Electrolyte tank volume rebalancing
US-2024396064-A1 · Nov 28, 2024 · US
US9966626B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9966626-B2 |
| Application number | US-201515119908-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 16, 2015 |
| Priority date | Feb 20, 2014 |
| Publication date | May 8, 2018 |
| Grant date | May 8, 2018 |
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The present invention relates to a redox flow battery, and more particularly, to a redox flow battery which is charged and discharged by supplying a positive electrolyte and a negative electrolyte to a battery cell using an active material containing vanadium and a cation exchange membrane, in which the positive electrolyte and the negative electrolyte contain vanadium ions as active ions, the difference in volume between the positive electrolyte and the negative electrolyte is maintained at 10% or less, and the total concentration of anions in the negative electrolyte is higher than the total concentration of anions in the positive electrolyte, whereby the transfer of water in the battery is controlled and a change in the volume of the electrolytes is minimized.
Opening claim text (preview).
The invention claimed is: 1. A redox flow battery which is charged and discharged by supplying a positive electrolyte and a negative electrolyte to a battery cell, wherein the battery cell includes a cation exchange membrane, and the positive electrolyte and the negative electrolyte include an active material containing vanadium ions, and wherein while charging and discharging the redox flow battery, a difference in volume between the positive electrolyte and the negative electrolyte is maintained at 10% or less, and a total anion concentration of the negative electrolyte is higher than a total anion concentration of the positive electrolyte. 2. The redox flow battery of claim 1 , wherein anions in each of the positive electrolyte and the negative electrolyte includes: anion (A) dissociated from the active material; and anion (B) dissociated from a supporting electrolyte, in which the anion (A) and the anion (B) are the same or different. 3. The redox flow battery of claim 2 , wherein the amount of the active material in the positive electrolyte is the same as the amount of the active material in the negative electrolyte, and the amount of the supporting electrolyte in the negative electrolyte is larger than the amount of the supporting electrolyte in the positive electrolyte. 4. The redox flow battery of claim 1 , wherein the concentration of the vanadium ions in the positive electrolyte is the same as the concentration of the vanadium ions in the negative electrolyte. 5. The redox flow battery of claim 1 , wherein a ratio of a total anion concentration (C 1 ) of the negative electrolyte to a total anion concentration (C 2 ) of the positive electrolyte satisfies the following condition 1: 1< C 1 /C 2 ≤2. Condition 1 6. The redox flow battery of claim 1 , wherein a ratio of a total anion concentration (C 1 ) of the negative electrolyte to a vanadium ion concentration (C 3 ) of the negative electrolyte satisfies the following condition 2: 2≤ C 1 /C 3 ≤3.5. Condition 2 7. The redox flow battery of claim 1 , wherein a ratio of a total anion concentration (C 2 ) of the positive electrolyte to a vanadium ion concentration (C 4 ) of the positive electrolyte satisfies the following condition 3: 2≤ C 2 /C 4 ≤3.5. Condition 3 8. The redox flow battery of claim 1 , wherein the positive electrolyte or the negative electrolyte further includes a cation selected from the group consisting of alkali metal ions, alkaline earth metal ions and zinc group metal ions.
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