Process for producing improved electrolytic manganese dioxide

Claim 2

A process for treating electrolytic manganese dioxide to enhance the alkaline discharge capacity thereof comprising: forming a mixture of electrolytic manganese dioxide, a carbon material and a strong base electrolyte; subjecting said mixture to electrochemical oxidation in the presence of additional strong base electrolyte while maintaining said mixture in an anodic condition; subjecting said oxidized mixture to an aqueous leach treatment to effect a removal of water soluble manganese salt byproducts formed during the electrochemical oxidation of said mixture; and recovering said oxidized and leached mixture substantially as produced.

Claim 3

The process of claim 1 wherein said electrolytic manganese dioxide and said carbon material are present in said mixture in a weight ratio of the electrolytic manganese dioxide to the carbon material up to about 12:1.

Claim 4

The process of claim 2 wherein said weight ratio ranges from about 0.33:1 to about 12:1.

Claim 5

The process of claim 3 wherein said weight ratio ranges from about 0.33:1 to about 8:1.

Claim 6

The process of claim 1 wherein said carbon material present in said mixture is selected from the group consisting of electrically conductive carbon blacks and graphite.

Claim 7

The process of claim 1 wherein said mixture is subjected to electrochemical oxidation by passing a current of at least about 5 milliamperes per gram of the electrolytic manganese dioxide contained in said mixture through said mixture.

Claim 8

The process of claim 1 wherein said strong base electrolyte is selected from the group consisting of alkali metal and alkaline earth metal hydroxides.

Claim 9

The process of claim 1 wherein the electrolytic manganese dioxide contained in the recovered oxidized and leached mixture exhibits an increase in alkaline discharge capacity of at least about 10 milliiampere-hours per gram of said electrolytic manganese dioxide when cathodically discharged in a 9 M KOH solution at a rate of 20 milliamperes per gram of said electrolytic manganese dioxide to a terminus of one volt at ambient temperature versus a zinc counter electrode.

Claim 10

A process for treating electrolytic manganese dioxide to enhance the alkaline discharge capacity thereof comprising: forming a mixture of electrolytic manganese dioxide, a carbon material selected from the group consisting of electrically conducting carbon blacks and graphite and a strong base electrolyte selected from the group consisting of alkali metal and alkaline earth metal hydroxides; subjecting said mixture to electrochemical oxidation in the presence of additional strong base electrolyte, while maintaining said mixture in an anodic condition, by passing a current of at least about 5 milliamperes per gram of the electrolytic manganese dioxide contained in said mixture through said mixture; subjecting the oxidized mixture to an aqueous leach treatment to effect a removal of water soluble manganese salt byproducts formed during the electrochemical oxidation of said mixture; and recovering said oxidized and leached mixture substantially as produced.

Claim 11

A process for treating electrolytic manganese dioxide to enhance the alkaline discharge capacity thereof comprising: forming a mixture of electrolytic manganese dioxide, a carbon material selected from the group consisting of electrically conducting carbon blacks and graphite and a strong base electrolyte selected from the group consisting of alkali metal and alkaline earth metal hydroxides; subjecting said mixture to electrochemical oxidation in the presence of additional strong base electrolyte, while maintaining said mixture in an anodic condition, by passing a current of at least about 5 milliamperes per gram of the electrolytic manganese dioxide contained in said mixture through said mixture; subjecting the oxidized mixture to an aqueous leach treatment to effect a removal of water soluble manganese salt byproducts formed during the electrochemical oxidation of said mixture; and recovering said oxidized and leached mixture substantially as produced.

Claim 12

The process of claim 9 wherein said carbon material present in said mixture is graphite

Claim 13

The process of claim 10 wherein said manganese dioxide and said graphite are present in said mixture in a weight ratio of the manganese dioxide to the graphite of up to about 12:1.

Claim 14

The process of claim 11 wherein said weight ratio ranges from about 0.33:1 to about 12:1.

Claim 15

The process of claim 12 wherein said weight ratio ranges from about 0.33:1 to about 8:1.

Claim 16

The process of claim 9 wherein said strong base electrolyte is potassium hydroxide.

Claim 17

The process of claim 9 wherein said mixture is subjected to electrochemical oxidation by passing a current ranging from about 5 to about 200 milliamperes per gram of the electrolytic manganese dioxide contained in said mixture, through said mixture.

Claim 18

The process of claim 15 wherein said current imparts a charge to the electrolytic manganese dioxide contained in said mixture ranging from about 15 to about 125 milliampere-hours per gram of said electrolytic manganese dioxide.

Claim 19

The process of claim 15 wherein said current ranges from about 10 to about 60 milliamperes per gram of the electrolytic manganese dioxide contained in said mixture.

Claim 20

The process of claim 17 wherein said current imparts a charge to the electrolytic manganese dioxide contained in said mixture ranging from about 25 to about 80 milliampere-hours per gram of said electrolytic manganese dioxide.

Claim 21

The process of claim 9 wherein the manganese dioxide contained in the recovered oxidized and leached mixture exhibits an increase in alkaline discharge capacity of at least about 10 milliampere-hours per gram of said manganese dioxide when cathodically discharged in a 9 M KOH solution at a rate of 20 milliamperes per gram of said manganese dioxide to a terminus of one volt at ambient temperature versus a zinc electrode.