Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/04—Processes of manufacture in general
  • H01M4/043—Processes of manufacture in general involving compressing or compaction
  • H01M4/0433—Molding
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/05—Accumulators with non-aqueous electrolyte
  • H01M10/052—Li-accumulators
  • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
  • H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
  • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
  • H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
  • H01M4/621—Binders
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
  • H01M4/621—Binders
  • H01M4/622—Binders being polymers
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/64—Carriers or collectors
  • H01M4/66—Selection of materials
  • H01M4/661—Metal or alloys, e.g. alloy coatings
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M2004/021—Physical characteristics, e.g. porosity, surface area
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/10—Energy storage using batteries
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T29/00—Metal working
  • Y10T29/49—Method of mechanical manufacture
  • Y10T29/49002—Electrical device making
  • Y10T29/49108—Electric battery cell making
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T29/00—Metal working
  • Y10T29/49—Method of mechanical manufacture
  • Y10T29/49002—Electrical device making
  • Y10T29/49108—Electric battery cell making
  • Y10T29/49115—Electric battery cell making including coating or impregnating

Definitions

• the present invention relates to a carbonaceous negative electrode material for producing a lithium battery having high volumetric charge/discharge capacity, and exhibiting excellent characteristics in terms of the charge/discharge cycle and large-current load; to a composition for forming the negative electrode material (hereinafter may be referred to as a “negative electrode material composition”); to a method for producing the composition; to a lithium battery and a lithium secondary battery employing the carbonaceous negative electrode material.
• a secondary battery having high energy density i.e., high capacity.
• a number of small-sized portable apparatuses such as cellular phones and video cameras have employed a non-aqueous lithium secondary battery such as a lithium ion battery employing a non-aqueous electrolytic solution or a lithium polymer battery, which exhibits high energy density and high voltage.
• a lithium secondary battery employs, as a negative electrode material, a carbon material such as graphite, which exhibits high charge/discharge capacity per unit mass at low electric potential nearly equal to that of lithium (Li).
• fluorine-containing resins such as polyvinylidene fluoride (abbreviated as “PVDF”) and copolymers thereof have generally been employed as a binder for a negative electrode.
• PVDF polyvinylidene fluoride
• SBR styrene-butadiene rubber
• an electrically conductive additive there has been widely employed vapor grown carbon fiber, which exhibits high electrical conductivity and exerts the effect of enhancing the strength of an electrode, as compared with the case of carbon black (e.g., acetylene black), which has conventionally been employed as an electrically conductive additive.
• carbon black e.g., acetylene black
• VGCF vapor grown carbon fiber
• vapor grown carbon fiber which exhibits hydrophobicity, is employed in combination with PVDF as a binder, which is used in the form of organic solvent dispersion, but is not employed in combination with SBR, which is used in the form of aqueous dispersion.
• a secondary battery employed in a small-sized portable apparatus is required to have a smaller size, high gravimetric energy density and high volumetric energy density. Therefore, attempts have been made to increase the amount of an electrode material charged into a battery housing by increasing the density of the electrode material, wherein charge/discharge capacity is nearly equal to the theoretical value as described above, so as to enhance the volumetric energy density of the resultant electrode and battery.
• Graphite which is at present most widely employed as a negative electrode material, has a true density of about 2.2 g/cm 3 , but graphite has conventionally been employed in a negative electrode having a density of about 1.5 g/cm 3 .
• the density of the negative electrode employing graphite is increased to 1.7 g/cm 3 or higher, conceivably, the volumetric energy density of the resultant battery can be enhanced.
• the density of a negative electrode is increased, the amount of pores contained in the negative electrode is reduced, leading to problems such as deficiency of an electrolytic solution, which is generally present in the pores and plays an important role for electrode reaction, and lowering of the rate of permeation of the electrolytic solution into the negative electrode.
• An object of the present invention is to provide a carbonaceous negative electrode material of high energy density, which is required for producing a lithium battery of high energy density exhibiting excellent cycle characteristics and high-speed charging/discharging performance.
• the present inventors have conducted extensive studies, and as a result have found that when SBR, which exhibits bindability even in a relatively small amount, is added as a binder to a carbonaceous negative electrode material, and carbon fiber having a fiber diameter of 1 to 1,000 nm, serving as an electrically conductive additive, is uniformly dispersed in the negative electrode material, the resultant battery exhibits excellent characteristics; i.e., low electrode resistance, high electrode strength, high electrolytic solution permeability, high energy density and good high-speed charging/discharging performance.
• the present invention has been accomplished on the basis of this finding.
• the present invention provides a negative electrode material for a lithium battery (hereinafter may be referred to as a “carbonaceous negative electrode material for a lithium battery”), and a producing method and use thereof as described below.
• a negative electrode material for a lithium battery characterized by comprising a carbonaceous negative electrode active substance having a specific surface area of 1 m 2 /g or more, a binder formed of styrene-butadiene rubber and a carbon fiber having a fiber diameter of 1 to 1,000 nm.
• the negative electrode material for a lithium battery according to 1 or 2 above wherein the amount of the carbon fiber is 0.05 to 20 mass % and the amount of the binder formed of styrene-butadiene rubber is 0.1 to 6.0 mass %, on the basis of the total amount of the carbonaceous negative electrode active substance, the binder, and the carbon fiber.
• the carbonaceous negative electrode active substance is in the form of carbonaceous particles containing, in an amount of 50 mass % or more, graphite particles satisfying the following requirements:
• C 0 of a (002) plane as measured by X-ray diffractometry is 0.6900 nm or less, La (the size of a crystallite as measured along the a-axis) is greater than 100 nm, and Lc (the size of a crystallite as measured along the c-axis) is greater than 100 nm;
• laser Raman R value (the ratio of the intensity of a peak at 1,360 cm ⁇ 1 in a laser Raman spectrum to that of a peak at 1,580 cm ⁇ 1 in the spectrum) is 0.01 to 0.9.
• a method for producing a composition for forming a negative electrode material for a lithium battery comprising adding an aqueous styrene-butadiene rubber dispersion to a carbon fiber/active substance dispersion prepared by dispersing, in an aqueous thickener solution, a carbon fiber having a fiber diameter of 1 to 1,000 nm, a carbonaceous negative electrode active substance having a specific surface area of 1 m 2 /g or more; and stirring the resultant mixture.
• composition for forming a negative electrode material for a lithium battery which composition is produced by means of a method as recited in any one of 22 to 28 above.
• a composition for forming a negative electrode material for a lithium battery which composition comprises an aqueous thickener solution, wherein carbon fiber having a fiber diameter of 1 to 1,000 nm is dispersed.
• composition for forming a negative electrode material for a lithium battery according to 30 above wherein the content of the thickener in the aqueous thickener solution is 0.3 to 5 mass %, and the amount of the carbon fiber is 0.1 to 10 mass % on the basis of the entirety of the composition.
• the negative electrode material for a lithium battery according to any one of 1 to 21 above which is produced by applying the composition for forming the negative electrode material for a lithium battery as recited in 29 above onto a metallic collector foil, and drying the thus-applied composition, followed by pressure molding.
• a lithium battery comprising the negative electrode material for a lithium battery as recited in any of 1 to 21, 33 and 34 above.
• a lithium secondary battery comprising the negative electrode material for a lithium battery as recited in any of 1 to 21, 33 and 34 above.
• the lithium secondary battery according to 36 above which comprises a non-aqueous electrolyte and a non-aqueous solvent for the non-aqueous electrolyte, which is at least one species selected from the group consisting of ethylene carbonate, diethyl carbonate, dimethyl carbonate, methyl ethyl carbonate, propylene carbonate, butylene carbonate and vinylene carbonate.
• a carbonaceous negative electrode material is produced by wet-mixing carbonaceous electrode active substance powder (average powder particle size: several to some tens of ⁇ m) with a binder and an electrically conductive additive, and uniformly applying the resultant mixture onto a metallic collector coil, followed by drying and pressure molding.
• carbon black powder e.g., acetylene black powder
• an electrically conductive additive which has a high aspect ratio e.g., carbon fiber
• adding an electrically conductive additive which has a high aspect ratio e.g., carbon fiber
• an amount of about 5 mass % is required based on the total amount of a carbonaceous negative electrode active substance, binder and electrically conductive additive for enhancement of the electrical conductivity of an electrode.
• electrically conductive fiber having a high aspect ratio such as vapor grown carbon fiber
• the fiber exhibits its effects sufficiently.
• the energy density of a battery employing a carbonaceous electrode active substance is approaching its limit, in order to increase the volumetric energy density of the battery, attempts have been made to increase the density of an electrode employed therein.
• a conventional carbon black electrically conductive additive when the density of an electrode is increased through molding (high-pressure pressing), the electrode is deformed, resulting in damage to electrically conductive paths or electrolytic solution permeation paths formed in the electrode.
• the carbon fiber exhibits excellent electrical conductivity, and has a minimum possible fiber diameter and a maximum possible fiber length so that the number of electrically conductive paths can be increased. From such a viewpoint, the carbon fiber to be added must be fine carbon fiber exhibiting electrical conductivity and toughness.
• the fiber diameter of the carbon fiber employed in the negative electrode material for a lithium battery of the present invention is excessively large, the size of pores formed in the resultant electrode becomes excessively large, and thus the electrode density fails to be increased, which is not preferred.
• the carbon fiber to be employed Since the average particle size of carbonaceous electrode active substance particles which are currently employed in Li ion batteries or Li polymer batteries is several to some tens of ⁇ m, the carbon fiber to be employed must have a fiber diameter of about 1 ⁇ m at most. Meanwhile, when the fiber diameter of the carbon fiber to be employed is excessively small, fiber filaments of the carbon fiber are buried between active substance particles, and thus a network fails to be formed in the resultant electrode, and pores cannot be formed among the active substance particles.
• the carbon fiber to be employed must have a fiber diameter of at least 1 to several nm.
• the fiber diameter of the carbon fiber which can be employed in the negative electrode material for a lithium battery of the present invention is 1 to 1,000 nm, preferably 10 to 500 nm.
• the average fiber diameter of the carbon fiber is preferably 5 to 500 nm, more preferably 10 to 200 nm.
• the crystallization degree (i.e., graphitization degree) of the carbon fiber is preferably high.
• carbon fiber exhibiting high graphitization degree has a developed layer structure, becomes harder, and exhibits enhanced electrical conductivity. Therefore, as described above, such carbon fiber is suitable for use in a carbonaceous negative electrode material for a lithium battery.
• Graphitization of the carbon fiber can be generally attained through high-temperature treatment of the carbon fiber.
• the treatment temperature for graphitization which varies depending on the type of carbon fiber to be employed, is preferably 2,000° C. or higher, more preferably 2,500° C. or higher.
• the carbon fiber When a graphitization promoter which facilitates graphitization, such as boron or Si, is added to the carbon fiber before thermal treatment, the carbon fiber can be effectively graphitized.
• a graphitization promoter which facilitates graphitization such as boron or Si
• the carbon fiber can be effectively graphitized.
• the amount of the promoter to be added is preferably 0.1 to 100,000 ppm, more preferably 10 to 50,000 ppm.
• the average interlayer distance (d 002 ) of the carbon fiber as measured by X-ray diffractometry is preferably 0.344 nm or less, more preferably 0.339 nm or less, with the thickness (Lc) of a carbon crystal as measured along the c-axis is 40 nm or less.
• the average fiber length which varies depending on the type and the fiber diameter of carbon fiber to be employed, is preferably 0.5 to 100 ⁇ m, more preferably 1 to 50 ⁇ m.
• the range of the average fiber length is represented by average aspect ratio (ratio of fiber length to fiber diameter), the average aspect ratio is preferably 5 to 50,000, more preferably 10 to 15,000.
• the carbon fiber contains branched carbon fiber
• the electrical conductivity, strength, and electrolytic solution retainability of the resultant electrode are further enhanced, which is preferable.
• the amount of branched carbon fiber is excessively large, as in the case where the fiber length of the carbon fiber is excessively large, dispersibility of the carbon fiber in the electrode is impaired. Therefore, preferably, the amount of branched carbon fiber is regulated to an appropriate level.
• the amount of branched carbon fiber can be regulated to some extent by means of a carbon fiber production process or a pulverization process performed subsequent to the production process.
• the carbon fiber production method examples include a method in which a polymer is formed into fiber through spinning or a similar technique, and the resultant fiber is thermally treated in an inert atmosphere; and a vapor growth method in which an organic compound is subjected to reaction at high temperature in the presence of a catalyst.
• the crystal growth direction is parallel to the axis of each fiber filament of the carbon fiber, and the crystallinity of a graphite structure tends to become high along with the fiber length direction tends to become high. Therefore, vapor grown carbon fiber has relatively a small fiber diameter, and exhibits relatively high electrical conductivity and strength.
• Vapor grown carbon fiber which contains crystals grown in the direction along the fiber axis and has branches, is suitably employed for attaining the object of the present invention.
• Vapor grown carbon fiber can be produced through, for example, the following procedure: a gasified organic compound is fed into a high-temperature atmosphere together with iron serving as a catalyst.
• the vapor grown carbon fiber to be employed may be “as-produced” carbon fiber; carbon fiber which has undergone thermal treatment at 800 to 1,500° C.; or carbon fiber which has undergone graphitization treatment at 2,000 to 3,000° C.
• the vapor grown carbon fiber is chosen in accordance with the type of electrical active substance powder to be employed. However, vapor grown carbon fiber which has undergone thermal treatment or graphitization treatment is preferred, since the thus-treated carbon fiber, wherein carbon is highly crystallized, exhibits high carbon crystallinity, high electrical conductivity and high pressure resistance.
• the vapor grown carbon fiber has a branched structure.
• carbon layers forming a cylinder-shape of fiber assume uninterrupted layers.
• the term “hollow structure” refers to a structure in which a plurality of carbon layers form a cylinder.
• the hollow structure encompass an imperfect cylindrical structure, a structure in which the carbon layers are partially broken, and a structure in which the laminated two carbon layers are bonded into a single carbon layer.
• the cross-section of the cylinder does not necessarily assume a perfect circle, but may assume an oval or a polygonal shape.
• Vapor grown carbon fiber generally has, on its surface, irregularities and rough portions, and therefore exhibits enhanced adhesion to an electrode active substance.
• the vapor grown carbon fiber exhibits enhanced adhesion to the carbonaceous particles serving as nuclei.
• the carbon fiber which also serves as an electrically conductive additive, is firmly deposited on the carbonaceous powder particles and is not dissociated therefrom, whereby electronic conductivity can be maintained and cycle characteristics are improved.
• the carbon fiber can be dispersed in the active substance so as to wrap up the active substance, thereby enhancing the strength of the resultant electrode and establishing favorable contact between the particles.
• the amount of the carbon fiber to be added is preferably 0.05 to 20 mass %, more preferably 0.1 to 15 mass %, much more preferably 0.5 to 10 mass %, on the basis of the total amount of the carbon fiber, a carbonaceous negative electrode active substance, a binder, and a thickener (which is added if desired).
• the amount of the carbon fiber can be regulated to the above preferred range by adding the carbon fiber to the electrode material so that the carbon fiber amount falls within the above range during the course of preparation of the electrode material.
• the carbon fiber to be employed may be subjected to surface treatment in order to control the dispersion state of the carbon fiber in the resultant electrode. No particular limitations are imposed on the surface treatment method.
• the carbon fiber may be subjected to oxidation treatment, thereby introducing an oxygen-containing functional group to the carbon fiber and imparting hydrophilicity thereto; or the carbon fiber may be subjected to fluorination treatment or silicon treatment, thereby imparting hydrophobicity to the carbon fiber.
• the carbon fiber may be coated with, for example, phenolic resin, or may be subjected to mechanochemical treatment or a similar treatment.
• Oxidation treatment of the carbon fiber can be carried out through, for example, the following procedure: the carbon fiber is heated in air at 500° C. for about one hour. The hydrophilicity of the carbon fiber is enhanced by the treatment.
• carbon fiber which has undergone oxidation treatment i.e., carbon fiber having a hydrophilic surface
• styrene-butadiene rubber serving as a binder is often employed in the form of aqueous dispersion.
• SBR Styrene-Butadiene Rubber
• SBR is employed as an electrode binder.
• the amount of SBR to be used can be reduced as compared with the case of a fluorine-containing resin binder (e.g., PVDF), which has generally been employed.
• PVDF fluorine-containing resin binder
• SBR is mixed with an electrode active substance in the form of aqueous dispersion, explosion-proof facilities is not required. Therefore, employment of SBR is advantageous in enabling to simplify an electrode production process. Since SBR generally has a low glass transition temperature (Tg), an electrode employing SBR as a binder exhibits excellent low-temperature characteristics and high-speed charging/discharging characteristics.
• SBR is classified into two types: emulsion-polymerized SBR and solution-polymerized SBR.
• emulsion-polymerized SBR is obtained as latex and may be dried and used as dry rubber.
• the solution-polymerized SBR include random SBR, block SBR, and symmetric block SBR, which have different types of copolymerization of styrene and butadiene.
• SBR also includes high styrene rubber, which has high compositional proportion of styrene and a high glass transition temperature (Tg).
• SBR includes a modified SBR, which is copolymerized with an unsaturated carboxylic acid or an unsaturated nitrile compound.
• SBR semrene-maleic anhydride copolymer
• the type of SBR employed as a binder in the carbonaceous negative electrode material for a lithium battery of the present invention can be appropriately selected in accordance with the type of a negative electrode active substance to be employed.
• a latex-type aqueous dispersion prepared by dispersing emulsion- or solution-polymerized SBR in water is suitable for use in the carbonaceous negative electrode material for a lithium battery of the present invention, since the aqueous dispersion is readily mixed with a carbonaceous negative electrode active substance.
• SBR preferably has a styrene content of 50 mass % or less in copolymerization and a glass transition temperature of 0° C. or lower.
• the size of SBR particles contained in the aqueous dispersion should not be excessively large or excessively small, in order to be uniformly dispersed in a carbonaceous negative electrode active substance and to attain effective adhesion between the active substance particles. Therefore, the average particle size of SBR employed in the carbonaceous negative electrode material for a lithium battery of the present invention is preferably 10 to 500 nm.
• the amount of SBR to be added to the negative electrode material cannot be uniformly determined, depending on the amounts of carbon fiber and a carbonaceous negative electrode active substance which are to be mixed with SBR.
• the SBR amount is excessively large, the content of the carbonaceous negative electrode active substance in the negative electrode material is reduced, and thus the capacity of the resultant negative electrode is reduced, and the resistance of the electrode is increased.
• the number of reaction sites of the negative electrode may be reduced, leading to further reduction of the electrode capacity.
• the amount of SBR to be added is preferably 0.1 to 6.0 mass %, more preferably 0.3 to 5.0 mass %, on the basis of the total amount of the carbonaceous negative electrode active substance, the binder, the carbon fiber, and a thickener (which is added if desired).
• An carbonaceous negative electrode active substance is a substance which contains carbon and is capable of electrochemically absorbing (occluding) and releasing ions.
• SBR preferably an aqueous SBR dispersion
• a carbonaceous negative electrode active substance having a maximum possible specific surface area is preferably employed, from the viewpoints of wettability improvement, handling, electrode strength, and electrolytic solution retainability.
• a carbonaceous negative electrode active substance having a specific surface area as measured by means of the BET method i.e., a BET specific surface area
• the BET specific surface area is preferably 1.0 to 7.0 m 2 /g, more preferably 1.5 to 6.0 m 2 /g.
• the carbonaceous negative electrode active substance may be an active substance mainly comprising a non-graphite carbon material, or an active substance mainly comprising a graphite carbon material.
• a non-graphite carbon material is a carbon material which does not contain a three-dimensional regularity of graphite crystals, and includes a turbostratic structure carbon material and an amorphous carbon material, e.g., vitreous carbon and a carbon material which does not exhibit high crystallinity due to a thermal treatment at a low temperature.
• a graphite carbon material is a carbon material which contains a three-dimensional regularity of graphite crystals, and includes a natural graphite and artificial graphite obtained by thermally treating a readily-graphitizable carbon material, as well as kish graphite obtained by redeposition of graphite from melted iron.
• the term “mainly comprising” refers to the component whose content of the active substance is 50 mass % or higher, preferably 60 mass % or higher, more preferably 80 mass % or higher, particularly preferably 90 mass % or higher.
• Examples of the active substance mainly comprising a non-graphite carbon material include a carbon material obtained through thermal treatment of a difficult-to-graphitize polymer such as phenolic resin; a carbon material obtained through thermal treatment of pitch or coke at about 1,000° C.; a carbon material obtained through thermal treatment of a conjugated polymer such as an electrically conductive polymer; and a CVD carbon material deposited onto a substrate by means of thermal CVD.
• Si is added to such a carbon material during the course of thermal treatment of the material, the electrical capacity of the resultant negative electrode can be increased.
• Such a non-graphite carbon material preferably assumes a spherical shape of maximum possible roundness, from the viewpoints of handling of the material when an electrode sheet is prepared, and prevention of side reaction between the material and an electrolytic solution when the material is employed in a battery.
• the average roundness of such a non-graphite carbon material is preferably 0.70 to 0.99 as measured by use of a flow particle image analyzer.
• non-graphite carbon material having an average particle size of 1 to 50 ⁇ m as measured by means of laser diffractometry.
• the bulk density of the negative electrode material employing such a non-graphite carbon material since the bulk density varies depending on the true density of the carbonaceous active substance.
• the true density of such a non-graphite carbon material is generally 1.9 g/cm 3 or higher
• the bulk density of the layer of the synthesized agent comprising a negative electrode active substance, binder and electrically conductive additive is preferably 1.5 g/cm 3 or higher, more preferably 1.7 g/cm 3 or higher.
• the active substance mainly comprising a graphite carbon material may be a graphite carbon material, which is generally employed as a carbon active substance in an Li ion battery.
• a graphite active substance exhibits high crystallinity, enables uniform intercalation and release of lithium ions, and is rapidly dispersed. Therefore, when the graphite active substance is employed in a battery, the resultant battery undergoes little change in discharge potential, and exhibits excellent large current load characteristics.
• Such a graphite active substance has a true density as high as about 2.2 g/cm 3 and also, the electrode formed thereof has a bulk density of 1.5 g/cm 3 .
• the porosity of such an electrode can be reduced, so as to increase the bulk density of the electrode to 1.7 g/cm 3 or higher.
• the graphite active substance to be employed preferably has a maximum possible roundness. Specifically, there is employed a graphite active substance having an average roundness of 0.70 to 0.99 as measured by use of a flow particle image analyzer, and an average particle size of about 1 to about 50 ⁇ m as measured by means of laser diffractometry.
• the graphite active substance to be employed preferably has maximum possible crystallinity.
• La the size of a crystallite as measured along the a-axis
• Lc the size of a crystallite as measured along the c-axis
• Laser Raman R value is preferably 0.01 to 0.9.
• the true density of the graphite active substance is preferably 2.20 g/cm 3 or higher.
• the amount of boron to be added is preferably 0.1 mass ppm to 100,000 mass ppm, more preferably 10 mass ppm to 50,000 mass ppm.
• a carbonaceous negative electrode material for a lithium battery is produced through the following procedure: a carbonaceous negative electrode active substance, an electrode binder and, if desired, an electrically conductive additive (e.g., carbon black or graphite fine powder) are wet- or dry-mixed in predetermined proportions; and the resultant mixture is applied onto a metallic collector (e.g., Cu collector), followed by drying and pressing.
• a metallic collector e.g., Cu collector
• the carbonaceous negative electrode material for a lithium battery of the present invention is produced by applying, onto a collector, a negative electrode material composition containing a carbonaceous negative electrode active substance, carbon fiber and an SBR binder, followed by molding.
• the negative electrode material composition is prepared by a method which has not yet been known; specifically, a method in which carbon fiber having a fiber diameter of 1 to 1,000 nm, a carbonaceous negative electrode active substance having a BET specific surface area of 1 m 2 /g or more, and, if desired, a carbonaceous powder as an electrically conductive additive are fully dispersed in an aqueous thickener solution (e.g., an aqueous solution of a carboxymethyl cellulose compound); and an aqueous dispersion of styrene-butadiene rubber is added to the resultant dispersion, followed by stirring for a relatively short period of time.
• an aqueous thickener solution e.g., an aqueous solution of a carb
• This preparation method is intended to simplify a step of stirring a mixture obtained through addition of an aqueous SBR dispersion to a dispersion which has been prepared by fully dispersing carbon fiber filaments in an aqueous solution.
• the carbon fiber filaments which have been dispersed may reaggregate, resulting in an increase in specific resistance of the electrode and lowering of electrolytic solution permeability; i.e., deterioration of battery performance.
• the reason for reaggregation of the carbon fiber filaments is considered as follows.
• the binder which is added after dispersion of the carbon fiber filaments, exhibits high affinity with the aqueous thickener solution, and therefore, the hydrophobic carbon fiber filaments, which have been dispersed in the thickener solution, are gradually separated from the thickener solution.
• Specific examples of the preparation method include the below-described methods (A) through (D).
• (C) A method in which a carbonaceous negative electrode active substance and, if desired, another carbon-powder electrically conductive additive are added to an aqueous thickener solution, followed by stirring; carbon fiber is added to the resultant mixture and is fully dispersed therein under stirring; and an aqueous SBR dispersion is added to the resultant dispersion, followed by stirring for a relatively short period of time.
• a rough standard of the time (relatively short period of time) for stirring after addition of an aqueous SBR dispersion cannot be uniformly determined depending on, for example, the type and amount of carbon fiber or the stirring method.
• the stirring time is appropriately determined in accordance with the state of the composition which has been allowed to stand after stirring.
• the stirring time is generally 120 minutes or less, preferably 10 to 90 minutes.
• methods (A) and (B), which enable relatively easy dispersion of carbon fiber are particularly preferred.
• carbon fiber is added to an aqueous thickener solution such that the carbon fiber content of the resultant dispersion becomes 0.1 to 10 mass % on the basis of the total amount of a carbonaceous negative electrode active substance, binder and electrically conductive additive.
• a thickener is a nonionic polymer employed for regulating the viscosity of the negative electrode material composition to a level such that the composition can be applied onto a collector.
• the thickener to be employed examples include aqueous solutions of nonionic polymers such as polyethylene glycol, cellulose, polyacrylamide, poly(N-vinylamide), and poly(N-vinylpyrrolidone).
• nonionic polymers such as polyethylene glycol, cellulose, polyacrylamide, poly(N-vinylamide), and poly(N-vinylpyrrolidone).
• nonionic polymers polyethylene glycol and celluloses such as carboxymethyl cellulose (CMC) are preferred, with carboxymethyl cellulose (CMC) being particularly preferred.
• the amount of the thickener to be added cannot be uniformly determined depending on the type of the thickener. However, the amount of the thickener is preferably 0.1 to 4 mass %, more preferably 0.3 to 3 mass %, on the basis of the total amount of the carbonaceous negative electrode active substance, binder, carbon fiber, and thickener.
• the thickener is preferably used in a form of an aqueous solution, wherein the viscosity of the solution as measured at room temperature is 50 to 5,000 mPa ⁇ s (preferably 100 to 3,000 mPa ⁇ s) and the thickener content is preferably 0.3 to 5 mass %.
• CMC carboxymethyl cellulose
• the amount of the CMC compound to be added which varies depending on the type of the carbon fiber or negative electrode active substance to be employed, is preferably regulated to a minimum possible level, since the CMC compound does not participate in battery reaction, and when an excessively large amount of the CMC compound is added, the content of the negative electrode active substance in the resultant electrode is reduced.
• the content of the CMC compound in an aqueous CMC compound solution is preferably regulated to a minimum possible level, so long as the CMC compound can exhibit its thickening effects.
• the amount of the CMC compound to be added is preferably 0.1 to 4.0 mass %, more preferably 0.3 to 3 mass %, on the basis of the total amount of the carbonaceous negative electrode active substance, binder, carbon fiber and CMC compound.
• the CMC compound is used in the form of a 0.3 to 5 mass % (preferably about 1 mass %) aqueous solution.
• the viscosity of such an aqueous CMC compound solution as measured at room temperature is 50 to 5,000 mPa ⁇ s, preferably 100 to 3,000 mPa ⁇ s.
• the content of SBR in the aqueous SBR dispersion is preferably 10 to 60 mass %.
• the dispersion state of the components of the electrode material in the electrode varies depending on, for example, the types, compositional proportions and combinations of the components. Since the dispersion state affects the resistance, liquid absorbability or other characteristics of the electrode, optimal compositional proportions and concentration conditions of the components must be selected.
• stirring apparatuses may be used.
• the stirring apparatus which may be employed include a ribbon mixer, a screw kneader, a Spartan ryuzer, a Lodige mixer, a planetary mixer, a defoaming kneader, a stirring-blade-equipped general-purpose mixer and a paint shaker.
• a planetary mixer, a defoaming kneader and a stirring-blade-equipped general-purpose mixer enable relatively easy stirring in the above-described four preparation methods, and a defoaming kneader and a stirring-blade-equipped general-purpose mixer are preferred, with a stirring-blade-equipped general-purpose mixer being particularly preferred.
• a negative electrode material sheet for a lithium battery of the present invention can be prepared by applying the above-obtained negative electrode material composition to a collector foil.
• compositions to a collector foil may be carried out by means of any known technique.
• the composition is applied to a collector foil by use of a doctor blade, a bar coater or a similar apparatus, and then the resultant product is subjected to molding through, for example, roll pressing.
• Examples of the collector which may be employed include known materials, such as a copper foil (which is employed in currently available Li ion batteries), an aluminum foil, a stainless steel foil, a nickel foil, a titanium foil, a foil of an alloy of such metals, and a carbon sheet.
• a copper foil and a copper alloy foil are preferred from the viewpoints of such as strength, electrochemical stability and production cost.
• the thickness of the collector foil employed in the present invention is preferably 0.5 to 100 ⁇ m, particularly preferably 1 to 50 ⁇ m.
• composition-applied electrode material sheet is dried by means of any known technique, and subsequently subjected to molding by means of a known technique such as roll pressing or pressure pressing, so as to be shaped with a desired thickness and density.
• the pressing pressure since the pressure varies depending on the type of the negative electrode active substance to be employed, or depending on the target electrode density. However, the pressure is generally regulated to 1 ton/cm 2 or higher. No particular limitations are imposed on the thickness of the electrode material sheet, since the thickness varies in accordance with the target shape of the resultant battery. However, the thickness is generally regulated to 0.5 to 2,000 ⁇ m, preferably 5 to 1,000 ⁇ m.
• the carbonaceous negative electrode material for a lithium battery of the present invention which is produced through the above-described method, contains uniformly dispersed carbon fiber. Therefore, an electrode formed of the electrode material exhibits low specific resistance.
• the lower specific resistance of electrode is, current density during charging/discharging of the battery can be increased, and high-speed charging/discharging can be attained.
• Low specific resistance of electrode indicates that a carbon fiber network is distributed throughout the electrode; i.e., the electrode has enhanced strength. Therefore, the battery exhibits long charging/discharging cycle life.
• An electrode formed of the negative electrode material of the present invention exhibits, at 25° C., a specific resistance of 0.5 ⁇ cm or less, or even 0.3 ⁇ cm or less.
• any of the above-described preparation methods (A) through (D) when stirring after addition of SBR is performed for a long period of time, carbon fiber filaments which have been dispersed tend to reaggregate as described above, and thus the resultant negative electrode material exhibits high specific resistance.
• a negative electrode material formed of the resultant composition exhibits a specific resistance lower by at most about 10% than that of a negative electrode material formed of a composition which does not contain carbon fiber, the composition being prepared through any of the above-described preparation methods (A) through (D).
• the negative electrode material of the present invention which is formed of a composition prepared through any of the above-described preparation methods (A) through (D), exhibits a specific resistance lower by at least 20% (generally 40% or more) than that of a negative electrode material formed of a composition which does not contain carbon fiber, the composition being prepared through any of the above-described preparation methods (A) through (D). That is, the specific resistance of the negative electrode material of the present invention can be reduced to 80% or less (even to 60% or less) of the specific resistance of a negative electrode material formed of a composition which does not contain carbon fiber having a fiber diameter of 1 to 1,000 nm, the composition being prepared through any of the above-described preparation methods (A) through (D).
• the time for stirring after addition of SBR affects the electrolytic solution permeability of the negative electrode material. Specifically, when stirring after addition of SBR is performed for a long period of time in any of the above-described preparation methods (A) through (D), the resultant negative electrode material fails to exhibit sufficiently improved electrolytic solution permeability. This phenomenon becomes pronounced in the case of an electrode formed to have high density.
• a negative electrode material formed of the resultant composition exhibits an electrolytic solution permeation rate higher by at most about 30% than that of a negative electrode material formed of a composition which does not contain carbon fiber, the composition being prepared through any of the above-described preparation methods (A) through (D).
• the negative electrode material of the present invention which is formed of a composition prepared through any of the above-described preparation methods (A) through (D), exhibits an electrolytic solution permeation rate higher by at least 35% (generally 60% or more) than that of a negative electrode material formed of a composition which does not contain carbon fiber, the composition being prepared through any of the above-described preparation methods (A) through (D).
• a lithium battery of high performance can be produced by employing the negative electrode material for a lithium battery of the present invention in combination with a various positive electrode materials such as lithium cobaltate.
• the negative electrode material for a lithium battery of the present invention is suitable for the needs in a non-aqueous secondary battery of high energy density which is currently prevalent in the market, such as an Li ion battery or an Li polymer battery.
• a cobalt oxide such as lithium cobaltate, a manganese oxide such as lithium manganate, a nickel oxide such as lithium nickelate, a composite oxide formed of such oxides, or a mixture of such oxides.
• a lithium-containing transition metal oxide can be employed as a positive electrode active substance.
• the lithium-containing transition metal oxide is preferably an oxide predominantly containing lithium and at least one transition metal selected from Ti, V, Cr, Mn, Fe, Co, Ni, Mo and W, in which the ratio by mol between lithium and the transition metal is 0.3 to 2.2.
• the positive electrode active substance is an oxide predominantly containing lithium and at least one transition metal selected from V, Cr, Mn, Fe, Co and Ni, in which the ratio by mol between lithium and the transition metal is 0.3 to 2.2.
• the positive electrode active substance may contain Al, Ga, In, Ge, Sn, Pb, Sb, Bi, Si, P, B, etc. in an amount of less than 30 mol % on the basis of the entirety of the transition metal existing as a primary component.
• a preferred substance is at least one species selected from the materials being represented by the formula Li x MO 2 (wherein M represents at least one element selected from Co, Ni, Fe and Mn, and x is 0 to 1.2); or at least one species selected from the materials having a spinel structure and being represented by the formula Li y N 2 O 4 (wherein N includes at least Mn, and y is 0 to 2).
• the positive electrode active substance is at least one species selected from the materials containing Li y M a D 1-a O 2 wherein M represents at least one element selected from Co, Ni, Fe and Mn; D represents at least one element selected from among Co, Ni, Fe, Mn, Al, Zn, Cu, Mo, Ag, W, Ga, In, Sn, Pb, Sb, Sr, B and P, with the proviso that the element corresponding to M being excluded; y is 0 to 1.2; and a is 0.5 to 1; or at least one species selected from the materials having a spinel structure and being represented by the formula Li z (N b E 1-b ) 2 O 4 /wherein N represents Mn; E represents at least one element selected from Co, Ni, Fe, Mn, Al, Zn, Cu, Mo, Ag, W, Ga, In, Sn, Pb, Sb, Sr, B and P; b is 1 to 0.2; and z is 0 to 2.
• M represents at least one element selected from Co, Ni
• the positive electrode active substance include Li x CoO 2 , Li x NiO 2 , Li x MnO 2 , Li x Co a Ni 1-a O 2 , Li x Co b V 1-b O z , Li x Co b Fe 1-b O 2 , Li x Mn 2 O 4 , Li x Mn c Co 2-c O 4 , Li x Mn c Ni 2-c O 4 , Li x Mn c V 2-c O 4 and Li x Mn c Fe 2-c O 4 , wherein x is 0.02 to 1.2, a is 0.1 to 0.9, b is 0.8 to 0.98, c is 1.6 to 1.96, and z is 2.01 to 2.3.
• lithium-containing transition metal oxides examples include Li x CoO 2 , Li x NiO 2 , Li x MnO 2 , Li x Co a Ni 1-a O 2 , Li x Mn 2 O 4 and Li x Co b V 1-b O z , wherein x is 0.02 to 1.2, a is 0.1 to 0.9, b is 0.9 to 0.98, and z is 2.01 to 2.3.
• the value x is a value as measured before the start of charging/discharging, and is increased or decreased through charging/discharging.
• the positive electrode active substance may be a positive electrode material for a next-generation Li battery, such as a metal sulfide (e.g., titanium sulfide or molybdenum sulfide) or an iron olivine compound such as LiFePO 4 .
• a metal sulfide e.g., titanium sulfide or molybdenum sulfide
• an iron olivine compound such as LiFePO 4
• An iron olivine compound such as LiFePO 4 which contains iron, is particularly preferred, from the viewpoints of high theoretical capacity, resource abundance, environmental safety, heat resistance, etc.
• the average particle size of particles of the positive electrode active substance is not particularly limited but is preferably 0.1 to 50 ⁇ m.
• the volume of particles having a particle size of 0.5 to 30 ⁇ m is 95% or more on the basis of the entire volume of the positive electrode active substance particles. More preferably, the volume of particles having a particle size of 3 ⁇ m or less is 18% or less, and the volume of particles having a particle size of 15 ⁇ m to 25 ⁇ m inclusive is 18% or less on the basis of the entire volume of the positive electrode active substance particles.
• the specific surface area of the positive electrode active substance is not specifically limited but is preferably 0.01 to 50 m 2 /g, particularly preferably 0.2 to 10 m 2 /g as measured by means of the BET method.
• the positive electrode material sheet can be prepared through the following procedure: a positive electrode active substance (e.g., lithium cobaltate), an electrode binder, and, if desired, an electrically conductive additive (e.g., carbon black or graphite fine powder) or carbon fiber to be employed in the carbonaceous negative electrode material for a lithium battery of the present invention are wet- or dry-mixed together in predetermined proportions; and the resultant mixture is applied onto a collector formed of Al and the like, followed by drying and pressing.
• a positive electrode active substance e.g., lithium cobaltate
• an electrode binder e.g., an electrically conductive additive (e.g., carbon black or graphite fine powder) or carbon fiber to be employed in the carbonaceous negative electrode material for a lithium battery of the present invention are wet- or dry-mixed together in predetermined proportions; and the resultant mixture is applied onto a collector formed of Al and the like, followed by drying and pressing.
• an electrically conductive additive e.g
• a composition for a positive electrode material (hereinafter may be referred to as a “positive electrode material composition”) is prepared through the following procedure: lithium cobaltate powder and acetylene black (abbreviated as “AB”) are dry-mixed together in predetermined proportions by use of a high-speed, small-sized mixer equipped with blades (IK mixer); and subsequently, an N-methylpyrrolidone (NMP) solution containing polyvinylidene fluoride (PVDF) serving as an electrode binder is added to the above-formed mixture so as to attain predetermined proportions by mass, followed by kneading of the resultant mixture by use of a planetary mixer.
• NMP N-methylpyrrolidone
• PVDF polyvinylidene fluoride
• NMP is further added to the thus-prepared positive electrode material composition, for regulation of the viscosity of the composition.
• the resultant composition is applied onto a rolled Al foil (25 ⁇ m) by use of a doctor blade, so as to attain a predetermined thickness, followed by drying by heating under reduced pressure.
• the composition-applied foil is molded by pressing, so as to attain target thickness and density.
• the pressure for molding is not particularly limited but is generally about 1 ⁇ 10 3 to about 3 ⁇ 10 3 kg/cm 2 .
• the thus-molded product is further dried by heating under reduced pressure, to thereby prepare the positive electrode material sheet.
• the electrode binder to be employed in the positive electrode material may be, in addition to the aforementioned PVDF, a fluorine-containing polymer such as polytetrafluoroethylene or a rubber such as SBR which is employed in the aforementioned negative electrode material or an acrylate polymer.
• a fluorine-containing polymer such as polytetrafluoroethylene or a rubber such as SBR which is employed in the aforementioned negative electrode material or an acrylate polymer.
• Any known solvent suitable for each electrode binder may be employed.
• N-methylpyrrolidone, toluene, acetone, etc. is employed as a solvent for a fluorine-containing polymer
• water and the like is employed as a solvent for SBR as a binder.
• the amount of the electrode binder employed in the positive electrode material is preferably 0.5 to 20 parts by mass, particularly preferably about 1 to about 15 parts by mass, on the basis of 100 parts by mass of the positive electrode active substance.
• kneading which is performed after addition of the solvent
• kneading can be carried out by use of any known apparatus such as a ribbon mixer, a screw kneader, a Spartan ryuzer, a Lodige mixer, a planetary mixer, or a stirring-blade-equipped general-purpose mixer.
• the above-described negative electrode material sheet and positive electrode material sheet for the lithium battery of the present invention are formed into a predetermined shape, and the resultant sheets are prepared into a laminate of positive electrode material sheet/separator/negative electrode material sheet.
• the thus-prepared laminate is stored in a container having a shape of a coin, rectangle, cylinder, sheet, etc., such that the positive electrode and the negative electrode do not come into contact with each other.
• the laminate is again dried under reduced pressure and/or in an inert atmosphere of low dew point ( ⁇ 50° C. or lower), with the laminate being stored in the container, and then the laminate is transferred into an inert atmosphere of low dew point.
• an electrolytic solution is added to the container, and the container is sealed, to thereby produce an Li ion battery and/or an Li polymer battery.
• any known separator may be employed, but a polyethylene- or polypropylene-made microporous film is particularly preferred due to its slimness and strength.
• the porosity of the separator is preferably high, from the viewpoint of ion conduction. However, excessively high porosity could cause deterioration of the strength of the separator, as well as short circuit between the positive and negative electrodes. Therefore, the porosity of the separator is generally regulated to 30 to 90%, preferably 50 to 80%.
• the thickness of the separator is preferably small, from the viewpoints of ion conduction and battery capacity. However, excessively small thickness could cause deterioration of the strength of the separator, as well as short circuit between the positive and negative electrodes.
• the thickness of the separator is generally regulated to 5 to 100 ⁇ m, preferably 5 to 50 ⁇ m.
• Such microporous films may be employed in combination of two or more species, or may be employed in combination with another type of a separator such as non-woven fabric.
• non-aqueous secondary battery of the present invention particularly a lithium ion battery and/or an Li polymer battery, any known non-aqueous electrolyte may be used.
• the non-aqueous electrolyte of the present invention may be any known one such as a non-aqueous electrolytic solution prepared by dissolving an electrolyte salt in an non-aqueous solvent, and a non-aqueous polymer electrolyte prepared by swelling a polymer solid electrolyte with a non-aqueous solvent.
• Examples of preferred organic solvents serving as the aforementioned non-aqueous solvent include ethers such as diethyl ether, dibutyl ether, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, diethylene glycol monomethyl ether, diethylene glycol monoethyl ether, diethylene glycol monobutyl ether, diethylene glycol dimethyl ether and ethylene glycol phenyl ether; amides such as formamide, N-methylformamide, N,N-dimethylformamide, N-ethylformamide, N,N-diethylformamide, N-methylacetamide, N,N-dimethylacetamide, N-ethylacetamide, N,N-diethylacetamide, N,N-dimethylpropionamide and hexamethylphosphoryl amide; sulfur-containing compounds such as dimethyl sulfoxide and sulfolane; dialkyl ketones such as
• esters such as ethylene carbonate, butylene carbonate, diethyl carbonate, dimethyl carbonate, propylene carbonate, vinylene carbonate and ⁇ -butyrolactone; ethers such as dioxolan, diethyl ether and diethoxyethane; dimethyl sulfoxide; acetonitrile; and tetrahydrofuran.
• carbonate-based non-aqueous solvents such as ethylene carbonate and propylene carbonate are preferably employed. These solvents may be employed singly or in combination of two or more species.
• a lithium salt is employed as an electrolytic salt.
• lithium salts generally known to serve as an electrolytic salt include LiClO 4 , LiBF 4 , LiPF 6 , LiAlCl 4 , LiSbF 6 , LiSCN, LiCl, LiCF 3 SO 3 , LiCF 3 CO 2 and LiN(CF 3 SO 2 ) 2 .
• polymer solid electrolyte examples include electrolytes obtained by adding the aforementioned electrolyte salts to, for example, polyethylene oxide derivatives and polymers containing the derivatives, polypropylene oxide derivatives and polymers containing the derivatives, phosphoric acid ester polymers, and polycarbonate derivatives and polymers containing the derivatives.
• Mean roundness of the carbon material was measured by use of a flow particle image analyzer FPIA-2100 (product of Sysmex Corporation), as described below.
• a measurement sample was subjected to cleaning (removal of micro dust) by use of a 106 ⁇ m filter.
• the sample (0.1 g) was added to ion-exchange water (20 mL), and an anionic/nonionic surfactant (0.1 to 0.5 mass %) was added to the resultant mixture so as to uniformly disperse the sample in the mixture, thereby preparing a measurement dispersion containing the sample.
• Dispersion of the sample was carried out for five minutes by use of ultrasonic cleaner UT-105S (product of Sharp Manufacturing Systems Corporation).
• the term “circle-equivalent diameter” refers to the diameter of a true circle having an area equal to the actual projection area of a particle that has been obtained from a photograph of the particle.
• the roundness of the particle is obtained by dividing the circumference of a circle as calculated from the circle-equivalent diameter by the actual peripheral length of the projected particle. For example, a particle having a true round shape has a roundness of 1, whereas a particle having a more complicated shape has a roundness of a smaller value.
• the mean roundness of particles is an average of the roundness values of the particles respectively measured by the above-described method.
• the average particle size was measured by use of a particle size distribution analyzer by laser diffraction scattering (Microtrac HRA, product of Nikkiso Co., Ltd.).
• the specific surface area was measured by use of a specific surface area measuring apparatus (NOVA-1200, product of Yuasa Ionics Inc.) by means of the BET method, which is generally employed for specific surface area measurement.
• NOVA-1200 product of Yuasa Ionics Inc.
• a predetermined amount of carbon fiber was added to 1 mass % aqueous CMC solution (Daicel 2200, product of Daicel Chemical Industries, Ltd.) at room temperature, followed by stirring at a rotation speed of 25 rpm for 30 minutes, to thereby disperse the carbon fiber in the solution.
• a predetermined amount of carbonaceous negative electrode active substance powder was added to the resultant dispersion, followed by stirring for 30 minutes.
• 40 mass % aqueous SBR dispersion (BM400B, product of Zeon Corporation) was added to the resultant mixture, followed by stirring for 15 minutes, to thereby prepare a carbonaceous negative electrode material composition.
• a predetermined amount of carbon fiber was added to 1 mass % aqueous CMC solution (Daicel 2200, product of Daicel Chemical Industries, Ltd.) at room temperature, followed by stirring at a rotation speed of 25 rpm for 30 minutes, to thereby disperse the carbon fiber in the solution. Subsequently, a predetermined amount of carbonaceous negative electrode active substance powder was added to the resultant dispersion, followed by stirring for 30 minutes.
• a predetermined amount of 1 mass % aqueous CMC solution as described above was added to the resultant mixture for regulation of the viscosity thereof, and then 40 mass % aqueous SBR dispersion (BM400B, product of Zeon Corporation) was added to the resultant mixture, followed by stirring for 15 minutes, to thereby prepare a carbonaceous negative electrode material composition.
• BM400B product of Zeon Corporation
• a stirring-blade-equipped general-purpose mixer (T.K. HIVIS MIX, product of Tokushu Kikakogyo Co., Ltd.), at room temperature, a predetermined amount of carbonaceous negative electrode active substance powder was added to 1 mass % aqueous CMC solution (Daicel 2200, product of Daicel Chemical Industries, Ltd.) at room temperature, followed by stirring at a rotation speed of 25 rpm for 30 minutes. Subsequently, a predetermined amount of carbon fiber was added to the resultant mixture, followed by stirring for 30 minutes, to thereby disperse the carbon fiber in the mixture. Thereafter, 40 mass % aqueous SBR dispersion (BM400B, product of Zeon Corporation) was added to the resultant mixture, followed by stirring for 15 minutes, to thereby prepare a carbonaceous negative electrode material composition.
• BM400B product of Zeon Corporation
• a stirring-blade-equipped general-purpose mixer (T.K. HIVIS MIX, product of Tokushu Kikakogyo Co., Ltd.), a predetermined amount of carbonaceous negative electrode active substance powder was added to 1 mass % aqueous CMC solution (Daicel 2200, product of Daicel Chemical Industries, Ltd.) at room temperature, followed by stirring for 30 minutes. Thereafter, 40 mass % aqueous SBR dispersion (BM400B, product of Zeon Corporation) was added to the resultant mixture, followed by stirring for 15 minutes, to thereby prepare a carbonaceous negative electrode material composition.
• BM400B product of Zeon Corporation
• each of the above-prepared carbonaceous negative electrode material compositions was applied onto a rolled copper foil (product of Nippon Foil Mfg. Co., Ltd.) (18 ⁇ m) so as to attain a predetermined thickness.
• the resultant product was dried under vacuum at 120° C. for one hour, and then subjected to punching, to thereby form an electrode having a size of 18 mm ⁇ .
• the thus-formed electrode was sandwiched by super-steel-made pressing plates, and then subjected to pressing such that a pressure of 1 ⁇ 10 3 to 3 ⁇ 10 3 kg/cm 2 was applied to the electrode, to thereby attain a thickness of about 100 ⁇ m and a target electrode density (1.6 g/cm 3 or 1.8 g/cm 3 ).
• the resultant electrode was dried in a vacuum drying apparatus at 120° C. for 12 hours, and was employed as a carbonaceous negative electrode sheet for battery evaluation.
• LiCoO 2 (a positive electrode active substance), Acetylene Black (product of Denki Kagaku Kogyo Kabushiki Kaisha), and vapor grown graphite fiber (product of Showa Denko K.K.) were dry-mixed in proportions by mass of 93:1:2 at 10,000 rpm (one minute ⁇ twice) by use of a high-speed table mixer equipped with blades (IK mixer).
• KF Polymer L1320 N-methylpyrrolidone (NMP) solution containing 12 mass % polyvinylidene fluoride (PVDF), product of Kureha Chemical Industry Co., Ltd.
• NMP N-methylpyrrolidone
• PVDF polyvinylidene fluoride
• NMP was further added to the positive electrode material composition so as to regulate the viscosity of the composition. Subsequently, by use of a doctor blade, the resultant composition was applied onto a rolled Al foil (product of Showa Denko K.K.) (25 ⁇ m) so as to attain a predetermined thickness. The resultant product was dried under vacuum at 120° C. for one hour, and then subjected to punching, to thereby form an electrode having a size of 18 mm ⁇ .
• a rolled Al foil product of Showa Denko K.K.
• the thus-formed electrode was sandwiched by super-steel-made pressing plates, and then subjected to pressing such that a pressure of 1 ⁇ 10 3 kg/cm 2 was applied to the electrode, to thereby attain a thickness of about 100 ⁇ m and an electrode density of 3.3 g/cm 3 .
• the resultant electrode was dried in a vacuum drying apparatus at 120° C. for 12 hours, and was employed for evaluation.
• PC Propylene carbonate
• the volume resistivity (25° C.) of each negative electrode sheet was measured by means of the four-probe method.
• a three-electrode cell was produced through the below-described procedure in an atmosphere of dried argon having a dew point of ⁇ 80° C. or lower.
• a separator polypropylene-made microporous film (Celgard 2400), 25 ⁇ m) was sandwiched by the copper-foil-coated negative electrode sheet prepared above in (1) and the Al-foil-coated positive electrode sheet prepared above in (3), to thereby form a laminate.
• a metallic lithium foil 50 ⁇ m serving as a reference electrode was laminated in a manner similar to that described above. Thereafter, an electrolytic solution was added to the cell, and the resultant cell was employed for testing.
• the electrolytic solution was prepared by dissolving LiPF 6 (1 mol/liter), serving as an electrolyte, in a mixture of EC (ethylene carbonate) (8 parts by mass) and DEC (diethyl carbonate) (12 parts by mass).
• Constant-current constant-voltage charging/discharging test was performed at a current density of 0.6 mA/cm 2 (corresponding to 0.3 C).
• Constant-current (CC) charging was performed at 0.6 mA/cm 2 while voltage was increased from rest potential to 4.2 V. Subsequently, constant-voltage (CV) charging was performed at 4.2 V, and charging was stopped when the current value decreased to 25.4 ⁇ A.
• CV constant-voltage
• CC discharging was performed at 0.6 mA/cm 2 (corresponding to 0.3 C), and was cut off when a voltage of 2.7 V was attained.
• SCMG-1 Spherical Graphite Particles (Product of Showa-Denko K.K.)
• SCMG-2 Spherical Graphite Particles (Product of Showa Denko K.K.)
• MCMB Mesophase Spherical Graphite Particles (Product of Osaka Gas Chemicals Co., Ltd.)
• VG-A Vapor Grown Carbon Fiber (Non-Graphitized, Fired at 1,200° C.)
• VG-B Vapor Grown Graphite Fiber (Addition of 2% Boron During Graphitization)
• VG-H Vapor Grown Graphite Fiber (Milled by Use of a Jet Mill)
• VG-O Vapor Grown Graphite Fiber (Oxidized at 500° C.)
• VG-F Vapor Grown Graphite Fiber
• VG-T Vapor Grown Graphite Fiber
• BM-400B 40 Mass % Aqueous Dispersion (Product of Zeon Corporation)
• Carbonaceous negative electrodes were prepared from compositions shown in Table 1 (negative electrode density: 1.6 g/cm 3 in Table 1-1 and 1.8 g/cm 3 in Table 1-2) by means of methods shown in Table 1. Each of the thus-prepared negative electrodes was subjected to measurement of specific resistance and electrolytic solution permeation rate. Subsequently, a Li ion cell for testing was produced using each negative electrode in combination with the above-prepared positive electrode, and the thus-produced cell was subjected to measurement and evaluation in terms of negative electrode capacity density and (charging/discharging) cycle characteristics.
• a negative electrode produced from a negative electrode material composition prepared by means of any of the methods (A) through (D), (A-2), and (A-3) exhibits improved electrolytic solution permeability as compared with the case of a negative electrode produced from a negative electrode material composition containing no carbon fiber, and a battery produced by use of the former negative electrode exhibits improved cycle characteristics.
• a negative electrode produced from a negative electrode material composition prepared by means of any of the methods (A) through (D) exhibits improved specific resistance, electrolytic solution permeability, and capacity density, and a battery produced by use of the negative electrode exhibits considerably improved cycle characteristics.
• the negative electrode material for a lithium battery of the present invention contains SBR as a binder, and carbon fiber having a fiber diameter of 1 to 1,000 nm, highly dispersed in the binder and serving as an electrically conductive additive.
• the negative electrode material enables to produce a battery having excellent characteristics; i.e., low electrode resistance, high electrode strength, excellent electrolytic solution permeability, high energy density, and good high-speed charging/discharging performance.

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• 2004
  • 2004-12-28 KR KR1020087007714A patent/KR20080040049A/ko not_active Ceased
  • 2004-12-28 KR KR1020067013071A patent/KR100855595B1/ko not_active Expired - Fee Related
  • 2004-12-28 WO PCT/JP2004/019835 patent/WO2005067081A1/en not_active Ceased
  • 2004-12-28 JP JP2004378431A patent/JP4084353B2/ja not_active Expired - Lifetime
  • 2004-12-28 US US10/585,205 patent/US20070275302A1/en not_active Abandoned
  • 2004-12-28 CN CNB2004800399143A patent/CN100541870C/zh not_active Expired - Fee Related
  • 2004-12-28 CN CN2008101461616A patent/CN101373827B/zh not_active Expired - Fee Related
• 2011
  • 2011-04-19 US US13/089,588 patent/US8388922B2/en not_active Expired - Fee Related