Metal/air cells and improved air electrodes for use therein

• US 3,977,901 A
• Filed: 10/23/1974
• Issued: 08/31/1976
• Est. Priority Date: 10/23/1974
• Status: Expired due to Term

• Current Assignee: Westinghouse Electric Company LLC (Brookfield Asset Management Incorporated)
• Original Assignee: Westinghouse Electric Company LLC (Brookfield Asset Management Incorporated)
• Inventors: Buzzelli, Edward S.
• Primary Examiner(s): Mack, John H.
• Assistant Examiner(s): Feeley, H. A.
• Application Number:
  US05/517,115
• Time in Patent Office: 678 Days
• Field of Search: 136/86 A, 136/86 D, 136/86 R, 136/120 FC, 204/195
• US Class Current: 429/406
• CPC Class Codes: H01M 4/8615 Bifunctional electrodes for rechargeable cells
• CPC Class Codes: H01M 4/96 Carbon-based electrodes
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

Air electrodes for use in electrochemical energy cells which comprise a hydrophilic layer and a hydrophobic layer laminated thereto. The hydrophilic layer essentially comprises a hydrophilic composite which includes

I. an oxygen absorption/reduction carbon,

Ii. a material selected from the group consisting of

A. CuWO₄, NiWO₄, CoWO₄ and WC with 1-20 wt. % Co. for a unifunctional electrode, or

B. WS₂, WC, and WC with 1-20 Wt.% Co. for a bi-functional electrode, and

Iii. a nonwetting agent containing a polytetrafluoroethylene. A metal current collector is molded into the composite to form a substantially flat hydrophilic layer. A catalyst is preferably incorporated into the composite of a bifunctional electrode to increase cycling life. The hydrophobic layer, comprising a sheet of porous fluorinated ethylene propylene, polypropylene or polytetrafluoroethylene, is laminated to the hydrophilic layer to complete the air electrodes of the invention.

Claims

1. An air electrode for use in electrochemical energy cells comprising:

A. a hydrophilic layer consisting essentially of

1. a hydrophilic composite comprising

i. about 1 part by weight of oxygen absorption/reduction carbon particles having a total surface area of from about 30 to about 600 sq. meters/gram;

ii. about 0.5-4 parts by weight of a low oxygen overvoltage material selected from the group consisting of CuWO₄, NiWO₄ CoWO₄, WS₂, WC and WC fuse sinter coated with 1-20 wt.% Co and mixtures thereof;

iii. an effective amount of a bonding/nonwetting agent including at least polytetrafluoroethylene; and

iv. an effective amount of a catalyst for oxygen reduction and decomposition of perhydroxides selected from the group consisting of silver, platinum and silver mercury alloy; and

2. a metal current collector molded into said composite to form a hydrophilic layer; and

B. a hydrophobic layer laminated to said hydrophilic layer.

2. An electrode as set forth in claim 1 wherein

iv. the current collector is a metal fiber current collector.

3. An electrode as set forth in claim 1 wherein said hydrophobic layer conprises a sheet of porous, plastic selected from the group consisting of polytetrafluoroethylene, polypropylene, fluorinated ethylene propylene and mixtures thereof and the low oxygen overvoltage material is selected from the group consisting of WS₂, WC and WC fuse sinter coated with 1-20 wt.% Co.

4. An electrode as set forth in claim 1 wherein said hydrophilic composite is substantially flat and the catalyst is silver.

5. A metal/air cell comprising a metal electrode selected from the group consisting of iron, zinc, and cadmium;

at least one air electrode as set forth in claim 1 spaced apart from said metal electrode; and

an alkali hydroxide electrolyte in contact with said metal and air electrode.

6. An air electrode for use in electrochemical energy cells capable of non destructive charging comprising:

A. a hydrophilic layer consisting essentially of

1. a hydrophilic composite comprising

i. about 1 part by weight of substantially discrete oxygen absorption/reduction carbon black particles having a particle size range of between about 0.005-0.13 microns and a total probable surface area of from about 30-600 sq. meters/gram.;

ii. about 0.5-4 parts by weight of low oxygen over voltage material selected from the group consisting of CuWO₄, NiWO₄, CoWO₄, WS₂, WC and WC fuse sinter coated with 1-20 wt.% Co. and mixtures thereof;

iii. an effective amount of bonding/nonwetting agent including at least polytetrafluoroethylene; and

iv. an effective amount of a catalyst for oxygen reduction and decomposition of perhydroxides selected from the group consisting of silver, platinum and silver mercury alloy; and

2. a metal current collector molded into said composite to form a hydrophilic layer; and

B. a hydrophobic layer laminated to said hydrophilic layer.

7. An air electrode as set forth in claim 6 wherein said oxygen absorption/reduction carbon black has an interlayer spacing between about 7.0 to 7.2A and the particles have a pore diameter between about 0.005-0.002 microns.

8. An air electrode as set forth in claim 6 wherein said oxygen absorption/reduction carbon consists essentially of an acetylene black having a total surface area of between about 30-450 sq. meters/gram, and is in a form wherein generally spherical particles are separated from each other and joined together in a three dimensional fashion by carbon-oxygen complexes which provide links between the separated carbon particles.

9. An air electrode as set forth in claim 6 wherein the current collector is a metal fiber current collector and the low oxygen overvoltage material is selected from the group consisting of WS₂, WC and WC fuse sinter coated with 1-20 wt.% Co.

10. An air electrode as set forth in claim 7 wherein said hydrophobic layer comprises a sheet of porous, plastic selected from the group consisting of polytetrafluoroethylene, polypropylene, fluorinated ethylene propylene and mixtures thereof.

11. An air electrode as set forth in claim 9 wherein said hydrophilic composite is substantially flat and includes 0.15-1.5 parts by weight of catalyst.

12. A metal/air cell comprising a metal electrode selected from the group consisting of iron, zinc, and cadmium;

at least one air electrode as set forth in claim 9 spaced apart from said metal electrode; and

an alkali hydroxide electrolyte in contact with said metal and air electrode.

13. A metal/air battery comprising a metal electrode selected from the group consisting of iron, zinc and cadmium;

at least one electrode, effective to allow non destructive battery charging at between about 0.50-0.75 volts above a Hg/HgO reference electrode, spaced apart from said metal electrode, the electrode comprising;

A. a hydrophilic layer consisting essentially of

1. a hydrophilic composite comprising

i. acetylene black carbon;

ii. a low oxygen over voltage material selected from the group consisting of CuWO₄, NiWO₄, CoWO₄, WS₂, WC and WC fuse sinter coated with 1-20 wt.% Co. and mixtures thereof;

iii. an effective amount of bonding/non-wetting agent including at least polytetrafluoroethylene; and

iv. an effective amount of a catalyst for oxygen reduction and decomposition of perhydroxides selected from the group consisting of silver, platinum and silver mercury alloy; and

15. The metal/air battery as set forth in claim 13 wherein said hydrophilic composite includes about 0.5-4 parts by weight low oxygen overvoltage material for each part carbon, (iv) 0.15-1.5 parts by weight of catalyst, the acetylene black carbon is in a form wherein generally spherical particles are separated from each other and joined together in a three dimensional fashion by carbon-oxygen complexes which provide links between the separated carbon particles, said acetylene black carbon having a particle size range of between about 0.005-0.13 microns and a total surface area from about 30-300 sq. meters/gram and the low oxygen over voltage material is WC fuse sinter coated with 10-15 wt.% Co.

16. The metal/air battery as set forth in claim 13 wherein the low oxygen overvoltage material is selected from the group consisting of WS₂, WC and WC fuse sintered coated with 1-20 wt.% Co.

14. A metal current collector molded into said composite to form a substantially flat hydrophilic layer;

and

B. a hydrophobic layer laminated to said hydrophilic layer; and

an alkali hydroxide electrolyte in contact with said metal electrode and the hydrophilic layer of said air electrode.