Electrolyte tank volume rebalancing
US-2024396064-A1 · Nov 28, 2024 · US
US9859583B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9859583-B2 |
| Application number | US-201414515423-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 15, 2014 |
| Priority date | Mar 4, 2014 |
| Publication date | Jan 2, 2018 |
| Grant date | Jan 2, 2018 |
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The fundamental charge storage mechanisms in a number of currently studied high energy redox couples are based on intercalation, conversion, or displacement reactions. With exception to certain metal-air chemistries, most often the active redox materials are stored physically in the electrochemical cell stack thereby lowering the practical gravimetric and volumetric energy density as a tradeoff to achieve reasonable power density. In a general embodiment, a mediated redox flow battery includes a series of secondary organic molecules that form highly reduced anionic radicals as reaction mediator pairs for the reduction and oxidation of primary high capacity redox species ex situ from the electrochemical cell stack. Arenes are reduced to stable anionic radicals that in turn reduce a primary anode to the charged state. The primary anode is then discharged using a second lower potential (more positive) arene. Compatible separators and solvents are also disclosed herein.
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What is claimed is: 1. A redox flow battery comprising: a half-cell electrode chamber coupled to a current collector electrode; and a polymeric lithium and/or sodium ion conducting separator coupled to the half-cell electrode chamber, wherein the half-cell electrode chamber comprises a first redox-active mediator and a second redox-active mediator, wherein the first redox-active mediator and the second redox-active mediator are circulated through the half-cell electrode chamber into an external container, wherein the external container comprises an active electrode material; the active electrode material has a redox potential between a redox potential of the first redox-active mediator and a redox potential of the second redox-active mediator, wherein the first mediator is reduced at the current collector electrode and the reduced first mediator reduces the active electrode material during a charging cycle and wherein the second mediator is reduced by the reduced active anode material and the reduced second mediator is oxidized at the current collector electrode during, a discharging cycle; and the first mediator comprises a first arene, wherein the first arene is a polyaromatic hydrocarbon, biphenyl, or a substituted derivative of either thereof. 2. The redox flow battery of claim 1 , wherein the second mediator comprises a second arene, wherein the second arene is a polyaromatic hydrocarbon, biphenyl, or a substituted derivative of either thereof, with the proviso that the second mediator is not the same as the first mediator. 3. The redox flow battery of claim 1 , wherein the first and second mediator are dissolved in a non-aqueous solvent. 4. The redox flow battery of claim 3 , wherein the solvent is selected from the group consisting of: diglyme, triglyme, tetraethyleneglycol dimethylether, and mixtures thereof. 5. The redox flow battery of claim 1 , wherein the first or second arene is biphenyl or a substituted derivative thereof. 6. The redox flow battery of claim 1 , wherein the first, second, or first and second arene is substituted, and includes one or more substituent groups, R, wherein each R is independently selected from a linear, branched, cyclic, or aromatic alkyl group having 1-50 carbon atoms, optionally functionalized with a functional group including O, S, or N. 7. The redox flow battery of claim 1 , wherein the active electrode in the external container is in a plug-flow reactor configuration. 8. The redox flow battery of claim 1 , wherein the first mediator is soluble in a solvent at a molarity 0.5 M to 5 M. 9. The redox flow battery of claim 1 , wherein the half-cell electrode chamber is an anode cell chamber and the electrode is an anode. 10. A redox flow battery comprising: a half-cell electrode chamber coupled to a current collector electrode, wherein the half-cell electrode chamber comprises a first redox-active mediator and a second redox-active mediator, wherein the first redox-active mediator and the second redox-active mediator are circulated through the half-cell electrode chamber into an external container, wherein the external container comprises an active electrode material; the active electrode material has a redox potential between a redox potential of the first redox-active mediator and a redox potential of the second redox-active mediator, wherein the first mediator is reduced at the current collector electrode and the reduced first mediator reduces the active electrode material during a charging cycle and wherein the second mediator is reduced by the reduced active anode material and the reduced second mediator is oxidized at the current collector electrode during a discharging cycle; and the first mediator comprises a first arene, wherein the first arene is biphenyl or a substituted derivative thereof. 11. The redox flow battery of claim 10 , wherein the second mediator comprises a second arene, wherein the second arene is substituted or unsubstituted, with the proviso that the second arene is not the same as the first arene. 12. The redox flow battery of claim 10 , wherein a single cell of the battery has a voltage of 1 to 4. 13. The redox flow battery of claim 10 , wherein the first and second mediator are dissolved in a non-aqueous solvent. 14. The redox flow battery of claim 13 , wherein the solvent is selected from the group consisting of: tetrahydrofuran, dimethoxyethane, diglyme, triglyme, tetraethyleneglycol dimethylether and mixtures thereof. 15. The redox flow battery of claim 13 , wherein the second arene is selected from the group consisting of: biphenyl, methylnaphthalene, naphthalene, acenaphthalyne, pyrene, anthracene, coronene, perylene, tetracene, fluorene, azulene, and chrysene, and substituted derivatives of any thereof, with the proviso that the second arene is not the same as the first arene.
Organic resins; Organic polymers · CPC title
Cross-Sectional Technologies · mapped topic
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
Metals or alloys (H01M4/92 takes precedence) · CPC title
as mixture · CPC title
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