pH BUFFERING REGION IN A FLOW BATTERY REBALANCING CELL
US-2020313212-A1 · Oct 1, 2020 · US
US12288912B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12288912-B2 |
| Application number | US-202117644396-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 15, 2021 |
| Priority date | Dec 31, 2020 |
| Publication date | Apr 29, 2025 |
| Grant date | Apr 29, 2025 |
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A redox flow battery with an electrochemical balancing cell having first and second chambers. The first chamber includes a catalyst coated substrate and the second chamber includes an electrode. Each receives an electrolyte from the redox flow battery. There is a single interface between the two chambers. The balancing cell reverses parasitic reactions in the first chamber that occur in the redox flow battery. The products of the reversed reactions are carried away from the electrochemical balancing cell and back to the redox flow battery in the electrolyte that carried the reactant to the first chamber. Also, processes for reversing a parasitic reaction in a redox flow battery.
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What is claimed is: 1. A redox flow battery, comprising: a redox flow battery cell, and an electrochemical balancing cell comprising: a first chamber comprising an inlet for a first electrolyte, an outlet for the first electrolyte, and a catalyst coated substrate; a second chamber comprising an inlet for a second electrolyte, an outlet for the second electrolyte, and an electrode, and, a separator forming an interface between the first electrolyte in the first chamber and the second electrolyte in the second chamber, wherein the interface formed by the separator is the only interface between the first electrolyte and the second electrolyte in the electrochemical balancing cell, wherein the first chamber comprises an inlet configured to receive a stream of a gas from the redox flow battery cell, and wherein the first electrolyte includes a reaction product from an oxidation or reduction of the gas, wherein the first chamber comprises a T-shape, with a lower portion and an upper portion that is wider than the lower portion. 2. The redox flow battery of claim 1 , wherein the first chamber of the electrochemical balancing cell further comprises: an upper portion configured to receive the gas from the inlet for the stream of the gas; and, a lower portion configured to receive the first electrolyte from the inlet for the first electrolyte. 3. The redox flow battery of claim 2 , wherein the catalyst coated substrate extends between upper portion and the lower portion. 4. The redox flow battery of claim 1 , wherein the first chamber further comprises an outlet for a gaseous effluent. 5. The redox flow battery of claim 1 , wherein the catalyst coated substrate comprises a catalyst supported on an electrically conductive porous substrate. 6. The redox flow battery of claim 1 , further comprising: a control valve in a line in communication with the inlet for the first electrolyte, wherein the control valve is configured to adjust an amount of the gas passed to the first chamber of the electrochemical balancing cell. 7. A redox flow battery comprising: an anode half-cell comprising an anode and an anolyte flowing through an anode chamber; a cathode half-cell comprising a cathode and a catholyte flowing through a cathode chamber, the cathode in electrical communication with the anode; and, an electrochemical balancing cell comprising: a first chamber comprising an inlet for the anolyte, an outlet for the anolyte, and a catalyst coated substrate; a second chamber comprising an inlet for the catholyte, an outlet for the catholyte, and an electrode; and, a separator forming an interface between the anolyte in the first chamber and the catholyte in the second chamber, wherein the interface formed by the separator is the only interface between the first electrolyte and the second electrolyte in the electrochemical balancing cell, wherein the first chamber comprises an inlet configured to receive a gaseous reaction product produced at the anode and an outlet for a gaseous effluent, and wherein the anolyte includes a reaction product from an oxidation reaction, at the catalyst coated substrate, of the gaseous reaction product, wherein the first chamber comprises a T-shape, with a lower portion and an upper portion that is wider than the lower portion. 8. The redox flow battery of claim 7 , wherein the first chamber comprises: an upper portion configured to receive the stream of the gaseous reaction product from the inlet for the stream of the gaseous reaction product; and, a lower portion configured to receive the anolyte from the inlet for the anolyte. 9. The redox flow battery of claim 8 , wherein the catalyst coated substrate extends between the upper portion and the lower portion. 10. The redox flow battery of claim 7 , wherein a substrate of the catalyst coated substrate comprises a porous substrate. 11. The redox flow battery of claim 7 , further comprising: a control valve in a line in communication with the inlet for the anolyte, wherein the control valve is configured to adjust an amount of the gaseous reaction product to the first chamber. 12. A redox flow battery comprising: an anode half-cell comprising an anode and an anolyte flowing through an anode chamber; a cathode half-cell comprising a cathode and a catholyte flowing through a cathode chamber, the cathode in electrical communication with the anode; and, an electrochemical balancing cell comprising: a first chamber comprising an inlet for the anolyte, an outlet for the anolyte, and a catalyst coated substrate; a second chamber comprising an inlet for the catholyte, an outlet for the catholyte, and an electrode; and, a separator forming an interface between the anolyte in the first chamber and the catholyte in the second chamber, wherein the interface formed by the separator is the only interface between the first electrolyte and the second electrolyte in the electrochemical balancing cell, wherein the first chamber is configured to receive a gaseous reaction product produced at the anode, wherein the anolyte includes a reaction product from an oxidation reaction, at the catalyst coated substrate, of the gaseous reaction product, wherein a stream of the gaseous reaction product is introduced to the first chamber with the anolyte via the inlet for the anolyte, and wherein the inlet for the anolyte is located at a height in the first chamber that is lower than a height of the outlet for the anolyte, wherein the first chamber comprises a T-shape, with a lower portion and an upper portion that is wider than the lower portion.
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