Electrolyte membrane for redox flow battery, redox flow battery, and method for producing electrolyte membrane

Patent metadata

Field	Value
Publication number	US-11876267-B2
Application number	US-202017436466-A
Country	US
Kind code	B2
Filing date	Mar 6, 2020
Priority date	Mar 8, 2019
Publication date	Jan 16, 2024
Grant date	Jan 16, 2024

Abstract

The present invention provides an electrolyte membrane for a redox flow battery, comprising a perfluorocarbon polymer having an ion-exchange group, wherein the perfluorocarbon polymer has equivalent weight EW of the ion-exchange group of 600 g/eq or more and 2000 g/eq or less, a craze area ratio of the electrolyte membrane is 1.5% or less, and a relative dimension of the electrolyte membrane in at least one of a X direction and a Y direction is 80% or more and less than 100% in the following relative dimension by dipping in 2 M aqueous sulfuric acid solution.

First claim

The invention claimed is:

1. An electrolyte membrane for a redox flow battery, comprising a perfluorocarbon polymer having an ion-exchange group, wherein
the perfluorocarbon polymer has equivalent weight EW of the ion-exchange group of 600 g/eq or more and 2000 g/eq or less,
a craze area ratio of the electrolyte membrane is 1.5% or less, and
a relative dimension of the electrolyte membrane in at least one of a X direction and a Y direction is 80% or more and less than 100% in the following relative dimension by dipping in 2 M aqueous sulfuric acid solution:

<relative dimension by dipping in 2 M aqueous sulfuric acid solution>
an electrolyte membrane for testing having a water content of 1 % or less is prepared; the electrolyte membrane for testing is dipped in a 2 M aqueous sulfuric acid solution at 25° C. for 30 minutes; and ratios of change in dimension in a X direction on a surface of the electrolyte membrane for testing and a Y direction orthogonal to the X direction are calculated according to the following expression:
Relative dimension (%)={(Dimension in a specific direction after the dipping)/(Dimension in the specific direction before the dipping)}×100.

2. An electrolyte membrane for a redox flow battery, comprising a perfluorocarbon polymer having an ion-exchange group, wherein
the perfluorocarbon polymer has equivalent weight EW of the ion-exchange group of 600 g/eq or more and 2000 g/eq or less,
a craze area ratio of the electrolyte membrane is 1.5% or less, and
a relative dimension of the electrolyte membrane in at least one of a X direction and a Y direction is 80% or more and less than 100%, and a relative dimension thereof in a Z direction is 115% or more, in the following relative dimension by dipping in distilled water:

<relative dimension by dipping in distilled water>
an electrolyte membrane for testing having a water content of 1% or less is prepared; the electrolyte membrane for testing is dipped in distilled water at 25° C. for 30 minutes; and ratios of change in dimension in a X direction on a surface of the electrolyte membrane for testing, a Y direction orthogonal to the X direction, and a Z direction orthogonal to the X direction and the Y direction are calculated:
Relative dimension (%)={(Dimension in a specific direction after the dipping)/(Dimension in the specific direction before the dipping)}×100.

3. The electrolyte membrane according to claim 2 , wherein the perfluorocarbon polymer has a structure represented by the following formula (1):
—[CF 2 —CX 1 X 2 ] a —[CF 2 —CF(—O—(CF 2 —CF(CF 2 X 3 )) b —O c —(CFR 1 ) d —(CFR 2 ) e —(CF 2 ) f —X 4 )] g —  (1)

wherein X 1 , X 2 and X 3 are each independently a halogen atom or a perfluoroalkyl group having 1 to 3 carbon atoms; X 4 is a —COOZ group, a —SO 3 Z group, a —PO 3 Z 2 group or a —PO 3 HZ group; Z is a hydrogen atom, an alkali metal atom, an alkaline earth metal atom, NH 4 , NH 3 R 11 , NH 2 R 11 R 12 , NHR 11 R 12 R 13 , or NR 11 R 12 R 13 R 14 ; R 11 , R 12 , R 13 , and R 14 are each independently an alkyl group or an aryl group; R 1 and R 2 are each independently a halogen atom, a perfluoroalkyl group having 1 to 10 carbon atoms or a fluorochloroalkyl group having 1 to 10 carbon atoms; a and g are numbers satisfying 0≤a<1, 0<g≤1, and a+g=1; b is an integer of 0 to 8; c is 0 or 1; and d, e and f are each independently an integer of 0 to 6 provided that d, e and f are not 0 at the same time.

4. The electrolyte membrane according to claim 2 , wherein the perfluorocarbon polymer has a structure represented by the following formula (2):
[CF 2 CF 2 ] a —[CF 2 —CF(—O—(CF 2 ) m —SO 3 H)] g —  (2)

wherein a and g are numbers satisfying 0≤a<1, 0<g≤1, and a+g=1; and m is an integer of 1 to 6.

5. The electrolyte membrane according to claim 2 , wherein an ion cluster size of the electrolyte membrane in a direction perpendicular to a membrane surface measured by small-angle X-ray scattering is 3.0 nm or larger.

6. The electrolyte membrane according to claim 2 , wherein peak intensity of a long period of crystals measured by small-angle X-ray scattering in the electrolyte membrane is 0.5 or less.

7. The electrolyte membrane according to claim 2 , wherein at least one surface of the electrolyte membrane is covered with an anion-exchange compound.

8. The electrolyte membrane according to claim 7 , wherein the anion-exchange compound has a tertiary amino group or a quaternary ammonium group.

9. A redox flow battery comprising an electrolyzer, the electrolyzer comprising: a positive electrode cell chamber comprising a positive electrode consisting of a carbon electrode; a negative electrode cell chamber comprising a negative electrode consisting of a carbon electrode; and an electrolyte membrane as a membrane that separates the positive electrode cell chamber and the negative electrode cell chamber, wherein
the positive electrode cell chamber comprises a positive electrode electrolyte solution comprising an active material,
the negative electrode cell chamber comprises a negative electrode electrolyte solution comprising an active material, and
the electrolyte membrane is an electrolyte membrane according to any one of claim 2 .

10. The redox flow battery according to claim 9 , wherein the positive electrode electrolyte solution and the negative electrode electrolyte solution comprise a vanadium ion.

11. The redox flow battery according to claim 9 ,
wherein
the carbon electrode has a continuous void,
the carbon electrode has fibrous carbon, and
the fibrous carbon has an average fiber diameter of 0.1 to 5.0 μm.

12. The redox flow battery according to claim 11 , wherein the carbon electrode has a three-dimensionally continuous carbon structure.

13. The redox flow battery according to claim 11 , wherein the carbon electrode is a carbon foam having linear portions and node portions connecting the linear portions.

14. The redox flow battery according to claim 13 , wherein the ratio of the number of the linear portions to the number of the node portions in the carbon foam is 1.2 or more and 1.7 or less.

15. The redox flow battery according to claim 13 , wherein a density of the node portions in at least a portion of the carbon foam is 15,000 portions/mm 3 or more.

16. A method for producing an electrolyte membrane for a redox flow battery, comprising:
drawing a raw material membrane containing a perfluorocarbon polymer having an ion-exchange group under heating, wherein
the perfluorocarbon polymer has equivalent weight EW of the ion-exchange group of 600 g/eq or more and 2000 g/eq or less,
a craze area ratio of the electrolyte membrane is 1.5% or less, and
a relative dimension of the electrolyte membrane in at least one of a X direction and a Y direction is 80% or more and less than 100%, and a relative dimension thereof in a Z direction is 115% or more, in the following relative dimension by dipping in distilled water:

<relative dimension by dipping in distilled water>
an electrolyte membrane for testing having a water content of 1% or less is prepared; the electrolyte membrane for testing is dipped in distilled water at 25° C. for 30 minutes; and ratios of change in dimension in a X direction on a surface of the electrolyte membrane for testing, a Y direction orthogonal to the X direction, and a Z direction orthogonal to the X direction and the Y direction are calculated:
Relative dimension (%)={(Dimension in a specific direction after the dipping)/(Dimension in the specific direction before the dipping)}×100.

17.

Assignees

• Asahi Chemical Ind

Inventors

• Kanada Yuka
• Yamashita Junya
• Kamochi Hiroko
• Kai Kazuya

Classifications

• H01M8/1025 Primary

  having only carbon and oxygen, e.g. polyethers, sulfonated polyetheretherketones [S-PEEK], sulfonated polysaccharides, sulfonated celluloses or sulfonated polyesters · CPC title

• H01M4/96

  Carbon-based electrodes · CPC title

• H01M8/109

  thermal other than drying, e.g. sintering · CPC title

• H01M8/1039

  halogenated, e.g. sulfonated polyvinylidene fluorides · CPC title

• H01M8/1067

  characterised by their physical properties, e.g. porosity, ionic conductivity or thickness · CPC title