Electrolyte tank volume rebalancing
US-2024396064-A1 · Nov 28, 2024 · US
US2016276696A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016276696-A1 |
| Application number | US-201615166174-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 26, 2016 |
| Priority date | Aug 15, 2012 |
| Publication date | Sep 22, 2016 |
| Grant date | — |
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Stable solutions comprising high concentrations of charged coordination complexes, including iron hexacyanides are described, as are methods of preparing and using same in chemical energy storage systems, including flow battery systems. The use of these compositions allows energy storage densities at levels unavailable by other iron hexacyanide systems.
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What is claimed is the following: 1 . A method comprising: dissolving Na 4 [Fe(CN) 6 ] and K 4 [Fe(CN) 6 ] in an amount of aqueous solvent, so as to provide a concentration of Fe(CN) 6 4− in the aqueous solvent that exceeds the concentration of Fe(CN) 6 4− in either a saturated solution of Na 4 [Fe(CN) 6 ] or a saturated solution of K 4 [Fe(CN) 6 ] in the aqueous solvent at the same temperature. 2 . The method of claim 1 , wherein the aqueous solvent has a pH ranging between about 7 and about 14. 3 . The method of claim 1 , wherein the aqueous solvent has a pH ranging between about 8 and about 13. 4 . The method of claim 1 , wherein Na 4 [Fe(CN) 6 ] and K 4 [Fe(CN) 6 ] are co-mixed as solids with the aqueous solvent. 5 . The method of claim 1 , wherein Na 4 [Fe(CN) 6 ] is added as a solid to a solution of K 4 [Fe(CN) 6 ] in the aqueous solvent. 6 . The method of claim 1 , wherein K 4 [Fe(CN) 6 ] is added as a solid to a solution of Na 4 [Fe(CN) 6 ] in the aqueous solvent. 7 . The method of claim 1 , wherein the aqueous solvent is substantially free of a co-solvent. 8 . The method of claim 1 , wherein the Fe(CN) 6 4− is present in the aqueous solvent at a concentration ranging between about 1 M and about 3 M. 9 . The method of claim 1 , wherein a molar ratio of sodium ions to potassium ions in the aqueous solvent after dissolution of the Na 4 [Fe(CN) 6 ] and K 4 [Fe(CN) 6 ] ranges between about 1:10 and about 10:1. 10 . The method of claim 9 , wherein the molar ratio of sodium ions to potassium ions ranges between about 0.9:1 and about 1.1:1. 11 . The method of claim 1 , wherein the aqueous solvent contains additional sodium and potassium ions. 12 . A method comprising: dissolving H 4 [Fe(CN) 6 ], NaOH and KOH in water, so as to provide a concentration of Fe(CN) 6 4− in an aqueous solution that exceeds the concentration of Fe(CN) 6 4− in either a saturated solution of Na 4 [Fe(CN) 6 ] or a saturated solution of K 4 [Fe(CN) 6 ] in water at the same temperature. 13 . The method of claim 12 , wherein the aqueous solution is substantially free of a co-solvent. 14 . The method of claim 12 , wherein the Fe(CN) 6 4− is present in the aqueous solution at a concentration ranging between about 1 M and about 3 M. 15 . The method of claim 12 , wherein a molar ratio of sodium ions to potassium ions in the aqueous solution ranges between about 1:10 and about 10:1. 16 . The method of claim 15 , wherein the molar ratio of sodium ions to potassium ions ranges between about 0.9:1 and about 1.1:1. 17 . A method comprising: dissolving Ca 4 [Fe(CN) 6 ], NaOH and KOH in water, so as to provide a concentration of Fe(CN) 6 4− in an aqueous solution that exceeds the concentration of Fe(CN) 6 4− in either a saturated solution of Na 4 [Fe(CN) 6 ] or a saturated solution of K 4 [Fe(CN) 6 ] in water at the same temperature. 18 . The method of claim 17 , further comprising: removing precipitated Ca(OH) 2 from the aqueous solution. 19 . The method of claim 17 , wherein the aqueous solution is substantially free of a co-solvent. 20 . The method of claim 17 , wherein the Fe(CN) 6 4− is present in the aqueous solution at a concentration ranging between about 1 M and about 3 M. 21 . The method of claim 17 , wherein a molar ratio of sodium ions to potassium ions in the aqueous solution ranges between about 1:10 and about 10:1. 22 . The method of claim 21 , wherein the molar ratio of sodium ions to potassium ions ranges between about 0.9:1 and about 1.1:1.
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
Indirect fuel cells, e.g. fuel cells with redox couple being irreversible (H01M8/18 takes precedence) · CPC title
Fuel cells in which the fuel is based on compounds containing nitrogen, e.g. hydrazine, ammonia · CPC title
Simple or complex iron cyanides · CPC title
Aqueous electrolytes · CPC title
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