EP2661781A1 - Matériaux pour électrodes et procédé de fabrication de ces matériaux - Google Patents

Matériaux pour électrodes et procédé de fabrication de ces matériaux

Info

Publication number
EP2661781A1
EP2661781A1 EP12704053.3A EP12704053A EP2661781A1 EP 2661781 A1 EP2661781 A1 EP 2661781A1 EP 12704053 A EP12704053 A EP 12704053A EP 2661781 A1 EP2661781 A1 EP 2661781A1
Authority
EP
European Patent Office
Prior art keywords
compound
iron
range
carbon
lithium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP12704053.3A
Other languages
German (de)
English (en)
Inventor
Robert Bayer
Bastian Ewald
Jordan Keith Lampert
Simon SCHRÖDLE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Priority to EP12704053.3A priority Critical patent/EP2661781A1/fr
Publication of EP2661781A1 publication Critical patent/EP2661781A1/fr
Withdrawn legal-status Critical Current

Links

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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00—Phosphorus; Compounds thereof
    • C01B25/16—Oxyacids of phosphorus; Salts thereof
    • C01B25/26—Phosphates
    • C01B25/45—Phosphates containing plural metal, or metal and ammonium
    • 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
    • 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
    • H01M4/04—Processes of manufacture in general
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0416—Methods of deposition of the material involving impregnation with a solution, dispersion, paste or dry powder
    • 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
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0419—Methods of deposition of the material involving spraying
    • 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
    • H01M4/362—Composites
    • H01M4/364—Composites as mixtures
    • 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
    • H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/40—Electric properties
    • 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
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028—Positive electrodes
    • 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
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
    • 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
    • H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
    • 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
    • H01M4/1397—Processes of manufacture of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • 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
    • H01M4/623—Binders being polymers fluorinated polymers
    • 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 a process for the production of electrode materials, which is characterized in that
  • At least one carbon source which may be a separate carbon source or at least one iron compound (A) or phosphorus compound (B) or lithium compound (C),
  • the present invention relates to electrode materials which are obtainable by the process according to the invention. Furthermore, the present invention relates to the use of electrode materials according to the invention in electrochemical cells.
  • numerous materials have hitherto been proposed, for example lithium-containing spinels, layered mixed oxides such as lithiated nickel-manganese-cobalt oxides and lithium-iron-phosphates.
  • Lithium iron phosphates are of particular interest because they contain no toxic heavy metals and in many cases are very robust against oxidation and water.
  • a disadvantage of lithium iron phosphates may be the comparatively low energy density.
  • lithium iron phosphates should be very finely divided to have suitable electrochemical properties. With finely divided lithium iron phosphates, high levels of dust and poor rheological properties are often observed, which cause problems in production and processing.
  • a further object was to provide chemically insensitive electrode materials which can be produced with as little effort as possible and which do not cause any great dust load. chen.
  • the object was to provide electrochemical cells which have overall positive application properties. Examples of application properties are the properties when processing into batteries or battery components as well as the properties of the batteries produced therefrom.
  • inventive method the method defined above was found, hereinafter also referred to as inventive method.
  • stage (a) several of the starting materials, preferably all the starting materials involved, are mixed in several or preferably in one step.
  • vessels for mixing for example, stirred tank and stirred flasks are suitable.
  • the starting material (A) is selected from at least one iron compound, hereinafter also called iron compound (A).
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or +3.
  • iron compound (A) is chosen from those in which iron, ie Fe, is present in the oxidation state +2 or
  • Preferred iron compounds (A) are Fe (OH) 3, basic Fe (lll) hydroxide, particularly FeOOH, ammonium citrate, Fe20 3, Fe 3 0 4, iron acetate, iron citrate, iron lactate, iron phosphate, iron carbonate and Eisenphosphonat.
  • At least two iron compounds are selected as starting material (A), at least one of which has at least one, preferably at least two, Fe in the oxidation state +2 or +3.
  • starting material (A) at least three iron compounds are chosen, all of which have Fe in the oxidation state +2 or +3.
  • the starting material (A) selected is exactly one iron compound present in Fe in the oxidation state +2 or +3.
  • Starting material (A) can be used, for example, as an aqueous solution, as an aqueous suspension or as a powder, for example with average particle diameters in the range from 10 to 750 nm, preferably in the range from 25 to 500 nm.
  • At least one phosphorus compound is chosen , hereinafter also called phosphorus compound (B), selected from phosphine and compounds in which phosphorus is in the oxidation state +1 or +3 or +5, for example phosphines having at least one alkyl group or at least one alkoxy group per molecule, phosphorus halides, phosphonic acid , hypophosphorous acid and phosphoric acid.
  • Preferred phosphanes are PH 3 and phosphanes of the general formula (I)
  • R 1 may be different or the same and is selected from phenyl and preferably C 1 -C 10 -alkyl, cyclic or linear, for example methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, cyclopentyl, iso-amyl, iso-pentyl, n-hexyl, iso-hexyl, cyclohexyl, and 1, 3-dimethylbutyl, preferably n-Ci-Cö-alkyl, more preferably methyl, Ethyl, n-propyl, isopropyl, and most preferably methyl or ethyl.
  • R 1 may be different or preferably identical and are selected from the above-mentioned Ci-C ß alkyl radicals.
  • X 1 may be different or the same and is selected from halogen, phenoxy groups and alkoxy groups, preferably of the formula OR 1 , in particular methoxy and ethoxy, and wherein
  • Halogen is preferably bromine and particularly preferably chlorine, r, s are selected from integers in the range from zero to three,
  • phosphorus compound (B) is selected from compounds of general formula P (OR 1 ) 3 , wherein R 1 is different or preferably may be the same and selected from phenyl and C 1 -C 10 -alkyl, particularly preferred are P (OCH 3) 3 and P (OC 2 H 5 ) 3 .
  • hypophosphorous acid and phosphoric acid can be selected in each case the free acid or corresponding salts, in particular lithium and ammonium salts.
  • phosphoric acid and phosphonic acid can be selected in each case the mononuclear acids H 3 P0 3 or H 3 P0 4 , but also two-, three- or more-nuclear acids, for example I-ÜP2O7 or polyphosphoric acid.
  • the starting material (B) two or more phosphorus compounds (B) are selected.
  • exactly one phosphorus compound (B) is chosen.
  • the starting material (C) used is at least one lithium compound, also called lithium compound (C), preferably at least one inorganic lithium compound.
  • suitable inorganic lithium compounds are lithium halides, for example lithium chloride, furthermore lithium sulfate, lithium acetate, LiOH, Li 2 CO 3 , L 12 O and LiNO 3 ; preferred are L12SC, LiOH, Li2C0 3 , L12O and LiN0 3 .
  • lithium compound can contain water of crystallization, for example LiOH ⁇ H2O.
  • phosphorus compound (B) and lithium compound (C) are each selected from lithium phosphate, lithium orthophosphate, lithium metaphosphate, lithium phosphonate, lithium phosphite, lithium hydrogen phosphate or lithium dihydrogen phosphate, ie lithium phosphate, lithium phosphonate, lithium phosphite or lithium (di) Hydrogen phosphate can each serve simultaneously as a phosphorus compound (B) and as a lithium compound (C).
  • At least one carbon source also called carbon source (D) for short, may be used, which may be a separate carbon source or at least one iron compound (A) or phosphorus compound (B) or lithium compound (C).
  • a separate carbon source (D) is to be understood as meaning that a further starting material is used which is selected from elemental carbon in a modification which conducts the electric current or a compound which is used in the thermal treatment in step (c) is decomposed into carbon and different from iron compound (A), phosphorus compound (B) and lithium compound (C).
  • carbon source (D) for example, carbon in a modification that conducts the electric current is suitable, for example, carbon black, graphite, graphene, carbon nanotubes or activated carbon.
  • graphite are not only mineral and synthetic graphite, but also expanded graphite and intercalated graphite.
  • Carbon black may, for example, be selected from lampblack, furnace black, flame black, thermal black, acetylene black, carbon black and furnace carbon black.
  • Carbon black may contain impurities, for example hydrocarbons, in particular aromatic hydrocarbons, or oxygen-containing compounds or oxygen-containing groups, for example OH groups.
  • sulfur or iron-containing impurities in carbon black are possible.
  • Further suitable carbon sources (D) are compounds of carbon which are decomposed to carbon during the thermal treatment in step (c). For example, synthetic and natural polymers, unmodified or modified, are suitable.
  • Examples of synthetic polymers are polyolefins, for example polyethylene and polypropylene, furthermore polyacrylonitrile, polybutadiene, polystyrene, and copolymers of at least two comonomers selected from ethylene, propylene, styrene, (meth) acrylonitrile and 1,3-butadiene.
  • polyisoprene and polyacrylates are suitable. Particularly preferred is polyacrylonitrile.
  • polyacrylonitrile is understood to mean not only polyacrylonitrile homopolymers, but also copolymers of acrylonitrile with 1,3-butadiene or styrene. Preference is given to polyacrylonitrile homopolymers.
  • polyethylene is understood to mean not only homo-polyethylene, but also copolymers of ethylene which contain at least 50 mol% of ethylene in copolymerized form and up to 50 mol% of at least one further comonomer, for example Olefins such as propylene, butylene (1-butene), 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-pentene, also isobutene, vinyl aromatics such as styrene, further
  • Olefins such as propylene, butylene (1-butene), 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-pentene, also isobutene, vinyl aromatics such as styrene, further
  • Polyethylene may be HDPE or LDPE.
  • polypropylene is understood to mean not only homo-polypropylene but also copolymers of propylene which contain at least 50 mol% of propylene polymerized and up to 50 mol% of at least one further comonomer, for example ethylene and ⁇ -propylene.
  • Olefins such as butylene, 1-hexene, 1-octene, 1-decene, 1-dodecene and 1-pentene.
  • Polypropylene is preferably isotactic or substantially isotactic polypropylene.
  • polystyrene is understood to mean not only homopolymers of styrene, but also copolymers with acrylonitrile, 1,3-butadiene, (meth) acrylic acid, C 1 -C 10 -alkyl esters of (meth) acrylic acid, divinylbenzene, in particular 1, 3-divinylbenzene, 1, 2-diphenylethylene and ⁇ -methylstyrene.
  • Another suitable synthetic polymer is polyvinyl alcohol.
  • Suitable natural polymers as carbon source (D) are for example starch, cellulose, alginates (eg agar agar, furthermore pectins, gum arabic, oligo and polysaccharides, guar gum and locust bean gum as well as amylose and amylopectin.) Also suitable Examples of modified natural polymers include methanol-etherified starch, acetylated starch and acetylcellulose, and further phosphated and sulfated starch.
  • carbides are suitable as the carbon source (D), preferably covalent carbides, for example iron carbide Fe 3 C.
  • low volatility low molecular weight organic compounds are suitable as carbon source (D).
  • Particularly suitable compounds are those which react at temperatures in the
  • Range of 350 to 1200 ° C does not evaporate, but decompose, for example as a solid or in the melt.
  • dicarboxylic acids for example phthalic acid, phthalic anhydride, isophthalic acid, terephthalic acid, tartaric acid, citric acid, pyruvic acid, furthermore sugars, for example monosaccharides having 3 to 7 carbon atoms per molecule (trioses, tetroses, pentoses, hexoses, heptoses) and condensates of monosaccharides such as for example, di-, tri- and oligosaccharides, in particular lactose, glucose and fructose, as well as sugar alcohols and sugar acids, for example aldonic acids, ketoaldonic acids, uronic acids and aldaric acids, in particular galactonic acid.
  • dicarboxylic acids for example phthalic acid, phthalic anhydride, isophthalic acid, terephthalic acid, tartaric acid,
  • low molecular weight organic compounds as carbon source (D) are urea and its less volatile condensates biuret, melamine, melam (N2- (4,6-diamino-1, 3,5-triazin-2-yl) -1, 3, 5-triazine-2,4,6-triamine) and Meiern (1, 3,4,6,7,9,9b-heptaazaphenalene-2,5,8-triamine).
  • carbon sources (D) are salts, preferably iron, ammonium salts and alkali metal salts, more preferably iron, sodium, potassium, ammonium or lithium salts, of organic acids, for example acetates, propionates, lactates, citrates, tartrates, benzoates , Butyrates.
  • Particularly preferred examples are ammonium acetate, potassium ammonium tartrate, potassium hydrogen tartrate, potassium sodium tartrate, sodium tartrate (disodium tetradrate), sodium hydrogentartrate, lithium hydrogentate, lithium ammonium tartrate, lithium tartrate, lithium citrate,
  • an organic phosphorus compound which may include, for example, trimethyl trimethylate, triethyl phosphite, triphenyl phosphine and triphenylphosphine oxide (CeHs ⁇ PO.
  • lithium acetate, lithium lactate or lithium hydrogen tartrate are respectively selected.
  • Lithium compound (C) Lithium acetate, lithium lactate or lithium hydrogen tartrate can each serve simultaneously as carbon source (D).
  • the carbon source (D) and iron compound (A) are each selected from iron acetate, iron citrate, iron carbide or ammonium citrate, i. the iron compound (A) iron acetate, iron citrate, iron carbide or ammonium citrate can simultaneously serve as carbon source (D).
  • the iron compound (A), carbon source (D) and lithium compound (C) are each selected from lithium iron citrate, i. Lithium-iron citrate can in each case simultaneously serve as iron compound (A), carbon source (D) and as lithium compound (C).
  • two different carbon sources (D) and two different phosphorus compounds (B) are chosen.
  • starting material (E) it is also possible to use a reducing agent, also called reducing agent (E) for short.
  • the reducing agent (E) it is possible to use gaseous, liquid or solid substances which, under the conditions of step (a), (b) or (c), convert iron, if necessary, into the oxidation state +2.
  • a solid reducing agent (E) is selected from a metal, for example nickel or manganese, or a metal hydride.
  • gaseous reducing agent (E) can be used for example hydrogen, carbon monoxide, ammonia and / or methane.
  • a very suitable reducing agent is H3PO3 and its ammonium and lithium salts.
  • Suitable reducing agents are metallic iron and iron pentacarbonyl.
  • phosphoric acid (B) and reducing agent (E) are each selected to be H3PO3, ie H3PO3 can simultaneously serve as phosphorus compound (B) and as reducing agent (E). In one embodiment of the present invention, no reducing agent (E) is used.
  • starting material (F) it is possible to use at least one further metal compound in which the one or more metals are different from iron, in short also called metal compound (F).
  • metal compound (F) it is preferable to use one or more metals from the first period of the transition metals as the metal. It is particularly preferable to choose metal compound (F) from compounds of Ti, V, Cr, Mn, Co, Ni, Mg, Al, Nb, W, Mo, Cu and Zn. Sc, V, Mn, Ni, Co. Most preferably one selects metal compound (F) from oxides, hydroxides, carbonates and sulfates of metals of the first period of the transition metals.
  • Metal compound (F) may be anhydrous or hydrous. Metal cation in metal compound (F) can be present in complexed form, for example as hydrate complex, or uncomplexed.
  • Metal compound (F) can be a salt, for example halide, in particular chloride, furthermore nitrate, carbonate, sulfate, oxide, hydroxide, acetate, citrate, tartrate or salts with different anions.
  • salts are selected from oxides, carbonates, hydroxides and nitrates, basic or neutral.
  • Very particularly preferred examples of metal compounds (F) are oxides, hydroxides, carbonates and sulfates.
  • metal compound (F) is selected from fluorides, for example as alkali metal fluoride, especially sodium fluoride.
  • metal compound (F) may function as one or the sole carbon source (D), exemplified by nickel acetate, cobalt acetate, zinc acetate and manganese (II) acetate.
  • metal compound (F) may act as one or the sole reducing agent (E).
  • examples include manganese (II) acetate, MnC0 3 , MnS0 4 , nickel lactate, manganese hydride, nickel hydride, nickel suboxide, nickel carbide, manganese carbide and manganese (ll) lactate called.
  • one or more solvents may be added in step (a), for example one or more organic solvents (G) and / or water.
  • Organic solvents (G) are to be understood as meaning those substances which are liquid at the temperature of step (a) of the process according to the invention and which have at least one CH bond per molecule.
  • water and an organic solvent (G) are added.
  • suitable organic solvents (G) are, in particular, halogen-free organic solvents. such as methanol, ethanol, isopropanol or n-hexane, cyclohexane, acetone, ethyl acetate, diethyl ether and diisopropyl ether.
  • step (a) can be carried out, for example, by stirring one or more suspensions of the starting materials (A) to (D) and optionally (E), (F) and (G).
  • the starting materials (A) to (D) and optionally (E) and (F) are intimately mixed together as solids.
  • the starting materials (A) to (D) and optionally (E), (F) and (G) may be kneaded together to form a paste.
  • the mixing in step (a) is carried out at temperatures in the range from zero to 200 ° C, preferably it is carried out at temperatures in the range of room temperature up to 1 10 ° C, particularly preferably up to 80 ° C.
  • the mixing in step (a) is carried out under atmospheric pressure. In other embodiments, the mixing is carried out at elevated pressure, for example at 1, 1 up to 20 bar. In other embodiments, the mixing in step (a) is carried out under reduced pressure, for example at 10 mbar up to 990 mbar.
  • the mixing in step (a) can be carried out over a period in the range of one minute to 12 hours, preferred are 30 minutes to 4 hours, more preferably 45 minutes to 2 hours.
  • step (a) the mixing in step (a) is performed in one step.
  • the mixing in step (a) is carried out in two or more stages.
  • Step (a) gives a mixture of at least one iron compound (A), at least one phosphorus compound (B), at least one lithium compound (C), at least one carbon source (D), optionally reducing agent (E), optionally further metal compound ( F) and preferably water and / or at least one organic solvent (G) in pasty form, as a water-containing powder, as a suspension or as a solution.
  • the mixture from step (a) is spray-dried by means of an at least apparatus which uses for spraying at least one spray nozzle, i. one carries out a spray drying or spray drying.
  • the spray drying can be carried out in a spray dryer.
  • Suitable spray dryers are drying towers, for example drying towers with one or more atomizing nozzles and spray dryer with integrated fluidized bed.
  • Particularly preferred nozzles are two-phase nozzles, in other words nozzles in the interior of which or at the mouth of which substances of different physical state are intensively mixed by means of separate accesses.
  • step (b) it is possible in a variant to compress the mixture obtained in step (a) through one or more spray devices, for example through one or more nozzles or into a hot air stream or into a hot inert gas stream or hot burner exhaust gases wherein the hot gas stream or the hot inert gas stream or the hot burner exhaust gases may have a temperature in the range of 90 to 500 ° C.
  • the mixture is dried within a fraction of a second or within a few seconds to a dry material, which is preferably obtained as a powder.
  • the resulting powder may have a certain residual moisture, for example in the range of 500 ppm to 10 wt .-%, preferably in the range of 1 to 8 wt .-%, particularly preferably in the range of 2 to 6 wt .-%.
  • the temperature of the hot air stream or of the hot inert gas stream or of the hot burner exhaust gas in step (b) is selected to be above the temperature in step (a).
  • the hot air stream or the hot inert gas stream or the hot burner exhaust gases flow in the direction of the introduced mixture from step (a) (DC method).
  • the hot air stream or hot inert gas stream flows the hot burner exhaust gases in the direction opposite to the introduced mixture from step (a) (countercurrent process).
  • the spraying device is preferably located at the upper part of the spray dryer, in particular the spray tower.
  • the dry material obtained in step (b) can be separated off after the actual spray drying by a separator, for example a cyclone from the hot air stream or hot inert gas stream or from the hot burner exhaust gases.
  • the dry material obtained in step (b) is separated from the hot air stream or hot inert gas stream or from the hot burner exhaust gases after the actual spray drying by one or more filters.
  • the dry material obtained in step (b) may, for example, have an average particle diameter (D50, weight average) in the range from 1 to 50 ⁇ m. It is preferred if the average particle diameter (D90, volume average) is up to 120 ⁇ , more preferably up to 50 ⁇ and most preferably up to 20 ⁇ .
  • D50 weight average
  • D90 volume average
  • Step (b) can be carried out batchwise (batchwise) or else continuously.
  • step (c) the dry material from step (b) is treated thermally, specifically at temperatures in the range from 350 to 1200 ° C., preferably from 400 to 900 ° C.
  • the thermal treatment in step (c) is carried out in a temperature profile with two to five, preferably with three or four zones, wherein each zone of the temperature profile preferably has a higher temperature than the preceding one.
  • a temperature in the range of 350 to 550 ° C can be set, in a second zone in the range of 450 to 750 ° C, the temperature being higher than in the first zone.
  • you wish to introduce a third zone you can thermally treat in the third zone at 700 to 1200 ° C, but in any case at a temperature higher than in the second zone.
  • the zones can be created, for example, by setting certain heating zones.
  • step (c) If one wishes to carry out step (c) intermittently, one can set a temporal temperature profile, ie. H. For example, it is first treated at 350 to 550 ° C, then at 450 to 750 ° C, the temperature being higher than in the first phase. If you wish to introduce a third phase, you can treat in the third phase at 700 to 1200 ° C, but in any case at a temperature that is higher than in the second phase.
  • the thermal treatment according to step (c) can be carried out, for example, in a rotary kiln, a pendulum reactor, a muffle open, a calcination furnace, a, a quartz ball furnace or a push-through furnace (English roller hearth kiln or RHK).
  • the thermal treatment according to step (c) can be carried out, for example, in a weakly oxidizing atmosphere, preferably in an inert or reducing atmosphere.
  • weakly oxidizing means an oxygen-containing nitrogen atmosphere which contains up to 2% by volume of oxygen, preferably up to 1% by volume.
  • inert atmosphere are noble gas, in particular argon atmosphere, and nitrogen atmosphere.
  • a reducing atmosphere are nitrogen or noble gases containing 0.1 to 10% by volume of carbon monoxide, hydrocarbon, ammonia or hydrogen.
  • Further examples of a reducing atmosphere are air or air enriched with nitrogen or with carbon dioxide, each containing more than one mole of carbon monoxide, rather than oxygen.
  • step (c) may be carried out over a period in the range of 1 minute to 24 hours, preferably in the range of 10 minutes to 3 hours.
  • the inventive method can be carried out without much dust.
  • electrode materials with excellent Theological properties are accessible, which are suitable as electrode materials and can be processed very well. For example, they can be processed into pastes with good rheological properties, such pastes have a lower viscosity.
  • Another object of the present invention are electrode materials containing
  • M is selected from Sc, Ti, V, Cr, Mn, Co, Ni, Mg, Al, Nb, W, Mo, Cu and Zn, preferably selected from Sc, V, Mn, Ni and Co.
  • x is a number in the range of 0.1 to 4, preferably at least 0.8, particularly preferably 1 to
  • y is a number in the range of 0.1 to 1, preferably at least 0.2;
  • carbon (H) is present in the pores of secondary particles of transition metal compound (I) or in the form of particles which can contact particles of transition metal compound (I) at one point or one or more particles of carbon (H).
  • x is a number in the range of 0.8 to 3
  • y is a number in the range of 0.01 to 1
  • z is a number in the range of 3 to 5
  • a is a number in the range of 0.2 to 2.0
  • transition metal compound (I) of the formula LiFeP0 4 or LiFeo, 2Mn 0 , 8P0 4 or LiFe 0 , 5Mn 0 , 5PO 4 or LiFe 0 , 7Mn 0 , 3PO 4 .
  • transition metal compound (I) may be doped or contaminated with one or more other metal cations, for example with alkaline earth metal cations, in particular with Mg 2+ or Ca 2+ , or with alkali metal cations, in particular with K + or Na + .
  • electrode material according to the invention has a BET surface area in the range from 10 to 40 m 2 / g, determined in accordance with DIN 66131. In one embodiment of the present invention, electrode material according to the invention has a monomodal pore diameter distribution. In another embodiment of the present invention, electrode material according to the invention has a bimodal pore diameter distribution. In another embodiment of the present invention, electrode material according to the invention has a multimodal pore diameter distribution.
  • Carbon in an electrically conductive modification (H), or carbon for short is, for example, carbon black, graphite, graphene, carbon nanotubes, expanded graphites, intercalated graphites or activated carbon.
  • electrically conductive carbonaceous material is carbon black.
  • Carbon black may, for example, be selected from lampblack, furnace black, flame black, thermal black, acetylene black, carbon black and furnace carbon black.
  • Carbon black may contain impurities, for example hydrocarbons, in particular aromatic hydrocarbons, or oxygen-containing compounds or oxygen-containing groups, for example OH groups, epoxide groups, carbonyl groups and / or carboxyl groups.
  • sulfur or iron-containing impurities in carbon black are possible.
  • electrically conductive, carbonaceous material is partially oxidized carbon black.
  • Partially oxidized carbon black also referred to as activated carbon black, contains oxygen-containing groups such as, for example, OH groups, epoxide groups, carbonyl groups and / or carboxyl groups.
  • electrically conductive carbonaceous material is carbon nanotubes.
  • Carbon nanotubes carbon nanotubes, short CNT or English carbon nanotubes
  • SW CNT single-walled carbon nanotubes
  • MW CNT multi-walled carbon nanotubes
  • carbon nanotubes have a diameter in the range of 0.4 to 50 nm, preferably 1 to 25 nm.
  • carbon nanotubes have a length in the range of 10 nm to 1 mm, preferably 100 nm to 500 nm.
  • Carbon nanotubes can be prepared by methods known per se. For example, one can use a volatile carbon-containing compound such as methane or carbon monoxide, acetylene or ethylene, or a mixture of volatile carbon-containing compounds such as synthesis gas in the presence of one or more reducing agents such as hydrogen and / or another gas such as nitrogen decompose. Another suitable gas mixture is a mixture of carbon monoxide with ethylene.
  • Suitable decomposition temperatures are, for example, in the range from 400 to 1000.degree. C., preferably from 500 to 800.degree.
  • Suitable pressure conditions for the decomposition are, for example, in the range of atmospheric pressure to 100 bar, preferably up to 10 bar.
  • Single- or multi-walled carbon nanotubes can be obtained, for example, by decomposition of carbon-containing compounds in the arc, in the presence or absence of a decomposition catalyst.
  • the decomposition of volatile carbon-containing compound or carbon-containing compounds in the presence of a decomposition catalyst for example Fe, Co or preferably Ni.
  • graphene is understood as meaning almost ideal or ideally two-dimensional hexagonal carbon crystals, which are constructed analogously to individual graphite layers. They can be one C-atom layer thick or only a few, for example 2 to 5 C-atom layers.
  • Graphene can be prepared by exfoliation or by delamination of graphite.
  • intercalated graphites are understood to mean not completely delaminated graphites which contain other atoms, ions or compounds intercalated between the hexagonal C atom layers. For example, alkali metal ions, S0 3 , nitrate or acetate can be incorporated.
  • the production of intercalated graphites (also: expandable graphites) are known, see for example Rüdorff, Z. anorg. Gen. Chem. 1938, 238 (1), 1.
  • Intercalated graphites can be prepared, for example, by thermal expansion of graphite.
  • Expanded graphites can be obtained, for example, by expansion of intercalated graphites, see, e.g. McAllister et al. Chem. Mater. 2007, 19, 4396-4404.
  • the weight ratio of transition metal compound (I) and carbon (H) is in the range from 200: 1 to 5: 1, preferably 100: 1 to 10: 1, more preferably 100: 1, 5 to 20: 1 ,
  • Carbon (H) exists in the pores of secondary particles of transition metal compound (I) or in the form of particles which can contact particles of transition metal compound (I) at a point or one or more particles of carbon (H). Carbon (H) is not present as a coating of secondary particles of transition metal compound (I), neither as a complete coating nor as a partial coating. Particles of carbon (H) do not contact secondary particles of transition metal compound (I) beyond edges. In one embodiment of the present invention, carbon (H) and transition metal compound (I) coexist in discrete particles which contact each other point-wise or not at all.
  • TEM TEM
  • SEM scanning electron microscopy
  • primary particles of compound (I) have an average diameter in the range from 1 to 2000 nm, preferably 10 to 1000 nm, particularly preferably 50 to 500 nm.
  • the mean primary particle diameter can be determined, for example, by SEM or TEM.
  • transition metal compound (I) is present in the form of particles which have an average particle diameter in the range from 1 to 150 ⁇ m (d50) and can be present in the form of agglomerates (secondary particles).
  • average particle diameter (d50) in the range of 2 to 50 ⁇ , more preferably in the range of 4 to 30 ⁇ .
  • transition metal compound (I) is in the form of particles which have an average pore diameter in the range from 0.05 ⁇ m to 2 ⁇ m and which can be present in agglomerates.
  • the average pore diameter can be determined, for example, by mercury porosimetry, for example according to DIN 66133.
  • transition metal compound (I) is present in the form of particles which have an average pore diameter in the range of 0.05 ⁇ m to 2 ⁇ m and exhibit a mono- or multimodal course of the intrusion volumes in the range 100-0.001 ⁇ m and thereby preferably have a pronounced maximum in the range between 10 ⁇ and 1 ⁇ , preferably two distinct maxima, one each between 10 and 1 and between 1 and 0.1 ⁇ .
  • carbon (H) has an average primary particle diameter in the range of 1 to 500 nm, preferably in the range of 2 to 100 nm, more preferably in the range of 3 to 50 nm, most preferably in the range of 4 to 10 nm.
  • electrode material according to the invention additionally contains at least one binder (J), for example a polymeric binder.
  • Suitable binders (J) are preferably selected from organic (co) polymers.
  • Suitable (co) polymers, ie homopolymers or copolymers, can be selected, for example, from anionic, catalytic or free-radical (co) polymerization
  • (Co) polymers in particular of polyethylene, polyacrylonitrile, polybutadiene, polystyrene, and copolymers of at least two comonomers selected from ethylene, propylene, styrene, (meth) acrylonitrile and 1, 3-butadiene.
  • polypropylene is suitable.
  • polyisoprene and polyacrylates are suitable. Particularly preferred is polyacrylonitrile.
  • polyacrylonitrile is understood to mean not only polyacrylonitrile homopolymers, but also copolymers of acrylonitrile with 1,3-butadiene or styrene. Preference is given to polyacrylonitrile homopolymers.
  • polyethylene is understood to mean not only homo-polyethylene, but also copolymers of ethylene which contain at least 50 mol% of ethylene in copolymerized form and up to 50 mol% of at least one further comonomer, for example example, ⁇ -olefins such as propylene, butylene (1-butene), 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-pentene, also isobutene, vinyl aromatics such as styrene, continue
  • Polyethylene may be HDPE or LDPE.
  • polypropylene is understood to mean not only homo-polypropylene but also copolymers of propylene which contain at least 50 mol% of propylene polymerized and up to 50 mol% of at least one further comonomer, for example ethylene and ⁇ -propylene.
  • Olefins such as butylene, 1-hexene, 1-octene, 1-decene, 1-dodecene and 1-pentene.
  • Polypropylene is preferably isotactic or substantially isotactic polypropylene.
  • polystyrene is understood to mean not only homopolymers of styrene, but also copolymers with acrylonitrile, 1,3-butadiene, (meth) acrylic acid, C 1 -C 10 -alkyl esters of (meth) acrylic acid, divinylbenzene, in particular 1, 3. Divinylbenzene, 1, 2-diphenylethylene and a-methylstyrene.
  • Another preferred binder (J) is polybutadiene.
  • Suitable binders (J) are selected from polyethylene oxide (PEO), cellulose, carboxymethyl cellulose, polyimides and polyvinyl alcohol.
  • binders (J) are selected from those (co) polymers which have an average molecular weight M w in the range from 50,000 to 1,000,000 g / mol, preferably up to 500,000 g / mol. Binders (J) may be crosslinked or uncrosslinked (co) polymers.
  • binders (J) are selected from halogenated (co) polymers, in particular from fluorinated (co) polymers.
  • Halogenated or fluorinated (co) polymers include those (co) polymers which contain at least one (co) monomer in copolymerized form which has at least one halogen atom or at least one fluorine atom per molecule, preferably at least two halogen atoms or at least two fluorine atoms per molecule.
  • Examples are polyvinyl chloride, polyvinylidene chloride, polytetrafluoroethylene, polyvinylidene fluoride (PVdF), tetrafluoroethylene-hexafluoropropylene copolymers, vinylidene fluoride-hexafluoropropylene copolymers (PVdF-HFP), vinylidene fluoride-tetrafluoroethylene copolymers, perfluoroalkylviny- lether copolymers, ethylene-tetrafluoroethylene copolymers, vinylidene fluoride-chlorotrifluoroethylene copolymers and ethylene-chlorofluoroethylene copolymers.
  • Suitable binders (J) are in particular polyvinyl alcohol and halogenated (co) polymers, for example polyvinyl chloride or polyvinylidene chloride, in particular fluorinated (co) polymers such as polyvinyl fluoride and in particular polyvinylidene fluoride and polytetrafluoroethylene.
  • electrode material according to the invention contains:
  • transition metal compound (I) in the range from 60 to 98% by weight, preferably from 70 to 96% by weight of transition metal compound (I), in the range from 1 to 25% by weight, preferably from 2 to 20% by weight, of carbon (H),
  • Inventive electrode materials can be used well for the production of electrochemical cells. For example, they can be processed into pastes with good theological properties.
  • Another object of the present invention are electrochemical cells prepared using at least one electrode according to the invention.
  • a further subject of the present invention are electrochemical cells containing at least one electrode according to the invention.
  • Another aspect of the present invention is an electrode containing at least one transition metal compound (I), carbon (H) and at least one binder (J).
  • the geometry of electrodes according to the invention can be chosen within wide limits. It is preferred to design electrodes according to the invention in thin films, for example in films having a thickness in the range from 10 ⁇ m to 250 ⁇ m, preferably from 20 to 130 ⁇ m.
  • electrodes according to the invention comprise a foil, for example a metal foil, in particular an aluminum foil, or a polymer foil, for example a polyester foil, which may be untreated or siliconized.
  • Another object of the present invention is the use of electrode materials according to the invention or electrodes according to the invention in electrochemical cells.
  • a further subject of the present invention is a process for the production of electrochemical cells using electrode material according to the invention or electrodes according to the invention.
  • Another object of the present invention are e- electrochemical cells containing at least one electrode material according to the invention or at least one electrode according to the invention.
  • Electrochemical cells according to the invention definitely serve as cathodes in electrochemical cells according to the invention.
  • Electrochemical cells according to the invention contain a counterelectrode which is defined as an anode in the context of the present invention and which can be, for example, a carbon anode, in particular a graphite anode, a lithium anode, a silicon anode or a lithium titanate anode.
  • Electrochemical cells according to the invention may be, for example, batteries or accumulators.
  • Electrochemical cells according to the invention may comprise, in addition to the anode and the electrode according to the invention, further constituents, for example conductive salt, nonaqueous solvent, separator, current conductor, for example of a metal or an alloy, furthermore cable connections and housing.
  • further constituents for example conductive salt, nonaqueous solvent, separator, current conductor, for example of a metal or an alloy, furthermore cable connections and housing.
  • electrical cells according to the invention contain at least one non-aqueous solvent which may be liquid or solid at room temperature, preferably selected from polymers, cyclic or non-cyclic ethers, cyclic and non-cyclic acetals and cyclic or not cyclic organic carbonates.
  • non-aqueous solvent which may be liquid or solid at room temperature, preferably selected from polymers, cyclic or non-cyclic ethers, cyclic and non-cyclic acetals and cyclic or not cyclic organic carbonates.
  • suitable polymers are in particular polyalkylene glycols, preferably P0IV-C1-C4-alkylene glycols and in particular polyethylene glycols.
  • Polyethylene glycols may contain up to 20 mol% of one or more C 1 -C 4 -alkylene glycols in copolymerized form.
  • polyalkylene glycols are polyalkylene glycols double capped with methyl or ethyl.
  • the molecular weight M w of suitable polyalkylene glycols and especially of suitable polyethylene glycols may be at least 400 g / mol.
  • the molecular weight M w of suitable polyalkylene glycols and in particular of suitable polyethylene glycols may be up to 5,000,000 g / mol, preferably up to 2,000,000 g / mol
  • non-cyclic ethers are, for example, diisopropyl ether, di-n-butyl ether, 1, 2-dimethoxyethane, 1, 2-diethoxyethane, preference is 1, 2-dimethoxyethane.
  • Suitable cyclic ethers are tetrahydrofuran and 1,4-dioxane.
  • suitable non-cyclic acetals are, for example, dimethoxymethane, diethoxymethane, 1,1-dimethoxyethane and 1,1-diethoxyethane.
  • Suitable cyclic acetals are 1, 3-dioxane and in particular 1, 3-dioxolane.
  • non-cyclic organic carbonates examples include dimethyl carbonate, ethyl methyl carbonate and diethyl carbonate.
  • Suitable cyclic organic carbonates are compounds of the general formulas (I I) and (II I)
  • R 3 , R 4 and R 5 may be identical or different and selected from hydrogen and C 1 -C 4 -alkyl, for example methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec. Butyl and tert-butyl, preferably R 4 and R 5 are not both tert-butyl.
  • R 3 is methyl and R 4 and R 5 are each hydrogen or R 5 , R 3 and R 4 are each hydrogen.
  • Another preferred cyclic organic carbonate is vinylene carbonate, formula (IV).
  • the solvent or solvents are used in the so-called anhydrous state, i. with a water content in the range of 1 ppm to 0.1 wt .-%, determined for example by Karl Fischer titration.
  • Inventive electrochemical cells also contain at least one conductive salt.
  • Suitable conductive salts are in particular lithium salts.
  • suitable lithium salts are LiPF 6, LiBF 4, L1CIO4, LiAsF 6, L1CF3SO3, LiC (CnF 2 n + IS0 2) 3, lithium imides such as LiN (CnF 2 n + IS0 2) 2, where n is an integer ranging from 1 to 20; LiN (SO 2 F) 2, Li 2 SiF 6, LiSbF 2 O, LiAICU, and salts of the general formula (C n F 2n + i SO 2) mYLi, where m is defined as follows:
  • m 2 when Y is selected from nitrogen and phosphorus
  • m 3 when Y is selected from carbon and silicon.
  • Preferred conducting salts are selected from LiC (CF 3 SO 2 ) 3, LiN (CF 3 SO 2 ) 2, LiPF 6 , LiBF 4 ,
  • L1CIO4 and particularly preferred are LiPF ⁇ and LiN (CF3SC> 2) 2.
  • electrochemical cells according to the invention contain one or more separators, by means of which the electrodes are mechanically separated.
  • Suitable separators are polymer films, in particular porous polymer films, which are unreactive with respect to metallic lithium.
  • Particularly suitable materials for separators are polyolefins, in particular film-shaped porous polyethylene and film-shaped porous polypropylene.
  • Polyolefin separators particularly polyethylene or polypropylene, may have a porosity in the range of 35 to 45%. Suitable pore diameters are for example in the range from 30 to 500 nm.
  • separators may be selected from inorganic particle filled PET webs.
  • Such separators may have a porosity in the range of 40 to 55%. Suitable pore diameters are, for example, in the range from 80 to 750 nm.
  • Electrochemical cells according to the invention furthermore contain a housing which can have any shape, for example cuboidal or the shape of a cylindrical disk.
  • a metal foil developed as a bag is used as the housing.
  • Inventive electrochemical cells provide a high voltage and are characterized by a high energy density and good stability.
  • Electrochemical cells according to the invention can be combined with one another, for example in series connection or in parallel connection. Series connection is preferred.
  • Another object of the present invention is the use of electrochemical cells according to the invention in devices, in particular in mobile devices.
  • mobile devices are vehicles, for example automobiles, two-wheelers, aircraft or watercraft, such as boats or ships.
  • Other examples of mobile devices are those that you move yourself, such as computers, especially laptops, phones, or electrical tools, for example in the field of construction, in particular drills, cordless screwdrivers or cordless tackers.
  • electrochemical cells in devices according to the invention offers the advantage of a longer running time before reloading. If one wanted to realize an equal running time with electrochemical cells with a lower energy density, then one would have to accept a higher weight for electrochemical cells.
  • step (a.1) The solution from step (a.1) was sprayed in a spray tower by program under air.
  • the hot air flow had a temperature of 330 ° C at the entrance, at the exit still 1 10 ° C.
  • the dryer was operated with 350 kg / h of drying gas and 33 kg / h of nozzle gas (sputtering gas) with an atomization pressure of 3.5 bar.
  • a yellow free-flowing powder with a residual moisture content of 8% was obtained. It was in the form of particles whose diameter (D50) was 19 ⁇ m. SEM images showed spherical agglomerates of yellow powder held together by the organic components lactose and starch.
  • Step (c.1) The yellow powder from step (b.1) was thermally treated in a 2 liter steel laboratory rotary kiln under an N 2 atmosphere.
  • the 2-liter steel laboratory rotary kiln had three temperature zones and rotated at a speed of 10 revolutions / min.
  • the temperature in zone 1 was 450 ° C.
  • in zone 2 the temperature was 725 ° C. and in zone 3 it was 775 ° C.
  • the mean residence time was one hour.
  • Inventive electrode material containing transition metal compound (1.1) and carbon (H.1) was obtained. Carbon (H.1) and transition metal compound (1.1) were present in discrete particles, as shown by light microscopy, which did not touch at all or only at a single point. Diameter (D50): 17.2 ⁇ .
  • the tamped density of the sieve fraction ⁇ 32 ⁇ was 0.92 g / ml.
  • Inventive electrode material was processed with a binder (J.1): copolymer of vinylidene fluoride and hexafluopropene, as a powder, commercially available as Kynar Flex® 2801 from Arkema, Inc., as follows.
  • J.1 copolymer of vinylidene fluoride and hexafluopropene
  • Electrochemical cells were prepared from the electrodes thus obtained.
  • As the electrolyte a 1 mol / l solution of LiPFß in ethylene carbonate / dimethyl carbonate (1: 1 based on mass fractions) was used.
  • the anode of the test cells consisted of a lithium foil, which is in contact with the cathode foil via a separator made of glass fiber paper.
  • the invention gives electrochemical cells EZ.1.
  • Inventive electrochemical cells EZ.1 show good cycling stability.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Composite Materials (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Nanotechnology (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Dispersion Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

Procédé de fabrication de matériaux pour électrodes, caractérisé en ce que l'on (a) mélange : (A) au moins un composé de fer, dans lequel Fe est présent au degré d'oxydation +2 ou +3, (B) au moins un composé de phosphore, (C) au moins un composé de lithium, (D) au moins une source de carbone pouvant être une source de carbone distincte ou identique à au moins un composé de fer (A), un composé de phosphore (B) ou un composé de lithium (C), (E) le cas échéant, au moins un agent de réduction, (F) le cas échéant, au moins un composé métallique additionnel comprenant un métal différent du fer, (G) le cas échéant de l'eau ou au moins un solvant organique, (b) sèche ces éléments ensemble par atomisation à l'aide d'au moins un équipement d'atomisation dotée d'au moins une buse d'atomisation, et (c) les soumet à un traitement thermique dans une plage de températures allant de 350 à 1200 °C.
EP12704053.3A 2011-02-14 2012-02-10 Matériaux pour électrodes et procédé de fabrication de ces matériaux Withdrawn EP2661781A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP12704053.3A EP2661781A1 (fr) 2011-02-14 2012-02-10 Matériaux pour électrodes et procédé de fabrication de ces matériaux

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP11154422 2011-02-14
PCT/EP2012/052257 WO2012110404A1 (fr) 2011-02-14 2012-02-10 Matériaux pour électrodes et procédé de fabrication de ces matériaux
EP12704053.3A EP2661781A1 (fr) 2011-02-14 2012-02-10 Matériaux pour électrodes et procédé de fabrication de ces matériaux

Publications (1)

Publication Number Publication Date
EP2661781A1 true EP2661781A1 (fr) 2013-11-13

Family

ID=45607247

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12704053.3A Withdrawn EP2661781A1 (fr) 2011-02-14 2012-02-10 Matériaux pour électrodes et procédé de fabrication de ces matériaux

Country Status (5)

Country Link
EP (1) EP2661781A1 (fr)
JP (1) JP2014507050A (fr)
KR (1) KR20140001997A (fr)
CN (1) CN103354959A (fr)
WO (1) WO2012110404A1 (fr)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103000896B (zh) * 2012-12-20 2016-02-03 中国东方电气集团有限公司 一种锂电池掺杂改性磷酸亚铁锂正极材料的制备方法
SG11201606500WA (en) * 2014-02-07 2016-09-29 Basf Se Electrode unit for an electrochemical device
CN104003481B (zh) * 2014-05-09 2016-08-24 昆明理工大学 一种电滤板及其在高浓度有机废水中的应用
CN105322162B (zh) * 2014-08-04 2018-04-10 湖北工程学院 一种高性能磷酸铁锂复合正极材料的制备方法
KR102100879B1 (ko) * 2015-10-30 2020-04-13 주식회사 엘지화학 이차전지용 양극, 이의 제조 방법 및 이를 포함하는 리튬 이차전지
DE102016203349A1 (de) * 2016-03-01 2017-09-07 Wacker Chemie Ag Herstellung von Si/C-Kompositpartikeln
CN108448079B (zh) * 2018-02-11 2020-06-19 江苏合志新能源材料技术有限公司 正极复合材料及其制备方法
CN112119131B (zh) * 2018-05-15 2023-03-10 锡克拜控股有限公司 机器可读安全特征
CN110255522B (zh) * 2019-07-03 2020-11-06 重庆特瑞电池材料股份有限公司 一种多级造孔式磷酸铁锂的制备方法
CN111115604A (zh) * 2020-01-03 2020-05-08 博创宏远新材料有限公司 一种碳掺杂磷酸铁的制备方法
CN112897491B (zh) * 2021-01-21 2023-01-13 广东邦普循环科技有限公司 磷酸铁锂正极材料的制备方法和应用
CN116409767A (zh) * 2022-12-19 2023-07-11 宜都兴发化工有限公司 一种纳米磷酸铁的制备方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3827313B2 (ja) * 2003-05-07 2006-09-27 エヌ・イーケムキャット株式会社 チタニア被覆アルミナ粒子の製造方法
CN100511778C (zh) * 2007-08-24 2009-07-08 郑州德朗能电池有限公司 高性能锂离子电池正极材料LiFePO4/C的制备方法
JP5263807B2 (ja) * 2007-09-12 2013-08-14 国立大学法人福井大学 電極用リン酸鉄リチウム粉体の製造方法
CN101399343B (zh) * 2007-09-25 2011-06-15 比亚迪股份有限公司 锂离子二次电池正极活性物质磷酸铁锂的制备方法
CN101436667A (zh) * 2007-11-14 2009-05-20 中国科学院理化技术研究所 一种锂离子电池用正极多孔材料及其制备方法
KR101408884B1 (ko) * 2007-11-27 2014-06-19 삼성에스디아이 주식회사 리튬 이차 전지용 전극 및 이를 포함하는 리튬 이차 전지
JP5388822B2 (ja) * 2009-03-13 2014-01-15 Ｊｆｅケミカル株式会社 リン酸鉄リチウムの製造方法
CN101635352A (zh) * 2009-07-20 2010-01-27 万向电动汽车有限公司 一种碳包覆锂离子电池正极材料的制备方法
JP2011086524A (ja) * 2009-10-16 2011-04-28 Univ Of Fukui リチウムイオン二次電池正極活物質の製造方法

Also Published As

Publication number Publication date
WO2012110404A1 (fr) 2012-08-23
CN103354959A (zh) 2013-10-16
KR20140001997A (ko) 2014-01-07
JP2014507050A (ja) 2014-03-20

Similar Documents

Publication Publication Date Title
EP2850681B1 (fr) Procédé destiné à la fabrication de matériau d'électrode
WO2012110404A1 (fr) Matériaux pour électrodes et procédé de fabrication de ces matériaux
EP2663527B1 (fr) Procédé de production d'hydroxydes de métaux de transition
EP2884568A1 (fr) Procédé de production de matériaux d'électrodes
EP2994425B1 (fr) Particule sphérique, sa fabrication et son utilisation
EP2814778B1 (fr) Particules, procédé de production desdites particules et utilisation desdites particules
WO2012038269A1 (fr) Procédé de fabrication de matériaux d'électrodes
US20120205594A1 (en) Electrode materials and process for producing them
EP2619139B1 (fr) Procede de preparation de materiaux d'electrode
EP2457873A1 (fr) Procédé de fabrication d'ébauches pour oxydes mixtes de métal de transition
EP2487746A2 (fr) Matériaux d'électrode et leur procédé de fabrication
EP2572397B1 (fr) Composés et leur utilisation pour produire des piles électrochimiques
WO2013102533A1 (fr) Matériaux, production et utilisation desdits matériaux
WO2011113921A1 (fr) Matériau d'électrode et son utilisation pour la fabrication de cellules électrochimiques
EP2458665A2 (fr) Procédé de fabrication d'ébauches pour oxydes mixtes de métal de transition
EP2663528B1 (fr) Procédé de préparation de carbonates de métaux de transition
EP2619141B1 (fr) Procédé de production d'oxydes mixtes de métaux de transition modifiés
EP4149890B1 (fr) Matériaux actifs d'électrode et leur procédé de fabrication

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20130805

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
RIC1 Information provided on ipc code assigned before grant

Ipc: C08K 3/04 20060101ALI20140509BHEP

Ipc: H01M 4/1397 20100101ALI20140509BHEP

Ipc: C01B 25/37 20060101ALI20140509BHEP

Ipc: C01B 25/45 20060101AFI20140509BHEP

Ipc: H01M 4/62 20060101ALI20140509BHEP

Ipc: H01M 10/0525 20100101ALI20140509BHEP

Ipc: H01M 4/36 20060101ALI20140509BHEP

Ipc: H01M 4/58 20100101ALI20140509BHEP

Ipc: B82Y 30/00 20110101ALI20140509BHEP

Ipc: H01M 4/02 20060101ALI20140509BHEP

Ipc: H01M 4/04 20060101ALI20140509BHEP

17Q First examination report despatched

Effective date: 20140527

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20141007