Alternative low cost electrodes for hybrid flow batteries

Patent metadata

Field	Value
Publication number	US-11043679-B2
Application number	US-201514984416-A
Country	US
Kind code	B2
Filing date	Dec 30, 2015
Priority date	Dec 30, 2014
Publication date	Jun 22, 2021
Grant date	Jun 22, 2021

Abstract

An electrode for use in an all-iron redox flow battery is provided. In one example, the electrode may include a plastic mesh; and a coating on the plastic mesh. The coating may be a hydrophilic coating or a conductive coating and the electrode may have an electrode reaction potential is less than 0.8V. Further, a method of manufacturing a coated plastic mesh electrode for use in an all-iron redox flow battery is provided. In one example method, the steps include fabricating a plastic mesh, treating the plastic mesh by applying a solvent treatment or a plasma treatment or a mechanical abrasion treatment; coating the plastic mesh with a material selected from: carbon inks, metal oxides, and hydrophilic polymers.

First claim

The invention claimed is:

1. An electrode for use in an all-iron redox flow battery, comprising: a plastic mesh positioned adjacent to flow plate channels, the flow plate channels and the plastic mesh configured for receiving and directing an iron salt electrolyte pumped from an electrolyte source of the all-iron redox flow battery; and a coating on the plastic mesh to form a coated plastic mesh for plating iron metal from the iron salt electrolyte, wherein the coating is a hydrophilic coating or a conductive coating, and the coating is selected for interfacing with the iron salt electrolyte as used in the all-iron redox flow battery; wherein an electrode reaction potential is less than 0.8 V; and wherein the coated plastic mesh has an open area of 15% to 65% and an open volume of 10% to 70%.

2. The electrode of claim 1 , wherein the hydrophilic coating is selected from: hydrophilic polymers.

3. The electrode of claim 2 , wherein the hydrophilic coating is a hydrophilic perfluorosulfonic acid polymer.

4. The electrode of claim 1 , wherein the conductive coating is a conductive carbon based material.

5. The electrode of claim 4 , wherein the conductive coating is a carbon ink.

6. The electrode of claim 1 , wherein the coated plastic mesh is treated with a solvent treatment technique or a plasma treatment technique or a mechanical abrasion technique.

7. The electrode of claim 1 , wherein the coated plastic mesh has a thickness of between about 0.20 mm to about 0.50 mm.

8. The electrode of claim 1 , wherein the coated plastic mesh has a water contact angle of less than 45°.

9. The electrode of claim 1 , wherein a non-conductive coating is used for a plating electrode.

10. The electrode of claim 1 , wherein the plastic mesh is one of polypropylene or polyolefin.

11. The electrode of claim 1 , wherein the plastic mesh is coated with the coating by using a technique selected from:
air brushing, dip coating, or roller coating.

12. The electrode of claim 1 , wherein a potential of the electrode does not decrease by more than 0.1 volts at a current density less than 20 mA/cm 2 .

13. The electrode of claim 6 , wherein the coated plastic mesh is treated with the plasma treatment technique, where the plasma treatment technique is an electron-beam plasma treatment technique or a cold-gas plasma treatment technique.

14. The electrode of claim 1 , wherein the coated plastic mesh is treated with a UV radiation treatment technique.

15. An electrode for use in an all-iron redox flow battery, comprising: a plastic mesh positioned adjacent to flow plate channels, the flow plate channels and the plastic mesh configured for receiving and directing an electrolyte pumped from one of a plurality of tanks of the ail-iron redox flow battery; and a coating on the plastic mesh to form a coated plastic mesh for plating an iron electro-active material on the electrode from the electrolyte, wherein the coating is a hydrophilic coating or a conductive coating, and the coating is selected for interfacing with the electrolyte as used in the all-iron redox flow battery; wherein the coated plastic mesh has an open area of 15% to 65% and an open volume of 10% to 70%, and a thickness of between about 0.20 mm to about 0.50 mm; and wherein the coated plastic mesh has a greater conductive surface area than a titanium mesh electrode.

16. The electrode of claim 15 , wherein the flowing electrolyte has a pH of between 1 to 4.

17. The electrode of claim 15 , wherein
the conductive coating is a conductive carbon based material; and
the coating uniformly covers the plastic mesh.

Assignees

• Ess Technology Inc

Inventors

• Evans Craig E
• Song Yang
• Chen Jeffrey

Classifications

• H01M4/8803 Primary

  Supports for the deposition of the catalytic active composition (H01M4/90 takes precedence) · CPC title

• Y02E60/50

  Fuel cells · CPC title

• H01M8/20

  Indirect fuel cells, e.g. fuel cells with redox couple being irreversible (H01M8/18 takes precedence) · CPC title

• H01M4/8817

  Treatment of supports before application of the catalytic active composition (coated porous composites H01M8/0245) · CPC title

• H01M8/0239

  Organic resins; Organic polymers · CPC title