Continuous-feed electrochemical cell with nonpacking particulate electrode

• US 5,434,020 A
• Filed: 11/15/1993
• Issued: 07/18/1995
• Est. Priority Date: 11/15/1993
• Status: Expired due to Term

• Current Assignee: Lawrence Livermore National Security LLC (Government of the United States of America)
• Original Assignee: Regents of the University of California (University of California)
• Inventors: Cooper, John F.
• Primary Examiner(s): GORGOS, KATHRYN L
• Application Number:
  US08/152,964
• Time in Patent Office: 610 Days
• Field of Search: 204/237, 204/242, 204/263, 204/283, 204/284, 429/210, 429/221, 429/229, 429/233, 429/234, 429/239, 429/245
• US Class Current: 429/210
• CPC Class Codes: H01M 12/06 with one metallic and one gaseous electrode
• CPC Class Codes: H01M 4/02 Electrodes composed of, or comprising, active material
• CPC Class Codes: H01M 6/48 with bipolar electrodes
• CPC Class Codes: H01M 8/225 Fuel cells in which the fuel is based on materials comprising particulate active material in the form of a suspension, a dispersion, a fluidised bed or a paste
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

An electrochemical cell providing full consumption of electrochemically active particles in a nonpacking, electrolyte-permeable bed has a tapered cell cavity bounded by two nonparallel surfaces separated by a distance that promotes bridging of particles across the cavity. The gap/particle size ratio is maintained as the particles are consumed, decrease in size, and travel from the point of entry to the narrower end of the cell. A cell of this configuration supports a bed of low packing density maintained in a dynamic steady state by alternate formation and collapse of particle bridges across the gap and associated voids over the entire active area of the cell. The cell design can be applied to refuelable zinc/air cells and zinc/ferrocyanide storage batteries.

Claims

1. An electrochemical cell having a nonpacking, electrolyte-permeable bed of electrochemically active particles having an average diameter, comprising a tapered cell cavity defined by at least two nonparallel cell walls separated by a distance and containing an electrolyte solution;

wherein the cell cavity has an open end where the particles enter the cell and pass through the cavity in one direction;

wherein the distance between the cell walls promotes bridging of particles across the cell cavity and formation of voids between particles in the cavity;

wherein the ratio of the distance between the cell walls at any point along the cell walls and the average diameter of the particles at that point is in the range of about 1 to 7.

2. An electrochemical cell as recited in claim 1, wherein the cell walls are substantially vertical and the particles enter the open end of the cavity.

3. An electrochemical cell as recited in claim 1, wherein the ratio is in the range of about 1 to 5.

4. An electrochemical cell as recited in claim 1, wherein the ratio is in the range of about 1 to 3.

5. An electrochemical cell as recited in claim 1, wherein the ratio is in the range of about 2 to 3.

6. An electrochemical cell as recited in claim 1, wherein at least one cell wall comprises an anode current collector, and at least one cell wall comprises a non-electronically conducting separator permeated with the electrolyte solution.

7. An electrochemical cell as recited in claim 6, further comprising:

a cathode in contact with the separator on a surface opposed to the cell cavity;

means for circulating a fluid next to the cathode on a surface opposed to the separator;

means for circulating the electrolyte solution through the cell cavity; and

non-conducting means for housing the cell.

8. An electrochemical cell as recited in claim 7, wherein the cell is a metal/air cell, the cathode is a gas diffusion electrode supporting oxygen reduction, and the fluid is air.

9. An electrochemical cell as recited in claim 8, wherein the cell is a zinc/air cell.

10. An electrochemical cell as recited in claim 7, wherein the cell is a zinc/ferricyanide cell, the cathode is a porous, inert electrode supporting ferricyanide ion reduction, and the fluid is an electrolyte solution comprising ferrocyanide and ferricyanide.

11. An electrochemical cell as recited in claim 1, further comprising a reservoir overlying the cell for feeding particles into the cell cavity, wherein the width or length of the reservoir is wider than the open end of the cell cavity.

12. A bipolar electrochemical cell having a nonpacking, electrolyte-permeable bed of electrochemically active particles having an average diameter, comprising a plurality of cells connected in electrical series, wherein each cell comprises;

a tapered cell cavity defined by at least two nonparallel cell walls separated by a distance and containing an electrolyte solution;

wherein the cell cavity has an open end where the particles enter the cell and pass through the cavity in one direction;

wherein the distance between the cell walls promotes bridging of particles across the cell cavity and formation of voids between particles in the cavity;

wherein the ratio of the distance between the cell walls at any point along the cell walls and the average diameter of the particles at that point is in the range of about 1 to 7.

13. A bipolar electrochemical cell as recited in claim 12, wherein the cell walls are substantially vertical and the particles enter the open end of the cavity.

14. A bipolar electrochemical cell as recited in claim 12, wherein the ratio is in the range of about 1 to 5.

15. A bipolar electrochemical cell as recited in claim 12, wherein the ratio is in the range of about 1 to 3.

16. A bipolar electrochemical cell as recited in claim 12, wherein the ratio is in the range of about 2 to 3.

17. A bipolar electrochemical cell as recited in claim 12, further comprising:

cell partition means disposed in at least one cell cavity, extending between the cell walls and comprising means for the diffusion of the electrolyte solution therethrough.

18. A bipolar electrochemical cell as recited in claim 12, wherein at least one cell wall comprises an anode current collector, and at least one cell wall comprises an electrically conductive transfer plate.

19. A bipolar electrochemical cell as recited in claim 18, further comprising:

a non-electronically conducting separator permeated with the electrolyte solution in contact with the anode current collector on a surface opposed to the cell cavity;

a cathode in contact with the separator on a surface opposed to the cell cavity;

means for circulating a fluid next to the cathode on a surface opposed to the separator;

means for circulating the electrolyte solution through the cell cavity; and

non-conducting means for housing the cell.

20. A bipolar electrochemical cell as recited in claim 19, further comprising:

cell partition means disposed in at least one fluid circulating means and comprising means for the diffusion of the fluid therethrough.

21. A bipolar electrochemical cell as recited in claim 19, further comprising a perforated support plate situated next to the separator.

22. A bipolar electrochemical cell as recited in claim 19, wherein the cell is a metal/air cell, the cathode is a gas diffusion electrode supporting oxygen reduction, and the fluid is air.

23. A bipolar electrochemical cell as recited in claim 22, wherein the cell is a zinc/air cell.

24. A bipolar electrochemical cell as recited in claim 19, wherein the cell is a zinc/ferricyanide cell, the cathode is a porous, inert electrode supporting ferricyanide ion reduction, and the fluid is an electrolyte solution comprising ferrocyanide and ferricyanide.

25. A bipolar electrochemical cell as recited in claim 12, further comprising a reservoir overlying the cell for feeding particles into the cell cavity, wherein the width or length of the reservoir is wider than the open end of the cell cavity.