WO2004001881A2 - Carbon-coated li-containing powders and process for production thereof - Google Patents

Carbon-coated li-containing powders and process for production thereof Download PDF

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Publication number
WO2004001881A2
WO2004001881A2 PCT/EP2003/006628 EP0306628W WO2004001881A2 WO 2004001881 A2 WO2004001881 A2 WO 2004001881A2 EP 0306628 W EP0306628 W EP 0306628W WO 2004001881 A2 WO2004001881 A2 WO 2004001881A2
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carbon
coated
water
lifep0
nasicon
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PCT/EP2003/006628
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French (fr)
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WO2004001881A3 (en
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Albane Audemer
Calin Wurm
Mathieu Morcrette
Sylvain Gwizdala
Christian Masquelier
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Umicore
Le Centre National De La Recherche Scientifique
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Priority to JP2004530900A priority Critical patent/JP4654686B2/en
Priority to CNB038145634A priority patent/CN100379062C/en
Priority to US10/518,560 priority patent/US7618747B2/en
Priority to DE60333921T priority patent/DE60333921D1/en
Priority to KR1020137005923A priority patent/KR20130038952A/en
Priority to KR1020137034378A priority patent/KR101452679B1/en
Priority to CA2490091A priority patent/CA2490091C/en
Priority to KR1020127025123A priority patent/KR20120123585A/en
Priority to EP03760688A priority patent/EP1518284B1/en
Priority to AT03760688T priority patent/ATE479207T1/en
Application filed by Umicore, Le Centre National De La Recherche Scientifique filed Critical Umicore
Priority to AU2003250847A priority patent/AU2003250847A1/en
Priority to KR1020147016846A priority patent/KR101502294B1/en
Publication of WO2004001881A2 publication Critical patent/WO2004001881A2/en
Publication of WO2004001881A3 publication Critical patent/WO2004001881A3/en
Priority to US12/270,969 priority patent/US7923154B2/en
Priority to US13/042,653 priority patent/US8236453B2/en

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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
    • H01M4/04—Processes of manufacture in general
    • H—ELECTRICITY
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    • 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
    • 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
    • C01B25/37—Phosphates of heavy metals
    • 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
    • C01B25/37—Phosphates of heavy metals
    • C01B25/375—Phosphates of heavy metals of iron
    • C—CHEMISTRY; METALLURGY
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    • 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
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    • H01M10/052—Li-accumulators
    • 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
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • 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
    • H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
    • H01M10/0562—Solid materials
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • H—ELECTRICITY
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    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
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    • H01M4/36—Selection of substances as active materials, active masses, active liquids
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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
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
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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
    • H01M4/58—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
    • H—ELECTRICITY
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    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • H01M4/625—Carbon or graphite
    • H—ELECTRICITY
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    • H01M6/00—Primary cells; Manufacture thereof
    • H01M6/14—Cells with non-aqueous electrolyte
    • H01M6/18—Cells with non-aqueous electrolyte with solid electrolyte
    • H01M6/185—Cells with non-aqueous electrolyte with solid electrolyte with oxides, hydroxides or oxysalts as solid electrolytes
    • H—ELECTRICITY
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    • H01M2004/021—Physical characteristics, e.g. porosity, surface area
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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
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • 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 the field of rechargeable lithium batteries and to positive electrode materials operating at voltages greater than 2.8 V vs. Li + / Li in non-aqueous electrochemical cells.
  • This invention relates in particular to the use of phosphates or sulphates of transition metals as positive electrodes and allows the manufacturing of powdered Li- containing olivine-like and NASICON-like material, with the particles efficiently coated with a controlled amount of conductive carbon.
  • Lithium secondary batteries are now widely used in consumer electronics. They benefit from the light weight of Li and from its strong reducing character, thus providing the highest power and energy density among known rechargeable battery systems.
  • Lithium secondary batteries are of various configurations depending on the nature of the electrode materials and of the electrolyte used.
  • the commercialised Li-ion system for instance, uses LiCoO 2 and Carbon graphite as positive and negative electrodes, respectively with LiPFg in EC/DEC/PC as a liquid electrolyte.
  • the operating voltage of the battery is related to the difference between thermodynamic free energies within the negative and positive electrodes.
  • Solid oxidants are therefore required at the positive electrode, the materials of choice, up to now, being either the layered LiMO 2 oxides (with M is Co or Ni) or the 3-dimensional spinel structure of Li[Mn 2 ]O 4 . Extraction of Li from each of these three oxides gives access to M 4+ / M 3+ redox couples located between 3.5 to 5 V vs. Li + /Li.
  • LiFePO 4 and Li 3 Fe 2 (PO ) 3 are the most promising Fe-containing materials that can work at attractive potentials vs. Li + / Li (3.5 V and 2.8 V respectively). Both compounds operate on the Fe 3+ / Fe 2+ redox couple which take advantage from the inductive effect of the XO 4 n" groups that diminishes the strength of the Fe-O bond compared to a simple oxide.
  • the poor electronic conductivity of the product can be improved by coating the particles with conductive carbon. This has been done by ball milling LiFePO 4 and carbon (Huang et al., Electrochem. Solid-State Lett., 4, A170 (2001)) or by adding a carbon containing compound to already made LiFePO 4 and proceeding to a subsequent calcination at about 700 °C (CA)
  • Carbon, and preferably amorphous carbon can also be introduced in the LiFeP0 4 synthesis process, being mixed with the solid synthesis precursors before calcination (EP 1184920 A2).
  • the ionic conduction problem can be solved by producing very fine-grained particles.
  • Using a solution route synthesis has been found to be advantageous compared to the classic solid synthesis route.
  • This solution route has been described in EP1261050.
  • This route provides for a very finely divided, homogeneous precursor which needs only moderate conditions of temperature and time to react to the desired crystalline structures. Thanks to the moderate conditions, grain growth, leading to unwanted coarse particles, is avoided.
  • After synthesis, such a powder has to be ball-milled with a relatively large quantity of conductive carbon, typically amounting to 17 wt.% .
  • This invention provides for an improved solution route, ensuring the production of fine grained particles efficiently covered with a conductive carbon layer.
  • the obtained powders deliver exceptional performances when used in Li-ion batteries.
  • the invention provides for a powder that needs much less total carbon in the electrode for a similar electrode capacity and discharge rate. Similarly, the invention provides for a powder that provides higher capacity and discharge rate when using the same amount of total carbon in the electrode.
  • a new process is presented for preparing a carbon-coated Li-containing olivine or NASICON powder, comprising the steps of
  • LiMPO4 such as in LiFeP0 4 , LiNiP0 4 , LiMnPO 4 ; LiM 2 (PO 4 ) 3 such as in LiTi 2 (PO 4 ) 3 , LiFeNb(PO 4 ) 3 ; Li 2 M 2 (PO 4 ) 3 such as in Li 2 FeTi(PO 4 ) 3 ; Li 3 M 2 (PO 4 ) 3 such as in Li 3 Ti 2 (PO 4 ) 3 , Li 3 Sc 2 (PO 4 ) 3 , Li 3 Cr 2 (PO 4 ) 3 , Li 3 In 2 (PO 4 ) 3 , Li 3 Fe 2 (PO 4 )3, Li 3 FeV(PO 4 ) 3 .
  • the invented process is especially suitable for the preparation of coated LiFePO 4 .
  • the precipitation of Li-containing olivine or NASICON precursor compounds and the polymerisation of the monomers can be performed by evaporating water from the water-based solution.
  • the carbon-bearing monomer compounds can be a polyhydric alcohol and a polycarboxylic acid, such as, respectively, ethylene glycol and citric acid.
  • Li, Fe and phosphate such as LiH 2 PO 4 and Fe(NO 3 ) 3
  • water is then evaporated at a temperature between 60 and 100 °C, and a heat-treatment is performed at a temperature between 600 and 800 °C, preferably between 650 and 750 °C.
  • the object of the invention also concerns a carbon-coated LiFePO 4 powder for use in Li insertion-type electrodes, which, when used as an active component in a cathode cycled between 2.0 and 4.5 V against a Li anode at a discharge rate of C / 5 at 25 °C, is characterised by a reversible electrode capacity expressed as a fraction of the theoretical capacity and a total carbon content of at least 75 % capacity and less than 4 wt.% carbon, or, at least 80 % capacity and less than 8 wt.% carbon.
  • a "Li-containing olivine or NASICON precursor compound” is to be understood as a metal- bearing compound such as a salt, oxide or hydroxide of one ore more metals susceptible to be converted to, or to react to, the desired final compound. Typically, the conversion or reaction is performed by applying a thermal treatment.
  • a "carbon-bearing monomer compound” is to be understood as an organic compound susceptible to polymerise with itself (to form a homopolymer) or together with other monomers (to form a copolymer).
  • a "reducing environment” can be obtained by using a reducing gas, or by relying on reducing properties of solids, such as carbon, present in the bulk of the material.
  • the “electrode capacity expressed as a fraction of the theoretical capacity” is the ratio of the capacity of the active product contained in the electrode, to the theoretical capacity of the active product.
  • a specific theoretical capacity of 170 mA / g is assumed.
  • C / x this means that one Li per LiFeP0 4 is exchanged in 'x' hour.
  • the general principle of the invention can be apphed whenever a high quality carbon coating is needed on a metal-bearing powder.
  • Olivine and NASICON phases when used in rechargeable Li-ion batteries, are known to be rather poor electronic conductors. As such, they particularly benefit from a carbon coating which is rendered conductive by a suitable heat treatment.
  • the metal bearing precursors such as Li, metal and phosphate or sulphate ions
  • the metal bearing precursors are trapped homogeneously on the atomic scale throughout the chelating polymer matrix.
  • Such a structure eliminates the needs for long range diffusion during the subsequent formation of the crystalline phase. Therefore, at relatively low temperature, the precursors can form a homogeneous single phase of precise stoichiometry, intimately coated by a conductive carbonaceous network.
  • Solvent evaporation conducting to an homogeneous mix of solid precursor compounds and the polymerisation of the monomers are performed in one single step. This requires the polymerisation to occur simultaneously with the solidification of at least part of the precursor.
  • the Fe source in the precursor compound can be Fe 11 or Fe m : the reducing conditions needed to avoid the burning of the carbon coating during the step of heat treatment ensures the conversion of any Fe m to the required Fe 1 state.
  • the preferred water evaporation temperature range is 60 to 100 °C. This ensures that the precipitation of the precursor compound and the polymerisation reaction occur at least partly simultaneously.
  • the conductivity of the carbon residue is enhanced when the heat treatment is performed at 600 °C or higher. However, a temperature of more than 800 °C may degrade the quality of the product because of grain-growth or because of excessive reduction by carbon. A heath treatment at 650 to 750 °C is preferred.
  • the positive electrode of the electrochemical cell is made of optimised LiFeP0 4 particles intimately mixed with an electronically conducting carbon species made as described below.
  • the active material / coated-carbon ratio can be adjust in the synthesis of LiFeP0 between 1 and 25 wt.% of carbon. It is preferred to minimise the relative amount of carbon, whether present as coating material or as carbon added during the manufacture of the electrode. Indeed, carbon does not participate in the redox reactions and therefore represents inert mass reducing the specific capacity of the electrode. Nevertheless, it is desired to have at least 2 wt.% of coated carbon to exploit the invention fully.
  • the invention is illustrated by the preparation of optimised LiMPO particles, coated with (electronic) conductive carbon through low-temperature chemical routes.
  • an aqueous solution containing Fe, Li and phosphate is prepared using e.g. Fe(N0 3 ) 3 .9H 2 0 and LiH 2 PO 4 .
  • the solution is added under stirring in air to an aqueous solution of citric acid.
  • Ethylene glycol is then added to the solution for an ethylene glycol / citric acid molar ratio of 1 / 1.
  • the precursor to carbon ratio in the solution will determine the relative amount of carbon in the coating. Key to this process are the fact that both the LiFeP0 4 precursors and the monomers are to be water-soluble.
  • the water is slowly evaporated at 80 °C under air.
  • the solution turns to a gel due to the polymerisation between citric acid and ethylene glycol.
  • the gel is dried by maintaining it at 80 °C.
  • monomers are chosen which have a lower partial pressure than water at the drying temperature. Premature evaporation of the monomers is thus avoided.
  • the homogeneous mixture is progressively heat-treated under a reducing atmosphere (N 2 / H 2 , 10 % H 2 ) to yield, at a temperature of about 500 °C, a crystalline LiFeP0 4 phase coated with a controlled amounts coated carbon.
  • a reducing atmosphere N 2 / H 2 , 10 % H 2
  • the coated carbon is partly insulating.
  • a treatment between 600 °C and 800 °C is thus preferred as it yields conductive carbon. Thanks to the presence of carbon, the surrounding environment of LiFeP0 4 is strongly reducing. This is useful to reduce remaining traces of Fe 111 precursors to Fe 11 , but can lead to unwanted results when the percentage of carbon is high.
  • the obtained optimised powder may still contain a small amount of Fe m (less than 3 M%), an amount which is in fact inferior to that obtained in the synthesis of pure LiFeP0 4 without carbon.
  • the result of the heat treatment can easily be monitored and optimised by e.g. X-ray diffraction or by Mossbauer spectroscopy, to ensure that Fe m is nearly completely reduced to Fe 11 and that no significant amount of Fe 11 is reduced to Fe°.
  • LiFeP0 4 / C composites were produced according to the process described above.
  • Aqueous solutions containing 0.4 M / 1 Fe, Li and phosphate and 0.1 to 1 M / 1 ethylene glycol and citric acid were prepared using Fe(N0 3 ) 3 .9H 2 0 and LiH 2 P0 4 .
  • the solutions were dried for 12 h at 80 °C.
  • the dry residues were then heat treated for 10 h at 700 °C under a N 2 / H 2 atmosphere with 10 % H 2 .
  • FIG. 1 to 5 illustrate the invention.
  • Fig. 1 X-ray diffractograms (CuK ⁇ ) and the S.E.M. photographs of two LiFeP0 powders coated with 3.6 (top) and 24 % (bottom) carbon
  • Fig. 2 Electrochemical response of a Li / LiPF ⁇ ECDMC / LiFePO 4 electrochemical cell (swagelok type) cycled at C / 5 and 25 °C, using LiFePO 4 with 3.6 (top) and 24 % (bottom) of coated carbon
  • Fig. 3 Results obtained with Li / LiPF 6 EC : DMC / LiFePO 4 electrochemical coin cells embedded in a plastic film.
  • Fig. 4 In situ XRD patterns of LiFeP0 4 in a Li / LiPF 6 EC : DMC / LiFePO 4 electrochemical cell cycled at C / 5 and 25 °C; LiFePO 4 prepared according to the invention (top) and according to the prior art solution route and ball-milled with 17 % of conductive carbon (bottom)
  • Fig. 5 Evolution of the specific active material capacity achieved in a Li / LiPF 6 EC : DMC / LiFeP0 4 prepared according to the invention with 3.6 (B) and 24 % (C) of coated carbon; LiFeP0 prepared according to the prior the art solution route and ball-milled with 17 % of conductive carbon (D); commercial LiCo0 2 are shown for comparison (A) Figures 1 to 5 are now discussed in more details. The X-ray diffractograms and the S.E.M. photographs of two LiFeP0 4 powders coated with 3.6 and 24 % of carbon are given in Figure 1. The photographs are representative for the overall powder.
  • the network formed by the coated particles is very well spaced and regular.
  • the particles are sufficiently fine (around 1 ⁇ m) to alleviate the penalising displacement length of the interface between LiFePO 4 and FePO , while enough space is left for species to migrate.
  • the carbon matrix itself can be observed.
  • the carbon network surrounds the LiFeP0 4 particles whose size is even smaller than in the former case.
  • the LiFePO 4 phase appears to be pure when 3.6 % of carbon is coated.
  • some LiFePO 4 is reduced to Fe 2 P after 10 h at 700 °C. This demonstrates that the higher the carbon percentage, the more efficient the reduction.
  • Figure 3 illustrates the stability of the LiFeP0 composite produced according to the invention using 3.6 % of coated carbon. This material was cycled at C / 5 at 25 and at 55 °C. The resulting specific capacity is superior to that obtained with uncoated material prepared according to the prior art solution route and ball-milled with 17 % of conductive carbon. If we compare the specific capacities of the total electrodes, the superiority of the invented process becomes even more apparent thanks to the much lower amount of total carbon.
  • LiFeP0 4 composite obtained by the process according to the invention with 3.6 and 24 % of coated carbon
  • commercial LiCo0 2 commercial LiCo0 2 .
  • the 3.6 % carbon-coated LiFeP0 4 performs better than any other at low discharge rates. At higher rates, it is outperformed by LiCo0 2 (a much more expensive product), and, as expected, by 24 % carbon-coated LiFePO . Indeed, the higher amount of coated carbon tends to improve the high current performance. Whatever the conditions, however, the products which are carbon- coated according to the invention remain superior to the prior art product.

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Abstract

The invention provides a new route for the synthesis of carbon-coated powders having the olivine or NASICON structure, which form promising classes of active products for the manufacture of rechargeable lithium batteries. Carbon-coating of the powder particles is necessary to achieve good performances because of the rather poor electronic conductivity of said structures. For the preparation of coated LiFePO4, sources of Li, Fe and phosphate are dissolved in an aqueous solution together with a polycarboxylic acid and a polyhydric alcohol. Upon water evaporation, polyesterification occurs while a mixed precipitate is formed containing Li, Fe and phosphate. The resin-encapsulated mixture is then heat treated at 700 °C in a reducing atmosphere. This results in the production of a fine powder consisting of an olivine LiFePO4 phase, coated with conductive carbon. When this powder is used as active material in a lithium insertion-type electrode, fast charge and discharge rates are obtained at room temperature and an excellent capacity retention is observed.

Description

Carbon-coated Li-containing powders and process for production thereof
The present invention relates to the field of rechargeable lithium batteries and to positive electrode materials operating at voltages greater than 2.8 V vs. Li+/ Li in non-aqueous electrochemical cells. This invention relates in particular to the use of phosphates or sulphates of transition metals as positive electrodes and allows the manufacturing of powdered Li- containing olivine-like and NASICON-like material, with the particles efficiently coated with a controlled amount of conductive carbon.
Lithium secondary batteries are now widely used in consumer electronics. They benefit from the light weight of Li and from its strong reducing character, thus providing the highest power and energy density among known rechargeable battery systems. Lithium secondary batteries are of various configurations depending on the nature of the electrode materials and of the electrolyte used. The commercialised Li-ion system, for instance, uses LiCoO2 and Carbon graphite as positive and negative electrodes, respectively with LiPFg in EC/DEC/PC as a liquid electrolyte. The operating voltage of the battery is related to the difference between thermodynamic free energies within the negative and positive electrodes. Solid oxidants are therefore required at the positive electrode, the materials of choice, up to now, being either the layered LiMO2 oxides (with M is Co or Ni) or the 3-dimensional spinel structure of Li[Mn2]O4. Extraction of Li from each of these three oxides gives access to M4+/ M3+ redox couples located between 3.5 to 5 V vs. Li+/Li.
Three-dimensional framework structures using (XO )n" polyanions have been proposed recently (US 5,910,382) as viable alternatives to the LiMxOy oxides. LiFePO4 and Li3Fe2(PO )3 in particular are the most promising Fe-containing materials that can work at attractive potentials vs. Li+/ Li (3.5 V and 2.8 V respectively). Both compounds operate on the Fe3+/ Fe2+ redox couple which take advantage from the inductive effect of the XO4 n" groups that diminishes the strength of the Fe-O bond compared to a simple oxide.
Pioneering work by Padhi (Padhi et al., /. Elec. Soc. 144(4)) demonstrated the reversible extraction of Li from the olivine-structured LiFePO4 prepared by solid state reaction at 800 °C under Ar atmosphere, starting fromLi2CO3 or LiOH.H2O, Fe(CH3COO)2 and NH4H2PO4.H2O. Unfortunately, probably due to kinetic limitations of the displacement of the LiFePO4/ FePO4 interface, only 60-70 % of the theoretical capacity of 170 mAh / g of active material, was achieved, whatever the charge or discharge rate applied. Indeed, the use of high synthesis temperatures leads to the formation of large particles in which ionic and electronic conductivity is the limiting factor. Several research groups recently reported improvements in the effective reversible capacity of LiFePO4 by decreasing the particle size. This can be done by using highly reactive Feπ precursors (JP 2000-294238 A2), or by using a solution route (WO 02 / 27824 Al), thus allowing LiFeP04 formation at lower temperatures compared to the solid state route described by Padhi.
The poor electronic conductivity of the product can be improved by coating the particles with conductive carbon. This has been done by ball milling LiFePO4 and carbon (Huang et al., Electrochem. Solid-State Lett., 4, A170 (2001)) or by adding a carbon containing compound to already made LiFePO4 and proceeding to a subsequent calcination at about 700 °C (CA
2,270,771). Carbon, and preferably amorphous carbon, can also be introduced in the LiFeP04 synthesis process, being mixed with the solid synthesis precursors before calcination (EP 1184920 A2).
The main problems that may jeopardise the effective use in a positive electrode for Li batteries of Li-containing olivine or NASICON powders such as LiFePO4 or other components mentioned by Goodenough et al. in US5,910,382, arises from their low electronic conductivity and from the fact that both end-members of the de-intercalation process (e.g. LiFePO4 and FeP04) are poor ionic conductors.
As described above, adding carbon, thereby coating the particles with a conductive layer, alleviates the electronic conductivity problem. However, high amounts of carbon are needed. Whereas carbon does not participate in the redox reactions useful for the operation of the battery, a strong penalty for the overall specific capacity of the composite positive electrode is paid. This is illustrated in JP 2000-294238 A2 wherein a LiFePO4/ Acetylene Black ratio of 70 / 25 is used.
The ionic conduction problem can be solved by producing very fine-grained particles. Using a solution route synthesis has been found to be advantageous compared to the classic solid synthesis route. This solution route has been described in EP1261050. This route provides for a very finely divided, homogeneous precursor which needs only moderate conditions of temperature and time to react to the desired crystalline structures. Thanks to the moderate conditions, grain growth, leading to unwanted coarse particles, is avoided. After synthesis, such a powder has to be ball-milled with a relatively large quantity of conductive carbon, typically amounting to 17 wt.% . This invention provides for an improved solution route, ensuring the production of fine grained particles efficiently covered with a conductive carbon layer. Compared to prior art powders, the obtained powders deliver exceptional performances when used in Li-ion batteries. The invention provides for a powder that needs much less total carbon in the electrode for a similar electrode capacity and discharge rate. Similarly, the invention provides for a powder that provides higher capacity and discharge rate when using the same amount of total carbon in the electrode.
A new process is presented for preparing a carbon-coated Li-containing olivine or NASICON powder, comprising the steps of
- preparing a water-based solution comprising, as solutes, one or more Li-containing olivine or NASICON precursor compounds and one or more carbon-bearing monomer compounds,
- precipitating a Li-containing olivine or NASICON precursor compounds and polymerising the monomer compounds in a single step, - heat treating the obtained precipitate in a neutral or reducing environment so as to form a Li- containing olivine or NASICON crystalline phase and decompose the polymer carbon.
The process is specially suitable for the preparation of LiuMv(XO4)w with u = l, 2 or 3, v = l or 2, w = 1 or 3, M is TiaVbCrcMndFeeCθfNigSchNbi with a+b+c+d+e+f+g+h+i = 1 and X is Px-1Sx with 0 ≤ x < l.
It is clear that the individual 'a' to ϊ' parameters have values going from 0 to 1. Obviously, their particular values should allow for electroneutrality of the crystalline phase when combined with a proper set 'u', V and 'w' parameters. Examples are: LiMPO4 such as in LiFeP04, LiNiP04, LiMnPO4; LiM2(PO4)3 such as in LiTi2(PO4)3, LiFeNb(PO4)3; Li2M2(PO4)3 such as in Li2FeTi(PO4)3; Li3M2(PO4)3 such as in Li3Ti2(PO4)3, Li3Sc2(PO4)3, Li3Cr2(PO4)3, Li3In2(PO4)3, Li3Fe2(PO4)3, Li3FeV(PO4)3.
The invented process is especially suitable for the preparation of coated LiFePO4.
The precipitation of Li-containing olivine or NASICON precursor compounds and the polymerisation of the monomers can be performed by evaporating water from the water-based solution. The carbon-bearing monomer compounds can be a polyhydric alcohol and a polycarboxylic acid, such as, respectively, ethylene glycol and citric acid. When the synthesis of coated LiFeP04, is envisaged, equimolar amounts of Li, Fe and phosphate, such as LiH2PO4 and Fe(NO3)3, are dissolved in water together with a polyhydric alcohol and a polyc'arboxylic acid, the water is then evaporated at a temperature between 60 and 100 °C, and a heat-treatment is performed at a temperature between 600 and 800 °C, preferably between 650 and 750 °C.
The object of the invention also concerns a carbon-coated LiFePO4 powder for use in Li insertion-type electrodes, which, when used as an active component in a cathode cycled between 2.0 and 4.5 V against a Li anode at a discharge rate of C / 5 at 25 °C, is characterised by a reversible electrode capacity expressed as a fraction of the theoretical capacity and a total carbon content of at least 75 % capacity and less than 4 wt.% carbon, or, at least 80 % capacity and less than 8 wt.% carbon.
Other objects of the invention are: an electrode mix containing the above-mentioned carbon- coated LiFePO4 and batteries containing the latter electrode mix.
For a proper understanding of the invention as described herein, the following definitions are to be considered.
A "Li-containing olivine or NASICON precursor compound" is to be understood as a metal- bearing compound such as a salt, oxide or hydroxide of one ore more metals susceptible to be converted to, or to react to, the desired final compound. Typically, the conversion or reaction is performed by applying a thermal treatment.
A "carbon-bearing monomer compound" is to be understood as an organic compound susceptible to polymerise with itself (to form a homopolymer) or together with other monomers (to form a copolymer).
A "reducing environment" can be obtained by using a reducing gas, or by relying on reducing properties of solids, such as carbon, present in the bulk of the material.
The "electrode capacity expressed as a fraction of the theoretical capacity" is the ratio of the capacity of the active product contained in the electrode, to the theoretical capacity of the active product. For FeLiP0 , a specific theoretical capacity of 170 mA / g is assumed. When the charge or discharge rate is expressed as C / x, this means that one Li per LiFeP04 is exchanged in 'x' hour.
The general principle of the invention can be apphed whenever a high quality carbon coating is needed on a metal-bearing powder. Olivine and NASICON phases, when used in rechargeable Li-ion batteries, are known to be rather poor electronic conductors. As such, they particularly benefit from a carbon coating which is rendered conductive by a suitable heat treatment.
It is assumed that the metal bearing precursors, such as Li, metal and phosphate or sulphate ions, are trapped homogeneously on the atomic scale throughout the chelating polymer matrix. Such a structure eliminates the needs for long range diffusion during the subsequent formation of the crystalline phase. Therefore, at relatively low temperature, the precursors can form a homogeneous single phase of precise stoichiometry, intimately coated by a conductive carbonaceous network.
Solvent evaporation conducting to an homogeneous mix of solid precursor compounds and the polymerisation of the monomers are performed in one single step. This requires the polymerisation to occur simultaneously with the solidification of at least part of the precursor.
Different means can be employed to form the homogeneous mix of precursor (e.g. change in pH, temperature) and to trigger the polymerisation (e.g. addition of catalyst, UV). However, when the polymerisation reaction produces water as a condensate, both the precipitation of the precursor and the polymerisation are triggered by identical means, i.e. by removal of water from the reaction vessel. This results in a particularly simple and efficient process.
It has been found that the presence of heteroatoms (i.e. atoms other than C, O and H) in the monomers may degrade the performance of the obtained carbon coating, in particular its electrical conductivity. It is therefore preferred to use monomer compounds containing only C, O and H atoms.
When the production of LiFeP0 is envisaged, the Fe source in the precursor compound can be Fe11 or Fem: the reducing conditions needed to avoid the burning of the carbon coating during the step of heat treatment ensures the conversion of any Fem to the required Fe 1 state. The preferred water evaporation temperature range is 60 to 100 °C. This ensures that the precipitation of the precursor compound and the polymerisation reaction occur at least partly simultaneously.
The conductivity of the carbon residue is enhanced when the heat treatment is performed at 600 °C or higher. However, a temperature of more than 800 °C may degrade the quality of the product because of grain-growth or because of excessive reduction by carbon. A heath treatment at 650 to 750 °C is preferred.
The positive electrode of the electrochemical cell is made of optimised LiFeP04 particles intimately mixed with an electronically conducting carbon species made as described below. The active material / coated-carbon ratio can be adjust in the synthesis of LiFeP0 between 1 and 25 wt.% of carbon. It is preferred to minimise the relative amount of carbon, whether present as coating material or as carbon added during the manufacture of the electrode. Indeed, carbon does not participate in the redox reactions and therefore represents inert mass reducing the specific capacity of the electrode. Nevertheless, it is desired to have at least 2 wt.% of coated carbon to exploit the invention fully.
The invention is illustrated by the preparation of optimised LiMPO particles, coated with (electronic) conductive carbon through low-temperature chemical routes.
For the preparation of a LiFeP04/ C composite, an aqueous solution containing Fe, Li and phosphate is prepared using e.g. Fe(N03)3.9H20 and LiH2PO4. The solution is added under stirring in air to an aqueous solution of citric acid. Ethylene glycol is then added to the solution for an ethylene glycol / citric acid molar ratio of 1 / 1. The precursor to carbon ratio in the solution will determine the relative amount of carbon in the coating. Key to this process are the fact that both the LiFeP04 precursors and the monomers are to be water-soluble.
In a second step, the water is slowly evaporated at 80 °C under air. When nearly dry, the solution turns to a gel due to the polymerisation between citric acid and ethylene glycol. The gel is dried by maintaining it at 80 °C. A very homogeneous mixture, containing Li, Fe and phosphate in the stoichiometric proportions of LiFePO4 together with the carbon bearing polymer, is then produced. Advantageously, monomers are chosen which have a lower partial pressure than water at the drying temperature. Premature evaporation of the monomers is thus avoided. In a third step, the homogeneous mixture is progressively heat-treated under a reducing atmosphere (N2/ H2, 10 % H2) to yield, at a temperature of about 500 °C, a crystalline LiFeP04 phase coated with a controlled amounts coated carbon. However, at 500 °C, the coated carbon is partly insulating. A treatment between 600 °C and 800 °C is thus preferred as it yields conductive carbon. Thanks to the presence of carbon, the surrounding environment of LiFeP04 is strongly reducing. This is useful to reduce remaining traces of Fe111 precursors to Fe11, but can lead to unwanted results when the percentage of carbon is high. Indeed, high carbon contents (more than 15 %) combined with prolonged treatment (more than 5 hours) at 700 to 800 °C partly reduces Fe11 in LiFePO4 to Fe°. This leads to the formation of impurities such as Fe2P. As determined by electrochemical titration, the obtained optimised powder may still contain a small amount of Fem (less than 3 M%), an amount which is in fact inferior to that obtained in the synthesis of pure LiFeP04 without carbon. The result of the heat treatment can easily be monitored and optimised by e.g. X-ray diffraction or by Mossbauer spectroscopy, to ensure that Fem is nearly completely reduced to Fe11 and that no significant amount of Fe11 is reduced to Fe°.
The invention is illustrated by the following examples. Four LiFeP04/ C composites were produced according to the process described above. Aqueous solutions containing 0.4 M / 1 Fe, Li and phosphate and 0.1 to 1 M / 1 ethylene glycol and citric acid were prepared using Fe(N03)3.9H20 and LiH2P04. The solutions were dried for 12 h at 80 °C. The dry residues were then heat treated for 10 h at 700 °C under a N2/ H2 atmosphere with 10 % H2.
The results, presented in Table 1, show the influence of the monomer concentrations in the solution on the amount of carbon coated on the LiFeP04 particles. The apparent loss of carbon, which is rather high compared to the theoretical amount expected, comes probably from the reduction of Fem to Fe11 during the heat treatment. The polymerisation needs not be complete.
Table 1: Theoretical vs. observed amount of carbon in the coating as a function of the monomer concentration in the solute (for 0.1 M / 1 of Fe, Li and phosphate in the solute)
Figure imgf000009_0001
Figures 1 to 5 illustrate the invention.
Fig. 1: X-ray diffractograms (CuKα) and the S.E.M. photographs of two LiFeP0 powders coated with 3.6 (top) and 24 % (bottom) carbon
Fig. 2: Electrochemical response of a Li / LiPFβ ECDMC / LiFePO4 electrochemical cell (swagelok type) cycled at C / 5 and 25 °C, using LiFePO4 with 3.6 (top) and 24 % (bottom) of coated carbon
Fig. 3: Results obtained with Li / LiPF6 EC : DMC / LiFePO4 electrochemical coin cells embedded in a plastic film. LiFePO4 with 3.6 % of coated carbon cycled at C / 5 and 25 °C (A) or 55 °C (B); LiFeP04 prepared according to the prior art solution route and ball-milled with 17 % of conductive carbon cycled at C / 10 and 55 °C (C)
Fig. 4: In situ XRD patterns of LiFeP04 in a Li / LiPF6 EC : DMC / LiFePO4 electrochemical cell cycled at C / 5 and 25 °C; LiFePO4 prepared according to the invention (top) and according to the prior art solution route and ball-milled with 17 % of conductive carbon (bottom)
Fig. 5: Evolution of the specific active material capacity achieved in a Li / LiPF6 EC : DMC / LiFeP04 prepared according to the invention with 3.6 (B) and 24 % (C) of coated carbon; LiFeP0 prepared according to the prior the art solution route and ball-milled with 17 % of conductive carbon (D); commercial LiCo02 are shown for comparison (A) Figures 1 to 5 are now discussed in more details. The X-ray diffractograms and the S.E.M. photographs of two LiFeP04 powders coated with 3.6 and 24 % of carbon are given in Figure 1. The photographs are representative for the overall powder. For LiFePO4 with 3.6 % of coated carbon, the network formed by the coated particles is very well spaced and regular. The particles are sufficiently fine (around 1 μm) to alleviate the penalising displacement length of the interface between LiFePO4 and FePO , while enough space is left for species to migrate. For 24 % of coated carbon, the carbon matrix itself can be observed. The carbon network surrounds the LiFeP04 particles whose size is even smaller than in the former case. The LiFePO4 phase appears to be pure when 3.6 % of carbon is coated. When 24 % is coated, some LiFePO4 is reduced to Fe2P after 10 h at 700 °C. This demonstrates that the higher the carbon percentage, the more efficient the reduction.
These powders give the electrochemical response shown in Figure 2. The electrochemical cells were built in Swagelok configuration with Li metal pasted on a Ni foil as the negative electrode, and LiPF6 in EC : DMC as the electrolyte. The positive electrode is the powder obtained directly from the described process. The signature of Figure 2 (voltage as a function of x in LixFeP04) was obtained at 25 °C for an equivalent charge / discharge rate of C / 5, i.e. 1 Li extracted or inserted in 5 h.
About 85 % of the theoretical capacity of the active material can be achieved when using 24 % of coated carbon. The performance of the total electrode is however rather penalised by the large quantity of carbon. The amount of carbon can be dramatically decreased. When using 3.6 % of coated carbon, 78 % of the capacity is still achieved. In each case, the irreversible capacity at first cycle is very small.
Figure 3 illustrates the stability of the LiFeP0 composite produced according to the invention using 3.6 % of coated carbon. This material was cycled at C / 5 at 25 and at 55 °C. The resulting specific capacity is superior to that obtained with uncoated material prepared according to the prior art solution route and ball-milled with 17 % of conductive carbon. If we compare the specific capacities of the total electrodes, the superiority of the invented process becomes even more apparent thanks to the much lower amount of total carbon.
In Figure 4, in situ X-ray diffraction patterns are shown for a full charge / discharge cycle. With the powder coated according to the invention, at the end of the charge cycle, all the diffraction peaks of LiFePO disappear at the benefit of triphylite-FeP0 peaks. The biphasic phenomenon is thus complete. However, with powder prepared according to the prior art solution route, this is not the case.
In Figure 5, the specific capacity of several active materials is reported in function of the cycling rate. Materials tested are: LiFeP04 composite obtained by the process according to the invention with 3.6 and 24 % of coated carbon, LiFeP0 prepared according to the prior art solution route and ball-milled with 17 % of conductive carbon, and commercial LiCo02. The 3.6 % carbon-coated LiFeP04 performs better than any other at low discharge rates. At higher rates, it is outperformed by LiCo02 (a much more expensive product), and, as expected, by 24 % carbon-coated LiFePO . Indeed, the higher amount of coated carbon tends to improve the high current performance. Whatever the conditions, however, the products which are carbon- coated according to the invention remain superior to the prior art product.

Claims

Claims
1. Process for preparing a carbon-coated, Li-containing olivine or NASICON powder, comprising the steps of - preparing a water-based solution comprising, as solutes, one or more Li-containing olivine or NASICON precursor compounds and one or more carbon-bearing monomer compounds,
- precipitating the Li-containing olivine or NASICON precursor compounds and polymerising the monomer compounds in a single step
- heat treating the obtained precipitate in a neutral or reducing environment so as to form a Li- containing olivine or NASICON crystalline phase and decompose the polymer to carbon.
2. Process according to claim 1, whereby the crystalline phase is LiuMv(XO4)w with u = 1, 2 or 3, v = 1 or 2, w = 1 or 3, M is TiaVbCrcMndFeeCofNigSchNbi with a+b+c+d+e+f+g+h+i = 1 and X is PX-1SX with 0 < x < 1
3. Process according to claim 2, whereby the crystalline phase is LiFeP04
4. Process according to claim 1, whereby the precipitation of Li-containing olivine or NASICON compounds and the polymerisation of the monomers is performed by evaporating water from the water-based solution
5. Process according to claim 4, whereby the carbon-bearing monomer compounds are a polyhydric alcohol and a polycarboxylic acid
6. Process according to claim 5, whereby the polyhydric alcohol is ethylene glycol and the polycarboxylic acid is citric acid
7. Process for the production of carbon-coated LiFeP0 according to claim 5, whereby
- the water-based solution contains equimolar amounts of Li, Fe and phosphate, - the evaporation of water from the solution is performed at a temperature between 60 and 100 °C,
- the heat-treatment is performed at a temperature between 600 and 800 °C, preferably between 650 and 750 °C
8. Process according to claim 7 whereby the water-based solution is prepared using LiH2PO4 and Fe(NO3)3.aq
9. A carbon-coated LiFePO powder for use in Li insertion-type electrodes, which, when used as an active component in a cathode cycled between 2.0 and 4.5 V against a Li anode at a discharge rate of C / 5 at 25 °C, is characterised by a reversible electrode capacity expressed as a fraction of the theoretical capacity and a total carbon content of at least 75 % capacity and less than 4 wt.% carbon, or, at least 80 % capacity and less than 8 wt.% carbon.
10. Electrode mix containing carbon-coated LiFeP04 according to claim 9
11. A battery containing an electrode mix according to claims 10
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