Redox flow batteries having multiple electroactive elements
Introducing multiple redox reactions with a suitable voltage range can improve the energy density of redox flow battery (RFB) systems. One example includes RFB systems utilizing multiple redox pairs in the positive half cell, the negative half cell, or in both. Such RFB systems can have a negative electrolyte, a positive electrolyte, and a membrane between the negative electrolyte and the positive electrolyte, in which at least two electrochemically active elements exist in the negative electrolyte, the positive electrolyte, or both.
1. A battery comprising:
a redox flow battery (RFB) system having an aqueous-based negative electrolyte, an aqueous-based positive electrolyte, and a membrane between the negative electrolyte and the positive electrolyte, the system further comprising:
at least two electrochemically active elements in the negative electrolyte, the positive electrolyte, or both, thereby employing at least two electrochemically active redox pairs, the at least two electrochemically active redox pairs being present in the RFB negative half cell, positive half cell, or both, during both charging and discharging of the RFB system, wherein the positive electrolyte comprises electrochemically active redox pair ions consisting of electrochemically active V redox ions and electrochemically active Fe redox ions.
2. The system of claim 1 , wherein the volume of the negative electrolyte is approximately twice that of the positive electrolyte.
3. The system of claim 1 , wherein the negative electrolyte and the positive electrolyte further comprise chloride.
4. The system of claim 1 , wherein the negative electrolyte and the positive electrolyte further comprise sulfate.
5. The system of claim 1 , wherein the negative electrolyte and the positive electrolyte further comprise chloride and sulfate.
6. The system of claim 5 , wherein the chloride to sulfate concentration ratio is between 1:10 and 10:1.
7. The system of claim 5 , wherein the chloride to sulfate concentration ratio is between 1:3 and 3:1.
8. The system of claim 1 , wherein negative electrolyte comprises V 2+ and V 3+ with total concentrations of V 2+ and V 3+ greater than 1M.
9. The system of claim 1 , wherein positive electrolyte total concentrations of V 4+ and V 5+ are greater than 1M.
10. The system of claim 1 , wherein positive electrolyte total concentrations of Fe 2+ and Fe 3+ are greater than 1M.
11. The system of claim 1 , wherein the negative electrolyte comprises Zn.
12. The system of claim 1 , having a cell temperature less than 60° C. during operation.
13. The system of claim 1 , having a cell temperature between −20° C. and 50° C. during operation.
14. A redox flow battery (RFB) system having:
a membrane separating an aqueous-based negative electrolyte and an aqueous-based positive electrolyte, the positive electrolyte comprises electrochemically active redox pair ions V 4+ and V 5+ as well as electrochemically active redox pair ions Fe 2+ and Fe 3+ , the negative electrolyte comprises electrochemically active redox pair ions consisting of electrochemically active redox pair ions V 2+ and V 3+ ;
an operational voltage window having a lower limit not greater than 0.6 V and an upper limit not less than 1.5 V; and
a volume of the negative electrolyte that is approximately twice that of the positive electrolyte, the RFB system thereby employing at least two electrochemically active redox pairs in the RFB positive half cell during charging and discharging of the RFB system.
15. The RFB system of claim 14 , wherein the negative electrolyte and the positive electrolyte further comprise a mixture of chloride and sulfate.