Battery cathode and method of manufacture therefor

• US 6,620,550 B2
• Filed: 01/23/2001
• Issued: 09/16/2003
• Est. Priority Date: 01/23/2001
• Status: Expired due to Term

• Current Assignee: Duracell U.S. Operations, Inc. (Berkshire Hathaway Incorporated)
• Original Assignee: Gillette Company (The Procter & Gamble Company)
• Inventors: Mao, Ou, Christian, Paul A., Zeng, Shuming
• Primary Examiner(s): CHANEY, CAROL DIANE
• Application Number:
  US09/768,138
• Publication Number:
  US 20020134964A1
• Time in Patent Office: 966 Days
• Field of Search: 429/224, 429/232, 429/231.1
• US Class Current: 429/224
• CPC Class Codes: B82Y 30/00 Nanotechnology for materials or surface science, e.g. nanocomposites
• CPC Class Codes: H01M 2300/0014 Alkaline electrolytes
• CPC Class Codes: H01M 4/08 Processes of manufacture
• CPC Class Codes: H01M 4/50 of manganese
• CPC Class Codes: H01M 4/625 Carbon or graphite

Abstract

The invention provides an improved method for preparing homogeneous intermixtures of particulate manganese dioxide and conductive carbon for use in cathodes for electrochemical cells, in particular alkaline primary cells. Homogeneous intermixtures can be prepared by mechanically activating an essentially dry admixture of particulate electrolytic manganese dioxide and a natural graphite, an expanded graphite or combinations thereof with inert, rigid milling media by the agitation process of the invention. Improved cell discharge performance at both low and high rates of discharge can be achieved for extremely low levels of highly expanded graphite, typically between about 1 and 5 wt %.

Claims

1. A process for preparing a cathode mixture for an electrochemical cell comprising the steps of:

(a) forming a mixture comprising milling media and an essentially dry reaction mixture, said reaction mixture comprising particulate manganese dioxide and conductive carbon, wherein the weight ratio of said reaction mixture to said milling media is between about 1;

3 to 1;

10;

(b) mechanically agitating said reaction mixture with said milling media therein at ambient temperature to form a homogeneously intermixed product mixture without reducing the average particle size of said manganese dioxide by more than about 10 percent.

2. The process of claim 1 wherein said manganese dioxide comprises particulate electrolytic manganese dioxide (EMD) and aqueous electrolyte is added to said homogeneously intermixed product mixture after step (b).

3. The process of claim 1 wherein said reaction mixture comprising particulate manganese dioxide and conductive carbon comprises between about 1 and 10 percent by weight conductive carbon.

4. The process of claim 1 wherein said reaction mixture comprising particulate manganese dioxide and conductive carbon comprises between about 2 and 4 percent by weight conductive carbon.

5. The process of claim 1 wherein said conductive carbon comprises expanded graphite.

6. The process of claim 1 wherein said conductive carbon comprises expanded graphite having an average particle size in the range between 0.5 and 40 microns.

7. The process of claim 1 wherein said conductive carbon comprises an admixture of expanded graphite and a graphite selected from the group consisting of natural graphite and synthetic non-expanded graphite and any mixture thereof.

8. The process of claim 1 wherein said conductive carbon comprises a graphite selected from the group consisting of natural crystalline, and synthetic crystalline graphite, and any mixture thereof, wherein said graphite, before said mechanical agitation in step (b) has an average particle size in the range between 2 and 50 microns.

9. The process of claim 1 wherein said manganese dioxide is particulate manganese dioxide having an average particle size, before said mechanical agitation in step (b), in the range between 10 and 50 microns.

10. The process of claim 1 wherein said mechanical activation step is accomplished by agitating said reaction mixture with said milling media.

11. The process of claim 1 wherein said milling media comprise rigid, chemically inert particles that do not react with said reaction mixture during said mechanical activation step.

12. The process of claim 1 wherein said reaction mixture additionally comprises a polymeric binder.

13. The process of claim 1 wherein said milling media comprises a material selected from the group consisting of ceramic, glass, metallic, and polymeric materials.

14. The process of claim 1 wherein said milling media comprises particles in the shape of at least one of beads, spheres, cylinders, rods and radius-end cylinders, wherein said milling media particles have a mean effective diameter between 0.2 and 5 mm.

15. The process of claim 1 wherein said milling media have a density ranging from about 3 to 15 g/cm³.

16. The process of claim 1 wherein said weight ratio of said reaction mixture to said milling media is between 1:

4 and 1;

6.

17. The process of claim 1 wherein said milling media comprise a ceramic material selected from the group consisting of steatite, aluminum oxide, zirconium oxide, zirconia-silica, yttria-stabilized zirconium oxide, magnesia-stabilized zirconium oxide, silicon nitride, silicon carbide, and cobalt-stabilized tungsten carbide.

18. The process of claim 1 wherein said reaction mixture is mechanically activated in step (b) by contacting said reaction mixture and said milling media therein with a mechanical apparatus selected from the group consisting of ball mill, planetary mill, stirred ball mill, vibrating ball mill, multi-axial shaker/mixer, and any combination thereof.

19. The process of claim 1 wherein said mechanical activation in step (b) is conducted for a period of time of from about 0.1 to 8 hours.

20. The process of claim 1 wherein said mechanical activation in step (b) is conducted for a period of time of from about 0.5 to 4 hours.

21. An alkaline electrochemical cell comprising a case;

positive and negative terminals;

an anode comprising zinc metal or a zinc alloy;

an aqueous electrolyte; and

a cathode comprising a homogeneous mixture of manganese dioxide and graphite, said homogeneous mixture made by the process of;

(a) forming a mixture comprising milling media and an essentially dry reaction mixture, said reaction mixture comprising particulate manganese dioxide and graphite, wherein the weight ratio of said reaction mixture to milling media is between about 1;

3 to 1;

10;

(b) mechanically agitating said reaction mixture with said milling media therein at ambient temperature to form said homogeneous mixture without reducing the average particle size of said manganese dioxide by more than about 10 percent.

22. The alkaline electrochemical cell of claim 21 further comprising:

(c) separating said milling media from said reaction mixture after step (b) and subsequently adding aqueous electrolyte to said mixture.

23. The alkaline electrochemical cell of claim 21 wherein said mechanical activation is accomplished by agitating said reaction mixture with said milling media.

24. The alkaline electrochemical cell of claim 21 wherein said particulate manganese dioxide has been treated by contact with ozone gas prior to forming said mixture in step (a).

25. The alkaline electrochemical cell of claim 21 wherein said particulate maganese dioxide, before said mechanical agitation in step (b), has an average particle size between 10 and 50 microns.

26. The alkaline electrochemical cell of claim 21 wherein said reaction mixture comprising manganese dioxide and graphite comprises between about 1 and 10 percent by weight graphite.

27. The alkaline electrochemical cell of claim 21 wherein said reaction mixture comprising manganese dioxide and graphite comprises between about 2 and 4 percent by weight graphite.

28. The alkaline electrochemical cell of claim 21 wherein said graphite comprises expanded graphite.

29. The alkaline electrochemical cell of claim 21 wherein said graphite comprises an admixture of expanded graphite and a graphite selected from the group consisting of natural graphite and synthetic non-expanded graphite and any mixture thereof.

30. The alkaline electrochemical cell of claim 21 wherein said graphite comprises expanded graphite having an average particle size, before said mechanical agitation in step (b), in the range between 0.5 and 40 microns.

31. The alkaline electrochemical cell of claim 21 wherein said milling media is chemically inert in that it does not react with said mixture comprising manganese dioxide and graphite during said mechanical agitation step.

32. The alkaline electrochemical cell of claim 21 wherein said milling media comprises a material selected from the group consisting of ceramic, glass, metallic, and polymeric materials.

33. The alkaline electrochemical cell of claim 21 wherein said milling media comprises particles in the shape of at least one of beads, spheres, cylinders and radius-end cylinders, wherein said milling media particles have mean diameters between 0.2 and 5 mm.

34. The alkaline electrochemical cell of claim 21 wherein said milling media comprises yttria-stabilized zirconium oxide spheres.

35. The alkaline electrochemical cell of claim 21 wherein said mechanical agitation in step (b) is accomplished by agitating said reaction mixture and said milling media therein with a mechanical apparatus selected from the group consisting of ball mill, planetary mill, stirred ball mill, vibrating ball mill, multi-axial shaker/mixer, and any combination thereof.

36. The alkaline electrochemical cell of claim 21 wherein said mechanical agitation in step (b) is conducted for a period of time of from about 0.5 to 4 hours.

37. A process for treating manganese dioxide comprising the steps of:

(a) forming a mixture comprising milling media and a dry reaction mixture, said reaction mixture comprising particulate manganese dioxide and conductive carbon, said conductive carbon selected from the group consisting of graphite, acetylene black, graphitized carbon fibers, carbon nanofibers and carbon nanotubules, and any mixture thereof, wherein the weight ratio of said reaction mixture to said milling media is between about 1;

3 to 1;

10;

(b) mechanically agitating said reaction mixture with said milling media therein at ambient temperature to form a homogeneous product mixture without reducing the average particle size of said manganese dioxide by more than about 10 percent.

38. An alkaline electrochemical cell comprising a case;

positive and negative terminals;

an anode comprising zinc metal or a zinc alloy;

an aqueous electrolyte; and

a cathode comprising a homogeneous mixture of particulate manganese dioxide and conductive carbon, said homogeneous mixture made by the process of;

(a) forming a mixture comprising milling media and an essentially dry reaction mixture, said reaction mixture comprising particulate manganese dioxide and conductive carbon, said conductive carbon selected from the group consisting of graphite, acetylene black, graphitized carbon fibers, carbon nanofibers and carbon nanotubules, and any mixture thereof, wherein the weight ratio of said reaction mixture to milling media is between about 1;

3 to 1;

10;

(b) mechanically agitating said reaction mixture with said milling media therein at ambient temperature to form a homogeneous product mixture without reducing the average particle size of said manganese dioxide by more than about 10 percent.

39. The alkaline electrochemical cell of claim 38 further comprising:

(c) separating said milling media from said reaction mixture after step (b) and subsequently adding aqueous electrolyte to said mixture.