Flow battery cleansing cycle to maintain electrolyte health and system performance
US-2018316037-A1 · Nov 1, 2018 · US
US11749827B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11749827-B2 |
| Application number | US-202017080702-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 26, 2020 |
| Priority date | Nov 1, 2019 |
| Publication date | Sep 5, 2023 |
| Grant date | Sep 5, 2023 |
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Methods and systems are provided for iron preformation in a redox flow battery. In one example, a method may include, in a first condition, discharging and then charging the redox flow battery, and in a second condition, charging the redox flow battery including preforming iron metal at a negative electrode of the redox flow battery, and thereafter entering an idle mode of the redox flow battery including adjusting one or more electrolyte conditions. In some examples, each of preforming the iron metal and adjusting the one or more electrolyte conditions may increase a battery charge capacity to greater than a threshold battery charge capacity.
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The invention claimed is: 1. A method for a redox flow battery, the method comprising: in a first condition, discharging the redox flow battery and then, in response to a battery charge capacity falling below a battery cycling charging threshold, charging the redox flow battery without entering an idle mode of the redox flow battery; and in a second condition, in response to the battery charge capacity falling below a system conditioning charging threshold, charging the redox flow battery, including preforming an iron plating amount at a negative electrode of the redox flow battery, and thereafter entering the idle mode, including adjusting each of an electrolyte pH and an electrolyte state of charge (SOC) imbalance, wherein the system conditioning charging threshold is lower than the battery cycling charging threshold. 2. The method of claim 1 , further comprising, in a third condition, charging the redox flow battery and then discharging the redox flow battery without entering the idle mode. 3. The method of claim 2 , further comprising: determining whether a threshold degradation level of the redox flow battery is met; responsive to the threshold degradation level of the redox flow battery being met, entering the second condition; and responsive to the threshold degradation level of the redox flow battery not being met: determining an SOC of the redox flow battery, responsive to the SOC being greater than or equal to a threshold SOC, entering the first condition, and responsive to the SOC being less than the threshold SOC, entering the third condition. 4. The method of claim 1 , further comprising, in the second condition: determining the iron plating amount preformed at the negative electrode during charging of the redox flow battery; and responsive to the iron plating amount being less than a threshold amount, continuing charging the redox flow battery to preform a further iron plating amount. 5. The method of claim 4 , wherein determining the iron plating amount includes: determining one or more of a ferric iron electrolyte concentration and a previous cycling efficiency of the redox flow battery; and inferring the iron plating amount based on the one or more of the ferric iron electrolyte concentration and the previous cycling efficiency of the redox flow battery. 6. The method of claim 1 , wherein, in the second condition: charging the redox flow battery includes increasing an electrolyte tank pressure to greater than a first threshold pressure; and entering the idle mode includes decreasing the electrolyte tank pressure to less than a second threshold pressure, the second threshold pressure being less than the first threshold pressure, wherein the electrolyte tank pressure is increased due to generation of hydrogen gas at a negative electrode of the redox flow battery. 7. The method of claim 1 , wherein, in the second condition: charging the redox flow battery includes increasing a ferric iron electrolyte concentration by a first amount; and entering the idle mode includes decreasing the ferric iron electrolyte concentration by a second amount, the second amount being greater than the first amount, wherein the ferric iron electrolyte concentration is decreased by employing a catalytic electrolyte rebalancing subsystem to supply hydrogen gas to reduce ferric iron to ferrous iron. 8. The method of claim 2 , wherein preforming an iron plating amount in the second condition includes raising the SOC of the redox flow battery at a rate that is faster than a rate of SOC increase during the first condition or the third condition.
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
of iron for aqueous cells · CPC title
Power, energy, capacity or load · CPC title
Current · CPC title
Regulation of differential pressures · CPC title
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