Electrolytes for iron flow battery
A method of operating an iron redox flow battery system may comprise fluidly coupling a plating electrode of an iron redox flow battery cell to a plating electrolyte; fluidly coupling a redox electrode of the iron redox flow battery cell to a redox electrolyte; fluidly coupling a ductile plating additive to one or both of the plating electrolyte and the redox electrolyte; and increasing an amount of the ductile plating additive to the plating electrolyte in response to an increase in the plating stress at the plating electrode. In this way, ductile Fe can be plated on the negative electrode, and the performance, reliability and efficiency of the iron redox flow battery can be maintained. In addition, iron can be more rapidly produced and plated at the plating electrode, thereby achieving a higher charging rate for all iron flow batteries.
1. A method of operating an iron redox flow battery system, comprising:
fluidly coupling a plating electrode of an iron redox flow battery cell to a plating electrolyte;
fluidly coupling a redox electrode of the iron redox flow battery cell to a redox electrolyte;
fluidly coupling a ductile plating additive to one or both of the plating electrolyte and the redox electrolyte; and
increasing a first amount of the ductile plating additive delivered to the plating electrolyte in response to an increase in a plating stress at the plating electrode, the increase determined by monitoring one or more operating parameters during charging of the iron redox flow battery system.
2. The method of claim 1 , further comprising increasing a second amount of the ductile plating additive delivered to the redox electrolyte in response to the increase in the plating stress at the plating electrode.
3. The method of claim 2 , further comprising raising a plating electrolyte temperature responsive to the increase in the plating stress at the plating electrode.
4. The method of claim 3 , further comprising raising a redox electrolyte temperature responsive to the increase in the plating stress at the plating electrode.
5. The method of claim 4 , further comprising raising the plating electrolyte temperature responsive to the increase in the plating stress at the plating electrode while maintaining a plating electrolyte composition and a plating electrolyte pH.
6. The method of claim 5 , further comprising raising the redox electrolyte temperature responsive to the increase in the plating stress at the plating electrode while maintaining a redox electrolyte composition and a redox electrolyte pH.
7. The method of claim 6 , further comprising reducing a charging current density applied to the redox flow battery cell responsive to the increase in the plating stress of the plating electrode.
8. The method of claim 7 , further comprising reducing the charging current density applied to the redox flow battery cell responsive to the increase in the plating stress of the plating electrode while maintaining the plating electrolyte composition and the plating electrolyte temperature.
9. The method of claim 8 , further comprising purging one or both of the plating electrolyte and the redox electrolyte with an inert gas.
10. The method of claim 9 , wherein fluidly coupling the ductile plating additive to one or both of the plating electrolyte and the redox electrolyte includes supplying MnCl 2 to one or both of the plating electrolyte and the redox electrolyte, wherein the plating electrolyte and the redox electrolyte comprise FeCl 2 , KCl, and H 3 BO 3 .
11. A method of operating an iron redox flow battery system, comprising:
responsive to a charging current density applied to an iron redox flow battery (IFB) cell increasing above a threshold charging current density, raising a concentration of a ductile plating additive above a threshold concentration in a plating electrolyte fluidly coupled to a plating electrode, during charging of the iron redox flow battery system.
12. The method of claim 11 , further comprising increasing a temperature of the IFB cell while maintaining a composition of the plating electrolyte and the concentration of the ductile plating additive responsive to the charging current density applied to the IFB cell increasing above the threshold charging current density.
13. The method of claim 12 , further comprising reducing the concentration of the ductile plating additive responsive to the charging current density applied to the IFB cell decreasing below the threshold charging current density.
14. A redox flow battery system, comprising:
a redox flow battery cell, including a plating compartment and a redox compartment;
a plating electrode fluidly coupled to a plating electrolyte in the plating compartment;
a redox electrode fluidly coupled to a redox electrolyte in the redox compartment;
a ductile plating additive stored in one or more storage tanks fluidly coupled to one or both of the plating electrolyte and the redox electrolyte; and
a controller, including executable instructions to raise a concentration of the ductile plating additive in one or both of the plating compartment and the redox compartment in response to a charging current density increasing above a threshold charging current density during charging of the redox flow battery system.
15. The redox flow battery system of claim 14 , wherein the executable instructions further include raising the concentration of the ductile plating additive in one or both of the plating compartment and the redox compartment in response to the charging current density increasing above the threshold charging current density while maintaining a temperature of the plating compartment and the redox compartment.
16. The redox flow battery system of claim 15 , wherein the executable instructions further include raising the concentration of the ductile plating additive in one or both of the plating compartment and the redox compartment in response to the charging current density increasing above the threshold charging current density while maintaining a pH of the plating electrolyte and the redox electrolyte.
17. The redox flow battery system of claim 16 , further comprising a heater thermally coupled to the plating electrolyte, wherein the executable instructions further include increasing an amount of heat supplied to the plating electrolyte from the heater in response to the charging current density increasing above the threshold charging current density.
18. The redox flow battery system of claim 17 , wherein the executable instructions further include increasing the amount of heat supplied to the plating electrolyte from the heater in response to the charging current density increasing above the threshold charging current density, while maintaining a composition of the plating electrolyte.
19. The redox flow battery system of claim 18 , wherein the executable instructions further include decreasing the concentration of the ductile plating additive in one or both of the plating compartment and the redox compartment in response to the charging current density decreasing below the threshold charging current density.
20. The redox flow battery system of claim 19 , wherein
the plating electrolyte and the redox electrolyte comprise one or more of FeCl 2 , KCl, and H 3 BO 3 , and
the ductile plating additive comprises one or more of MnCl 2 , InCl 2 , and BiCl 2 .