Micro-architected flow through electrodes for energy storage

Patent metadata

Field	Value
Publication number	US-11996535-B2
Application number	US-202217667489-A
Country	US
Kind code	B2
Filing date	Feb 8, 2022
Priority date	Feb 10, 2021
Publication date	May 28, 2024
Grant date	May 28, 2024

Abstract

Disclosed are electrochemical reactors with electrodes that have variable porosity across the electrode. The electrodes are designed and micro-architected to have variable porosity and 3D flow. In one aspect, an electrochemical cell apparatus is disclosed. The apparatus includes an electrochemical vessel and an electrochemical fluid contained in the electrochemical vessel. The apparatus further includes a porous electrode submerged in the electrochemical fluid in the electrochemical vessel, the porous electrode having different porosities in different areas of the porous electrode. The different porosities inhibit electrochemical fluid flow and increase electrical conductivity in first areas of the porous electrode with decreased porosity compared to second areas, and enable increased electrochemical fluid flow and decrease electrical conductivity in the second areas of the porous electrode with increased porosity compared to the first areas.

First claim

The invention claimed is:

1. An electrochemical cell apparatus comprising:
an electrochemical vessel;
an electrochemical fluid contained in the electrochemical vessel; and
a porous electrode submerged in the electrochemical fluid in the electrochemical vessel, the porous electrode being divided into a plurality of unit cells individually configured with cell-specific porosities corresponding to respective locations of the plurality of unit cells within the porous electrode,
wherein a cell-specific porosity of each unit cell is configured based on a rod diameter of each unit cell's internal structure relative to each unit cell's cell length,
wherein different cell-specific porosities across the plurality of unit cells inhibit electrochemical fluid flow and increase electrical conductivity in first areas of the porous electrode with decreased porosity compared to second areas, and enable increased electrochemical fluid flow and decrease electrical conductivity in the second areas of the porous electrode with increased porosity compared to the first areas.

2. The electrochemical cell apparatus of claim 1 , wherein the plurality of unit cells comprises at least five unit cells.

3. The electrochemical cell apparatus of claim 2 , wherein at least one unit cell compared to other unit cells has at least one of a different:
porosity;
surface area;
conductivity;
permeability; or
mass transfer property.

4. The electrochemical cell apparatus of claim 1 , wherein each unit cell's internal structure comprises one or more rods in an isotruss configuration, and wherein the rod diameter of each unit cell is selected to adjust a cell-specific porosity of the unit cell.

5. The electrochemical cell apparatus of claim 1 , wherein a first unit cell having a larger rod diameter than a second unit cell causes the first unit cell to have a lower porosity than the second unit cell.

6. The electrochemical cell apparatus of claim 1 , wherein a first unit cell having a larger rod diameter than a second unit cell causes the first unit cell to have a lower ohmic resistance than the second unit cell.

7. The electrochemical cell apparatus of claim 1 , wherein each unit cell's internal structure configures one or more of:
a cell-specific surface area;
a cell-specific conductivity;
a cell-specific permeability;
a cell-specific mass transfer; or
a cell-specific movability or permeation of gas bubbles.

8. The electrochemical cell apparatus of claim 1 , wherein the cell-specific porosities of the plurality of unit cells are selected to adjust one or more localized features of the porous electrode comprising:
a fluid distribution;
an electrical resistance;
a species reaction; or
a flow resistance.

9. The electrochemical cell apparatus of claim 1 , wherein the electrochemical cell apparatus is configured as a fuel cell.

10. The electrochemical cell apparatus of claim 1 , wherein the electrochemical cell apparatus is configured as a battery.

11. The electrochemical cell apparatus of claim 1 , wherein the electrochemical cell apparatus is configured as a flow-through electrochemical reactor.

12. The electrochemical cell apparatus of claim 1 , wherein the electrochemical cell apparatus is configured as a flow distribution system.

13. The electrochemical cell apparatus of claim 1 , wherein the electrochemical cell apparatus is configured as an electroactive component.

14. The electrochemical cell apparatus of claim 1 , wherein the porous electrode is configured as a porous flowfield plate.

15. The electrochemical cell apparatus of claim 14 , wherein the porous flowfield plate is positioned adjacent to an electroactive component.

16. The electrochemical cell apparatus of claim 1 , wherein each of the plurality of unit cells has a dimension on at least one side thereof that is between 100 nm and 100 microns.

17. The electrochemical cell apparatus of claim 1 , wherein the porous electrode has pore sizes between 100 nm and 100 microns.

18. The electrochemical cell apparatus of claim 1 , wherein the electrochemical fluid comprises a mixture of a liquid and a gas, and wherein the mixture includes bubbles of the gas entrained in the liquid.

Assignees

• L Livermore Nat Security Llc

Inventors

• Beck Victor Alfred
• Baker Sarah
• Davis Jonathan Tesner
• Duoss Eric
• Tortorelli Daniel
• Watts Seth Evan
• Worsley Marcus A

Classifications

• C02F2001/46161

  Porous electrodes · CPC title

• C02F1/46

  by electrochemical methods · CPC title

• H01M10/6568 Primary

  characterised by flow circuits, e.g. loops, located externally to the cells or cell casings · CPC title

• C25B9/15

  Flow-through cells · CPC title

• C25B9/70

  Assemblies comprising two or more cells · CPC title