Charge capacity management in redox flow battery string

1. A method of operating a redox flow battery string, comprising:

providing a plurality of redox flow batteries, each redox flow battery in electrical communication with at least one other redox flow battery, and each redox flow battery comprising an anolyte storage tank including a quantity of anolyte, a catholyte storage tank including a quantity of catholyte, and an electrochemical cell in fluid communication with the anolyte and catholyte storage tanks;

obtaining an open circuit voltage value for each redox flow battery in the string;

identifying a predetermined open circuit voltage value in the string; and

adjusting the open circuit voltage value for each redox flow battery to correspond to the predetermined open circuit voltage value, wherein adjusting the open circuit voltage for each redox flow battery comprises transferring a volume of catholyte to the anolyte storage tank, or a volume of anolyte to the catholyte storage tank of the redox flow battery, and wherein the volume of catholyte is transferred from the catholyte storage tank of a redox flow battery or wherein the volume of anolyte is transferred from the anolyte storage tank of a redox flow battery.

2. The method of claim 1 , wherein each redox flow battery is not in fluid communication with any other redox flow battery.

3. The method of claim 1 , wherein each redox flow battery comprises a predetermined ratio of an amount of redox-active materials in the anolyte and an amount of redox-active materials in the catholyte, the predetermined ratio being correlated to the open circuit voltage value.

4. The method of claim 1 , wherein each redox flow battery comprises a predetermined volume ratio of anolyte and the catholyte, the predetermined volume ratio being correlated to the open circuit voltage value.

5. The method of claim 4 , wherein the predetermined volume ratio of the anolyte to the catholyte, or the catholyte to the anolyte, is 1:1.05 to 1:1.50.

6. The method of claim 1 , wherein the volume of catholyte is transferred from the catholyte storage tank of the same redox flow battery.

7. The method of claim 1 , wherein the volume of catholyte is transferred from a catholyte storage tank of a different redox flow battery.

8. The method of claim 1 , wherein the volume of anolyte is transferred from the anolyte storage tank of the same redox flow battery.

9. The method of claim 1 , wherein the volume of anolyte is transferred from an anolyte storage tank of a different redox flow battery.

10. The method of claim 1 , wherein transferring the volume of catholyte or anolyte comprises a continuous catholyte or anolyte transfer.

11. The method of claim 1 , wherein transferring the volume of catholyte or anolyte comprises a periodic catholyte or anolyte transfer.

12. The method of claim 1 , wherein transferring the volume of catholyte or anolyte comprises flowing the volume of catholyte or anolyte through a conduit interconnecting the anolyte storage tank and catholyte storage tank of each redox flow battery.

13. The method of claim 12 , wherein the conduit is an overflow pipe.

14. The method of claim 12 , wherein transferring the volume of catholyte or anolyte comprises pumping the catholyte or anolyte through the conduit interconnecting the anolyte storage tank and catholyte storage tank.

15. The method of claim 1 , comprising passively transferring the volume of catholyte or anolyte.

16. The method of claim 1 , comprising actively transferring the volume of catholyte or anolyte.

17. The method of claim 1 , comprising passively and actively transferring the volume of catholyte or anolyte.

18. The method of claim 1 , wherein adjusting the open circuit voltage comprises adding an oxidizing agent or a reducing agent to the anolyte storage tank or the catholyte storage tank of one or more redox flow batteries in the plurality of redox flow batteries.

19. The method of claim 18 , wherein the oxidizing agent is selected from the group consisting of air, oxygen, hydrogen peroxide, ozone, or any combination thereof.

20. The method of claim 18 , wherein the reducing agent is selected from the group consisting of sugars, alcohols, organic acids, oils, hydrocarbons, and any combination thereof.

21. The method of claim 1 , wherein adjusting the open circuit voltage is controlled by a battery management system.

22. The method of claim 1 , wherein adjusting the open circuit voltage is performed during maintenance of the redox flow battery system.

23. A method of operating a redox flow battery string, comprising:

providing a plurality of redox flow batteries, each redox flow battery in electrical communication with at least one other redox flow battery, and each redox flow battery comprising an anolyte storage tank including a quantity of anolyte, a catholyte storage tank including a quantity of catholyte, and an electrochemical cell in fluid communication with the anolyte and catholyte storage tanks;

obtaining an open circuit voltage value for each redox flow battery in the string;

identifying a predetermined open circuit voltage value in the string; and

adjusting the open circuit voltage value for each redox flow battery to correspond to the predetermined open circuit voltage value, wherein adjusting the open circuit voltage comprises adding an oxidizing agent or a reducing agent to the anolyte storage tank or the catholyte storage tank of one or more redox flow batteries in the plurality of redox flow batteries.

24. The method of claim 23 , wherein the oxidizing agent is selected from the group consisting of air, oxygen, hydrogen peroxide, ozone, or any combination thereof.

25. The method of claim 23 , wherein the reducing agent is selected from the group consisting of sugars, alcohols, organic acids, oils, hydrocarbons, and any combination thereof.