction is phosphoric acid or silicate ions contained in the slurry water X from the viewpoint of the solubility of the metal salt used, the ease of stirring, the efficiency of synthesis, etc.
- the amount is preferably 10 to 50 mol, more preferably 12.5 to 45 mol, relative to 1 mol. More specifically, when the ions contained in the slurry water X are phosphate ions, the amount of water used for the hydrothermal reaction is preferably 10 to 30 mol, more preferably 12 .5 to 25 moles. Further, when the ions contained in the slurry water X are silicate ions, the amount of water used for the hydrothermal reaction is preferably 10 to 50 mol, more preferably 12.5 to 45. Is a mole.
- the order of adding the iron compound, manganese compound and metal (M, N or Q) salt is not particularly limited. Moreover, while adding these metal salts, you may add antioxidant as needed. As such an antioxidant, sodium sulfite (Na 2 SO 3 ), hydrosulfite sodium (Na 2 S 2 O 4 ), aqueous ammonia and the like can be used.
- the content of the oxide precursor in the slurry water X obtained by adding an iron compound, a manganese compound, and a metal (M, N or Q) salt or an antioxidant used as necessary is preferably 10 to It is 50% by mass, more preferably 15 to 45% by mass, and still more preferably 20 to 40% by mass.
- the hydrothermal reaction in the step (I) or (Ib) may be 100 ° C. or higher, and preferably 130 to 180 ° C.
- the hydrothermal reaction is preferably carried out in a pressure-resistant vessel.
- the pressure at this time is preferably 0.3 to 0.9 MPa, and the reaction is carried out at 140 to 160 ° C.
- the pressure is preferably 0.3 to 0.6 MPa.
- the hydrothermal reaction time is preferably 0.1 to 48 hours, more preferably 0.2 to 24 hours.
- the obtained oxide X is an oxide represented by the above formulas (A) to (C), which can be isolated by filtration, washing with water, and drying. As the drying means, freeze drying or vacuum drying is used.
- the BET specific surface area of the resulting oxide X is preferably 5 to 40 m 2 / g, more preferably 5 to 40 m from the viewpoint of efficiently carrying the coexisting carbon and effectively reducing the amount of adsorbed water. 20 m 2 / g.
- the BET specific surface area of the oxide X is less than 5 m 2 / g, the primary particles of the positive electrode active material for the secondary battery become too large, and the battery characteristics may be deteriorated.
- the BET specific surface area exceeds 40 m 2 / g, the amount of adsorbed moisture of the positive electrode active material for the secondary battery may increase and affect the battery characteristics.
- Step (II) is a step of adding the water-insoluble conductive carbon material to the oxide X obtained in step (I) and then dry mixing to obtain the composite Y.
- a water-soluble carbon material may be further supplementarily added.
- the order of addition is not particularly limited.
- the amount of the water-insoluble conductive carbon material added is preferably 0.5 to 24.2 parts by mass, more preferably 1.5 to 20.5 parts by mass with respect to 100 parts by mass of the oxide X, for example.
- the amount is preferably 2.6 to 17.0 parts by mass.
- the addition amount of the water-insoluble conductive carbon material is preferably 0.5 to 17.0 in the case of the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C). Secondary battery in which the oxide is represented by the above formula (B), more preferably 1.5 to 14.9 parts by mass, and still more preferably 2.6 to 13.0 parts by mass.
- the positive electrode active material for use is preferably 1.3 to 23.8 parts by mass, more preferably 2.3 to 20.1 parts by mass, and still more preferably 3.4 to 16.6 parts by mass.
- the mass of the addition amount of the water-insoluble conductive carbon material and the carbon atom equivalent amount of the addition amount of the water-soluble carbon material is preferably 100: 2 to 3: 100, more preferably 100: 10 to 10: 100.
- the dry mixing in the step (II) is preferably mixing by a normal ball mill, and more preferably by a planetary ball mill capable of revolving. Further, the water-insoluble conductive carbon material and the water-soluble carbon material used in combination as necessary are densely and uniformly dispersed on the oxide surface represented by the above formulas (A) to (C) and carbonized. From the viewpoint of effectively supporting the carbon, it is more preferable to mix the composite Y while applying a compressive force and a shearing force to obtain a composite Y ′.
- the process of mixing while applying a compressive force and a shearing force is preferably performed in a closed container equipped with an impeller.
- the peripheral speed of the impeller is preferably 25 to 40 m / s, more preferably 27 from the viewpoint of increasing the tap density of the obtained positive electrode active material and reducing the BET specific surface area to effectively reduce the amount of adsorbed water. ⁇ 40 m / s.
- the mixing time is preferably 5 to 90 minutes, more preferably 10 to 80 minutes.
- the peripheral speed of the impeller means the speed of the outermost end of the rotary stirring blade (impeller), which can be expressed by the following formula (1), and is mixed while applying compressive force and shearing force.
- the processing time and / or the impeller peripheral speed when performing the mixing process while applying the compressive force and the shearing force need to be appropriately adjusted according to the amount of the composite Y to be charged into the container.
- the container By operating the container, it is possible to perform a process of mixing the mixture while applying a compressive force and a shearing force between the impeller and the inner wall of the container, and the above formulas (A) to (C).
- the water-insoluble conductive carbon material and the water-soluble carbon material to be used in combination as needed are densely and uniformly dispersed on the oxide surface represented by Combined with the added water-soluble carbon material, a positive electrode active material for a secondary battery that can effectively reduce the amount of adsorbed water can be obtained.
- a container corresponding to a part capable of accommodating the complex Y is preferably 0.1 to 0.7 g, more preferably 0.15 to 0.4 g per 1 cm 3 .
- the apparatus equipped with a closed container that can easily perform mixing while applying compressive force and shear force examples include a high-speed shear mill, a blade-type kneader, and the like. Fine particle composite apparatus Nobilta (manufactured by Hosokawa Micron Corporation) can be suitably used.
- the treatment temperature is preferably 5 to 80 ° C., more preferably 10 to 50 ° C.
- the treatment atmosphere is not particularly limited, but is preferably an inert gas atmosphere or a reducing gas atmosphere.
- Step (III) is a step of adding a water-soluble carbon material obtained in step (I), wet mixing, and baking. This effectively suppresses the exposure of the surface of the oxide X represented by the above (A) to (C), while the water-insoluble conductive carbon material and the water-soluble carbon material are carbonized on the oxide X.
- the formed carbon can be supported firmly together.
- the amount of the water-soluble carbon material added in the step (III) is such that carbon obtained by carbonizing the water-soluble carbon material is effectively supported on the surface of the oxide X where no water-insoluble conductive carbon material is present, and sufficient charge is obtained.
- 100 parts by mass of composite Y (or composite Y ′ when the above-described process (II) is further mixed while applying the compressive force and shearing force) On the other hand, it is preferably 1.0 to 55.0 parts by mass, more preferably 1.0 to 40.0 parts by mass, and still more preferably 1.0 to 30.0 parts by mass.
- step (III) it is preferable to add water together with the water-soluble carbon material from the viewpoint of favorably supporting the carbon obtained by carbonizing the water-soluble carbon material on the oxide surface.
- the amount of water added is preferably 30 to 300 parts by mass, more preferably 50 to 250 parts by mass, and even more preferably 75 to 200 parts by mass with respect to 100 parts by mass of the complex Y (or complex Y ′). Part.
- the water-soluble carbon material is supplementarily added in step (II) with this water, the supplementally added water-soluble carbon material supported on the composite Y (or composite Y ′) is dissolved, The same action as the water-soluble carbon material added in (III) can be exhibited.
- the wet mixing means in step (III) is not particularly limited, and can be performed by a conventional method.
- the temperature at the time of mixing after adding the water-soluble carbon material to the composite Y (or the composite Y ′) is preferably 5 to 80 ° C., more preferably 7 to 70 ° C.
- the resulting mixture is preferably dried before firing. Examples of the drying means include spray drying, vacuum drying, freeze drying and the like.
- step (III) the mixture obtained by the wet mixing is fired. Firing is preferably performed in a reducing atmosphere or an inert atmosphere.
- the firing temperature is preferably 500 to 800 ° C., more preferably 600 from the viewpoint of improving the conductivity by improving the crystallinity of the water-insoluble conductive carbon material and from the viewpoint of more effectively carbonizing the water-soluble carbon material. It is ⁇ 770 ° C., more preferably 650 to 750 ° C.
- the firing time is preferably 10 minutes to 3 hours, more preferably 30 minutes to 1.5 hours.
- the positive electrode active material for a secondary battery according to the present invention has the water-insoluble conductive carbon material and the carbon obtained by carbonizing the water-soluble carbon material both supported on the oxide and acting synergistically.
- the amount of moisture adsorbed in the positive electrode active material for batteries can be effectively reduced.
- the amount of adsorbed moisture of the positive electrode active material for secondary battery of the present invention is the same for the secondary battery in the case of the positive electrode active material for secondary battery in which the oxide is represented by the formula (A) or (C).
- the positive electrode active material it is preferably 850 ppm or less, more preferably 700 ppm or less, and in the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (B), preferably 2900 ppm or less, and more Preferably it is 2500 ppm or less.
- the amount of adsorbed moisture is such that moisture is adsorbed until equilibrium is reached at a temperature of 20 ° C. and a relative humidity of 50%, the temperature is raised to 150 ° C. and held for 20 minutes, and further raised to a temperature of 250 ° C. Measured as the amount of water volatilized from the start point to the end point, starting from when the temperature rise is resumed from 150 ° C.
- the amount of adsorbed moisture of the positive electrode active material for a secondary battery and the amount of moisture volatilized from the start point to the end point are the same, and the measured value of the volatilized moisture amount is This is the amount of moisture adsorbed on the positive electrode active material for the secondary battery.
- the positive electrode active material for a secondary battery of the present invention hardly adsorbs moisture, the amount of adsorbed moisture can be effectively reduced without requiring strong drying conditions as a production environment, and the resulting lithium In both the ion secondary battery and the sodium ion secondary battery, it is possible to stably exhibit excellent battery characteristics even under various usage environments.
- the tap density of the positive electrode active material for a secondary battery of the present invention is preferably 0.5 to 1.6 g / cm 3 , more preferably 0.8 from the viewpoint of effectively reducing the amount of adsorbed moisture. ⁇ 1.6 g / cm 3 .
- the BET specific surface area of the positive electrode active material for a secondary battery of the present invention is preferably 5 to 21 m 2 / g, more preferably 7 to 20 m 2 / g, from the viewpoint of effectively reducing the amount of adsorbed moisture. It is.
- the secondary battery to which the positive electrode for the secondary battery including the positive electrode active material for the secondary battery of the present invention can be applied is not particularly limited as long as the positive electrode, the negative electrode, the electrolytic solution, and the separator are essential components.
- the material configuration is not particularly limited, and those having a known material configuration can be used.
- a carbon material such as lithium metal, sodium metal, graphite, or amorphous carbon. It is preferable to use an electrode formed of an intercalating material capable of electrochemically inserting and extracting lithium ions or sodium ions, particularly a carbon material.
- the electrolytic solution is obtained by dissolving a supporting salt in an organic solvent.
- the organic solvent is not particularly limited as long as it is an organic solvent that is usually used for an electrolyte solution of a lithium ion secondary battery or a sodium ion secondary battery.
- carbonates, halogenated hydrocarbons, ethers, ketones Nitriles, lactones, oxolane compounds and the like can be used.
- the type of the supporting salt is not particularly limited, but in the case of a lithium ion secondary battery, an inorganic salt selected from LiPF 6 , LiBF 4 , LiClO 4 , LiAsF 6 , a derivative of the inorganic salt, LiSO 3 CF 3 , an organic material selected from LiC (SO 3 CF 3 ) 2 , LiN (SO 3 CF 3 ) 2 , LiN (SO 2 C 2 F 5 ) 2 and LiN (SO 2 CF 3 ) (SO 2 C 4 F 9 ) It is preferably at least one of a salt and a derivative of the organic salt.
- an inorganic salt selected from NaPF 6 , NaBF 4 , NaClO 4 and NaAsF 6 a derivative of the inorganic salt, NaSO 3 CF 3 , NaC (SO 3 CF 3 ) 2 and NaN (SO 3 CF 3 ) 2 , NaN (SO 2 C 2 F 5 ) 2, and an organic salt selected from NaN (SO 2 CF 3 ) (SO 2 C 4 F 9 ), and at least one derivative of the organic salt It is preferable.
- the separator plays a role of electrically insulating the positive electrode and the negative electrode and holding the electrolytic solution.
- a porous synthetic resin film particularly a polyolefin polymer (polyethylene, polypropylene) porous film may be used.
- Example 1-1 The slurry water was obtained by mixing 4.9 kg of LiOH.H 2 O and 11.7 kg of water. Next, while maintaining the obtained slurry water at a temperature of 25 ° C. and stirring for 30 minutes at a speed of 400 rpm, 5.09 kg of a 70% phosphoric acid aqueous solution was dropped at 35 mL / min to obtain a mixture A 1 . . The pH of the mixed slurry was 10.0 and contained 0.33 mol of phosphoric acid with respect to 1 mol of lithium hydroxide.
- the resulting mixture A 1 was purged with nitrogen while stirring at a speed of 400 rpm for 30 minutes to complete the reaction with the mixture A 1 (dissolved oxygen concentration 0.5 mg / L). Subsequently, 1.63 kg of FeSO 4 .7H 2 O and 5.60 kg of MnSO 4 .H 2 O are added to 21.7 kg of the mixture A 1, and 0.0468 kg of Na 2 SO 3 is further added, and the speed is 400 rpm. to obtain a mixture a 2 are stirred and mixed at. In this case, the added FeSO 4 ⁇ 7H 2 O and MnSO 4 ⁇ H 2 O molar ratio of (FeSO 4 ⁇ 7H 2 O: MnSO 4 ⁇ H 2 O) is 20: was 80.
- the mixture A 2 was put into a synthesis container installed in a steam heating autoclave. After the addition, the mixture was heated with stirring at 170 ° C. for 1 hour using saturated steam obtained by heating water (dissolved oxygen concentration less than 0.5 mg / L) with a membrane separator. The pressure in the autoclave was 0.8 MPa. The formed crystals were filtered and then washed with water. The washed crystal was vacuum-dried under the conditions of 60 ° C. and 1 Torr to obtain an oxide X 1 (powder, chemical composition represented by the formula (A): LiFe 0.2 Mn 0.8 PO 4 ).
- the obtained oxide X 1 was fractionated, and 4 g of graphite (high-purity graphite powder, manufactured by Nippon Graphite Industry Co., Ltd., BET specific surface area 5 m 2 / g, average particle size 6.1 ⁇ m, in the active material) (Corresponding to 3.8% by mass in terms of carbon atoms) was mixed by a dry method using a ball mill.
- the obtained composite Y 1 was mixed with Nobilta (manufactured by Hosokawa Micron Corporation, NOB130) at 40 m / s (6000 rpm) for 5 minutes to obtain a composite Y 1 ′ (powder).
- Oxide X 2 (powder, represented by formula (A)) was prepared in the same manner as in Example 1-1, except that FeSO 4 ⁇ 7H 2 O was 7.34 kg and MnSO 4 ⁇ H 2 O was 0.7 kg.
- 4 g of graphite (corresponding to 3.8% by mass in terms of carbon atom in the active material) was mixed to obtain composite Y 2 and composite Y 2 ′.
- 0.25 g of glucose (corresponding to 1.0% by mass in terms of carbon atom in the active material) is added, and the lithium ion secondary battery in which graphite and carbon derived from glucose are supported is obtained.
- Example 2-1 3.75 L of ultrapure water was mixed with 0.428 kg of LiOH.H 2 O and 1.40 kg of Na 4 SiO 4 .nH 2 O to obtain slurry water. To this slurry water, 0.39 kg of FeSO 4 .7H 2 O, 0.79 kg of MnSO 4 .5H 2 O, and 0.053 kg of Zr (SO 4 ) 2 .4H 2 O were added and mixed. Subsequently, the obtained mixed liquid was put into an autoclave, and a hydrothermal reaction was performed at 150 ° C. for 12 hours. The pressure in the autoclave was 0.4 MPa.
- oxide X 3 (powder, chemical composition represented by formula (B): Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 ).
- 213.9 g of the obtained oxide X 3 was fractionated and mixed with 16.1 g of graphite (corresponding to 7.0% by mass in terms of carbon atom in the active material) by a ball mill in a dry manner.
- the obtained composite Y 3 was mixed with Nobilta (manufactured by Hosokawa Micron Corporation, NOB130) at 40 m / s (6000 rpm) for 5 minutes to obtain a composite Y 3 ′ (powder).
- 5 g of the obtained complex Y 3 ′ was fractionated, and 0.125 g of glucose (corresponding to 1.0% by mass in terms of carbon atom in the active material) and 10 mL of water were added to this, and mixed to 80 ° C.
- lithium ion secondary battery Li 2 Fe
- SiO 4 positive electrode active material for lithium ion secondary battery
- Example 2-2 A lithium ion secondary battery was produced in the same manner as in Example 2-1, except that the amount of glucose added to the complex Y 3 ′ was 0.25 g (corresponding to 2.0 mass% in terms of carbon atom in the active material).
- Example 3-1 A solution was obtained by mixing 0.60 kg of NaOH and 9.0 L of water. Next, the obtained solution is stirred for 5 minutes while maintaining the temperature at 25 ° C., and 0.577 kg of 85% phosphoric acid aqueous solution is dropped at 35 mL / min, followed by stirring at a speed of 400 rpm for 12 hours. Thus, a slurry containing the mixture A 4 was obtained. Such a slurry contained 3.00 moles of sodium per mole of phosphorus. The obtained slurry was purged with nitrogen gas to adjust the dissolved oxygen concentration to 0.5 mg / L, then 0.139 kg of FeSO 4 .7H 2 O, 0.964 kg of MnSO 4 .5H 2 O, MgSO 4.
- 153.6 g of the obtained oxide X 4 was fractionated and mixed with 6.4 g of graphite (corresponding to 4% by mass in terms of carbon atom in the active material) by a dry method using a ball mill.
- the obtained composite Y 4 was mixed with Nobilta (manufactured by Hosokawa Micron Corporation, NOB130) at 40 m / s (6000 rpm) for 5 minutes to obtain a composite Y 4 ′ (powder).
- 5 g of the obtained complex Y 4 ′ was fractionated, and 0.125 g of glucose (corresponding to 1.0% by mass in terms of carbon atom in the active material) and 10 mL of water were added to this, and mixed to 80 ° C.
- Example 3-4 A sodium ion secondary battery was prepared in the same manner as in Example 3-1, except that the glucose added to the complex Y 4 ′ was 0.92 g (corresponding to 6.8% by mass in terms of carbon atoms in the active material).
- each positive electrode active material obtained in Examples 1-1 to 3-4 and Comparative Examples 1-1 to 3-1 was measured according to the following method.
- the amount of water volatilized in the water was measured with a Karl Fischer moisture meter (MKC-610, manufactured by Kyoto Electronics Industry Co., Ltd.) and determined as the amount of water adsorbed on the positive electrode active material. The results are shown in Table 1.
- LiPF 6 in the case of a lithium ion secondary battery
- NaPF 6 in the case of a sodium ion secondary battery
- a known one such as a polymer porous film such as polypropylene was used.
- These battery components were assembled and housed in a conventional manner in an atmosphere having a dew point of ⁇ 50 ° C. or lower to produce a coin-type secondary battery (CR-2032).
- the charging condition is a constant current and constant voltage charge with a current of 1 CA (330 mA / g) and a voltage of 4.5 V
- the discharge condition is 1 CA (330 mA / g)
- a constant current discharge with a final voltage of 1.5 V.
- the discharge capacity at 1 CA was obtained.
- the charging conditions are a constant current and constant voltage charging with a current of 1 CA (154 mA / g) and a voltage of 4.5 V
- the discharging conditions are a constant current discharge of 1 CA (154 mA / g) and a final voltage of 2.0 V.
- the positive electrode active material of the example can surely reduce the amount of adsorbed moisture as compared with the positive electrode active material of the comparative example, and can also exhibit excellent performance in the obtained battery.
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Abstract
Description
例えば、特許文献4には、マリサイト型NaMnPO4を用いたナトリウム二次電池用活物質が開示されており、また特許文献5には、オリビン型構造を有するリン酸遷移金属ナトリウムを含む正極活物質が開示されており、いずれの文献においても高性能なナトリウムイオン二次電池が得られることを示している。 On the other hand, since lithium is a rare valuable material, various studies have been made on sodium ion secondary batteries using sodium instead of lithium ion secondary batteries.
For example, Patent Document 4 discloses a sodium secondary battery active material using marisite-type NaMnPO 4 , and Patent Document 5 discloses a positive electrode active material containing transition metal sodium phosphate having an olivine structure. Substances are disclosed, and any literature shows that a high-performance sodium ion secondary battery can be obtained.
LiFeaMnbMcPO4・・・(A)
(式(A)中、MはMg、Ca、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。a、b及びcは、0≦a≦1、0≦b≦1、0≦c≦0.2、及び2a+2b+(Mの価数)×c=2を満たし、かつa+b≠0を満たす数を示す。)
Li2FedMneNfSiO4・・・(B)
(式(B)中、NはNi、Co、Al、Zn、V又はZrを示す。d、e及びfは、0≦d≦1、0≦e≦1、及び0≦f<1、2d+2e+(Nの価数)×f=2を満たし、かつd+e≠0を満たす数を示す。)
NaFegMnhQiPO4・・・(C)
(式(C)中、QはMg、Ca、Co、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。g、h及びiは、0≦g≦1、0≦h≦1、0≦i<1、及び2g+2h+(Qの価数)×i=2を満たし、かつg+h≠0を満たす数を示す。)
で表される酸化物に、水不溶性導電性炭素材料と、水溶性炭素材料が炭化されてなる炭素とが担持されてなる二次電池用正極活物質を提供するものである。 That is, the present invention includes at least the following formula (A), (B) or (C) containing iron or manganese:
LiFe a Mn b M c PO 4 (A)
(In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. A, b, and c are 0 ≦ a ≦ 1, 0 ≦ b ≦ 1, 0 ≦ c ≦ 0.2, and 2a + 2b + (M valence) × c = 2 and a number satisfying a + b ≠ 0 are shown.)
Li 2 Fe d Mn e N f SiO 4 (B)
(In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr. D, e, and f are 0 ≦ d ≦ 1, 0 ≦ e ≦ 1, and 0 ≦ f <1, 2d + 2e +. (The valence of N) × f = 2 is satisfied, and d + e ≠ 0 is satisfied.)
NaFe g Mn h Q i PO 4 (C)
(In the formula (C), Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. G, h, and i are 0 ≦ g ≦. 1, 0 ≦ h ≦ 1, 0 ≦ i <1, and 2g + 2h + (valence of Q) × i = 2 and a number satisfying g + h ≠ 0 are shown.)
A positive electrode active material for a secondary battery is provided in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by:
LiFeaMnbMcPO4・・・(A)
(式(A)中、MはMg、Ca、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。a、b及びcは、0≦a≦1、0≦b≦1、0≦c≦0.2、及び2a+2b+(Mの価数)×c=2を満たし、かつa+b≠0を満たす数を示す。)
Li2FedMneNfSiO4・・・(B)
(式(B)中、NはNi、Co、Al、Zn、V又はZrを示す。d、e及びfは、0≦d≦1、0≦e≦1、及び0≦f<1、2d+2e+(Nの価数)×f=2を満たし、かつd+e≠0を満たす数を示す。)
NaFegMnhQiPO4・・・(C)
(式(C)中、QはMg、Ca、Co、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。を示す。g、h及びiは、0≦g≦1、0≦h≦1、0≦i<1、及び2g+2h+(Qの価数)×i=2を満たし、かつg+h≠0を満たす数を示す。)
で表される酸化物に、水不溶性導電性炭素材料と、水溶性炭素材料が炭化されてなる炭素とが担持されてなる二次電池用正極活物質の製造方法であって、
リチウム化合物又はナトリウム化合物、リン酸化合物又はケイ酸化合物、並びに少なくとも鉄化合物又はマンガン化合物を含む金属塩を含有するスラリー水を水熱反応に付して酸化物Xを得る工程(I)、
得られた酸化物Xに水不溶性導電性炭素材料を添加して乾式混合して複合体Yを得る工程(II)、並びに
得られた複合体Yに水溶性炭素材料を添加して湿式混合し、焼成する工程(III)を備える、二次電池用正極活物質の製造方法を提供するものである。 Further, the present invention provides the following formula (A), (B) or (C) containing at least iron or manganese:
LiFe a Mn b M c PO 4 (A)
(In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. A, b, and c are 0 ≦ a ≦ 1, 0 ≦ b ≦ 1, 0 ≦ c ≦ 0.2, and 2a + 2b + (M valence) × c = 2 and a number satisfying a + b ≠ 0 are shown.)
Li 2 Fe d Mn e N f SiO 4 (B)
(In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr. D, e, and f are 0 ≦ d ≦ 1, 0 ≦ e ≦ 1, and 0 ≦ f <1, 2d + 2e +. (The valence of N) × f = 2 is satisfied, and d + e ≠ 0 is satisfied.)
NaFe g Mn h Q i PO 4 (C)
(In the formula (C), Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. G, h, and i are 0. ≦ g ≦ 1, 0 ≦ h ≦ 1, 0 ≦ i <1, and 2g + 2h + (Q valence) × i = 2 and a number satisfying g + h ≠ 0 are shown.
A method for producing a positive electrode active material for a secondary battery in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by:
A step (I) of obtaining an oxide X by subjecting a slurry water containing a lithium compound or sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction;
Step (II) in which a water-insoluble conductive carbon material is added to the obtained oxide X and dry-mixed to obtain a composite Y, and a water-soluble carbon material is added to the obtained composite Y and wet-mixed. The manufacturing method of the positive electrode active material for secondary batteries provided with the process (III) to bake is provided.
本発明で用いる酸化物は、少なくとも鉄又はマンガンを含み、かつ下記式(A)、(B)又は(C):
LiFeaMnbMcPO4・・・(A)
(式(A)中、MはMg、Ca、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。a、b及びcは、0≦a≦1、0≦b≦1、0≦c≦0.2、及び2a+2b+(Mの価数)×c=2を満たし、かつa+b≠0を満たす数を示す。)
Li2FedMneNfSiO4・・・(B)
(式(B)中、NはNi、Co、Al、Zn、V又はZrを示す。d、e及びfは、0≦d≦1、0≦e≦1、0≦f<1、及び2d+2e+(Nの価数)×f=2を満たし、かつd+e≠0を満たす数を示す。)
NaFegMnhQiPO4・・・(C)
(式(C)中、QはMg、Ca、Co、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。g、h及びiは、0≦g≦1、0≦h≦1、0≦i<1、及び2g+2h+(Qの価数)×i=2を満たし、かつg+h≠0を満たす数を示す。)
のいずれかの式で表される。
これらの酸化物は、いずれもオリビン型構造を有しており、少なくとも鉄又はマンガンを含む。上記式(A)又は式(B)で表される酸化物を用いた場合には、リチウムイオン電池用正極活物質が得られ、上記式(C)で表される酸化物を用いた場合には、ナトリウムイオン電池用正極活物質が得られる。 Hereinafter, the present invention will be described in detail.
The oxide used in the present invention contains at least iron or manganese and has the following formula (A), (B) or (C):
LiFe a Mn b M c PO 4 (A)
(In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. A, b, and c are 0 ≦ a ≦ 1, 0 ≦ b ≦ 1, 0 ≦ c ≦ 0.2, and 2a + 2b + (M valence) × c = 2 and a number satisfying a + b ≠ 0 are shown.)
Li 2 Fe d Mn e N f SiO 4 (B)
(In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr. D, e, and f are 0 ≦ d ≦ 1, 0 ≦ e ≦ 1, 0 ≦ f <1, and 2d + 2e +. (The valence of N) × f = 2 is satisfied, and d + e ≠ 0 is satisfied.)
NaFe g Mn h Q i PO 4 (C)
(In the formula (C), Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. G, h, and i are 0 ≦ g ≦. 1, 0 ≦ h ≦ 1, 0 ≦ i <1, and 2g + 2h + (valence of Q) × i = 2 and a number satisfying g + h ≠ 0 are shown.)
It is expressed by one of the following formulas.
These oxides all have an olivine structure and contain at least iron or manganese. When the oxide represented by the above formula (A) or (B) is used, a positive electrode active material for a lithium ion battery is obtained, and when the oxide represented by the above formula (C) is used. Provides a positive electrode active material for a sodium ion battery.
また、水溶性炭素材料の炭素原子換算量、すなわち水溶性炭素材料が炭化されてなる炭素の担持量は、本発明の二次電池用正極活物質中に、好ましくは0.5~17.0質量%であり、より好ましくは0.5~13.5質量%であり、さらに好ましくは0.5~10.0質量%である。具体的には、水溶性炭素材料の炭素原子換算量は、酸化物が上記式(A)又は(C)で表される二次電池用正極活物質では、好ましくは0.5~10.0質量%であり、より好ましくは0.5~9.0質量%であり、さらに好ましくは0.5~8.0質量%であり、酸化物が上記式(B)で表される二次電池用正極活物質では、好ましくは0.75~17.0質量%であり、より好ましくは0.75~13.5質量%であり、さらに好ましくは0.75~10.0質量%である。
なお、二次電池用正極活物質中に存在する水不溶性導電性炭素材料と水溶性炭素材料の炭素原子換算量の合計量は、炭素・硫黄分析装置を用いて測定した全炭素量として、確認することができる。また、水溶性炭素材料の炭素原子換算量は、炭素・硫黄分析装置を用いて測定した上記合計の炭素量から、水不溶性導電性炭素材料の添加量を差し引くことにより、確認することができる。 The carbon atom equivalent of the water-insoluble conductive carbon material and the water-soluble carbon material is the positive electrode for the secondary battery of the present invention as the carbon in which the water-insoluble conductive carbon material and the carbonized water-soluble carbon material are supported on the oxide. It will coexist in the active material. The carbon atom equivalent amount of the water-insoluble conductive carbon material and the water-soluble carbon material corresponds to the total supported amount of carbon obtained by carbonizing the water-insoluble conductive carbon material and the water-soluble carbon material. The total amount in the positive electrode active material for batteries is preferably 1.0 to 20.0% by mass, more preferably 2.0 to 17.5% by mass, and still more preferably 3.0 to 15.0%. % By mass. Specifically, the carbon atom equivalent amount of the water-insoluble conductive carbon material and the water-soluble carbon material is preferably the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C). 1.0 to 15.0 mass%, more preferably 2.0 to 13.5 mass%, still more preferably 3.0 to 12.0 mass%, and the oxide is represented by the above formula (B). Is preferably 2.0 to 20.0% by mass, more preferably 3.0 to 17.5% by mass, and still more preferably 4.0 to 15%. 0.0% by mass.
Further, the carbon atom equivalent amount of the water-soluble carbon material, that is, the supported amount of carbon obtained by carbonizing the water-soluble carbon material is preferably 0.5 to 17.0 in the positive electrode active material for secondary battery of the present invention. % By mass, more preferably 0.5 to 13.5% by mass, and still more preferably 0.5 to 10.0% by mass. Specifically, the carbon atom equivalent amount of the water-soluble carbon material is preferably 0.5 to 10.0 for the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C). A secondary battery in which the oxide is represented by the above formula (B), preferably 0.5 to 9.0 mass%, more preferably 0.5 to 8.0 mass%. In the positive electrode active material for use, it is preferably 0.75 to 17.0% by mass, more preferably 0.75 to 13.5% by mass, and further preferably 0.75 to 10.0% by mass.
The total amount of carbon-atom equivalents of the water-insoluble conductive carbon material and the water-soluble carbon material present in the positive electrode active material for secondary batteries is confirmed as the total carbon amount measured using a carbon / sulfur analyzer. can do. Further, the carbon atom equivalent amount of the water-soluble carbon material can be confirmed by subtracting the addition amount of the water-insoluble conductive carbon material from the total carbon amount measured using a carbon / sulfur analyzer.
得られた酸化物Xに水不溶性導電性炭素材料を添加して乾式混合して複合体Yを得る工程(II)、並びに
得られた複合体Yに水溶性炭素材料を添加して湿式混合し、焼成する工程(III)を備える製造方法により得られるものであるのが好ましい。 More specifically, the positive electrode active material for a secondary battery of the present invention is a slurry water containing a lithium compound or a sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound. A step (I) of obtaining an oxide X by subjecting to a thermal reaction;
Step (II) in which a water-insoluble conductive carbon material is added to the obtained oxide X and dry-mixed to obtain a composite Y, and a water-soluble carbon material is added to the obtained composite Y and wet-mixed. It is preferably obtained by a production method comprising the step (III) of firing.
用い得るリチウム化合物又はナトリウム化合物としては、水酸化物(例えばLiOH・H2O、NaOH)、炭酸化物、硫酸化物、酢酸化物が挙げられる。なかでも、水酸化物が好ましい。
スラリー水におけるリチウム化合物又はケイ酸化合物の含有量は、水100質量部に対し、好ましくは5~50質量部であり、より好ましくは7~45質量部である。より具体的には、工程(I)においてリン酸化合物を用いた場合、スラリー水におけるリチウム化合物又はナトリウム化合物の含有量は、水100質量部に対し、好ましくは5~50質量部であり、より好ましくは10~45質量部である。また、ケイ酸化合物を用いた場合、スラリー水におけるケイ酸化合物の含有量は、水100質量部に対し、好ましくは5~40質量部であり、より好ましくは7~35質量部である。 Step (I) is a step of obtaining an oxide X by subjecting a slurry water containing a lithium compound or sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction. It is.
Examples of the lithium compound or sodium compound that can be used include hydroxides (for example, LiOH.H 2 O, NaOH), carbonates, sulfates, and acetates. Of these, hydroxide is preferable.
The content of the lithium compound or silicic acid compound in the slurry water is preferably 5 to 50 parts by mass, more preferably 7 to 45 parts by mass with respect to 100 parts by mass of water. More specifically, when a phosphoric acid compound is used in step (I), the content of the lithium compound or sodium compound in the slurry water is preferably 5 to 50 parts by mass with respect to 100 parts by mass of water. The amount is preferably 10 to 45 parts by mass. When a silicate compound is used, the content of the silicate compound in the slurry water is preferably 5 to 40 parts by mass, more preferably 7 to 35 parts by mass with respect to 100 parts by mass of water.
なお、混合物A1を撹拌する際、さらに混合物A1の沸点温度以下に冷却するのが好ましい。具体的には、80℃以下に冷却するのが好ましく、20~60℃に冷却するのがより好ましい。 The dropping rate of phosphoric acid into the mixture A 1 is preferably 15 to 50 mL / min, more preferably 20 to 45 mL / min, and further preferably 28 to 40 mL / min. The stirring time of the mixture A 1 while dropping phosphoric acid is preferably 0.5 to 24 hours, more preferably 3 to 12 hours. Further, the stirring speed of the mixture A 1 while dropping phosphoric acid is preferably 200 to 700 rpm, more preferably 250 to 600 rpm, and further preferably 300 to 500 rpm.
Note that when the mixture is stirred for A 1, preferred to further cool the mixture A in the following 1 the boiling point temperature. Specifically, cooling to 80 ° C. or lower is preferable, and cooling to 20 to 60 ° C. is more preferable.
また、窒素をパージする際、反応を良好に進行させる観点から、リン酸化合物又はケイ酸化合物を混合した後の混合物A2を撹拌するのが好ましい。このときの撹拌速度は、好ましくは200~700rpmであり、より好ましくは250~600rpmである。 The pressure for purging nitrogen is preferably 0.1 to 0.2 MPa, more preferably 0.1 to 0.15 MPa. The temperature of the mixture A 2 after mixing the phosphoric acid compound or the silicic acid compound is preferably 20 to 80 ° C., more preferably 20 to 60 ° C. For example, in the case of the oxide represented by the above formula (A), the reaction time is preferably 5 to 60 minutes, more preferably 15 to 45 minutes.
Further, when the purging nitrogen from the viewpoint of advancing satisfactorily reaction, it is preferred to stir the mixture A 2 after mixing the phosphoric acid compound or a silicic acid compound. The stirring speed at this time is preferably 200 to 700 rpm, more preferably 250 to 600 rpm.
これら金属(M、N又はQ)塩を用いる場合、鉄化合物、マンガン化合物、及び金属(M、N又はQ)塩の合計添加量は、上記工程(I)において得られた混合物中のリン酸又はケイ酸1モルに対し、好ましくは0.99~1.01モルであり、より好ましくは0.995~1.005モルである。 Furthermore, you may use metal (M, N, or Q) salts other than an iron compound and a manganese compound as a metal salt as needed. M, N, and Q in the metal (M, N, or Q) salt have the same meanings as M, N, and Q in the above formulas (A) to (C), and as the metal salt, sulfate, halogen compound, organic Acid salts and hydrates thereof can be used. These may be used alone or in combination of two or more. Among them, it is more preferable to use a sulfate from the viewpoint of improving battery physical properties.
When these metal (M, N, or Q) salts are used, the total amount of iron compound, manganese compound, and metal (M, N, or Q) salt added is phosphoric acid in the mixture obtained in the above step (I). Alternatively, the amount is preferably 0.99 to 1.01 mole, more preferably 0.995 to 1.005 mole relative to 1 mole of silicic acid.
得られた酸化物Xは、上記式(A)~(C)で表される酸化物であり、ろ過後、水で洗浄し、乾燥することによりこれを単離できる。なお、乾燥手段は、凍結乾燥、真空乾燥が用いられる。 The hydrothermal reaction in the step (I) or (Ib) may be 100 ° C. or higher, and preferably 130 to 180 ° C. The hydrothermal reaction is preferably carried out in a pressure-resistant vessel. When the reaction is carried out at 130 to 180 ° C., the pressure at this time is preferably 0.3 to 0.9 MPa, and the reaction is carried out at 140 to 160 ° C. The pressure is preferably 0.3 to 0.6 MPa. The hydrothermal reaction time is preferably 0.1 to 48 hours, more preferably 0.2 to 24 hours.
The obtained oxide X is an oxide represented by the above formulas (A) to (C), which can be isolated by filtration, washing with water, and drying. As the drying means, freeze drying or vacuum drying is used.
また、かかる工程(II)において、水不溶性導電性炭素材料と水溶性炭素材料を併用する場合、水不溶性導電性炭素材料の添加量と水溶性炭素材料の添加量の炭素原子換算量との質量比(水不溶性導電性炭素材料:水溶性炭素材料)は、好ましくは100:2~3:100であり、より好ましくは100:10~10:100である。 Step (II) is a step of adding the water-insoluble conductive carbon material to the oxide X obtained in step (I) and then dry mixing to obtain the composite Y. In addition to the water-insoluble conductive carbon material, a water-soluble carbon material may be further supplementarily added. In this case, the order of addition is not particularly limited. The amount of the water-insoluble conductive carbon material added is preferably 0.5 to 24.2 parts by mass, more preferably 1.5 to 20.5 parts by mass with respect to 100 parts by mass of the oxide X, for example. The amount is preferably 2.6 to 17.0 parts by mass. Specifically, the addition amount of the water-insoluble conductive carbon material is preferably 0.5 to 17.0 in the case of the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (A) or (C). Secondary battery in which the oxide is represented by the above formula (B), more preferably 1.5 to 14.9 parts by mass, and still more preferably 2.6 to 13.0 parts by mass. The positive electrode active material for use is preferably 1.3 to 23.8 parts by mass, more preferably 2.3 to 20.1 parts by mass, and still more preferably 3.4 to 16.6 parts by mass.
In addition, in the step (II), when the water-insoluble conductive carbon material and the water-soluble carbon material are used in combination, the mass of the addition amount of the water-insoluble conductive carbon material and the carbon atom equivalent amount of the addition amount of the water-soluble carbon material The ratio (water-insoluble conductive carbon material: water-soluble carbon material) is preferably 100: 2 to 3: 100, more preferably 100: 10 to 10: 100.
なお、インペラの周速度とは、回転式攪拌翼(インペラ)の最外端部の速度を意味し、下記式(1)により表すことができ、また圧縮力及びせん断力を付加しながら混合する処理を行う時間は、インペラの周速度が遅いほど長くなるように、インペラの周速度によっても変動し得る。
インペラの周速度(m/s)=
インペラの半径(m)×2×π×回転数(rpm)÷60・・・(1) The dry mixing in the step (II) is preferably mixing by a normal ball mill, and more preferably by a planetary ball mill capable of revolving. Further, the water-insoluble conductive carbon material and the water-soluble carbon material used in combination as necessary are densely and uniformly dispersed on the oxide surface represented by the above formulas (A) to (C) and carbonized. From the viewpoint of effectively supporting the carbon, it is more preferable to mix the composite Y while applying a compressive force and a shearing force to obtain a composite Y ′. The process of mixing while applying a compressive force and a shearing force is preferably performed in a closed container equipped with an impeller. The peripheral speed of the impeller is preferably 25 to 40 m / s, more preferably 27 from the viewpoint of increasing the tap density of the obtained positive electrode active material and reducing the BET specific surface area to effectively reduce the amount of adsorbed water. ~ 40 m / s. The mixing time is preferably 5 to 90 minutes, more preferably 10 to 80 minutes.
The peripheral speed of the impeller means the speed of the outermost end of the rotary stirring blade (impeller), which can be expressed by the following formula (1), and is mixed while applying compressive force and shearing force. The processing time may vary depending on the peripheral speed of the impeller so that it becomes longer as the peripheral speed of the impeller is slower.
Impeller peripheral speed (m / s) =
Impeller radius (m) × 2 × π × rotational speed (rpm) ÷ 60 (1)
例えば、上記混合する処理を、周速度25~40m/sで回転するインペラを備える密閉容器内で6~90分間行う場合、容器に投入する複合体Yの量は、有効容器(インペラを備える密閉容器のうち、複合体Yを収容可能な部位に相当する容器)1cm3当たり、好ましくは0.1~0.7gであり、より好ましくは0.15~0.4gである。 In the step (II), the processing time and / or the impeller peripheral speed when performing the mixing process while applying the compressive force and the shearing force need to be appropriately adjusted according to the amount of the composite Y to be charged into the container. There is. By operating the container, it is possible to perform a process of mixing the mixture while applying a compressive force and a shearing force between the impeller and the inner wall of the container, and the above formulas (A) to (C The water-insoluble conductive carbon material and the water-soluble carbon material to be used in combination as needed are densely and uniformly dispersed on the oxide surface represented by Combined with the added water-soluble carbon material, a positive electrode active material for a secondary battery that can effectively reduce the amount of adsorbed water can be obtained.
For example, when the mixing process is performed for 6 to 90 minutes in an airtight container equipped with an impeller rotating at a peripheral speed of 25 to 40 m / s, the amount of the composite Y charged into the container is an effective container (airtight equipped with an impeller). Of the containers, a container corresponding to a part capable of accommodating the complex Y) is preferably 0.1 to 0.7 g, more preferably 0.15 to 0.4 g per 1 cm 3 .
上記混合の処理条件としては、処理温度が、好ましくは5~80℃、より好ましくは10~50℃である。処理雰囲気としては、特に限定されないが、不活性ガス雰囲気下、又は還元ガス雰囲気下が好ましい。 Examples of the apparatus equipped with a closed container that can easily perform mixing while applying compressive force and shear force include a high-speed shear mill, a blade-type kneader, and the like. Fine particle composite apparatus Nobilta (manufactured by Hosokawa Micron Corporation) can be suitably used.
As the mixing treatment conditions, the treatment temperature is preferably 5 to 80 ° C., more preferably 10 to 50 ° C. The treatment atmosphere is not particularly limited, but is preferably an inert gas atmosphere or a reducing gas atmosphere.
このように、本発明の二次電池用正極活物質は、水分を吸着しにくいため、製造環境として強い乾燥条件を必要とすることなく吸着水分量を有効に低減することができ、得られるリチウムイオン二次電池及びナトリウムイオン二次電池の双方において、様々な使用環境下でも優れた電池特性を安定して発現することが可能となる。
なお、温度20℃及び相対湿度50%にて平衡に達するまで水分を吸着させ、温度150℃まで昇温して20分間保持した後、さらに温度250℃まで昇温して20分間保持したときの、150℃から昇温を再開するときを始点、及び250℃での恒温状態を終えたときを終点とする、始点から終点までの間に揮発した水分量は、例えばカールフィッシャー水分計を用いて測定することができる。 The positive electrode active material for a secondary battery according to the present invention has the water-insoluble conductive carbon material and the carbon obtained by carbonizing the water-soluble carbon material both supported on the oxide and acting synergistically. The amount of moisture adsorbed in the positive electrode active material for batteries can be effectively reduced. Specifically, the amount of adsorbed moisture of the positive electrode active material for secondary battery of the present invention is the same for the secondary battery in the case of the positive electrode active material for secondary battery in which the oxide is represented by the formula (A) or (C). In the positive electrode active material, it is preferably 850 ppm or less, more preferably 700 ppm or less, and in the positive electrode active material for a secondary battery in which the oxide is represented by the above formula (B), preferably 2900 ppm or less, and more Preferably it is 2500 ppm or less. The amount of adsorbed moisture is such that moisture is adsorbed until equilibrium is reached at a temperature of 20 ° C. and a relative humidity of 50%, the temperature is raised to 150 ° C. and held for 20 minutes, and further raised to a temperature of 250 ° C. Measured as the amount of water volatilized from the start point to the end point, starting from when the temperature rise is resumed from 150 ° C. when held for 20 minutes and ending at the constant temperature state at 250 ° C. It is assumed that the amount of adsorbed moisture of the positive electrode active material for a secondary battery and the amount of moisture volatilized from the start point to the end point are the same, and the measured value of the volatilized moisture amount is This is the amount of moisture adsorbed on the positive electrode active material for the secondary battery.
Thus, since the positive electrode active material for a secondary battery of the present invention hardly adsorbs moisture, the amount of adsorbed moisture can be effectively reduced without requiring strong drying conditions as a production environment, and the resulting lithium In both the ion secondary battery and the sodium ion secondary battery, it is possible to stably exhibit excellent battery characteristics even under various usage environments.
When water is adsorbed until equilibrium is reached at a temperature of 20 ° C. and a relative humidity of 50%, the temperature is raised to 150 ° C. and held for 20 minutes, and further raised to a temperature of 250 ° C. and held for 20 minutes. The amount of water volatilized between the start point and the end point, starting from when the temperature rise is resumed from 150 ° C. and the end point when the constant temperature state at 250 ° C. is completed, is measured using, for example, a Karl Fischer moisture meter Can be measured.
LiOH・H2O 4.9kg、及び水 11.7kgを混合してスラリー水を得た。次いで、得られたスラリー水を25℃の温度に保持しながら速度400rpmにて30分間撹拌しつつ、70%のリン酸水溶液 5.09kgを35mL/minで滴下して、混合物A1を得た。かかる混合スラリー液のpHは10.0であり、水酸化リチウム1モルに対し、0.33モルのリン酸を含有していた。 [Example 1-1]
The slurry water was obtained by mixing 4.9 kg of LiOH.H 2 O and 11.7 kg of water. Next, while maintaining the obtained slurry water at a temperature of 25 ° C. and stirring for 30 minutes at a speed of 400 rpm, 5.09 kg of a 70% phosphoric acid aqueous solution was dropped at 35 mL / min to obtain a mixture A 1 . . The pH of the mixed slurry was 10.0 and contained 0.33 mol of phosphoric acid with respect to 1 mol of lithium hydroxide.
次いで、混合物A2を蒸気加熱式オートクレーブ内に設置した合成容器に投入した。投入後、隔膜分離装置により水(溶存酸素濃度0.5mg/L未満)を加熱して得た飽和蒸気を用いて、170℃で1時間攪拌しながら加熱した。オートクレーブ内の圧力は、0.8MPaであった。生成した結晶をろ過し、次いで水により洗浄した。洗浄した結晶を60℃、1Torrの条件で真空乾燥し、酸化物X1(粉末、式(A)で表される化学組成:LiFe0.2Mn0.8PO4)を得た。 Next, the resulting mixture A 1 was purged with nitrogen while stirring at a speed of 400 rpm for 30 minutes to complete the reaction with the mixture A 1 (dissolved oxygen concentration 0.5 mg / L). Subsequently, 1.63 kg of FeSO 4 .7H 2 O and 5.60 kg of MnSO 4 .H 2 O are added to 21.7 kg of the mixture A 1, and 0.0468 kg of Na 2 SO 3 is further added, and the speed is 400 rpm. to obtain a mixture a 2 are stirred and mixed at. In this case, the added FeSO 4 · 7H 2 O and MnSO 4 · H 2 O molar ratio of (FeSO 4 · 7H 2 O: MnSO 4 · H 2 O) is 20: was 80.
Next, the mixture A 2 was put into a synthesis container installed in a steam heating autoclave. After the addition, the mixture was heated with stirring at 170 ° C. for 1 hour using saturated steam obtained by heating water (dissolved oxygen concentration less than 0.5 mg / L) with a membrane separator. The pressure in the autoclave was 0.8 MPa. The formed crystals were filtered and then washed with water. The washed crystal was vacuum-dried under the conditions of 60 ° C. and 1 Torr to obtain an oxide X 1 (powder, chemical composition represented by the formula (A): LiFe 0.2 Mn 0.8 PO 4 ).
複合体Y1’に添加するグルコースを0.5g(活物質中における炭素原子換算量で2.0質量%に相当)とした以外、実施例1-1と同様の方法でリチウムイオン二次電池用正極活物質(LiFe0.2Mn0.8PO4、炭素の量=5.8質量%)を得た。 [Example 1-2]
A lithium ion secondary battery was produced in the same manner as in Example 1-1 except that 0.5 g of glucose added to the complex Y 1 ′ (corresponding to 2.0 mass% in terms of carbon atom in the active material) was used. A positive electrode active material (LiFe 0.2 Mn 0.8 PO 4 , amount of carbon = 5.8 mass%) was obtained.
複合体Y1’に添加するグルコースを0.75g(活物質中における炭素原子換算量で2.9質量%に相当)とした以外、実施例1-1と同様の方法でリチウムイオン二次電池用正極活物質(LiFe0.2Mn0.8PO4、炭素の量=6.7質量%)を得た。 [Example 1-3]
A lithium ion secondary battery was produced in the same manner as in Example 1-1, except that 0.75 g of glucose added to the complex Y 1 ′ (corresponding to 2.9% by mass in terms of carbon atom in the active material) was used. A positive electrode active material (LiFe 0.2 Mn 0.8 PO 4 , amount of carbon = 6.7% by mass) was obtained.
複合体Y1’に添加するグルコースを1.25g(活物質中における炭素原子換算量で4.8質量%に相当)とした以外、実施例1-1と同様の方法でリチウムイオン二次電池用正極活物質(LiFe0.2Mn0.8PO4、炭素の量=8.6質量%)を得た。 [Example 1-4]
A lithium ion secondary battery was prepared in the same manner as in Example 1-1, except that 1.25 g of glucose added to the complex Y 1 ′ (corresponding to 4.8% by mass in terms of carbon atom in the active material) was used. A positive electrode active material (LiFe 0.2 Mn 0.8 PO 4 , amount of carbon = 8.6% by mass) was obtained.
FeSO4・7H2Oを7.34kg、MnSO4・H2Oを0.7kgとした以外、実施例1-1と同様の方法で、酸化物X2(粉末、式(A)で表される化学組成:LiFe0.9Mn0.1PO4)を得た後にグラファイトを4g(活物質中における炭素原子換算量で3.8質量%に相当)を混合して複合体Y2及び複合体Y2’を得て、次いでグルコースを0.25g(活物質中における炭素原子換算量で1.0質量%に相当)添加して、グラファイトとグルコース由来の炭素とが担持してなるリチウムイオン二次電池用正極活物質(LiFe0.9Mn0.1PO4、炭素の量=4.8質量%)を得た。 [Example 1-5]
Oxide X 2 (powder, represented by formula (A)) was prepared in the same manner as in Example 1-1, except that FeSO 4 · 7H 2 O was 7.34 kg and MnSO 4 · H 2 O was 0.7 kg. After obtaining LiFe 0.9 Mn 0.1 PO 4 ), 4 g of graphite (corresponding to 3.8% by mass in terms of carbon atom in the active material) was mixed to obtain composite Y 2 and composite Y 2 ′. Next, 0.25 g of glucose (corresponding to 1.0% by mass in terms of carbon atom in the active material) is added, and the lithium ion secondary battery in which graphite and carbon derived from glucose are supported is obtained. A positive electrode active material (LiFe 0.9 Mn 0.1 PO 4 , amount of carbon = 4.8% by mass) was obtained.
複合体Y2’にグルコースを添加しなかった以外、実施例1-5と同様の方法でリチウムイオン二次電池用正極活物質(LiFe0.9Mn0.1PO4、炭素の量=3.8質量%)を得た。 [Comparative Example 1-1]
A positive electrode active material for a lithium ion secondary battery (LiFe 0.9 Mn 0.1 PO 4 , amount of carbon = 3.8% by mass) in the same manner as in Example 1-5, except that glucose was not added to the complex Y 2 ′. )
LiOH・H2O 0.428kg、Na4SiO4・nH2O 1.40kgに超純水3.75Lを混合してスラリー水を得た。このスラリー水に、FeSO4・7H2O 0.39kg、MnSO4・5H2O 0.79kg、及びZr(SO4)2・4H2O 0.053kgを添加し、混合した。次いで、得られた混合液をオートクレーブに投入し、150℃で12時間水熱反応を行った。オートクレーブの圧力は0.4MPaであった。生成した結晶をろ過し、次いで結晶1質量部に対し、12質量部の水により洗浄した。洗浄した結晶を-50℃で12時間凍結乾燥して酸化物X3(粉末、式(B)で表される化学組成:Li2Fe0.28Mn0.66Zr0.03SiO4)を得た。 [Example 2-1]
3.75 L of ultrapure water was mixed with 0.428 kg of LiOH.H 2 O and 1.40 kg of Na 4 SiO 4 .nH 2 O to obtain slurry water. To this slurry water, 0.39 kg of FeSO 4 .7H 2 O, 0.79 kg of MnSO 4 .5H 2 O, and 0.053 kg of Zr (SO 4 ) 2 .4H 2 O were added and mixed. Subsequently, the obtained mixed liquid was put into an autoclave, and a hydrothermal reaction was performed at 150 ° C. for 12 hours. The pressure in the autoclave was 0.4 MPa. The produced crystal was filtered, and then washed with 12 parts by mass of water with respect to 1 part by mass of the crystal. The washed crystals were freeze-dried at −50 ° C. for 12 hours to obtain oxide X 3 (powder, chemical composition represented by formula (B): Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 ).
複合体Y3’に添加するグルコースを0.25g(活物質中における炭素原子換算量で2.0質量%に相当)とした以外、実施例2-1と同様の方法でリチウムイオン二次電池用正極活物質(Li2Fe0.28Mn0.66Zr0.03SiO4、炭素の量=9.0質量%)を得た。 [Example 2-2]
A lithium ion secondary battery was produced in the same manner as in Example 2-1, except that the amount of glucose added to the complex Y 3 ′ was 0.25 g (corresponding to 2.0 mass% in terms of carbon atom in the active material). A positive electrode active material (Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 , amount of carbon = 9.0% by mass) was obtained.
複合体Y3’に添加するグルコースを0.375g(活物質中における炭素原子換算量で2.9質量%に相当)とした以外、実施例2-1と同様の方法でリチウムイオン二次電池用正極活物質(Li2Fe0.28Mn0.66Zr0.03SiO4、炭素の量=9.9質量%)質を得た。 [Example 2-3]
A lithium ion secondary battery was produced in the same manner as in Example 2-1, except that 0.375 g of glucose added to the complex Y 3 ′ (corresponding to 2.9% by mass in terms of carbon atoms in the active material) was used. A positive electrode active material (Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 , amount of carbon = 9.9% by mass) was obtained.
複合体Y3’に添加するグルコースを0.875g(活物質中における炭素原子換算量で6.8質量%に相当)とした以外、実施例2-1と同様の方法でリチウムイオン二次電池用正極活物質(Li2Fe0.28Mn0.66Zr0.03SiO4、炭素の量=13.8質量%)を得た。 [Example 2-4]
A lithium ion secondary battery was prepared in the same manner as in Example 2-1, except that 0.875 g of glucose added to the complex Y 3 ′ (corresponding to 6.8% by mass in terms of carbon atom in the active material) was used. A positive electrode active material (Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 , amount of carbon = 13.8% by mass) was obtained.
複合体Y3’にグルコースを添加しなかった以外、実施例2-1と同様の方法でリチウムイオン二次電池用正極活物質(Li2Fe0.28Mn0.66Zr0.03SiO4、炭素の量=7.0質量%)を得た。 [Comparative Example 2-1]
A positive electrode active material for lithium ion secondary battery (Li 2 Fe 0.28 Mn 0.66 Zr 0.03 SiO 4 , amount of carbon = 7) in the same manner as in Example 2-1, except that glucose was not added to the composite Y 3 ′. 0.0 mass%) was obtained.
NaOH 0.60kgと水 9.0Lを混合して溶液を得た。次いで、得られた溶液を、25℃の温度に保持しながら5分間撹拌しつつ85%のリン酸水溶液0.577kgを35mL/分で滴下し、続いて12時間、400rpmの速度で撹拌することにより、混合物A4を含有するスラリーを得た。かかるスラリーは、リン1モルに対し、3.00モルのナトリウムを含有していた。得られたスラリーに対し、窒素ガスをパージして溶存酸素濃度を0.5mg/Lに調整した後、FeSO4・7H2O 0.139kg、MnSO4・5H2O 0.964kg、MgSO4・7H2O 0.124kgを添加した。次いで、得られた混合液を窒素ガスでパージしたオートクレーブに投入し、200℃で3時間水熱反応を行った。オートクレーブ内の圧力は、1.4MPaであった。生成した結晶をろ過し、次いで結晶1質量部に対し、12質量部の水により洗浄した。洗浄した結晶を-50℃で12時間凍結乾燥して酸化物X4(粉末、式(C)で表される化学組成:NaFe0.1Mn0.8Mg0.1PO4)を得た。 [Example 3-1]
A solution was obtained by mixing 0.60 kg of NaOH and 9.0 L of water. Next, the obtained solution is stirred for 5 minutes while maintaining the temperature at 25 ° C., and 0.577 kg of 85% phosphoric acid aqueous solution is dropped at 35 mL / min, followed by stirring at a speed of 400 rpm for 12 hours. Thus, a slurry containing the mixture A 4 was obtained. Such a slurry contained 3.00 moles of sodium per mole of phosphorus. The obtained slurry was purged with nitrogen gas to adjust the dissolved oxygen concentration to 0.5 mg / L, then 0.139 kg of FeSO 4 .7H 2 O, 0.964 kg of MnSO 4 .5H 2 O, MgSO 4. 0.124 kg of 7H 2 O was added. Subsequently, the obtained liquid mixture was thrown into the autoclave purged with nitrogen gas, and the hydrothermal reaction was performed at 200 degreeC for 3 hours. The pressure in the autoclave was 1.4 MPa. The produced crystal was filtered, and then washed with 12 parts by mass of water with respect to 1 part by mass of the crystal. The washed crystals were freeze-dried at −50 ° C. for 12 hours to obtain oxide X 4 (powder, chemical composition represented by formula (C): NaFe 0.1 Mn 0.8 Mg 0.1 PO 4 ).
複合体Y4’に添加するグルコースを0.25g(活物質中における炭素原子換算量で2.0質量%に相当)とした以外、実施例3-1と同様の方法でナトリウムイオン二次電池用正極活物質(NaFe0.1Mn0.8Mg0.1PO4、炭素の量=6.0質量%)を得た。 [Example 3-2]
Sodium ion secondary battery in the same manner as in Example 3-1, except that 0.25 g of glucose added to complex Y 4 ′ (corresponding to 2.0% by mass in terms of carbon atom in the active material) was used A positive electrode active material (NaFe 0.1 Mn 0.8 Mg 0.1 PO 4 , amount of carbon = 6.0% by mass) was obtained.
複合体Y4’に添加するグルコースを0.375g(活物質中における炭素原子換算量で2.9質量%に相当)とした以外、実施例3-1と同様の方法でナトリウムイオン二次電池用正極活物質(NaFe0.1Mn0.8Mg0.1PO4、炭素の量=6.9質量%)を得た。 [Example 3-3]
A sodium ion secondary battery was prepared in the same manner as in Example 3-1, except that 0.375 g of glucose added to the complex Y 4 ′ (corresponding to 2.9% by mass in terms of carbon atom in the active material) was used. A positive electrode active material (NaFe 0.1 Mn 0.8 Mg 0.1 PO 4 , amount of carbon = 6.9% by mass) was obtained.
複合体Y4’に添加するグルコースを0.92g(活物質中における炭素原子換算量で6.8質量%に相当)とした以外、実施例3-1と同様の方法でナトリウムイオン二次電池用正極活物質(NaFe0.1Mn0.8Mg0.1PO4、炭素の量=10.8質量%)を得た。 [Example 3-4]
A sodium ion secondary battery was prepared in the same manner as in Example 3-1, except that the glucose added to the complex Y 4 ′ was 0.92 g (corresponding to 6.8% by mass in terms of carbon atoms in the active material). A positive electrode active material (NaFe 0.1 Mn 0.8 Mg 0.1 PO 4 , amount of carbon = 10.8% by mass) was obtained.
複合体Y4’にグルコースを添加しなかった以外、実施例3-1と同様の方法でナトリウムイオン二次電池用正極活物質(NaFe0.1Mn0.8Mg0.1PO4、炭素の量=4.0質量%)を得た。 [Comparative Example 3-1]
A positive electrode active material for sodium ion secondary battery (NaFe 0.1 Mn 0.8 Mg 0.1 PO 4 , amount of carbon = 4.0) in the same manner as in Example 3-1, except that glucose was not added to the complex Y 4 ′. Mass%).
実施例1-1~3-4及び比較例1-1~3-1で得られた各正極活物質の吸着水分量は、下記方法にしたがって測定した。
正極活物質(複合体粒子)について、温度20℃、相対湿度50%の環境に1日間静置して平衡に達するまで水分を吸着させ、温度150℃まで昇温して20分間保持した後、さらに温度250℃まで昇温して20分間保持したときの、150℃から昇温を再開するときを始点とし、及び250℃での恒温状態を終えたときを終点とし、始点から終点までの間に揮発した水分量を、カールフィッシャー水分計(MKC-610、京都電子工業(株)製)で測定し、正極活物質における吸着水分量として求めた。
結果を表1に示す。 <Measurement of adsorbed water content>
The adsorbed moisture content of each positive electrode active material obtained in Examples 1-1 to 3-4 and Comparative Examples 1-1 to 3-1 was measured according to the following method.
About the positive electrode active material (composite particle), after allowing it to stand for 1 day in an environment of a temperature of 20 ° C. and a relative humidity of 50% and adsorbing moisture until reaching equilibrium, raising the temperature to 150 ° C. and holding for 20 minutes, Furthermore, when the temperature is raised to 250 ° C. and held for 20 minutes, the start point is when the temperature rise is resumed from 150 ° C., and the end point is when the constant temperature state at 250 ° C. is completed. The amount of water volatilized in the water was measured with a Karl Fischer moisture meter (MKC-610, manufactured by Kyoto Electronics Industry Co., Ltd.) and determined as the amount of water adsorbed on the positive electrode active material.
The results are shown in Table 1.
実施例1-1~3-4及び比較例1-1~3-1で得られた正極活物質を用い、リチウムイオン二次電池又はナトリウムイオン二次電池の正極を作製した。具体的には、得られた正極活物質、ケッチェンブラック、ポリフッ化ビニリデンを質量比75:20:5の配合割合で混合し、これにN-メチル-2-ピロリドンを加えて充分混練し、正極スラリーを調製した。正極スラリーを厚さ20μmのアルミニウム箔からなる集電体に塗工機を用いて塗布し、80℃で12時間の真空乾燥を行った。
その後、φ14mmの円盤状に打ち抜いてハンドプレスを用いて16MPaで2分間プレスし、正極とした。
次いで、上記の正極を用いてコイン型二次電池を構築した。負極には、φ15mmに打ち抜いたリチウム箔を用いた。電解液には、エチレンカーボネート及びエチルメチルカーボネートを体積比1:1の割合で混合した混合溶媒に、LiPF6(リチウムイオン二次電池の場合)又はNaPF6(ナトリウムイオン二次電池の場合)を1mol/Lの濃度で溶解したものを用いた。セパレータには、ポリプロピレンなどの高分子多孔フィルムなど、公知のものを用いた。これらの電池部品を露点が-50℃以下の雰囲気で常法により組み込み収容し、コイン型二次電池(CR-2032)を製造した。 << Evaluation of charge / discharge characteristics using secondary battery >>
Using the positive electrode active materials obtained in Examples 1-1 to 3-4 and Comparative Examples 1-1 to 3-1, positive electrodes of lithium ion secondary batteries or sodium ion secondary batteries were produced. Specifically, the obtained positive electrode active material, ketjen black, and polyvinylidene fluoride were mixed at a mixing ratio of 75: 20: 5, and N-methyl-2-pyrrolidone was added thereto and kneaded sufficiently. A positive electrode slurry was prepared. The positive electrode slurry was applied to a current collector made of an aluminum foil having a thickness of 20 μm using a coating machine, and vacuum dried at 80 ° C. for 12 hours.
Thereafter, it was punched into a disk shape of φ14 mm and pressed at 16 MPa for 2 minutes using a hand press to obtain a positive electrode.
Next, a coin-type secondary battery was constructed using the positive electrode. A lithium foil punched to φ15 mm was used for the negative electrode. For the electrolyte, LiPF 6 (in the case of a lithium ion secondary battery) or NaPF 6 (in the case of a sodium ion secondary battery) is added to a mixed solvent in which ethylene carbonate and ethyl methyl carbonate are mixed at a volume ratio of 1: 1. Those dissolved at a concentration of 1 mol / L were used. As the separator, a known one such as a polymer porous film such as polypropylene was used. These battery components were assembled and housed in a conventional manner in an atmosphere having a dew point of −50 ° C. or lower to produce a coin-type secondary battery (CR-2032).
容量保持率(%)=(50サイクル後の放電容量)/(1サイクル後の
放電容量)×100 ・・・(2)
結果を表2に示す。 A charge / discharge test was performed using the manufactured secondary battery. In the case of a lithium ion battery, the charging condition is a constant current and constant voltage charge with a current of 1 CA (330 mA / g) and a voltage of 4.5 V, the discharge condition is 1 CA (330 mA / g), and a constant current discharge with a final voltage of 1.5 V. As a result, the discharge capacity at 1 CA was obtained. In the case of a sodium ion battery, the charging conditions are a constant current and constant voltage charging with a current of 1 CA (154 mA / g) and a voltage of 4.5 V, the discharging conditions are a constant current discharge of 1 CA (154 mA / g) and a final voltage of 2.0 V. As a result, the discharge capacity at 1 CA was obtained. Furthermore, 50 cycle repetition tests were performed under the same charge / discharge conditions, and the capacity retention rate (%) was determined by the following formula (2). All charge / discharge tests were performed at 30 ° C.
Capacity retention (%) = (discharge capacity after 50 cycles) / (discharge capacity after 1 cycle) × 100 (2)
The results are shown in Table 2.
Claims (14)
- 少なくとも鉄又はマンガンを含む下記式(A)、(B)又は(C):
LiFeaMnbMcPO4・・・(A)
(式(A)中、MはMg、Ca、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。a、b及びcは、0≦a≦1、0≦b≦1、0≦c≦0.2、及び2a+2b+(Mの価数)×c=2を満たし、かつa+b≠0を満たす数を示す。)
Li2FedMneNfSiO4・・・(B)
(式(B)中、NはNi、Co、Al、Zn、V又はZrを示す。d、e及びfは、0≦d≦1、0≦e≦1、及び0≦f<1、2d+2e+(Nの価数)×f=2を満たし、かつd+e≠0を満たす数を示す。)
NaFegMnhQiPO4・・・(C)
(式(C)中、QはMg、Ca、Co、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。を示す。g、h及びiは、0≦g≦1、0≦h≦1、0≦i<1、及び2g+2h+(Qの価数)×i=2を満たし、かつg+h≠0を満たす数を示す。)
で表される酸化物に、水不溶性導電性炭素材料と、水溶性炭素材料が炭化されてなる炭素とが担持されてなる二次電池用正極活物質。 The following formula (A), (B) or (C) containing at least iron or manganese:
LiFe a Mn b M c PO 4 (A)
(In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. A, b, and c are 0 ≦ a ≦ 1, 0 ≦ b ≦ 1, 0 ≦ c ≦ 0.2, and 2a + 2b + (M valence) × c = 2 and a number satisfying a + b ≠ 0 are shown.)
Li 2 Fe d Mn e N f SiO 4 (B)
(In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr. D, e, and f are 0 ≦ d ≦ 1, 0 ≦ e ≦ 1, and 0 ≦ f <1, 2d + 2e +. (The valence of N) × f = 2 is satisfied, and d + e ≠ 0 is satisfied.)
NaFe g Mn h Q i PO 4 (C)
(In the formula (C), Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. G, h, and i are 0. ≦ g ≦ 1, 0 ≦ h ≦ 1, 0 ≦ i <1, and 2g + 2h + (Q valence) × i = 2 and a number satisfying g + h ≠ 0 are shown.
A positive electrode active material for a secondary battery, in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by: - 酸化物と水不溶性導電性炭素材料を含む複合体に、水溶性炭素材料が炭化されてなる炭素が担持されてなる請求項1に記載の二次電池用正極活物質。 The positive electrode active material for a secondary battery according to claim 1, wherein carbon obtained by carbonizing a water-soluble carbon material is supported on a composite including an oxide and a water-insoluble conductive carbon material.
- 水不溶性導電性炭素材料及び水溶性炭素材料の炭素原子換算量が、合計で1.0~20.0質量%である請求項1又は2に記載の二次電池用正極活物質。 The positive electrode active material for a secondary battery according to claim 1 or 2, wherein the water-insoluble conductive carbon material and the water-soluble carbon material have a total carbon atom conversion amount of 1.0 to 20.0 mass%.
- 水溶性炭素材料が、糖類、ポリオール、ポリエーテル、及び有機酸から選ばれる1種又は2種以上である請求項1~3のいずれか1項に記載の二次電池用正極活物質。 The positive electrode active material for a secondary battery according to any one of claims 1 to 3, wherein the water-soluble carbon material is one or more selected from saccharides, polyols, polyethers, and organic acids.
- 水不溶性導電性炭素材料が、グラファイトである請求項1~4のいずれか1項に記載の二次電池用正極活物質。 The positive electrode active material for a secondary battery according to any one of claims 1 to 4, wherein the water-insoluble conductive carbon material is graphite.
- 複合体が、水不溶性導電性炭素材料と、水熱反応により得られた酸化物と乾式混合されることにより、酸化物に担持されてなる請求項2~5のいずれか1項に記載の二次電池用正極活物質。 The composite according to any one of claims 2 to 5, wherein the composite is supported on an oxide by dry mixing with a water-insoluble conductive carbon material and an oxide obtained by a hydrothermal reaction. Positive electrode active material for secondary battery.
- 乾式混合が、酸化物と水不溶性導電性炭素材料とが予備混合され、次いで圧縮力及びせん断力を付加しながら混合される混合である請求項6に記載の二次電池用正極活物質。 The positive electrode active material for a secondary battery according to claim 6, wherein the dry mixing is a mixture in which an oxide and a water-insoluble conductive carbon material are premixed and then mixed while applying compressive force and shearing force.
- 水溶性炭素材料が、酸化物を含む複合体と湿式混合された後、焼成されることにより炭化されてなる炭素として酸化物に担持されてなる請求項2~7のいずれか1項に記載の二次電池用正極活物質。 The water-soluble carbon material according to any one of claims 2 to 7, wherein the water-soluble carbon material is supported on the oxide as carbon that is carbonized by being wet-mixed with the composite containing the oxide and then calcined. Positive electrode active material for secondary battery.
- 少なくとも鉄又はマンガンを含む下記式(A)、(B)又は(C):
LiFeaMnbMcPO4・・・(A)
(式(A)中、MはMg、Ca、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。a、b及びcは、0≦a≦1、0≦b≦1、0≦c≦0.2、及び2a+2b+(Mの価数)×c=2を満たし、かつa+b≠0を満たす数を示す。)
Li2FedMneNfSiO4・・・(B)
(式(B)中、NはNi、Co、Al、Zn、V又はZrを示す。d、e及びfは、0≦d≦1、0≦e≦1、及び0≦f<1、2d+2e+(Nの価数)×f=2を満たし、かつd+e≠0を満たす数を示す。)
NaFegMnhQiPO4・・・(C)
(式(C)中、QはMg、Ca、Co、Sr、Y、Zr、Mo、Ba、Pb、Bi、La、Ce、Nd又はGdを示す。を示す。g、h及びiは、0≦g≦1、0≦h≦1、0≦i<1、及び2g+2h+(Qの価数)×i=2を満たし、かつg+h≠0を満たす数を示す。)
で表される酸化物に、水不溶性導電性炭素材料と、水溶性炭素材料が炭化されてなる炭素とが担持されてなる二次電池用正極活物質の製造方法であって、
リチウム化合物又はナトリウム化合物、リン酸化合物又はケイ酸化合物、並びに少なくとも鉄化合物又はマンガン化合物を含む金属塩を含有するスラリー水を水熱反応に付して酸化物Xを得る工程(I)、
得られた酸化物Xに水不溶性導電性炭素材料を添加して乾式混合して複合体Yを得る工程(II)、並びに
得られた複合体Yに水溶性炭素材料を添加して湿式混合し、焼成する工程(III)を備える、二次電池用正極活物質の製造方法。 The following formula (A), (B) or (C) containing at least iron or manganese:
LiFe a Mn b M c PO 4 (A)
(In the formula (A), M represents Mg, Ca, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. A, b, and c are 0 ≦ a ≦ 1, 0 ≦ b ≦ 1, 0 ≦ c ≦ 0.2, and 2a + 2b + (M valence) × c = 2 and a number satisfying a + b ≠ 0 are shown.)
Li 2 Fe d Mn e N f SiO 4 (B)
(In the formula (B), N represents Ni, Co, Al, Zn, V, or Zr. D, e, and f are 0 ≦ d ≦ 1, 0 ≦ e ≦ 1, and 0 ≦ f <1, 2d + 2e +. (The valence of N) × f = 2 is satisfied, and d + e ≠ 0 is satisfied.)
NaFe g Mn h Q i PO 4 (C)
(In the formula (C), Q represents Mg, Ca, Co, Sr, Y, Zr, Mo, Ba, Pb, Bi, La, Ce, Nd, or Gd. G, h, and i are 0. ≦ g ≦ 1, 0 ≦ h ≦ 1, 0 ≦ i <1, and 2g + 2h + (Q valence) × i = 2 and a number satisfying g + h ≠ 0 are shown.
A method for producing a positive electrode active material for a secondary battery in which a water-insoluble conductive carbon material and carbon obtained by carbonizing a water-soluble carbon material are supported on an oxide represented by:
A step (I) of obtaining an oxide X by subjecting a slurry water containing a lithium compound or sodium compound, a phosphoric acid compound or a silicic acid compound, and a metal salt containing at least an iron compound or a manganese compound to a hydrothermal reaction;
Step (II) in which a water-insoluble conductive carbon material is added to the obtained oxide X and dry-mixed to obtain a composite Y, and a water-soluble carbon material is added to the obtained composite Y and wet-mixed. The manufacturing method of the positive electrode active material for secondary batteries provided with the process (III) baked. - 水溶性炭素材料が、糖類、ポリオール、ポリエーテル、及び有機酸から選ばれる1種又は2種以上である請求項9に記載の二次電池用正極活物質の製造方法。 The method for producing a positive electrode active material for a secondary battery according to claim 9, wherein the water-soluble carbon material is one or more selected from saccharides, polyols, polyethers, and organic acids.
- 水不溶性導電性炭素材料が、グラファイトである請求項9又は10に記載の二次電池用正極活物質の製造方法。 The method for producing a positive electrode active material for a secondary battery according to claim 9 or 10, wherein the water-insoluble conductive carbon material is graphite.
- 工程(II)において、水不溶性導電性炭素材料とともに水溶性炭素材料を添加する請求項9~11のいずれか1項に記載の二次電池用正極活物質の製造方法。 The method for producing a positive electrode active material for a secondary battery according to any one of claims 9 to 11, wherein a water-soluble carbon material is added together with the water-insoluble conductive carbon material in the step (II).
- 工程(III)における水溶性炭素材料の添加量が、複合体Y100質量部に対して1.0~55.0質量部である請求項9~12のいずれか1項に記載の二次電池用正極活物質の製造方法。 The secondary battery according to any one of claims 9 to 12, wherein the amount of the water-soluble carbon material added in step (III) is 1.0 to 55.0 parts by mass with respect to 100 parts by mass of the composite Y. A method for producing a positive electrode active material.
- 工程(II)における乾式混合が、酸化物と水不溶性導電性炭素材料とを予備混合し、次いで圧縮力及びせん断力を付加しながら混合する混合である請求項9~13のいずれか1項に記載の二次電池用正極活物質の製造方法。 14. The dry mixing in step (II) is a mixture in which an oxide and a water-insoluble conductive carbon material are premixed and then mixed while applying compressive force and shearing force. The manufacturing method of the positive electrode active material for secondary batteries of description.
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