Flow battery cleansing cycle to maintain electrolyte health and system performance

Patent metadata

Field	Value
Publication number	US-11296347-B2
Application number	US-201815965722-A
Country	US
Kind code	B2
Filing date	Apr 27, 2018
Priority date	Apr 28, 2017
Publication date	Apr 5, 2022
Grant date	Apr 5, 2022

Abstract

A method of cleansing a redox flow battery system may include operating the redox flow battery system in a charge, discharge, or idle mode, and responsive to a redox flow battery capacity being less than a threshold battery capacity, mixing the positive electrolyte with the negative electrolyte. In this way, battery capacity degradation following cyclic charging and discharging of the redox flow battery system can be substantially reduced.

First claim

The invention claimed is:

1. A method of operating a redox flow battery system, including:
circulating a positive electrolyte in a positive electrolyte circuit between a positive electrode compartment and a positive electrolyte chamber with a positive electrolyte pump,
circulating a negative electrolyte in a negative electrolyte circuit between a negative electrode compartment and a negative electrolyte chamber with a negative electrolyte pump, and
responsive to a cleansing condition being met, including
when a redox flow battery capacity is less than a threshold redox flow battery capacity,
when a discharge state of charge (SOC) of the positive electrolyte is less than a threshold discharge SOC, wherein the discharge SOC of the positive electrolyte corresponds to a SOC of the positive electrolyte during a discharge mode of the redox flow battery system, and
when a pH of the positive electrolyte is less than a threshold positive electrolyte pH,
performing a redox flow battery cleansing cycle, including mixing the positive electrolyte with the negative electrolyte while ion compositions of the positive electrolyte and the negative electrolyte are substantially similar, wherein mixing the positive electrolyte with the negative electrolyte includes,
opening a first mixing valve and directing flow of electrolyte from the positive electrolyte circuit to the negative electrolyte circuit, and
opening a second mixing valve and directing flow of electrolyte from the negative electrolyte circuit to the positive electrolyte circuit after flowing the electrolyte from the positive electrolyte circuit to the negative electrolyte circuit.

2. The method of claim 1 , wherein mixing the positive electrolyte with the negative electrolyte includes activating the negative electrolyte pump while opening the first mixing valve.

3. The method of claim 2 , wherein mixing the positive electrolyte with the negative electrolyte includes deactivating the positive electrolyte pump while opening the first mixing valve.

4. The method of claim 3 , wherein mixing the positive electrolyte with the negative electrolyte includes opening the first mixing valve for a first threshold duration.

5. The method of claim 1 , further comprising, in response to the cleansing condition being met, switching operation of the redox flow battery system to the discharge mode prior to mixing the positive electrolyte with the negative electrolyte.

6. The method of claim 1 , further comprising, in response to the cleansing condition being met, directing flow of the positive electrolyte through a rebalancing reactor prior to mixing the positive electrolyte with the negative electrolyte.

7. The method of claim 4 , wherein opening the second mixing valve and directing flow of the electrolyte from the negative electrolyte circuit to the positive electrolyte circuit after flowing the electrolyte from the positive electrolyte circuit to the negative electrolyte circuit further comprises, responsive to the first threshold duration elapsing, closing the first mixing valve and opening the second mixing valve to direct electrolyte from the negative electrolyte chamber to the positive electrolyte chamber.

8. The method of claim 1 , wherein the cleansing condition being met further includes when a difference between the redox flow battery capacity and the threshold redox flow battery capacity is greater than a threshold redox flow battery capacity difference.

9. The method of claim 1 , wherein the cleansing condition being met further includes when a charge current of the redox flow battery system is less than a threshold charge current.

10. The method of claim 1 , wherein the cleansing condition being met further includes when a discharge current of the redox flow battery system is less than a threshold discharge current.

11. The method of claim 4 , wherein mixing the positive electrolyte with the negative electrolyte further includes adjusting the first threshold duration based on a difference between the redox flow battery capacity and the threshold redox flow battery capacity, including increasing the first threshold duration when the difference between the redox flow battery capacity and the threshold redox flow battery capacity is larger and decreasing the first threshold duration when the difference between the redox flow battery capacity and the threshold redox flow battery capacity is smaller.

12. The method of claim 4 , wherein mixing the positive electrolyte with the negative electrolyte further includes, after the first threshold duration elapses, recirculating electrolyte in the negative electrolyte circuit without directing flow of electrolyte from the positive electrolyte circuit to the negative electrolyte circuit for a threshold time delay.

13. The method of claim 12 , further comprising increasing the threshold time delay in response to a longer first threshold duration, and decreasing the threshold time delay in response to a shorter first threshold duration.

14. The method of claim 1 , wherein the redox flow battery system includes an all iron redox flow battery system, wherein the threshold discharge SOC corresponds to a SOC of the positive electrolyte at which the positive electrolyte is free of ferric ion.

15. The method of claim 1 , further comprising, after opening the second mixing valve and directing flow of the electrolyte from the negative electrolyte circuit to the positive electrolyte circuit, in response to a redox flow battery SOC being less than a lower threshold redox flow battery SOC, stopping electrolyte flow between the positive electrolyte circuit and the negative electrolyte circuit.

16. The method of claim 15 , further comprising, after opening the second mixing valve and directing flow of the electrolyte from the negative electrolyte circuit to the positive electrolyte circuit, in response to the redox flow battery SOC being greater than the lower threshold redox flow battery SOC after a second threshold duration elapses,
closing the second mixing valve and stopping the directing of flow of the electrolyte from the negative electrolyte circuit to the positive electrolyte circuit, and
reopening the first mixing valve and directing flow of electrolyte from the positive electrolyte circuit to the negative electrolyte circuit.

Assignees

• Ess Technology Inc

Inventors

• Song Yang
• Evans Craig E

Classifications

• Y02E60/50

  Fuel cells · CPC title

• H01M8/188 Primary

  by recharging of redox couples containing fluids; Redox flow type batteries · CPC title

• G06V40/1394

  using acquisition arrangements · CPC title

• H01M8/04932

  of the individual fuel cell · CPC title

• H01M8/04186

  of liquid-charged or electrolyte-charged reactants · CPC title