Method of operating redox flow battery, and redox flow battery system

US10199672B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10199672-B2
Application numberUS-201515537581-A
CountryUS
Kind codeB2
Filing dateDec 7, 2015
Priority dateDec 22, 2014
Publication dateFeb 5, 2019
Grant dateFeb 5, 2019

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  4. Key dates

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  5. First independent claim

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Abstract

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Provided is a method of operating an RF battery in which charging and discharging are performed by circulating and supplying a positive electrode electrolyte in a positive electrode tank to a positive electrode and circulating and supplying a negative electrode electrolyte in a negative electrode tank to a negative electrode. The positive electrode electrolyte contains manganese ions and added metal ions. The negative electrode electrolyte contains at least one species of metal ions selected from the group consisting of titanium ions, vanadium ions, and chromium ions. The added metal ions are at least one selected from the group consisting of cadmium ions, tin ions, antimony ions, lead ions, and bismuth ions. The method of operating an RF battery includes a dissolution step in which, when metal precipitates, formed by reduction of the added metal ions which have moved from the positive electrode electrolyte to a circulating pathway of the negative electrode electrolyte, are contained in the circulating pathway of the negative electrode electrolyte, the metal precipitates are dissolved and ionized in the positive electrode electrolyte.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method of operating a redox flow battery in which charging and discharging are performed by circulating and supplying a positive electrode electrolyte in a positive electrode tank to a positive electrode and circulating and supplying a negative electrode electrolyte in a negative electrode tank to a negative electrode, wherein the positive electrode electrolyte contains manganese ions and added metal ions; the negative electrode electrolyte contains at least one species of metal ions selected from the group consisting of titanium ions, vanadium ions, and chromium ions; and the added metal ions are at least one selected from the group consisting of cadmium ions, tin ions, antimony ions, lead ions, and bismuth ions, the method comprising a dissolution step in which, when metal precipitates, formed by reduction of the added metal ions which have moved from the positive electrode electrolyte to a circulating pathway of the negative electrode electrolyte, are contained in the circulating pathway of the negative electrode electrolyte, the metal precipitates are dissolved and ionized in the positive electrode electrolyte. 2. The method of operating a redox flow battery according to claim 1 , wherein, in the dissolution step, when the metal precipitates are precipitated on the negative electrode, the metal precipitates precipitated on the negative electrode are dissolved by supplying the positive electrode electrolyte at the end of charging to the negative electrode. 3. The method of operating a redox flow battery according to claim 2 , further comprising: before the dissolution step, a mixing step in which, at the end of discharging, the positive electrode electrolyte in the positive electrode tank and the negative electrode electrolyte in the negative electrode tank are mixed to form a mixed solution; and a charging step in which the mixed solution is charged so that the added metal ions contained in the mixed solution in the negative electrode tank are precipitated on the negative electrode. 4. The method of operating a redox flow battery according to claim 1 , further comprising: a mixing step in which, when the state of charge is 50% or more, the positive electrode electrolyte in the positive electrode tank and the negative electrode electrolyte in the negative electrode tank are mixed to form a mixed solution; and a charging step in which the mixed solution is charged so that the added metal ions contained in the mixed solution in the negative electrode tank are precipitated and the metal precipitates are made to be present in the negative electrode tank, wherein the dissolution step includes switching between the negative electrode tank that stores the mixed solution containing the metal precipitates and the positive electrode tank, and charging the mixed solution in the exchanged positive electrode tank. 5. The method of operating a redox flow battery according to claim 4 , wherein the mixing step and the charging step are repeated a plurality of times. 6. The method of operating a redox flow battery according to claim 1 , further comprising a collection step in which the metal precipitates are collected by a filter portion provided in the circulating pathway of the negative electrode electrolyte, wherein, in the dissolution step, the collected metal precipitates are dissolved in the positive electrode electrolyte. 7. A redox flow battery system comprising a battery cell including a positive electrode, a negative electrode, and a membrane interposed between the two electrodes, a positive electrode tank that stores a positive electrode electrolyte to be circulated and supplied to the positive electrode, and a negative electrode tank that stores a negative electrode electrolyte to be circulated and supplied to the negative electrode, wherein the positive electrode electrolyte contains manganese ions and added metal ions; the negative electrode electrolyte contains at least one species of metal ions selected from the group consisting of titanium ions, vanadium ions, and chromium ions; and the added metal ions are at least one selected from the group consisting of cadmium ions, tin ions, antimony ions, lead ions, and bismuth ions, the redox flow battery system comprising: a detecting portion that detects the existence of metal precipitates formed by reduction of the added metal ions which have moved from the positive electrode electrolyte to a circulating pathway of the negative electrode electrolyte; and a branching introducing pipe that supplies the positive electrode electrolyte from the positive electrode tank to the negative electrode when the metal precipitates are contained in the circulating pathway of the negative electrode electrolyte, and a branching return pipe that returns the solution which has passed through the negative electrode to the positive electrode tank. 8. The redox flow battery system according to claim 7 , wherein the detecting portion includes at least one selected from an SOC measuring unit capable of measuring the state of charge of the positive electrode electrolyte and the state of charge of the negative electrode electrolyte, a transparent window provided in the circulating pathway of the negative electrode electrolyte, and a flow meter provided in the circulating pathway of the negative electrode electrolyte. 9. The redox flow battery system according to claim 7 , wherein the positive electrode electrolyte and the negative electrode electrolyte both contain manganese ions and titanium ions. 10. The redox flow battery system according to claim 7 , wherein the concentration of the added metal ions in the positive electrode electrolyte is 0.001 to 1 M. 11. The redox flow battery system according to claim 7 , wherein at least one of the concentration of the manganese ions in the positive electrode electrolyte and the concentration of the metal ions in the negative electrode electrolyte is 0.3 to 5 M. 12. A redox flow battery system comprising a battery cell including a positive electrode, a negative electrode, and a membrane interposed between the two electrodes, a positive electrode tank that stores a positive electrode electrolyte to be circulated and supplied to the positive electrode, and a negative electrode tank that stores a negative electrode electrolyte to be circulated and supplied to the negative electrode, wherein the positive electrode electrolyte contains manganese ions and added metal ions; the negative electrode electrolyte contains at least one species of metal ions selected from the group consisting of titanium ions, vanadium ions, and chromium ions; and the added metal ions are at least one selected from the group consisting of cadmium ions, tin ions, antimony ions, lead ions, and bismuth ions, the redox flow battery system comprising: a detecting portion that detects the existence of metal precipitates formed by reduction of the added metal ions which have moved from the positive electrode electrolyte to a circulating pathway of the negative electrode electrolyte; and a communicating pipe that allows the positive electrode tank and the negative electrode tank to communicate with each other, enabling mixing of the positive electrode electrolyte and the negative electrode electrolyte, when the metal precipitates are contained in the circulating pathway of the negative electrode electrolyte; a branching introducing pipe that supplies the mixed solution stored in the positive electrode tank to the negative electrode; and a branching return pipe that returns the solution which has passed through the negative electrode to the positive electrode tank. 13. A redox flow bat

Assignees

Inventors

Classifications

  • of liquid-charged or electrolyte-charged reactants · CPC title

  • Fuel cells with aqueous electrolytes · CPC title

  • H01M8/188Primary

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

  • Electricity · mapped topic

  • with external circulating path · CPC title

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What does patent US10199672B2 cover?
Provided is a method of operating an RF battery in which charging and discharging are performed by circulating and supplying a positive electrode electrolyte in a positive electrode tank to a positive electrode and circulating and supplying a negative electrode electrolyte in a negative electrode tank to a negative electrode. The positive electrode electrolyte contains manganese ions and added …
Who is the assignee on this patent?
Sumitomo Electric Industries
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 Feb 05 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 5 related publications on this page (citations in our corpus or others sharing the same primary CPC).