# US 12,191,547 B2 · Ferric ion reduction system to enable electrolyte rebalance within an iron flow battery > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,191,547 B2 - Document ID: US12191547B2 - Status: Granted - Kind: B2 - Application number: 17/820,272 - Filed: 2022-08-17 - Published: 2023-03-30 - Granted: 2025-01-07 - Earliest claimed: 2021-09-24 - Assignees: Uop LLC - Applicants: Uop LLC - Inventors: Stuart R. Miller; Christopher D. DiGiulio; William T. Kender - Web page: https://patentgrep.com/patent/US12191547B2 ## CPC - H01M 8/188: {by recharging of redox couples containing fluids; Redox flow type batteries} - H01M 8/04186: of liquid-charged or electrolyte-charged reactants - H01M 8/04313: characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function - H01M 50/46: Separators, membranes or diaphragms characterised by their combination with electrodes - H01M 50/673: Containers for storing liquids; Delivery conduits therefor - Y02E 60/50: Fuel cells - H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract A flow battery system with a cathode cell including a first electrode, an anode cell includes a second electrode, and a membrane between the two cells. A first electrolyte tank includes a catholyte. A second electrolyte tank includes an anolyte. The system includes two rebalancing cells. A first rebalancing cell is in fluid communication between the cathode cell and the first electrolyte tank and is configured to reduce active species from the catholyte. The second rebalancing cell is in fluid communication with the first electrolyte tank and the second electrolyte tank such that the first electrolyte tank and the second electrolyte tank are in direct fluid communication. The second rebalancing cell is configured to reduce active species from the catholyte and the reduced catholyte may be combined directly with the anolyte. The second rebalancing cell may be a chemical reactor, a catalytic reactor, or an electrochemical reactor. ## Claims ### Claim 1 An iron redox flow battery system comprising: a redox electrode in fluid communication to a first electrolyte tank with a catholyte; a plating electrode in fluid communication to a second electrolyte tank with an anolyte; a rebalancing cell in fluid communication with the redox electrode and configured to reduce active species from the catholyte; a second rebalancing cell in fluid communication with the first electrolyte tank and the second electrolyte tank such that the first electrolyte tank and the second electrolyte tank are in direct fluid communication; a monitoring device configured to provide an obtained value relating to a condition of the catholyte, or the anolyte, or both; and, a controller in communication with the monitoring device, the controller comprising non-transitory computer-readable media storing executable instructions that, when executed, cause the controller to: compare the obtained value against a threshold value; and when the obtained value is above or below a threshold, displace a volume of the catholyte from the first electrolyte tank to the second rebalancing cell to reduce ferric cations in the catholyte. ### Claim 2 (depends on 1) The iron redox flow battery system of claim 1, wherein the second rebalancing cell is a hydrogen recombination reactor. ### Claim 3 (depends on 2) The iron redox flow battery system of claim 2, wherein the hydrogen recombination reactor is a chemical reactor, a catalytic reactor, or an electrochemical reactor. ### Claim 4 (depends on 1) The iron redox flow battery system of claim 1, wherein the catholyte and the anolyte both comprise iron ions and wherein a source of the iron ions comprises FeCl2, FeCl3, FeSO4, Fe2(SO4)3, FeO, Fe, Fe2O3, or combinations thereof. ### Claim 5 (depends on 1) The iron redox flow battery system of claim 1, wherein the anolyte comprises Fe2+ at a concentration between 1.0 to 4.5 M. ### Claim 6 (depends on 5) The iron redox flow battery system of claim 5, wherein the anolyte further comprises one or more of NaCl, KCl, NH4Cl, boric acid, glycine, FeCl3, or combinations thereof. ### Claim 7 (depends on 5) The iron redox flow battery system of claim 5, wherein the catholyte comprises Fe2+ at a concentration between 0.5 to 4.0 M. ### Claim 8 (depends on 5) The iron redox flow battery system of claim 5, wherein the catholyte further comprises one or more of NaCl, KCl, NH4Cl, HCl, glycine, boric acid, FeCl3, or combinations thereof. ### Claim 9 (depends on 1) The iron redox flow battery system of claim 1, wherein the volume of the catholyte is displaced, via a pump. ### Claim 10 (depends on 9) The iron redox flow battery system of claim 9, further comprising: a storage vessel in fluid communication between the second rebalancing cell and the second electrolyte tank. ### Claim 11 (depends on 10) The iron redox flow battery system of claim 10, wherein the executable instructions, when executed, further cause the controller to: compare an obtained value against a threshold value; and when the obtained value is above or below the threshold, pump a volume of fluid, via a pump, from the storage vessel to the second electrolyte tank. ### Claim 12 An iron redox flow battery system comprising: a cathode cell having a first electrode; an anode cell having a second electrode; a membrane separating the cathode cell and the anode cell; a first electrolyte tank with a catholyte, the first electrolyte tank in fluid communication with the cathode cell; a second electrolyte tank with an anolyte, the second electrolyte tank in fluid communication with the anode cell; a first rebalancing cell in fluid communication between the cathode cell and the first electrolyte tank, the first rebalancing cell configured to reduce active species from the catholyte; and, a second rebalancing cell in fluid communication with the first electrolyte tank and the second electrolyte tank such that the first electrolyte tank and the second electrolyte tank are in direct fluid communication, the second rebalancing cell configured to reduce active species from the catholyte; a monitoring device configured to provide an obtained value relating to a condition of the catholyte, or the anolyte, or both; and, a controller in communication with the monitoring device, the controller comprising non- transitory computer-readable media storing executable instructions that, when executed, cause the controller to: compare the obtained value against a threshold value; and when the obtained value is above or below a threshold, displace a volume of the catholyte from the first electrolyte tank to the second rebalancing cell to reduce ferric cations in the catholyte. ### Claim 13 (depends on 12) The iron redox flow battery system of claim 12, wherein the second rebalancing cell comprises at least two chambers, wherein a first chamber of the at least two chambers is configured to receive a portion of the catholyte and provide a reduced catholyte to the second electrolyte tank and, wherein a second chamber of the at least two chambers is configured to receive a second portion of the catholyte. ### Claim 14 (depends on 13) The iron redox flow battery system of claim 13, wherein an effluent stream from the second chamber comprises H+ ions. ### Claim 15 (depends on 13) The iron redox flow battery system of claim 13, wherein the second rebalancing cell comprises a third chamber configured to oxidize hydrogen gas. ### Claim 16 (depends on 15) The iron redox flow battery system of claim 15, wherein the first chamber and the third chamber are in electrical communication, and wherein the second chamber is located between the first chamber and the third chambers. ### Claim 17 (depends on 13) The iron redox flow battery system of claim 13, wherein the reduced catholyte stream comprises H+ ions.