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
  • H01M4/13—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
  • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
  • H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
• • 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
  • H01M4/139—Processes of manufacture
  • H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
• • 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
  • H01M4/139—Processes of manufacture
  • H01M4/1393—Processes of manufacture of 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
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/05—Accumulators with non-aqueous electrolyte
  • H01M10/052—Li-accumulators
• • 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
  • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
  • H01M4/624—Electric conductive fillers
• • 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
  • H01M4/624—Electric conductive fillers
  • H01M4/625—Carbon or graphite
• • 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
• • 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

Definitions

• the present invention relates to electrodes for lithium ion batteries and, more particularly, to electrodes that include active composite materials dispersed in a porous conductive polymer matrix having channels for lithium ion diffusion.
• Lithium ion batteries are used in numerous portable electronic devices such as mobile telephones and laptop computers. Although lithium ion batteries have adequate characteristics for portable electronic devices, batteries for electronic vehicles typically require higher capacity than those currently available. Different approaches have been used to increase the capacity of lithium ion batteries, including formation of porous anodes and composite anodes are disclosed in U.S. Patent Publication Nos. 2011/0114254, 2008/0237536, 2010/0021819, 2010/0119942, 2010/0143798, 2010/0285365, and 2010/0062338, WO 2008/021961, and EP 1 207 572. While such anodes can improve battery performance, there remains a need in the art for improved lithium ion battery electrodes that can be easily and
• the present invention relates to a composite lithium ion battery electrode formed from an active composite material dispersed in a conductive porous matrix formed over a current collector.
• the active composite material includes nano-clusters of an active material dispersed on a conductive skeleton structure.
• the active material is selected from fine particles including Sn, Al, Si, Ti and C and having a particle size ranging from approximately 1 nanometers to approximately 10 microns.
• the conductive skeleton includes at least a conductive polymer or a conductive filament.
• the active material is dispersed on the conductive skeleton through an in situ polymerization process or a chemical grafting process.
• the conductive porous matrix includes a conductive polymeric binder and lithium ion diffusion channels created by a pore-forming material during mixture of the active composite material in the conductive porous matrix. Conductive particles are further included in the conductive porous matrix.
• FIG. 1 is a schematic representation of a composite lithium ion battery electrode according to one embodiment of the present invention.
• FIG. 2 is a schematic representation of an active composite material used in the electrode of FIG. 1.
• FIG. 1 depicts a composite lithium ion battery electrode 10 according to the invention.
• the electrode includes a current collector 20, typically a conductive metal plate such as copper.
• an active composite material 30 dispersed in a conductive porous matrix 40.
• the active composite material includes fine particles of an active material 32, best seen in FIG. 2, dispersed on a conductive skeleton structure 34.
• Active material 32 has fine particulate structure with a particle size ranging from approximately 1 nanometers to approximately 10 microns.
• the particles include metal-based materials such as Sn, Al, Si, Ti or carbon-based materials such as graphite, carbon fiber, carbon nanotube (CNT) or combinations thereof.
• metal-based materials such as Sn, Al, Si, Ti or carbon-based materials such as graphite, carbon fiber, carbon nanotube (CNT) or combinations thereof.
• CNT carbon nanotube
• Conductive skeleton 34 includes at least a conductive polymer or a conductive filament, with the active material 32 being dispersed on the conductive skeleton through an in situ polymerization process or a chemical grafting process (to be discussed below). By segregating the active material to the conductive skeleton in this manner, agglomeration of the active material in the porous conductive matrix 40 is avoided consequently increasing the manufacturability of the present invention for large-scale production.
• Exemplary conductive polymers for conductive skeleton 34 include pyrrole, anilline, or thiofuran; alternatively, conductive filaments such as carbon nanotubes or carbon nanofibers can be used as the skeleton 34.
• the open structure of skeleton 34 combined with dispersed active material 32 creates micro-diffusion channels for lithium ions, enhancing the intercalation of active material 32.
• the capacity of the resultant battery is increased through the structure of the active composite 30.
• the micro-channels also help accommodate the expansion and contraction of the active material particles as lithium ions are inserted and removed during charging and discharging.
• the conductive porous matrix 40 includes a conductive polymeric binder and lithium ion diffusion channels 42 created by a pore-forming material during mixture of the active composite material in the conductive porous matrix (to be discussed below).
• the conductive polymeric binder is selected from one or more of modified pyrrole, aniline, and thiofuran or other suitably conductive polymers, particularly those that have an electrical conductivity of greater than about 10 S/cm.
• the lithium ion channels 42 advantageously provide lithium transport access to the active material 32. Further, channels 42 help accommodate the expansion and contraction of the overall composite electrode as lithium ions are added or removed during charging and discharging, respectively. In one embodiment, the channels are selected to have a volume percentage of less than 5% of the electrode.
• At least one type of conductive particle such as particles 50 or 60 are included in the conductive porous matrix.
• particles 50 are graphite and particles 60 are carbon black; however, other conductive particles may also be selected for use in porous matrix 40.
• Formation of active composite material 30 includes precipitation of an active material 32 such as Sn, Al, Si, or Ti from a suitable precursor solution such as Sn, Al, Si, or Ti precursor salts (nitrates, carbonates, etc.) Precursor solutions are mixed with additives such as sulfonates, imines, and nitrides followed by dehydration to obtain a precipitate precursor powder having a particle size on the order of 1- 100 microns.
• an active material 32 such as Sn, Al, Si, or Ti from a suitable precursor solution
• a suitable precursor solution such as Sn, Al, Si, or Ti precursor salts (nitrates, carbonates, etc.)
• Precursor solutions are mixed with additives such as sulfonates, imines, and nitrides followed by dehydration to obtain a precipitate precursor powder having a particle size on the order of 1- 100 microns.
• Thermal treatment of the precipitate at a temperature of less than 1000°C in air or an inert environment produces a reduced/calcined powder of the active material; grinding and milling reduces the particle size to a range of less than 100 microns, preferably approximately 1 nm to 10 microns. This technique facilitates reproducible and cost-effective mass production of the electrode active material.
• a dispersed active material 32 on a skeleton structure 34 several techniques may be selected.
• carbon fibers, nanotubes, and/or rods are surface-treated to produce a -COOH group bound to the carbon-based skeleton.
• the fine particles of active material are mixed with additives such as APTES
• the carbon skeleton structure is mixed with a reagent such as EDC
• the carbon-based skeleton with -COOH groups is mixed in solution with the activated active material powder to chemically bind the active material to the carbon-based skeleton.
• in-situ polymerization is used.
• the fine particles of Sn, Al, Si, or Ti are mixed with an additive such as sulfonic acid, sodium salt, or sulfonates.
• This mixture is added to a polymerization solution including pyrrole, aniline, or thiofuran; an additive selected from materials such as ferric trichloride or ammonium sulfate is added.
• Polymerization preferable occurs at a temperature of less than approximately 10°C in a de-aerated solution.
• the resulting active material composite material includes the active material dispersed in a porous skeleton.
• the fine particles of active material are dispersed on the substrate skeleton.
• the skeleton can then be incorporated in the conductive porous matrix without agglomeration of the active material particles, ensuring a large surface area of active material for lithium intercalation.
• a conductive polymer such as one or more of pyrrole, aniline, or thiofuran is surface-modified to create a binder that will bind with the active material composite.
• the active material composite, the conductive polymer binder and a pore-forming agent that is either a pore-forming material and/or vesicant material such as carbonate salt, (NH 4 ) 2 CC>3, or C 2 H 4 N 4 0 2 are mixed together, along with further conductive particles such as particles 50 and/or 60 (graphite, carbon black).
• the mixture is applied to current collector 20 such as a copper plate and the gas is evacuated and the solvent evaporated, leaving behind the porous conductive matrix with the active material composite dispersed therein.
• the pore-forming material(s) result in in-situ pore formation, creating continuous interconnecting porous channels for enhancing lithium ion transport.

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• 2011
  • 2011-08-19 CN CN201180001321.8A patent/CN102439771B/zh not_active Expired - Fee Related
  • 2011-08-19 WO PCT/CN2011/078672 patent/WO2013026190A1/en active Application Filing
• 2012
  • 2012-10-30 HK HK12110826.5A patent/HK1173558A1/zh not_active IP Right Cessation

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