Method and system for rebalancing electrolytes in a redox flow battery system

Patent metadata

Field	Value
Publication number	US-10923753-B2
Application number	US-201816201974-A
Country	US
Kind code	B2
Filing date	Nov 27, 2018
Priority date	Jun 7, 2013
Publication date	Feb 16, 2021
Grant date	Feb 16, 2021

Abstract

A method of rebalancing electrolytes in a redox flow battery system comprises directing hydrogen gas generated on the negative side of the redox flow battery system to a catalyst surface, and fluidly contacting the hydrogen gas with an electrolyte comprising a metal ion at the catalyst surface, wherein the metal ion is chemically reduced by the hydrogen gas at the catalyst surface, and a state of charge of the electrolyte and pH of the electrolyte remain substantially balanced.

First claim

The invention claimed is:

1. A redox flow battery, comprising:
a redox flow battery cell, and
a catalyst bed positioned in a rebalancing reactor fluidly coupled to the redox flow battery cell, the catalyst bed including,
a substrate layer, a spacing layer, and a catalyst layer interposed between and attached to the substrate layer and the spacing layer to form a one-piece removable catalyst bed, wherein the rebalancing reactor rebalances electrolyte without connection to an external load.

2. A redox flow battery, comprising:
a redox flow battery cell, and
a catalyst bed positioned in a rebalancing reactor fluidly coupled to the redox flow battery cell, the catalyst bed including,
a substrate layer, a spacing layer, and a catalyst layer interposed between and attached to the substrate layer and the spacing layer to form a one-piece removable catalyst bed, wherein the one-piece removable catalyst bed is wound in on itself inside the rebalancing reactor.

3. The redox flow battery of claim 2 , wherein the one-piece removable catalyst bed is wound in on itself to form concentric layers.

4. The redox flow battery of claim 3 , wherein a number of the concentric layers is greater than one.

5. The redox flow battery of claim 4 , wherein electrolyte entering the rebalancing reactor passes through the substrate layer and the catalyst layer of a plurality of the concentric layers prior to exiting the rebalancing reactor.

6. The redox flow battery of claim 3 , wherein the concentric layers form a helically coiled one-piece removable catalyst bed.

7. The redox flow battery of claim 3 , wherein the spacing layer entirely separates the concentric layers.

8. The redox flow battery of claim 1 , wherein the spacing layer extends across an axial length of the catalyst layer.

9. A redox flow battery system, comprising:
a rebalancing reactor fluidly coupled to a redox flow battery cell, the rebalancing reactor including,
a catalyst bed including a substrate layer, a spacing layer, and a catalyst layer interposed between and attached to the substrate layer and the spacing layer to form a one-piece removable catalyst bed, wherein the rebalancing reactor rebalances electrolyte without connection to an external load.

10. A redox flow battery system, comprising:
a rebalancing reactor fluidly coupled to a redox flow battery cell, the rebalancing reactor including,
a catalyst bed including a substrate layer, a spacing layer, and a catalyst layer interposed between and attached to the substrate layer and the spacing layer to form a one-piece removable catalyst bed, wherein the catalyst bed is turned in on itself to form concentric layers, wherein each concentric layer includes the catalyst layer interposed between and attached to the substrate layer and the spacing layer.

11. The redox flow battery system of claim 10 , wherein the rebalancing reactor includes a flow distribution device, whereby inlet fluid to the rebalancing reactor is directed to one or more more central concentric layers without directing the inlet fluid to one or more less central concentric layers.

12. The redox flow battery system of claim 11 , wherein the rebalancing reactor further includes electrolyte fluid flowing radially outward through each of the concentric layers.

13. The redox flow battery system of claim 10 , wherein the rebalancing reactor includes a flow distribution device, whereby inlet fluid to the rebalancing reactor is directed to one or more less central concentric layers without directing the inlet fluid to one or more more central concentric layers.

14. The redox flow battery system of claim 13 , wherein the rebalancing reactor further includes electrolyte fluid flowing radially inward through each of the concentric layers.

15. The redox flow battery system of claim 10 , wherein the rebalancing reactor includes a higher aspect ratio shape, whereby inlet fluid to the rebalancing reactor is distributed across each of the concentric layers, in the absence of flow distribution devices positioned inside the rebalancing reactor.

16. A method of operating a redox flow battery system, comprising:
fluidly coupling a rebalancing reactor fluidly to a redox flow battery cell,
positioning a catalyst bed in the rebalancing reactor, and
preparing the catalyst bed, including,
interposing and attaching a catalyst layer between a substrate layer and a spacing layer to form a one-piece removable catalyst bed, wherein the rebalancing reactor rebalances electrolyte without connection to an external load.

17. A method of operating a redox flow battery system, comprising:
fluidly coupling a rebalancing reactor fluidly to a redox flow battery cell,
positioning a catalyst bed in the rebalancing reactor, and
preparing the catalyst bed, including,
interposing and attaching a catalyst layer between a substrate layer and a spacing layer to form a one-piece removable catalyst bed, wherein preparing the catalyst bed further includes coiling the catalyst bed to form concentric layers, wherein each concentric layer includes the catalyst layer interposed between and attached to the substrate layer and the spacing layer.

18. The method of claim 17 , wherein preparing the catalyst bed further includes coiling the catalyst bed more tightly to increase a density of the concentric layers, and wherein operating the redox flow battery system includes increasing a redox rate in the rebalancing reactor by including the increased density of the concentric layers in the rebalancing reactor.

19. The method of claim 17 , wherein preparing the catalyst bed further includes increasing a thickness of the spacing layer, and wherein operating the redox flow battery system includes reducing a pressure drop across the rebalancing reactor by including the thicker spacing layer in the rebalancing reactor.

20. The method of claim 17 , wherein preparing the catalyst bed further includes increasing a porosity of the substrate layer, and wherein operating the redox flow battery system includes reducing a pressure drop across the rebalancing reactor by including the higher porosity substrate layer.

Assignees

• Ess Technology Inc

Inventors

• Song Yang
• Evans Craig E

Classifications

• 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

• H01M8/188 Primary

  by recharging of redox couples containing fluids; Redox flow type batteries · CPC title

• H01M8/0693

  Treatment of the electrolyte residue, e.g. reconcentrating · CPC title

• H01M8/004

  Cylindrical, tubular or wound · CPC title