Gas management systems and methods in a redox flow battery
A redox flow battery includes an anolyte storage tank configured for containing a quantity of anolyte and an anolyte headspace; a catholyte storage tank configured for containing a quantity of a catholyte and a catholyte headspace; and a gas management system comprising at least one conduit interconnecting the anolyte headspace and the catholyte headspace, and a gas exchange device configured to contain or release an evolving gas from either or both of the anolyte and catholyte storage tanks to an exterior battery environment when an interior battery pressure exceeds an exterior battery pressure by a predetermined amount.
1. A redox flow battery comprising:
an anolyte storage tank configured for containing a quantity of anolyte and an anolyte headspace;
a catholyte storage tank configured for containing a quantity of a catholyte and a catholyte headspace; and
a gas management system comprising at least one open conduit interconnecting the anolyte headspace and the catholyte headspace for free gas exchange between the anolyte and catholyte headspaces, and a passive gas exchange device in gaseous fluid communication with the anolyte headspace, the passive gas exchange device configured to release gas from the anolyte headspace to an exterior battery environment when an interior battery pressure exceeds an exterior battery pressure by a predetermined amount.
2. The redox flow battery of claim 1 , wherein the gas exchange device and tank head space is further configured to allow entry of an external gas into the anolyte storage tank when an exterior battery pressure exceeds an interior battery pressure by a predetermined amount.
3. The redox flow battery of claim 1 , wherein the gas exchange device and tank head space does not allow entry of an external gas into the anolyte storage tank when the exterior battery pressure does not exceed the interior battery pressure by the predetermined amount.
4. The redox flow battery of claim 1 , wherein the interior battery pressure is between −10 kPa and 10 kPa.
5. The redox flow battery of claim 1 , wherein the gas exchange device is a liquid-filled U-shaped tube.
6. The redox flow battery of claim 1 , wherein the liquid is selected from the group consisting of water, an aqueous solution of inorganic compound, an aqueous solution of organic compound, a water insoluble organic liquid, and a combination thereof.
7. The redox flow battery of claim 6 , wherein the U-shaped tube has a length and a diameter, and the diameter varies along the length.
8. The redox flow battery of claim 6 , wherein the U-shaped tube has a length and a diameter, and the diameter is constant along the length.
9. The redox flow battery of claim 1 , wherein the gas management system includes an anti-siphon device.
10. The redox flow battery of claim 9 , wherein the anti-siphon device is passively operated.
11. The redox flow battery of claim 9 , wherein the anti-siphon device is a siphon break comprising tubing that connects discharge and return piping to head spaces in the anolyte and catholyte storage tanks.
12. The redox flow battery of claim 1 , wherein the gas in the headspace is not flammable.
13. The redox flow battery of claim 1 , wherein the headspace comprises 5% volume or less oxygen.
14. The redox flow battery of claim 1 , wherein the evolving gas comprises O2, CO2, H2, C12, and any combination thereof.
15. The redox flow battery of claim 1 , wherein the redox flow battery is selected from the group consisting of a vanadium-sulfate redox flow battery, a vanadium-chloride redox flow battery, a vanadium-mixed sulfate and chloride battery, a vanadium-iron redox flow battery, and an iron-chromium redox flow battery.
16. The redox flow battery of claim 1 , wherein the redox flow battery is a vanadium redox flow battery.
17. The redox flow battery of claim 1 , wherein the anolyte and the catholyte include HCl.
18. A method of operating a redox flow battery, comprising
providing a battery of claim 1 , wherein the anolyte headspace and the catholyte headspace comprise air; and
operating the battery.
19. The method of claim 18 , wherein operating the battery comprises reacting the charged anolyte with oxygen in air to form H2O.
20. A redox flow battery comprising:
an anolyte storage tank configured for containing a quantity of anolyte and an anolyte headspace;
a catholyte storage tank configured for containing a quantity of a catholyte and a catholyte headspace; and
a gas management system comprising at least one open conduit interconnecting the anolyte headspace and the catholyte headspace for free gas exchange between the anolyte and catholyte headspaces, and a gas exchange device in gaseous fluid communication with the anolyte headspace, wherein the gas exchange device is a liquid-filled U-shaped tube configured to contain or release gas from the anolyte headspace to an exterior battery environment when an interior battery pressure exceeds an exterior battery pressure by a predetermined amount.
21. A redox flow battery comprising:
an anolyte storage tank configured for containing a quantity of anolyte and an anolyte headspace;
a catholyte storage tank configured for containing a quantity of a catholyte and a catholyte headspace; and
a gas management system comprising at least one open conduit interconnecting the anolyte headspace and the catholyte headspace for free gas exchange between the anolyte and catholyte headspaces, a siphon break comprising tubing connection discharge and return piping to headspaces in the anolyte and catholyte storage tanks, and a gas exchange device in gaseous fluid communication with the anolyte headspace, wherein the gas exchange device is configured to contain or release gas from the anolyte headspace to an exterior battery environment when an interior battery pressure exceeds an exterior battery pressure by a predetermined amount.