Redox flow battery system including an anode electrode having a subsurface alloy

Patent metadata

Field	Value
Publication number	US-9728803-B2
Application number	US-201414184765-A
Country	US
Kind code	B2
Filing date	Feb 20, 2014
Priority date	Feb 21, 2013
Publication date	Aug 8, 2017
Grant date	Aug 8, 2017

Abstract

A hydrogen/bromine reduction-oxidation flow battery system includes a bromine electrode, a hydrogen electrode, a membrane, a first catalyst, and a second catalyst. The membrane is positioned between the bromine electrode and the hydrogen electrode. The first catalyst is associated with the bromine electrode. The second catalyst is associated with the hydrogen electrode and at least partially formed from a subsurface alloy configured (i) to promote facile dissociation of H 2 , and (ii) to prevent bromide from adsorbing onto the hydrogen electrode.

First claim

What is claimed is:

1. A hydrogen/bromine reduction-oxidation flow battery system comprising:
a bromine electrode;
a hydrogen electrode;
a membrane positioned between the bromine electrode and the hydrogen electrode;
a first catalyst associated with the bromine electrode; and
a second catalyst associated with the hydrogen electrode and at least partially formed from a subsurface alloy configured (i) to promote facile dissociation of H 2 , and (ii) to prevent bromide from adsorbing onto the hydrogen electrode,
wherein the subsurface alloy includes a solute metal and a host metal, and
wherein the subsurface alloy includes an atomically thin layer of the solute metal positioned at the surface of the host metal.

2. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , wherein:
the solute metal is copper, and
the host metal is Pt(111).

3. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , wherein:
the solute metal is gold, and
the host metal is Pt(111).

4. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , further comprising:
a first source fluidly coupled to the hydrogen electrode and configured to supply the hydrogen electrode with gaseous H 2 ; and
a second source fluidly coupled to the bromine electrode and configured to supply the bromine electrode with a Br 2 /HBr aqueous solution.

5. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , wherein:
the bromine electrode is at least partially formed from a first porous carbon substrate and the first catalyst is deposited on the first porous carbon substrate, and
the hydrogen electrode is at least partially formed from a second porous carbon substrate and the second catalyst is deposited on the second carbon substrate.

6. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , wherein the first catalyst is at least partially formed from one or more of platinum, tantalum, and iridium.

7. The hydrogen/bromine reduction-oxidation flow battery system of claim 1 , wherein the membrane is a cation-exchange membrane.

8. The hydrogen/bromine reduction-oxidation flow battery system of claim 7 , wherein the membrane includes a sulfonated polystyrene membrane.

9. A reduction-oxidation flow battery system comprising:
a cathode electrode;
an anode electrode;
a membrane positioned between the cathode electrode and the anode electrode;
a first catalyst associated with the cathode electrode; and
a second catalyst associated with the anode electrode and at least partially formed from a subsurface alloy including a solute metal and a host metal,
wherein the solute metal is one of copper and gold,
wherein the host metal is Pt(111), and
wherein the subsurface alloy includes an atomically thin layer of the solute metal positioned at the surface of the host metal.

10. The reduction-oxidation flow battery system of claim 9 , wherein the second catalyst is configured (i) to promote facile dissociation of H 2 , and (ii) to prevent bromide from adsorbing onto the anode electrode.

11. The reduction-oxidation flow battery system of claim 9 , further comprising:
a first source fluidly coupled to the anode electrode and configured to supply the anode electrode with gaseous H 2 ; and
a second source fluidly coupled to the cathode electrode and configured to supply the cathode electrode with a Br 2 /HBr aqueous solution.

12. The reduction-oxidation flow battery system of claim 9 , wherein:
the cathode electrode is at least partially formed from a first porous carbon substrate and the first catalyst is deposited on the first porous carbon substrate, and
the anode electrode is at least partially formed from a second porous carbon substrate and the second catalyst is deposited on the second carbon substrate.

13. The reduction-oxidation flow battery system of claim 9 , wherein the first catalyst is at least partially formed from one or more of platinum, tantalum, and iridium.

14. The reduction-oxidation flow battery system of claim 9 , wherein the membrane is a cation-exchange membrane.

15. The reduction-oxidation flow battery system of claim 14 , wherein the membrane includes a sulfonated polystyrene membrane.

16. A hydrogen/bromine reduction-oxidation flow battery system, comprising:
a bromine electrode;
a hydrogen electrode;
a membrane positioned between the bromine electrode and the hydrogen electrode;
a first catalyst associated with the bromine electrode; and
a second catalyst associated with the hydrogen electrode and at least partially formed from a subsurface alloy configured (i) to promote facile dissociation of H 2 , and (ii) to prevent bromide from adsorbing onto the hydrogen electrode,
wherein the subsurface alloy includes a solute metal and a host metal, and
wherein the subsurface alloy includes an atomically thin layer of the solute metal positioned between the surface of the host metal and an atomically thin layer of the host metal.

Assignees

• Bosch Gmbh Robert

Inventors

• Sanchez-Carrera Roel
• Kozinsky Boris
• Albertus Paul

Classifications

• H01M8/20

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

• H01M4/92

  Metals of platinum group (H01M4/94 {, H01M4/9058} take precedence) · CPC title

• Y02E60/528

  Cross-Sectional Technologies · mapped topic

• H01M4/9091

  Unsupported catalytic particles; loose particulate catalytic materials, e.g. in fluidised state · CPC title

• H01M4/921

  Alloys or mixtures with metallic elements · CPC title