Concentration management in flow battery systems using an electrochemical balancing cell

US10461352B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10461352-B2
Application numberUS-201715465502-A
CountryUS
Kind codeB2
Filing dateMar 21, 2017
Priority dateMar 21, 2017
Publication dateOct 29, 2019
Grant dateOct 29, 2019

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

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During operation of flow battery systems, the volume of one or more electrolyte solutions can change due to solvent loss processes. An electrochemical balancing cell can be used to combat volume variability. Methods for altering the volume of one or more electrolyte solutions can include: providing a first electrochemical balancing cell containing a membrane disposed between two half-cells, establishing fluid communication between a first aqueous electrolyte solution of a flow battery system and a first half-cell of the first electrochemical balancing cell, and applying a current to the first electrochemical balancing cell to change a concentration of one or more components in the first aqueous electrolyte solution. Applying the current causes water to migrate across the membrane, either to or from the first aqueous electrolyte solution, and a rate of water migration is a function of current.

First claim

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What is claimed is the following: 1. A method comprising: providing a first electrochemical balancing cell comprising a membrane disposed between two half-cells; establishing fluid communication between a first aqueous electrolyte solution of a flow battery system and a first half-cell of the first electrochemical balancing cell; and applying a current to the first electrochemical balancing cell to change a concentration of one or more components in the first aqueous electrolyte solution; wherein applying the current causes water to migrate across the membrane, either to or from the first aqueous electrolyte solution, and a rate of water migration is a function of current. 2. The method of claim 1 , wherein a second half-cell of the first electrochemical balancing cell contains a balancing aqueous fluid, and applying the current causes water to migrate from the second half-cell into the first aqueous electrolyte solution in the first half-cell, thereby decreasing an active material concentration in the first aqueous electrolyte solution. 3. The method of claim 2 , wherein the second half-cell of the first electrochemical balancing cell contains an oxygen-generation catalyst, and applying the current also generates protons from the balancing aqueous fluid; wherein the protons also migrate from the second half-cell into the first aqueous electrolyte solution in the first half-cell. 4. The method of claim 2 , further comprising: removing the balancing aqueous fluid from the second half-cell; and after removing the balancing aqueous fluid, applying the current to the first electrochemical balancing cell while the second half-cell is empty; wherein applying the current to the first electrochemical balancing cell while the second half-cell is empty causes water to migrate from the first half-cell into the second half-cell, thereby increasing an active material concentration in the first aqueous electrolyte solution. 5. The method of claim 1 , wherein a second half-cell of the first electrochemical balancing cell is left empty, and applying the current to the first electrochemical balancing cell causes water to migrate from the first half-cell into the second half-cell, thereby increasing an active material concentration in the first aqueous electrolyte solution. 6. The method of claim 5 , further comprising: introducing a balancing aqueous fluid into the second half-cell; and after introducing the balancing aqueous fluid into the second half-cell, applying the current to the first electrochemical balancing cell; wherein applying the current to the first electrochemical balancing cell causes water to migrate from the second half-cell into the first half-cell, thereby decreasing an active material concentration in the first aqueous electrolyte solution. 7. The method of claim 6 , wherein the second half-cell of the first electrochemical balancing cell contains an oxygen-generation catalyst, and applying the current also generates protons from the balancing aqueous fluid; wherein the protons also migrate from the second half-cell into the first aqueous electrolyte solution in the first half-cell. 8. The method of claim 1 , wherein a state of charge of the first aqueous electrolyte solution also changes while applying the current to the first electrochemical balancing cell. 9. The method of claim 1 , wherein the first aqueous electrolyte solution is circulated through a negative half-cell of the flow battery system. 10. The method of claim 1 , wherein a second aqueous electrolyte solution of the flow battery system is in fluid communication with a second electrochemical balancing cell. 11. A method comprising: providing a first electrochemical balancing cell comprising a membrane disposed between two half-cells; establishing fluid communication between a first aqueous electrolyte solution of a flow battery system and a first half-cell of the first electrochemical balancing cell; determining a quantity of the first aqueous electrolyte solution in the flow battery system; applying a current to the first electrochemical balancing cell; and either introducing a balancing aqueous fluid to a second half-cell of the first electrochemical balancing cell or emptying the second half-cell of the first electrochemical balancing cell in response to the quantity of the first aqueous electrolyte solution that is determined; wherein applying the current causes water to migrate across the membrane into the first aqueous electrolyte solution when the balancing aqueous fluid is present in the second half-cell of the first electrochemical balancing cell, and applying the current causes water to migrate across the membrane into the second half-cell when the balancing aqueous fluid is absent from the second half-cell of the first electrochemical balancing cell, and a rate of water migration is a function of current. 12. The method of claim 11 , wherein the second half-cell of the first electrochemical balancing cell contains an oxygen-generation catalyst, and applying the current to the first electrochemical balancing cell also generates protons when the balancing aqueous fluid is present; wherein the protons also migrate from the second half-cell into the first aqueous electrolyte solution in the first half-cell. 13. The method of claim 11 , wherein the balancing aqueous fluid is water or an aqueous electrolyte solution. 14. The method of claim 11 , wherein a state of charge of the first aqueous electrolyte solution also changes while applying the current to the first electrochemical balancing cell. 15. The method of claim 11 , wherein the first aqueous electrolyte solution is circulated through a negative half-cell of the flow battery system. 16. The method of claim 11 , wherein a second aqueous electrolyte solution of the flow battery system is in fluid communication with a second electrochemical balancing cell. 17. A flow battery system comprising: a first half-cell containing a first aqueous electrolyte solution; a second half-cell containing a second aqueous electrolyte solution; a first electrochemical balancing cell comprising a membrane disposed between two half-cells; wherein either the first half-cell or the second half-cell of the flow battery system is in fluid communication with a first half-cell of the first electrochemical balancing cell; and a source of a balancing aqueous fluid in fluid communication with the first electrochemical balancing cell, the flow battery system being configured to introduce the balancing aqueous fluid to a second half-cell of the first electrochemical balancing cell when a quantity of the first aqueous electrolyte solution falls below a lower threshold and to withdraw the balancing aqueous fluid from the second half-cell of the first electrochemical balancing cell when the quantity of the first aqueous electrolyte solution exceeds an upper threshold. 18. The flow battery system of claim 17 , further comprising: a detector configured to determine the quantity of the first aqueous electrolyte solution. 19. The flow battery system of claim 17 , further comprising: a processor responsive to the quantity of the first aqueous electrolyte solution and configured to initiate introduction or withdrawal of the first aqueous electrolyte solution to or from the second half-cell of the first electrochemical balancing cell. 20. The flow battery system of claim 17 , wherein the second half-cell of the first electrochemical balancing cell contains an oxygen-generation catalyst.

Assignees

Inventors

Classifications

  • H01M8/188Primary

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

  • Cross-Sectional Technologies · mapped topic

  • Cross-Sectional Technologies · mapped topic

  • Fuel cells · CPC title

  • Applications of fuel cells in buildings · CPC title

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What does patent US10461352B2 cover?
During operation of flow battery systems, the volume of one or more electrolyte solutions can change due to solvent loss processes. An electrochemical balancing cell can be used to combat volume variability. Methods for altering the volume of one or more electrolyte solutions can include: providing a first electrochemical balancing cell containing a membrane disposed between two half-cells, est…
Who is the assignee on this patent?
Lockheed Martin Energy Llc
What technology area does this patent fall under?
Primary CPC classification H01M8/188. Mapped technology areas include Electricity.
When was this patent published?
Publication date Tue Oct 29 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 4 related publications on this page (citations in our corpus or others sharing the same primary CPC).