Battery grade cathode coating formulation

1. A process for preparing a battery grade formulation comprising a carbon-deposited alkali metal phosphate, said process comprising a milling step of the carbon-deposited alkali metal phosphate C-A a M m (XO 4 ) x in the form of strong agglomerates, wherein the strong agglomerates are obtained by a process comprising a dry high-energy ball milling of precursors of the carbon-deposited alkali metal phosphate:

wherein C-A a M m (XO 4 ) x is composed of particles of a compound corresponding to the general formula A a M m (XO 4 ) x which have an olivine structure and which carry, on at least a portion of their surface, carbon deposited by a thermal process, the general formula A a M m (XO 4 ) x being such that:

A represents Li, alone or partially replaced by at most 20% as atoms of Na and/or K, and 0<a≦8;

M comprise at least 50% at, of Fe(II) or Mn(II) or mixture thereof, and 1≦m≦3; and

XO 4 represents PO 4 , alone or partially replaced by at most 30 mol % of at least one group chosen from SO 4 and SiO 4 , and 0<x≦3;

wherein M, X, a, m and x are selected as to maintain electroneutrality of said compound; and

wherein said milling step is performed in the presence of a solvent used for battery electrode coating.

2. A process as in claim 1 , wherein the milling step is performed in the presence of a solvent comprising at least 50% by volume of water or N-methyl-pyrrolidone.

3. A process as in claim 2 , wherein the milling step is performed in water.

4. A process as in claim 2 , wherein the milling step is performed in N-methylpyrrolidone.

5. A process as in claim 1 , wherein the formulation comprises at least one electric conductive additive and/or at least one binder.

6. A process as in claim 5 , wherein the electric conductive additive is selected from the group consisting of carbon black, graphite, carbon fiber, carbon nanotube, carbon nanofiber, graphene, vapor growth carbon fiber and metallic oxide.

7. A process as in claim 5 , wherein the binder is selected from polymers comprising repeating unit of hexafluoropropylene and/or vinylidene fluoride.

8. A process as in claim 5 , wherein the binder is selected from polymers comprising ethylene oxide repeating units.

9. A process as in claim 1 , wherein before the milling step, the C-A a M m (XO 4 ) x has a particle size distribution of D 90 ≧50 μm.

10. A process as in claim 1 , wherein after the milling step, the C-A a M m (XO 4 ) x has a particle size distribution of D 90 ≦30 μm.

11. A process as in claim 1 , wherein after the milling step, the C-A a M m (XO 4 ) x is composed of individual particles and/or agglomerates of individual particles.

12. A process as in claim 11 , wherein the individual particles are between 10 nm and 3 μm.

13. A process as in claim 11 , wherein the agglomerates are between 100 nm and 3 μm.

14. A process as in claim 1 , Wherein after the milling step, the C-A a M m (XO 4 ) x is composed of secondary particles with a 0.5 μm≦D 50 ≦10 μm.

15. A process as in claim 1 , wherein the formulation comprises a surface treatment agent.

16. A process as in claim 15 , wherein the surface treatment agent is selected from the group consisting of titanium, zirconium and silicon alkoxides.

17. A process as in claim 15 , wherein the formulation comprises up to 2% by weight, relatively to C-A a M m (XO 4 ) x , of the surface treatment agent.

18. A process as in claim 1 , wherein the formulation comprises at least one submicron-sized C-A a M m (XO 4 ) x and at least one micron-sized C-A a M m (XO 4 ) x .

19. A process as in claim 1 , wherein the C-A a M m (XO 4 ) x is obtained by a process comprising a thermal treatment of precursors, wherein the precursors comprises FePO 4 , Li 2 CO 3 and a carbon source.

20. A process as in claim 1 , wherein the C-A a M m (XO 4 ) x is obtained by a process comprising a thermal treatment of precursors, wherein the precursors comprises Fe 2 P 2 O 7 , optionally having a carbon deposit, Li 2 CO 3 and a carbon source.

21. A process as in claim 1 , wherein before the milling step, the C-A a M m (XO 4 ) x has a particle size distribution of D 90 ≧100 μm.

22. A process as in claim 1 , wherein before the milling step, the C-A a M m (XO 4 ) x has a particle size distribution of D 90 ≧150 μm.