Cathode architectures for alkali metal / oxygen batteries

• US 8,932,771 B2
• Filed: 06/15/2012
• Issued: 01/13/2015
• Est. Priority Date: 05/03/2012
• Status: Active Grant

• Current Assignee: PolyPlus Battery Company
• Original Assignee: PolyPlus Battery Company
• Inventors: Visco, Steven J., Nimon, Vitaliy, De Jonghe, Lutgard C., Volfkovich, Yury, Bograchev, Daniil
• Primary Examiner(s): DOUYETTE, KENNETH J
• Application Number:
  US13/525,128
• Publication Number:
  US 20130295471A1
• Time in Patent Office: 942 Days
• Field of Search: 429/402, 429/403, 429/404, 429/405, 429/188, 429/231.1, 429/246, 429/535, 429/118, 429/119, 429/210, 429/407
• US Class Current: 429/404
• CPC Class Codes: H01M 12/08 composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
• CPC Class Codes: H01M 2300/0025 Organic electrolyte
• CPC Class Codes: H01M 4/86 Inert electrodes with catalytic activity, e.g. for fuel cells
• CPC Class Codes: H01M 4/861 with a gradient in the porosity
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02P 70/50 Manufacturing or production processes characterised by the final manufactured product
• CPC Class Codes: Y10T 29/49108 Electric battery cell making

Abstract

Electrochemical energy storage devices, such as alkali metal-oxygen battery cells (e.g., non-aqueous lithium-air cells), have a cathode architecture with a porous structure and pore composition that is tailored to improve cell performance, especially as it pertains to one or more of the discharge/charge rate, cycle life, and delivered ampere-hour capacity. A porous cathode architecture having a pore volume that is derived from pores of varying radii wherein the pore size distribution is tailored as a function of the architecture thickness is one way to achieve one or more of the aforementioned cell performance improvements.

Claims

1. An alkali metal oxygen battery cell comprising:

an alkali metal anode having a major active surface; and

a porous cathode architecture adjacent the anode major active surface, the architecture comprising first and second porous regions each having a different entirely wettable porous structure and further comprising a certain volume of liquid electrolyte;

wherein the first porous region provides active surface sites for electron transfer, access for molecular oxygen to enter the cathode architecture, and is characterized as having a first region total pore volume;

the second porous region, not an electron transfer region, is;

i) in pore communication with the first porous region;

ii) disposed adjacent to the anode major surface; and

iii) characterized as having a second region total pore volume; and

the certain volume of liquid electrolyte is greater than the total pore volume of the second region but less than the cumulative total pore volumes of the first and second regions, and said certain volume of liquid electrolyte is the amount present in the architecture immediately prior to and upon initial cell operation.

2. The alkali metal oxygen battery cell of claim 1 wherein the second porous region is in direct contact with the anode major surface.

3. The alkali metal oxygen battery cell of claim 1 wherein the cell further comprises an external case or enclosure having at least one sidewall permeable to air or molecular oxygen-containing gas for harnessing molecular oxygen which is ultimately electro-reduced on the surface of the electron transfer medium during cell discharge.

4. The alkali metal oxygen battery cell of claim 3 wherein the first porous region is positioned in the cell nearby the molecular oxygen-permeable sidewall, and is in contiguous gas phase communication with the ambient air or molecular oxygen-containing gas.

5. The metal oxygen battery cell of claim 1 wherein the first and second porous regions are discrete porous body layers.

6. The metal oxygen battery cell of claim 1 wherein the porous structures of the first and second regions differ in at least one of pore composition, pore size distribution, and solid material from which the porous region is composed.

7. The metal oxygen battery cell of claim 6 wherein the difference in porous structure is at least based on a difference in pore size distribution.

8. The metal oxygen battery cell of claim 7 wherein the difference in pore size distribution is tailored to cause, via capillary forces, the liquid electrolyte to fill all the pores in the second porous region and only a portion of the pores in the first porous region, the liquid electrolyte substantially completely filling the second region total pore volume and only partially filling the first region total pore volume, with the remaining first region pore volume filled with air or molecular oxygen-containing gas.

9. The metal oxygen battery cell of claim 7 wherein the second region pore size distribution is defined by micropores, mesopores or a combination thereof, and the first region pore size distribution is defined by a combination of macropores and mesopores.

10. The metal oxygen battery cell of claim 9 wherein the mesopores in the second region are smaller than the mesopores in the first region.

11. The metal oxygen battery cell of claim 10 wherein substantially all the pores in the second region have pore radii smaller than the pore radii of the smallest pores in the first region.

12. The metal oxygen battery cell of claim 7 wherein the amount of liquid electrolyte in the architecture is greater than the cumulative pore volume of all the mesopores in the first region and all the micropores and mesopores in the second region, but is insufficient to fill the entire architecture such that the largest pores in the first region are gas filled.

13. The metal oxygen battery cell of claim 7 wherein the second region pore size distribution is defined by micropores, mesopores or a combination thereof, and the first region pore size distribution is defined solely by macropores.

14. The alkali metal oxygen battery cell of claim 7 wherein the first region comprises pores of relatively large and small pore radii and the majority of the second region pore volume is defined by pores of relatively intermediate size, the radii of the intermediate sized pores falling between those of the large and small pores in the first region.

15. The alkali metal oxygen battery cell of claim 14 wherein said intermediate pores of the second region and said small pores of the first region are substantially completely filled with said liquid electrolyte and only a portion, if any, of the large pores of the first region are filled with the liquid electrolyte, and the remaining large pores are gas filled and thereby provide fast oxygen diffusion channels into the depth of the architecture.

16. The alkali metal oxygen battery cell of claim 7 wherein the pore size distribution of the first porous region is multimodal, having at least a primary and a secondary modalities, and the pore size distribution of the second region is unimodal.

17. A method of making a metal oxygen battery cell, the method comprising:

i) providing an alkali metal anode having a major active surface;

ii) providing a porous cathode architecture having first and second porous regions each having a different entirely wettable porous structure;

the first porous region providing active surface sites for electron transfer, access for molecular oxygen to enter the cathode architecture, and characterized as having a first region total pore volume;

the second porous region, not an electron transfer region;

i) in pore communication with the first porous region;

ii) disposed adjacent to the anode major surface; and

iii) characterized as having a second region total pore volume;

iii) configuring the anode major active surface adjacent the cathode architecture;

iv) filling the cathode architecture with a volume of liquid electrolyte that is greater than the second region total pore volume but less than the combined total pore volume of the first and second regions; and

further wherein said volume of liquid electrolyte is the amount present in the architecture immediately prior to and upon initial cell operation.

18. The method of claim 17 wherein the first and second regions are defined by discrete solid porous body layers, a first solid porous body layer serving as the electron transfer region and a second solid porous body layer serving as a passive region.