US20050037262A1 - Cathode material for polymer batteries and method of preparing same - Google Patents

Cathode material for polymer batteries and method of preparing same Download PDF

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US20050037262A1
US20050037262A1 US10/902,174 US90217404A US2005037262A1 US 20050037262 A1 US20050037262 A1 US 20050037262A1 US 90217404 A US90217404 A US 90217404A US 2005037262 A1 US2005037262 A1 US 2005037262A1
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positive electrode
polymer
solid particles
mix
solid
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Alain Vallee
Paul-Andre Lavoie
Patrick Leblanc
Regis Gagnon
Fabrice Regisser
Dany Brouillette
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Bathium Canada Inc
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Assigned to AVESTOR LIMITED PARTNERSHIP reassignment AVESTOR LIMITED PARTNERSHIP ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LAVOIE, PAUL-ANDRE, BROUILLETTE, DANY, REGISSER, FABRICE, GAGNON, REGIS, VALLEE, ALAIN, LEBLANC, PATRICK
Publication of US20050037262A1 publication Critical patent/US20050037262A1/en
Priority to US11/836,575 priority patent/US8241541B2/en
Assigned to BATHIUM CANADA INC. reassignment BATHIUM CANADA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AVESTOR LIMITED PARTNERSHIP
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    • 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
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/20—Compounding polymers with additives, e.g. colouring
    • C08J3/205—Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase
    • H—ELECTRICITY
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    • H01M4/04—Processes of manufacture in general
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    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
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    • H01M4/0411—Methods of deposition of the material by extrusion
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    • H01M4/04—Processes of manufacture in general
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    • H01M4/0416—Methods of deposition of the material involving impregnation with a solution, dispersion, paste or dry powder
    • H—ELECTRICITY
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    • H01M4/04—Processes of manufacture in general
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    • H01M4/0419—Methods of deposition of the material involving spraying
    • H—ELECTRICITY
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    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0483—Processes of manufacture in general by methods including the handling of a melt
    • H—ELECTRICITY
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    • 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
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    • H01M4/36—Selection of substances as active materials, active masses, active liquids
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    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
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    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H—ELECTRICITY
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    • 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
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    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028—Positive electrodes
    • H—ELECTRICITY
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    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
    • 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
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • 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
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • 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
    • 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 generally to polymer batteries and more specifically to the preparation of cathode materials for polymer batteries.
  • Lithium/polymer electrolyte batteries are manufactured by superposing three main types of films: a film of metallic lithium, a film of an electrolyte comprising a polymer and a lithium salt, and a film of a positive electrode. Each of these films has a thickness between 5 and 200 ⁇ m, for a total thickness of 100 to 300 ⁇ m for the elementary film of battery.
  • the film of positive electrode is typically prepared by coating or extrusion, on a support film or directly on an aluminum foil or metallized plastic film, used as an electrical current collector, a dispersion containing an electrochemically active material such as a transitional metal oxide, carbon black and/or graphite to ensure electronic conduction, a polymer-salt electrolyte to ensure ionic conduction and the mechanical bond between the solid particles mentioned above and most often appropriate solvent or solvent mixtures which are evaporated totally or partially during the coating process or extrusion process.
  • an electrochemically active material such as a transitional metal oxide, carbon black and/or graphite to ensure electronic conduction
  • a polymer-salt electrolyte to ensure ionic conduction and the mechanical bond between the solid particles mentioned above and most often appropriate solvent or solvent mixtures which are evaporated totally or partially during the coating process or extrusion process.
  • the mixing and blending of the electrochemically active material, the electronic conduction additives, the polymer binder and the lithium salt forming the positive electrode is done in a compatible solvent or solvent mixtures that will dissolve the salt and the polymer immediately prior to coating.
  • the solution is then coated through a coating head in the form of a thin film.
  • the solvent is then evaporated and recovered, usually by condensation, for obvious environmental reasons.
  • the mixing and blending of the electrochemically active material, the electronic conduction additives, the polymer binder and the lithium salt forming the positive electrode material is carried out by the screw or screws of the extruder itself.
  • the polymer and lithium salt are generally introduced first in the extruder and melted followed by the introduction downstream from the polymer-salt melt of the electrochemically active material and the electronic conduction additives which are mixed and dispersed in the polymer-salt melt by the screw or screws of the extruder.
  • an appropriate solvent or solvent mixtures is added to reduce the viscosity of the melt and to help in the mixing of the solid particles of active material and electronic conduction additives, the solvent(s) which must be evaporated after the positive electrode material is extruded onto a support film, directly on a current collector or as a free-standing film.
  • a twin screw extruder is used for its superior ability over a single screw extruder for mixing and blending the various components of the positive electrode material.
  • the mixing and blending of the various components of positive electrode material is sometime inadequate. Specifically, the solid particles (active material and electronic conduction additive particles) are not properly mixed and dispersed, resulting in a less homogenous positive electrode material resulting in poor electrochemical performance of the electrochemical cells.
  • the use of a twin screw extruder involves high shear events which may potentially degrade the polymer thereby further decreasing the electrochemical performance of the cell during the cycles of charge and discharge.
  • the invention provides a pre-mix of positive electrode material in solid transportable form comprising a polymer and solid particles of electrochemically active material and preferably an electronic conductive additive.
  • the pre-mix of positive electrode material in solid transportable form comprises a polymer and at least 40% of solid particles of electrochemically active material and electronic conductive additives.
  • the pre-mix of positive electrode material comprises a alkali metal salt either dissolved or dispersed in the polymer.
  • the pre-mix of positive electrode material is in the form of small to medium size chunks, pucks, carrots, stripes, etc. or in pellet, granule, powder or flake form.
  • the pre-mix of positive electrode material in solid transportable form comprises a polymer and between 40%/wt and 80%/wt of solid particles of electrochemically active material and electronic conductive additives.
  • the polymer of the pre-mix of positive electrode material may contain a small amount of water within the range of 1000 ppm to 10,000 ppm.
  • the active material of the cathode may be selected from lithium cobalt/nickel oxide, lithium manganese oxide (LiMn 2 O 4 ), layered lithium manganese nickel oxide and their derivatives, mixtures and analogs for so-called 4V cathodes or among cathodes discharging below 4V such as phosphates or other polyanions of transition metals such as LiFePO 4 and Nasicon structures, also including V 2 O 5 , and Li x V3O8.
  • the alkali metal salt(s) may be for example salts based on lithium trifluorosulfonimide (LiTFSi) as described in U.S. Pat. No. 4,505,997, LIPF 6 , LiBF 4 , LiSO 3 CF 3 , LiClO 4 , and LiSCN, etc. and combinations thereof.
  • the nature of the salt or of the active material is not a limitation of the present invention.
  • the invention also provides a process for preparing a pre-mix positive electrode in solid transportable form comprising the steps of:
  • the invention also provides for a process for preparing a pre-mix positive electrode in transportable solid form comprising the steps of:
  • the invention also provides a process for extruding a thin positive electrode sheet having at least 40%/wt solid content for a lithium polymer battery through a single or twin screw extruder, said process comprises the steps of:
  • the invention also provides a process for extruding a thin positive electrode sheet having at least 40%/wt of solid content for a lithium polymer battery through a single or twin screw extruder, the process comprises the steps of:
  • the invention also provides a process for extruding a thin positive electrode sheet having at least 40%/wt of solid content for a lithium polymer battery through a single or twin screw extruder, the process comprises the steps of:
  • the invention also provides a process for making a positive electrode having at least 40%/wt of solid content for a lithium polymer battery, the process comprising the steps of:
  • the invention further provides an electrochemical generator having a electrode thin film obtained by the process of extruding pre-mix positive electrode material.
  • FIG. 1 is a flow chart illustrating the various step for preparing the cathode material according to one embodiment of the invention.
  • FIG. 2 is a flow chart illustrating the various step for preparing the cathode material according to a second embodiment of the invention.
  • a solution of polymer in solvent or mixture of solvents is mixed with solid particles of active cathode material and electronic conductive additives.
  • the polymer solution could be obtained by the dissolution of a polymer in a solvent(s) or directly at the outlet of a polymerization reactor if the polymer is already in solution.
  • the active cathode material and electronic conductive additives have been blended together prior to introduction into the polymer solution.
  • the active cathode material and the electronic conductive additives may be introduced separately into the polymer solution.
  • the polymer solution and the solid particles are mixed in any type of mixing device(s) capable of proper dispersion for a sufficient time to obtain a good dispersion of the solid particles in the polymer solution and/or in any equipment that homogenize the mixture in order to achieve the same dispersion.
  • the mixing process may be done in one step in a single mixing device or through multiple steps through a two or more mixing device with different mixing properties. Further solvent may be added if necessary to the mixture to facilitate the dispersion of the solid particles.
  • Solvent typically used in this process are polar or non-polar solvents into which the polymer is soluble such as Toluene, Acetonitrile, Methanol, Acetone, Benzene, and Methyl Ethyl Ketone (MEK) to name a few.
  • the polymer may be an homo- or co-polymer, may comprise two or more polymers, and may be cross linkable or not.
  • Anti-oxidants and other additives such as stabilizers, dispersion agents and fillers may be added to the polymer solution as necessary.
  • the solvent or solvents are evaporated by any means known to those skilled in the art such as an evaporator or spray dryer amongst others, to obtain a polymer-solid particles mixture adapted for a coating process or an extrusion process.
  • the polymer-solid particles mixture is then transformed into a transportable solid such as small or medium size chunks, carrots pucks or stripes, or granules, powder, pellets or flakes.
  • a transportable solid such as small or medium size chunks, carrots pucks or stripes, or granules, powder, pellets or flakes.
  • the polymer-solid particles mixture is introduced in a melting and pumping device such as extruder, where the polymer is melted and the composite is further mixed, then pumped into a cooling device where it hardens.
  • This hardened mixture is brought to a mechanical cutting device that transforms the hardened polymer-solid particles mixture into the desired shape such as a pelletizer which transforms the hardened polymer-solid particles mixture into pellets of a few millimeters in length and width or diameter.
  • a mechanical cutting device that transforms the hardened polymer-solid particles mixture into the desired shape
  • the polymer-solid particles mixture still in solution in the solvent is spay dried through a nozzle which yields a polymer-solid particles mixture in the form of granules, powder or flakes.
  • the pre-mix cathode material in chunks, carrots, pucks, granules, pellets or powder form is then ready for shipment or for processing by extrusion or coating to be transformed into thin films.
  • the term solid transportable form includes solids of any shapes which can be safely shipped in containers such as chunks, pucks, carrots, stripes, pellets, granules, powder and flakes.
  • the pre-mix cathode material in transportable solid form is stored and/or transported in a controlled environment. Specifically, it is preferable to maintain the temperature of the pre-mix cathode material in transportable solid form below 30° C. to prevent unwanted degradation of the performance of the cathode material.
  • the pre-mixed cathode material is introduced in a first feed throat of either a single (reciprocating or non-reciprocating) or twin screw extruder where it begins to melt.
  • a second feed throat downstream from the first feed throat is added an alkali metal salt which is dissolved and mixed in the melted cathode material.
  • the alkali metal salt may be introduced first and the pre-mix cathode material second.
  • the alkali metal salt provides ionic conductivity to the cathode material.
  • the cathode material including the dissolved alkali metal salt is extruded through a die as a thin sheet of between 5 and 200 ⁇ m thick, either directly onto a substrate support such as a metal foil current collector or a plastic film, or as a self-supporting sheet which is later on laminated onto a current collector.
  • the alkali metal salt(s) may be for example salts based on lithium trifluorosulfonimide (LiTFSi) as described in U.S. Pat. No. 4,505,997, LIPF 6 , LiBF 4 , LiSO 3 CF 3 , LiClO 4 , and LiSCN, etc. and combination thereof.
  • LiTFSi lithium trifluorosulfonimide
  • the nature of the salt is not a limitation of the present invention.
  • the pre-mixed solid particles are further mixed and blended and are therefore thoroughly mixed and dispersed resulting in an homogenous positive electrode material having a optimal energy content and excellent electrochemical performance or improved cyclability of the electrochemical cells produced thereafter.
  • the cathode material has been previously mixed and blended allows the use of an extruder having a screw designed to produce low shear as opposed to the high shear previously required to thoroughly mix and blend the cathode material. This results in a less energetic mixing and melting of the polymer that avoids potential degradation of the polymer with the result of improving the electrochemical performance of the electrochemical cells produced thereafter during the cycles of charge and discharge.
  • the pre-mixing of the solid particles into a polymer solution also enables an increased proportion of solid particles and specifically of active material into the resulting cathode which may contain up to 80%/wt of active material.
  • the polymer included in the pre-mixed cathode material in solid form may comprise a small amount of water such as between 1000 ppm and 10,000 ppm and preferably within the range of 2000 ppm to 5000 ppm, in order to adjust the rheological properties of the pre-mixed cathode material, for example, by lowering the viscosity of the material and therefore improving the processability the pre-mixed cathode material through an extruder.
  • FIG. 2 illustrates a variant of the process previously described where the polymer solution is prepared with a polar solvent into which both the polymer and the alkali metal salt are soluble as is well known in the art.
  • Polar solvents typically used in this process are Acetonitrile, Methanol, Acetone, and Methyl Ethyl Ketone (MEK) to name a few.
  • MEK Methyl Ethyl Ketone
  • the mixture of polymer-salt and solid particles is mixed in any type of mixing device(s) or homogenizer capable of proper dispersion for a sufficient time to obtain a good dispersion of the solid particles in the polymer-salt solution. Thereafter the solvent is removed through evaporation or other means from the mixture, and the remaining polymer-salt/solid particles mixture is transformed into a transportable solid such as small to medium size chunks pucks, carrots, stripes, granules, powder, pellets or flakes as previously described.
  • a transportable solid such as small to medium size chunks pucks, carrots, stripes, granules, powder, pellets or flakes as previously described.
  • the transportable solid pre-mix cathode material may be mixed into a substance like fumed silica which is compatible with the electrochemistry of the cells and microscopically separates the transportable solid, especially the pellets, granules, powder or flakes to inhibit their adhesion to each other.
  • the pre-mix polymer-salt/solid particles When brought to the extruder, or any types of melting and pumping device, for processing into thin sheets of between 5 and 200 ⁇ m thick, the pre-mix polymer-salt/solid particles (active material and electronic conduction additive particles) are further mixed and blended and are therefore thoroughly dispersed resulting in excellent electrochemical performance or improved cyclability of the electrochemical cells produced thereafter.
  • the pre-mixed cathode material in solid form is introduced into a feed throat of either a single (reciprocating or non-reciprocating) or twin screw extruder where it is melted and extruded through a die as a thin sheet of between 5 and 200 ⁇ m thick, either directly onto a substrate support such as a metal foil current collector or a plastic film, or as a self-supporting or free-standing sheet which is later on laminated onto a current collector.
  • the solid particles are therefore thoroughly mixed resulting in an homogenous positive electrode material having a optimal energy content in terms of volume as well as of mass.
  • the cathode material has been previously mixed and blended allows the use of an extruder having a screw designed to produce low shear as opposed to the high shear previously required to thoroughly mix and blend the cathode material. This results in a less energetic mixing and melting of the polymer that avoids potential degradation of the polymer with the result of improving the electrochemical performance of the electrochemical cells produced thereafter during the cycles of charge and discharge.
  • the polymer solution is prepared with a solvent or solvent mixture, into which the polymer is soluble but the alkali metal salt is not soluble, such as a non-polar solvent like Toluene or Benzene.
  • a solvent or solvent mixture into which the polymer is soluble but the alkali metal salt is not soluble, such as a non-polar solvent like Toluene or Benzene.
  • Toluene or Benzene To this polymer solution is added all solid particles of active cathode material and electronic conductive additives already pre-blended together and the alkali metal salt.
  • the alkali metal salt is not dissolved but dispersed into the polymer solution.
  • the mixture of polymer, salt and solid particles is mixed in any type of mixing device or devices (one or more) capable of good dispersion for a sufficient time to obtain solid particles and salt particles that are thoroughly dispersed within the polymer solution.
  • the solvent is removed through evaporation or other means from the mixture, and the remaining polymer
  • the alkali metal salt may be dissolved in the non-polar solvent.
  • raising the temperature of the mixture of polymer, salt and solid particles in solution in the non-polar solvent may enable the salt to dissolve in the polymer solution.
  • the mixture of polymer, salt and solid particles in solution in the non-polar solvent may be heated to a temperature of about 40° C. or more during mixing to enable the salt to dissolve in the polymer solution.
  • a combination of two or more solvents one of which being a non-polar solvent, may enable the salt to dissolve in the polymer solution. Thereafter the solvent(s) is/are removed through evaporation or other means from the mixture, and the remaining polymer/salt/solid particles mixture is transformed into a transportable solid such as the shapes or forms previously described.
  • the pre-mix polymer/salt/solid particles When brought to the extruder for processing into thin sheets of between 5 and 200 ⁇ m thick, the pre-mix polymer/salt/solid particles (active material and electronic conduction additive particles) are further mixed and blended and are therefore thoroughly mixed and dispersed resulting in excellent electrochemical performance or improved cyclability of the electrochemical cells produced thereafter.
  • the pre-mixed cathode material is introduced in a feed throat of either a single (reciprocating or non-reciprocating) or twin screw extruder where the polymer is melted, the alkali metal salt is dissolved in the polymer and the solid particles are re-dispersed into the polymer-salt solution.
  • the cathode material is extruded through a die as a thin sheet of between 5 and 200 ⁇ m thick, either directly onto a substrate support such as a metal foil current collector or a plastic film, or as a self-supporting sheet which is later on laminated onto a current collector.
  • a solution of polymer in solvent is mixed with solid particles of active cathode material only.
  • the mixture of polymer and solid particles of active cathode material is mixed in any type of mixing device(s) capable of good dispersion for a sufficient time to obtain solid particles that are thoroughly dispersed within the polymer solution.
  • the solvent is removed through evaporation or other means from the mixture, and the remaining polymer/solid particles of active cathode material mixture is transformed into a transportable solids as previously described.
  • the pre-mix polymer/solid particles (active material only) in solid form is introduced into a feed throat of the extruder, the alkali metal salt and the electronic conduction additive are fed into other feed throat(s); the various components are mixed and dispersed or dissolved in the molten polymer.
  • the alkali metal salt is dissolved in the polymer and the solid particles (active material and electronic conductive additives) are re-dispersed into the polymer-salt solution.
  • the cathode material is extruded through a die as a thin sheet of between 5 and 200 ⁇ m thick, either directly onto a substrate support such as a metal foil current collector or a plastic film, or as a self-supporting sheet which is later on laminated onto a current collector.
  • a solution of polymer in solvent is mixed with solid particles of electronic conductive additives material only.
  • the mixture of polymer and solid particles of electronic conductive additives is mixed in any type of mixing device(s) capable of good dispersion for a sufficient time to obtain solid particles of electronic conductive additives that are thoroughly dispersed within the polymer solution.
  • the solvent is removed through evaporation or other means from the mixture, and the remaining polymer/solid particles of electronic conductive additives mixture is transformed into a transportable solid as previously described.
  • the pre-mix polymer/solid particles (electronic conductive additives only) in solid transportable form is introduced into a feed throat of the extruder, the alkali metal salt and the active cathode material are fed into other feed throat(s); the various components are mixed and dispersed or dissolved in the molten polymer.
  • the alkali metal salt is dissolved in the polymer and the solid particles (active cathode material and electronic conductive additives) are re-dispersed into the polymer-salt solution.
  • the cathode material is extruded through a die as a thin sheet of between 5 and 200 ⁇ m thick, either directly onto a substrate support such as a metal foil current collector or a plastic film, or as a self-supporting sheet which is later on laminated onto a current collector.
  • the solvent or solvents of the solution of the pre-mix cathode material may be evaporated or dried just prior to the introduction of the pre-mix cathode material into the extruder such that the pre-mix cathode material remains in a fluid state and is never transformed into a transportable solid.
  • the pre-mix cathode material is introduced directly into the extruder while still in a fluid state and processed as described in the previous variants or embodiments thereby eliminating the necessity to transform it into a transportable solid.
  • the polymer is a polyether such as polyethylene oxide based polymer
  • the alkali metal salt is a lithium salt such as LiTFSi
  • the active material is a transition metal oxide such as lithium vanadium oxide (Li x V 3 O 8 )
  • the electronic conductive additive is carbon black or a binary mixture of carbon black and graphite.
  • the positive electrode material includes between 15%/wt and 45%/wt of polyether; between 40%/wt and 80%/wt of lithiated vanadium oxide; between 1.0%/wt and 5%/wt of Carbon black and Graphite particles and between 2%/wt and 15%/wt of lithium salt.
  • An antioxidant and other additives in minute proportion may also be added to the mixture.
  • each laminates comprises an anode film which is preferably a lithium metal sheet or a lithium alloy sheet, an electrolyte separator capable of Lithium ion transport, and a cathode thin film obtained by the process of extruding or coating pre-mixed positive electrode materials.
US10/902,174 2003-08-01 2004-07-30 Cathode material for polymer batteries and method of preparing same Abandoned US20050037262A1 (en)

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US20070273062A1 (en) 2007-11-29
CA2534155C (fr) 2012-10-02
WO2005013394A1 (fr) 2005-02-10
CA2534155A1 (fr) 2005-02-10
US8241541B2 (en) 2012-08-14
EP1665416A1 (fr) 2006-06-07
JP2007500926A (ja) 2007-01-18

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