Additives for electrochemical cells having zinc anodes

• US 5,401,590 A
• Filed: 12/07/1992
• Issued: 03/28/1995
• Est. Priority Date: 12/07/1992
• Status: Expired due to Term

• Current Assignee: Gillette Company (The Procter & Gamble Company)
• Original Assignee: Duracell Incorporated (Berkshire Hathaway Incorporated)
• Inventors: Bing-Wo, Ron, Kasianowicz, Fred, Padula, Henry S., Brual, Greg, Harris, Peter B., Chalilpoyil, Purush
• Primary Examiner(s): Dees, Jose G.
• Assistant Examiner(s): BARTS, SAMUEL A
• Application Number:
  US07/986,233
• Time in Patent Office: 841 Days
• Field of Search: 429/57, 429/185, 429/190, 429/229, 429/230, 429/231, 429/59, 429/212
• US Class Current: 429/59
• CPC Class Codes: H01M 4/244 Zinc electrodes
• CPC Class Codes: H01M 6/22 Immobilising of electrolyte
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

The invention relates to a method for inhibiting the occurrence of load voltage instability in zinc anodic alkaline cells. The anode active material contains a gelled slurry of zinc alloy particles, a gelling agent, an aqueous alkaline solution and a mixed surfactant containing an anionic surfactant and a non-ionic surfactant. The gelled anode active material inhibits the occurrence of load voltage instability and simultaneously reduces hydrogen evolution even though the cell contains no added amounts of mercury.

Claims

1. A method for both inhibiting the occurrence of load voltage instability and controlling the formation of hydrogen gas in an alkaline electrochemical cell containing less than 50 pans of mercury per million parts by weight of the cell and having a gelled zinc anode and an aqueous alkaline electrolyte, said method comprising adding a mixture of at least one anionic surfactant and one non-ionic surfactant to said zinc anode.

2. The method of claim 1 wherein the cell has a cathode active material therein comprising manganese dioxide and the aqueous alkaline solution comprises potassium hydroxide.

3. The method of claim 1 wherein the anionic surfactant is represented by the formula:

space="preserve" listing-type="equation">R.sup.1 (CH.sub.2 --CH.sub.2 --O).sub.n --X.sup.1

wherein, R¹ is selected from the group consisting of alkyl, aryl alkylaryl and combinations thereof;

X¹ is selected from an anionic group consisting of an anionic acid group, salt of an anionic acid group, and anionic phosphate ester group; and

n is between about 3 and 40.

4. The method of claim 1 wherein the non-ionic surfactant is represented by the formula:

space="preserve" listing-type="equation">R.sup.2 --(CH.sub.2 --CH.sub.2 --O).sub.n --X.sup.2

wherein, R² is selected from the group consisting of alkyl, aryl, alkylaryl, fluorinated aliphatic groups and combinations thereof;

X² is a non-ionic group; and

n is between about 3 and 250.

5. The method of claim 3 wherein the group R¹ is an an alkyl group containing between about 4 and 28 carbon atoms.

6. The method of claim 3 wherein the anionic surfactant has a molecular weight between about 200 and 2000.

7. The method of claim 4 wherein the group R² is a fluorinated aliphatic group having between about 3 and 16 carbon atoms.

8. The method of claim 4 wherein the non-ionic surfactant has a molecular weight between about 200 and 10000.

9. The method of claim 1 wherein the gelled anode active material comprises between about 25 and 200 parts anionic surfactant per million parts by weight of the zinc-alloy particles and between about 25 and 200 parts non-ionic surfactant per million parts by weight of the zinc-alloy particles.

10. The method of claim 1 wherein the cell contains less than 10 parts mercury per million parts by weight of the cell.

11. The method of claim 1 wherein the zinc alloy particles comprise an alloy comprising zinc and indium.

12. The method of claim 11 wherein said particles contain between about 50 and 1000 parts indium per million parts by weight of the particles.

13. The method of claim 1 wherein the gelling agent comprises a gelling component selected from the group consisting of crosslinked acrylic acid copolymers and starch graft copolymers, and mixtures thereof.

14. The method of claim 1 wherein the gelling agent comprises a mixture of CARBOPOL C940 crosslinked acrylic acid copolymer and WATER-LOCK A-221 starch graft copolymer.

15. The method of claim 13 wherein the gelling agent comprises SIGMA POLYGEL 4P (SYNTHALEN M) crosslinked acrylic acid polymer.

16. The method of claim 13 wherein the gelling agent comprises WATER-LOCK A-221 starch graft copolymer.

17. The method of claim 13 wherein the gelling agent comprises CARBOPOL C940 crosslinked acrylic acid copolymer.

18. A method for both inhibiting the occurrence of load voltage instability and controlling the formation of hydrogen gas in an alkaline electrochemical cell having a gelled zinc anode, an aqueous alkaline electrolyte, and "zero added" mercury, said method comprising .adding a mixture of at least one anionic surfactant and one non-ionic surfactant to said zinc anode, wherein the anionic surfactant is represented by the formula:

space="preserve" listing-type="equation">R.sup.1 (CH.sub.2 --CH.sub.2 --O).sub.n --X.sup.1

wherein, R¹ is selected from the group consisting of alkyl, aryl alkylaryl and combinations thereof;

X¹ is selected from an anionic group consisting of an anionic acid group, salt of an anionic acid group, and anionic phosphate ester group; and

n is between about 3 and 40, and wherein the non-ionic surfactant is represented by the formula;

space="preserve" listing-type="equation">R.sup.2 --(CH.sub.2 --CH.sub.2 --O).sub.n --X.sup.2

wherein, R² is selected from the group consisting of alkyl, aryl, alkylaryl, fluorinated aliphatic groups and combinations thereof;

X² is a non-ionic group; and

n is between about 3 and 250.

19. The method of claim 18 wherein the cell contains less than 50 parts mercury per million parts by weight of the cell.