Electrolyte tank volume rebalancing
US-2024396064-A1 · Nov 28, 2024 · US
US9077011B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9077011-B2 |
| Application number | US-201414261262-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 24, 2014 |
| Priority date | Sep 28, 2010 |
| Publication date | Jul 7, 2015 |
| Grant date | Jul 7, 2015 |
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Redox flow battery systems having a supporting solution that contains Cl − ions can exhibit improved performance and characteristics. Furthermore, a supporting solution having mixed SO 4 2− and Cl − ions can provide increased energy density and improved stability and solubility of one or more of the ionic species in the catholyte and/or anolyte. According to one example, a vanadium-based redox flow battery system is characterized by an anolyte having V 2+ and V 3+ in a supporting solution and a catholyte having V 4+ and V 5+ in a supporting solution. The supporting solution can contain Cl − ions or a mixture of SO 4 2− and Cl − ions.
Opening claim text (preview).
We claim: 1. An all-vanadium redox flow battery system, the system characterized by an anolyte comprising V2+ and V3+, a catholyte comprising V4+ and V5+, and an aqueous supporting solution comprising anions and cations for both the anolyte and the catholyte, wherein the anions of the supporting solution consist of sulfate ions, chloride ions hydrogen ions, vanadium ions and vanadium oxide ions. 2. The system of claim 1 , wherein the sulfate ions and chloride ions include Cl − SO 4 2− ions with Cl − to SO 4 2− concentration ratio of between 1:100 and 100:1. 3. The system of claim 2 , wherein the Cl − to SO 4 2− concentration ratio is between 1:10 and 10:1. 4. The system of claim 2 , wherein the Cl − to SO 4 2− concentration ratio is between 1:3 and 3:1. 5. The system of claim 1 , wherein the catholyte comprises VO 2 Cl(H 2 O) 2 . 6. The system of claim 1 having a cell temperature greater than 40° C. during operation. 7. The system of claim 1 having a cell temperature between −35° C. and 60° C. during operation. 8. The system of claim 7 absent a thermal management device actively regulating the cell temperature. 9. The system of claim 1 having a state-of-charge condition greater than 0% and less than 100% during operation. 10. The system of claim 1 , wherein vanadium cation concentration is greater than 0.5 M. 11. The system of claim 1 , wherein vanadium cation concentration is greater than 1.7 M. 12. The system of claim 1 , wherein vanadium cation concentration is greater than 2.5 M. 13. A vanadium-based redox flow battery system, the system characterized by an anolyte comprising V 2+ and V 3+ , a catholyte comprising V 4+ and V 5+ , and an aqueous supporting solution for both the anolyte and the catholyte, consisting of sulfate ions, chloride ions and cations, wherein the cations are selected from a group consisting of hydrogen ions, vanadium ions and/or vanadium oxide ions. 14. An all-vanadium redox flow battery system, the system characterized by an anolyte comprising V 2+ and V 3+ , a catholyte comprising V 4+ and V 5+ , and an aqueous supporting solution for both the anolyte and the catholyte consisting of sulfate ions, chloride ions, hydrogen ions and vanadium ions and/or vanadium oxide ions.
Liquid materials, e.g. for Li-SOCl2 cells · CPC title
Details (electrodes H01M4/86 - H01M4/98) · CPC title
Indirect fuel cells, e.g. fuel cells with redox couple being irreversible (H01M8/18 takes precedence) · CPC title
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
Acid electrolytes · CPC title
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