IP Library Granted Patent US 9,509,011
Granted Patent B2
US 9,509,011 · App. 14/199,794 · Granted Nov 29, 2016

Method and system for rebalancing electrolytes in a redox flow battery system

Inventors: Craig E. Evans (Portland, OR); Yang Song (Portland, OR)
Assignee: ESS Tech, Inc.
H01M8/188Y02E60/528
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Quick Facts
Patent No.
US 9,509,011
App. No.
14/199,794
Granted
Nov 29, 2016
Kind
B2
Abstract

A method of rebalancing electrolytes in a redox flow battery system comprises directing hydrogen gas generated on the negative side of the redox flow battery system to a catalyst surface, and fluidly contacting the hydrogen gas with an electrolyte comprising a metal ion at the catalyst surface, wherein the metal ion is chemically reduced by the hydrogen gas at the catalyst surface, and a state of charge of the electrolyte and pH of the electrolyte remain substantially balanced.

Claims (31)

1. A method of rebalancing electrolytes in a redox flow battery system, comprising:

directing hydrogen gas in the redox flow battery system to a catalyst surface;

fluidly contacting the hydrogen gas with an electrolyte comprising a metal ion at the catalyst surface; and

chemically reducing the metal ion by the hydrogen gas at the catalyst surface, while a state of charge of the electrolyte remains substantially balanced, or a pH of the electrolyte remains within a predetermined range.

2. The method of claim 1 , further comprising measuring a pH of the electrolyte and supplying hydrogen from an external source in response to a change in the pH of the electrolyte.

3. The method of claim 1 , further comprising measuring a state of charge of the electrolyte and supplying hydrogen from an external source in response to a change in the state of charge of the electrolyte.

4. The method of claim 1 ,

wherein the redox flow battery system comprises an iron redox flow battery system, and the metal ion comprises ferric ion, ferric complexes, or a combination thereof.

5. The method of claim 1 , wherein the redox flow battery system comprises a positive electrode and a negative electrode, and wherein directing the hydrogen gas to the catalyst surface comprises directing the hydrogen gas to a catalyst bed in a trickle bed reactor placed in the flow path of positive and negative electrolyte, and wherein fluidly contacting the hydrogen gas with the electrolyte at the catalyst surface comprises fluidly contacting the hydrogen gas with the electrolyte at the catalyst bed of the trickle bed reactor.

6. The method of claim 1 , wherein the redox flow battery system comprises a positive electrode and a negative electrode, and wherein directing the hydrogen gas to the catalyst surface comprises directing the hydrogen gas to a catalyst layer positioned at an electrically insulating ion conducting surface separating the positive electrode and the negative electrode.

7. A method of operating a redox flow battery system, comprising:

recirculating a positive electrolyte to a positive electrode;

recirculating a negative electrolyte to a negative electrode;

directing hydrogen gas to a first catalyst surface;

directing the positive electrolyte to the first catalyst surface; and

fluidly contacting the hydrogen gas with the positive electrolyte at the first catalyst surface, wherein

the positive electrolyte is chemically reduced by the hydrogen gas at the first catalyst surface;

a positive electrolyte pH is maintained within a first range; and

a state of charge of the positive electrolyte and a state of charge of the negative electrolyte remain substantially constant.

8. The method of operating the redox flow battery system of claim 7 , further comprising;

measuring the positive electrolyte pH;

measuring the negative electrolyte pH; and

supplying hydrogen gas from an external source to the redox flow battery system in response to at least one of a change in the positive electrolyte pH and the negative electrolyte pH.

9. The method of operating the redox flow battery system of claim 7 , wherein directing hydrogen gas to a first catalyst surface comprises directing the hydrogen gas to a first catalyst bed in a first trickle bed reactor, and wherein fluidly contacting the hydrogen gas with the positive electrolyte at the first catalyst surface comprises fluidly contacting the hydrogen gas with the positive electrolyte at the first catalyst bed in the first trickle bed reactor.

10. The method of operating the redox flow battery system of claim 8 , further comprising:

directing hydrogen gas to a second catalyst bed in a second trickle bed reactor;

directing the negative electrolyte to the second catalyst bed; and

fluidly contacting the hydrogen gas with the negative electrolyte at the second catalyst bed;

wherein

the negative electrolyte is chemically reduced by the hydrogen gas at the second catalyst surface, and

a negative electrolyte pH is maintained within a second range.

Assignments (6)
CONFIRMATORY LICENSE Recorded Oct 2, 2024
From: ESS TECH., INC.
To: US DEPARTMENT OF ENERGY
Reel/Frame 069105/0467 →
RELEASE OF SECURITY INTEREST Recorded Sep 17, 2019
From: SILICON VALLEY BANK
To: ESS TECH, INC.
Reel/Frame 050407/0752 →
CONFIRMATORY LICENSE Recorded Jan 8, 2019
From: ESS TECHNOLOGY INC.
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 048025/0201 →
SECURITY INTEREST Recorded Jul 11, 2018
From: ESS TECH, INC.
To: SILICON VALLEY BANK
Reel/Frame 047816/0520 →
CHANGE OF NAME Recorded Jul 18, 2016
From: ENERGY STORAGE SYSTEMS, INC.
To: ESS TECH, INC.
Reel/Frame 039383/0433 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 12, 2014
From: EVANS, CRAIG E.; SONG, YANG
To: ENERGY STORAGE SYSTEMS, INC.
Reel/Frame 032415/0912 →
Continuity (2)
Provisional Application 61832671 · Jun 7, 2013
Related Publication 20140363747A1 · Dec 11, 2014