Three-chamber electrochemical balancing cells for simultaneous modification of state of charge and acidity within a flow battery
Parasitic reactions, such as evolution of hydrogen at the negative electrode, can occur under the operating conditions of flow batteries and other electrochemical systems. Such parasitic reactions can undesirably impact operating performance by altering the pH and/or state of charge of one or both electrolyte solutions in a flow battery. Electrochemical balancing cells can allow adjustment of electrolyte solutions to take place. Electrochemical balancing cells suitable for placement in fluid communication with both electrolyte solutions of a flow battery can include: a first chamber containing a first electrode, a second chamber containing a second electrode, a third chamber disposed between the first chamber and the second chamber, a cation-selective membrane forming a first interface between the first chamber and the third chamber, and a bipolar membrane, a cation-selective membrane, or a membrane electrode assembly forming a second interface between the second chamber and the third chamber.
1. A flow battery system comprising:
a first half-cell containing a first electrolyte solution comprising a first active material; and
a second half-cell containing a second electrolyte solution;
wherein both the first half-cell and the second half-cell are in fluid communication with an electrochemical balancing cell comprising:
a first chamber containing a first electrode;
a second chamber containing a second electrode;
a third chamber disposed between the first chamber and the second chamber;
a first cation-selective membrane forming a first interface between the first chamber and the third chamber; and
a bipolar membrane, a second cation-selective membrane, or a membrane electrode assembly forming a second interface between the second chamber and the third chamber;
wherein the first half-cell is in fluid communication with the first chamber and the second half-cell is in fluid communication with the third chamber.
2. The flow battery system of claim 1 , wherein the first electrolyte solution is a positive electrolyte solution and the second electrolyte solution is a negative electrolyte solution.
3. The flow battery system of claim 1 , wherein a membrane electrode assembly forms the second interface wherein the membrane electrode assembly comprises a cation-selective membrane and an oxygen-formation catalyst.
4. The flow battery system of claim 3 , wherein the second chamber contains water or an acidic aqueous solution.
5. The flow battery system of claim 1 , wherein a bipolar membrane or a second cation selective membrane forms the second interface and the electrochemical balancing cell further comprises an oxygen-formation catalyst in the second chamber.
6. The flow battery system of claim 5 , wherein the second chamber contains an alkaline aqueous solution when a bipolar membrane forms the second interface.
7. The flow battery system of claim 5 , wherein the second chamber contains water or an acidic aqueous solution when a second cation-selective membrane forms the second interface.
8. The flow battery system of claim 1 , wherein the first electrode is a negative electrode and the second electrode is a positive electrode.
9. The flow battery system of claim 1 , wherein the first electrolyte solution and the second electrolyte solution each comprise an aqueous electrolyte solution.
10. The flow battery system of claim 1 , wherein at least one of the first electrolyte solution and the second electrolyte solution comprises a coordination complex as an active material.
11. A method of electrochemically rebalancing the state of charge in the flow battery system of claim 4 , the method comprising:
(a) transferring
(i) the first electrolyte solution between the first half-cell and the first chamber and
(ii) the second electrolyte solution between the second half-cell and the third chamber
of the flow battery system of claim 4 ;
(b) applying a potential across the electrochemical balancing cell to induce a current therein, such that the second electrode is a positive electrode and the first electrode is a negative electrode; and
(c) converting water into oxygen and protons in the second chamber and reducing the first active material in the first chamber under the potential;
wherein the protons migrate into the second electrolyte solution in the third chamber.
12. The method of claim 11 , wherein the first electrolyte solution and the second electrolyte solution each comprise an aqueous electrolyte solution.
13. The method of claim 11 , wherein at least one of the first electrolyte solution and the second electrolyte solution comprises a coordination complex as an active material.
14. A method of electrochemically rebalancing the state of charge in the flow battery system of claim 6 , the method comprising:
(a) transferring
(i) the first electrolyte solution between the first half-cell and the first chamber and
(ii) the second electrolyte solution between the second half-cell and the third chamber
of the flow battery system of claim 6 ;
(b) applying a potential across the electrochemical balancing cell to induce a current therein, such that the second electrode is a positive electrode and the first electrode is a negative electrode; and
(c) converting hydroxide ions into oxygen and water in the second chamber and reducing the first active material in the first chamber under the potential, while converting water into protons and hydroxide ions at the bipolar membrane;
wherein the protons migrate into the second electrolyte solution in the third chamber and the hydroxide ions migrate into the second chamber.
15. The method of claim 14 , wherein the first electrolyte solution and the second electrolyte solution each comprise an aqueous electrolyte solution.
16. The method of claim 14 , wherein at least one of the first electrolyte solution and the second electrolyte solution comprises a coordination complex as an active material.