Systems and methods for maintaining electrolyte health

Patent metadata

Field	Value
Publication number	US-2024243328-A1
Application number	US-202418409691-A
Country	US
Kind code	A1
Filing date	Jan 10, 2024
Priority date	Jan 18, 2023
Publication date	Jul 18, 2024
Grant date	—

Abstract

Systems and methods are provided for maintaining electrolyte health of a redox flow battery system. The redox flow battery system comprising a redox flow battery cell having a positive electrode compartment and a negative electrolyte compartment, an electrolyte storage tank storing positive and negative electrolyte, the positive and negative electrolyte circulated between the electrolyte storage tank and respective positive and negative electrode compartments. The redox flow battery system further comprises a rebalancing battery including a positive electrode arranged in a flow path of the positive electrolyte and a negative electrode arranged in a flow path of the negative electrolyte.

First claim

1 . A redox flow battery system, comprising:
a redox flow battery cell having a positive electrode compartment and a negative electrode compartment; an electrolyte storage tank storing a positive electrolyte and a negative electrolyte, the positive electrolyte circulated between the positive electrode compartment and the electrolyte storage tank and the negative electrolyte circulated between the negative electrode compartment and the electrolyte storage tank; and a rebalancing battery including a positive electrode arranged in a flow path of the positive electrolyte and a negative electrode arranged in a flow path of the negative electrolyte.

2 . The redox flow battery system of claim 1 , wherein the rebalancing battery is an all-aqueous iron battery.

3 . The redox flow battery system of claim 1 , wherein the rebalancing battery is arranged in the flow paths of the positive and negative electrolytes parallel to the positive and negative electrode compartments of the redox flow battery cell.

4 . The redox flow battery system of claim 1 , wherein the rebalancing battery is arranged in the flow paths of the positive and negative electrolytes in series with the positive and negative electrode compartments of the redox flow battery cell.

5 . The redox flow battery system of claim 4 , wherein the rebalancing battery is arranged in the flow path of the positive and negative electrolytes upstream or downstream of the positive and negative electrode compartments of the redox flow battery cell.

6 . The redox flow battery system of claim 1 , wherein Fe 3+ is reduced to Fe 2+ at the negative electrode of the rebalancing battery, and wherein Fe 2+ is oxidized to Fe 3+ at the positive electrode of the rebalancing battery.

7 . A method of operating a redox flow battery system, comprising:
fluidly coupling a rebalancing battery to a redox flow battery cell, wherein the rebalancing battery includes one or more iron battery cells, and a power source; requesting an operating mode of the rebalancing battery; maintaining a set voltage and current density applied across negative and positive electrodes of the rebalancing battery by the power source according to the operating mode; and wherein maintaining the set voltage and current density reduces Fe 3+ to Fe 2+ at the negative electrode.

8 . The method of claim 7 , wherein the rebalancing battery is fluidly coupled to the redox flow battery cell in series or in parallel.

9 . The method of claim 7 , wherein the set voltage is between 0.0 V and less than or equal to 1.2 V for each iron battery cell of the one or more iron battery cells, and wherein the current density is greater than 0 mA/cm 2 and less than 100 mA/cm 2 for each iron battery cell of the one or more iron battery cells.

10 . The method of claim 7 , wherein requesting the operating mode includes requesting one of continuous, interval, or triggered operating modes.

11 . The method of claim 10 , wherein requesting the continuous operating mode includes maintaining the set voltage and current density for a duration of operation of the rebalancing battery.

12 . The method of claim 10 , wherein requesting the interval operating mode includes selecting a duty cycle and applying the set voltage and current density at intervals according to the selected duty cycle.

13 . The method of claim 10 , wherein requesting the triggered operating mode includes maintaining the set voltage and current density when triggered by a sensor of the redox flow battery system.

14 . A redox flow battery system, comprising:
a positive electrolyte and a negative electrolyte; a redox flow battery cell including a positive electrode compartment configured to receive the positive electrolyte and a negative electrode compartment configured to receive the negative electrolyte; an iron battery fluidly coupled to the redox flow battery cell and including iron battery cells, and wherein each of the iron battery cells includes a negative electrode configured to receive the negative electrolyte, and a positive electrode configured to receive the positive electrolyte; and wherein the iron battery includes a power source configured to drive reduction at the negative electrode and oxidation at the positive electrode of each iron battery cell of the iron battery cells.

15 . The redox flow battery system of claim 14 , wherein the negative and positive electrodes are porous and formed of conductive carbon felt, graphene plates and/or conductive polymer plates, and wherein the iron battery does not plate iron and does not demand a catalyst formed of a precious metal.

16 . The redox flow battery system of claim 14 , wherein reduction at the negative electrode and oxidation at the positive electrode induces osmotic drag of water from the positive electrolyte to the negative electrolyte.

17 . The redox flow battery system of claim 14 , wherein reduction of Fe 3+ occurs at the negative electrode of the iron battery when the redox flow battery system is operating in charging mode and/or discharging mode.

18 . The redox flow battery system of claim 14 , wherein the iron battery is sized proportional to 1/100 th to ½ the active area the redox flow battery cell.

19 . The redox flow battery system of claim 14 , wherein the iron battery includes between 0 and 100 battery cells.

20 . The redox flow battery system of claim 14 , wherein the iron battery cells are electrically coupled to each other in series and fluidly coupled to each other in parallel.

Assignees

• Ess Technology Inc

Inventors

• Brindle Joseph
• Kissick Sean
• Mcdonald Timothy J
• Song Yang

Classifications

• H01M8/188 Primary

  by recharging of redox couples containing fluids; Redox flow type batteries · CPC title

• H01M16/006 Primary

  of fuel cells with rechargeable batteries · CPC title

• Y02E60/50

  Fuel cells · CPC title