CARBON-TREATED COMPLEX OXIDES AND METHOD FOR MAKING THE SAME

• US 20100297496A1
• Filed: 10/30/2007
• Published: 11/25/2010
• Est. Priority Date: 10/30/2006
• Status: Abandoned Application

• Current Assignee: Johnson Matthey Battery Materials Ltd., Universite De Montreal, L'
• Original Assignee: Johnson Matthey Battery Materials Ltd.
• Inventors: Liang, Guoxian, Gauthier, Michel, Lahrs, Thorsten, Michot, Christophe, Ravet, Nathalie
• Application Number:
  US12/445,645
• Publication Number:
  US 20100297496A1
• Time in Patent Office: Days
• US Class Current: 429/207
• CPC Class Codes: C01B 25/45 containing plural metal, or metal and ammonium
• CPC Class Codes: H01M 10/0525 Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
• CPC Class Codes: H01M 2004/028 Positive electrodes
• CPC Class Codes: H01M 2220/30 Batteries in portable systems, e.g. mobile phone, laptop
• CPC Class Codes: H01M 4/0402 Methods of deposition of the material
• CPC Class Codes: H01M 4/0471 involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
• CPC Class Codes: H01M 4/136 Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
• CPC Class Codes: H01M 4/1397 of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
• CPC Class Codes: H01M 4/5825 Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
• CPC Class Codes: H01M 4/622 being polymers
• CPC Class Codes: H01M 4/625 Carbon or graphite
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

The invention relates to a process for the preparation of a carbon-treated complex oxide having a very low water content and to its use as cathode material.

The carbon-treated complex oxide is composed of particles of a compound AMXO₄ having an olivine structure which carry, on at least a portion of their surface, a film of carbon deposited by pyrolysis. A represents Li, alone or partially replaced by at most 10% as atoms of Na or K. M represents Fe(II), alone or partially replaced by at most 50% as atoms of one or more other metals chosen from Mn, Ni and Co, and/or by at most 10% as atoms of one or more aliovalent or isovalent metals other than Mn, Ni or Co, and/or by at most 5% as atoms of Fe(III). X₄ represents PO₄, alone or partially replaced by at most 10 mol % of SO₄ and SiO₄. Said material has a water content <1000 ppm.

Claims

1. A material C-AMXO₄, composed of particles of a compound corresponding to the formula AMXO₄ which have an olivine structure and which carry, on at least a portion of their surface, a film of carbon deposited by pyrolysis, the formula AMXO₄ being such that:

A represents Li, alone or partially replaced by at most 10% as atoms of Na or K;

M represents Fe(II), alone or partially replaced by at most 50% as atoms of one or more other metals chosen from Mn, Ni and Co and/or by at most 10% as atoms of one or more aliovalent or isovalent metals other than Mn, Ni or Co, and/or by at most 5% as atoms of Fe(III);

XO₄ represents PO₄, alone or partially replaced by at most 10 mol % of at least one group chosen from SO₄ and SiO₄; and

said material having a water content of less than 1000 ppm.

2. The material as claimed in claim 1, wherein M represents Fe(II), alone or partially replaced by at most 50% as atoms of one or more other metals chosen from Mn, Ni and Co and/or by at most 10% as atoms of one or more aliovalent or isovalent metals chosen from Mg, Mo, Nb, Ti, Al, Ta, Ge, La, Y, Yb, Sm, Ce, Hf, Cr, Zr, Bi, Zn, Ca and W and/or by at most 5% as atoms of Fe(III).

3. The material as claimed in claim 1, wherein the water content is less than 500 ppm.

4. The material as claimed in claim 1, wherein the carbon film is uniform, adherent and nonpowdery.

5. The material as claimed in claim 1, wherein the carbon film represents from 0.03 to 15% by weight, with respect to the total weight.

6. The material as claimed in claim 1, wherein the complex oxide AMXO₄ comprises less than 1000 ppm of water and less than 1000 ppm of LiOH, of Li₃PO₄, of Li₄P₂O₇, of lithium polyphosphates, optionally hydrated, or of Li₂CO₃.

7. The material as claimed in claim 1, wherein the complex oxide AMXO₄ comprises less than 1000 ppm of water and less than 10 000 ppm of Fe₂O₃, Li₃Fe₂(PO₄)₃, LiFeP₂O₇, or an Fe³⁺ compound which can be detected electrochemically.

8. The material as claimed in claim 1, wherein the material C-AMXO₄ is C—

LiFePO₄.

9. The material as claimed in claim 8, wherein the complex oxide LiFePO₄ comprises:

less than 1000 ppm of water;

less than 1000 ppm of LiOH, of Li₃PO₄, of Li₄P₂O₇, of lithium polyphosphates, which are optionally hydrated, or Li₂CO₃, preferably less than 500 ppm and more particularly less than 200 ppm; and

less than 10 000 ppm of Fe₂O₃, of Li₃Fe₂(PO₄)₃, of LiFeP₂O₇ or of an Fe³⁺ compound which can be detected electrochemically, preferably less than 5000 ppm and more particularly less than 2000 ppm.

10. The material as claimed in claim 1, wherein it is composed of individual particles and agglomerates of individual particles.

11. The material as claimed in claim 10, wherein the size of the individual particles is between 10 nm and 3 μ

m and the size of the agglomerates is between 100 nm and 30 μ

m.

12. The material as claimed in claim 11, wherein it has a specific surface between 5 m²/g and 100 m²/g.

13. A process for producing a material as claimed in claim 1, which consists in preparing a material C-AMXO₄ by a process comprising a stage of pyrolysis of a source compound of conductive carbon, wherein said material C-AMXO₄ is placed, immediately after it has been obtained, in a controlled atmosphere and is then kept in said controlled atmosphere, said controlled atmosphere either being an oxidizing atmosphere with a dew point of less than −

30°

C., or a nonoxidizing atmosphere.

14. The process as claimed in claim 13, wherein the material C-AMXO₄ is prepared by reacting, by placing under thermodynamic or kinetic equilibrium, a gas atmosphere with a mixture in the required proportions of the following source compounds a), b), c), d) and e):

a) one or more compounds which are sources of the element or elements forming A;

b) a source or several sources of the element or elements forming M;

c) a compound which is a source of the element or elements X;

d) a compound which is a source of oxygen; and

e) a compound which is a source of conductive carbon;

the synthesis being carried out continuously in a rotary furnace while controlling the composition of said gas atmosphere, the temperature of the synthesis reaction and the level of the source compound c) relative to the other source compounds a), b), d) and e), in order to fix the oxidation state of the transition metal at the degree of valency desired for the structure of the compound of type AMXO₄,

the process comprising at least one stage of pyrolysis of the compound e).

15. The process as claimed in claim 14, wherein the gas atmosphere is a stream of dry nitrogen moving countercurrentwise with respect to the source compounds.

16. The process as claimed in claim 14 for the preparation of a material C—

LiFePO₄ comprising less than 1000 ppm of water, wherein;

the source compound a) is a lithium compound chosen from the group consisting of lithium oxide, lithium hydroxide, lithium carbonate, the neutral phosphate Li₃PO₄, the hydrogen phosphate LiH₂PO₄, lithium ortho-, meta- and polysilicates, lithium sulfate, lithium oxalate, lithium acetate and one of their mixtures;

the source compound b) is an iron compound chosen from the group consisting of iron(III) oxide, trivalent iron phosphate, lithium iron hydroxyphosphate, trivalent iron nitrate, ferrous phosphate, hydrated or nonhydrated vivianite Fe₃(PO₄)₂, iron acetate (CH₃COO)₂Fe, iron sulfate (FeSO₄), iron oxalate, ammonium iron phosphate (NH₄FePO₄) and one of their mixtures; and

the source compound c) is a phosphorus compound chosen from the group consisting of phosphoric acid and its esters, the neutral phosphate Li₃PO₄, the hydrogen phosphate LiH₂PO₄, mono- and diammonium phosphates, trivalent iron phosphate and manganese ammonium phosphate (NH₄MnPO₄).

17. The process as claimed in claim 14, wherein the pyrolysis of the compound e) is carried out at the same time as the synthesis reaction between the compounds a) to d) to form the compound AMXO₄ or in a stage in succession to the synthesis reaction.

18. The process as claimed in claim 13, wherein the source compound of conductive carbon is a compound which is in the liquid state or in the gas state, a compound which can be used in the form of a solution in a liquid solvent or a compound which changes to the liquid or gas state during its decomposition.

19. The process as claimed in claim 13, wherein the source compound of conductive carbon is chosen from the group consisting of liquid, solid or gaseous hydrocarbons and their derivatives, perylene and its derivatives, polyhydric compounds, polymers, cellulose, starch and their esters and ethers, and their mixtures.

20. The process as claimed in claim 13, wherein the source compound of conductive carbon is CO or a gaseous hydrocarbon and it is subjected to dismutation.

21. The process as claimed in claim 20, wherein the dismutation is catalyzed by a transition metal element present in at least one of the precursors a) to c) or by a compound of a transition metal added to the mixture of precursors.

22. The process as claimed in claim 13, wherein the source compound of conductive carbon is a gas chosen from the group consisting of ethylene, propylene, acetylene, butane, 1,3-butadiene, 1-butene and a mixture of at least two of them and the thermal decomposition is carried out by cracking in a furnace at a temperature between 100 and 1300°

C. in the presence of an inert carrier gas.

23. The process as claimed in claim 13, wherein the source compound of conductive carbon is a hydrocarbon and the pyrolysis is carried out by CVD.

24. The process as claimed in claim 13, wherein it comprises a milling stage carried out on a material C-AMXO₄, either under an oxidizing atmosphere with a dew point of less than −

30°

C., or under a nonoxidizing atmosphere.

25. The process as claimed in claim 24, wherein the milling is a jet milling.

26. The process as claimed in claim 13, wherein it comprises an additional stage which consists in washing the material C-AMXO₄ in water at a temperature of greater than 60°

C., in recovering the product by filtration and in drying it down to a maximum water content of 1000 ppm.

27. An electrode, composed of a film of composite material deposited on a conductive substrate forming the current collector, wherein said composite material is composed of a material C-AMXO₄ as claimed in claim 1, a binder and a compound which conducts electrons.

28. The electrode as claimed in claim 27, wherein the material C-AMXO₄ is C—

LiFePO₄.

29. A battery, composed of an anode, a cathode and an electrolyte comprising a lithium salt, wherein the cathode comprises a material as claimed in claim 1.

30. The battery as claimed in claim 29, wherein the material C-AMXO₄ is C—

LiFePO₄.