Ion exchange separation membrane, electrochemical cell including same, flow cell and fuel cell, and manufacturing method thereof
US-2019321814-A1 · Oct 24, 2019 · US
US12021284B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12021284-B2 |
| Application number | US-202016865576-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 4, 2020 |
| Priority date | Nov 6, 2017 |
| Publication date | Jun 25, 2024 |
| Grant date | Jun 25, 2024 |
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The present invention provides an ion exchange membrane can improve the current efficiency of a redox flow battery without a drop in voltage efficiency, when used in the redox flow battery. The ion exchange membrane of the present invention is an ion exchange membrane comprising a fluorinated polymer having sulfonic acid functional groups, wherein the difference (D−Dc) between the distance D between ionic clusters and the diameter Dc of ionic clusters as measured by the small angle X-ray scattering is 0.60 nm or more, and the ion exchange capacity of the fluorinated polymer is 0.95 meq/gram dry resin or more.
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What is claimed is: 1. A redox flow battery, comprising an ion exchange membrane comprising a fluorinated polymer having sulfonic acid functional groups, wherein a diameter Dc of ionic clusters is from 3.53 to 4.40 nm, the distance D between ionic clusters is from 4.25 to 5.00 nm, the difference (D-Dc) between the distance D between ionic clusters and the diameter De of ionic clusters as measured by small angle X-ray scattering is at least 0.60 nm, and the ion exchange capacity of the fluorinated polymer is at least 0.95 meq/g dry resin. 2. The redox flow battery according to claim 1 , wherein the difference (D−Dc) between the distance D between ionic clusters and the diameter De of ionic clusters is at least 0.70 nm. 3. The redox flow battery according to claim 1 , wherein the ion exchange capacity of the fluorinated polymer is from 1.00 to 1.10 meq/g dry resin. 4. The redox flow battery according to claim 1 , which is from 30 to 500 μm in thickness. 5. The redox flow battery according to claim 1 , wherein the fluorinated polymer comprises units based on a fluoroolefin and units based on a fluorine-containing monomer having a sulfonic acid functional group. 6. The redox flow battery according to claim 5 , wherein the units based on a fluoroolefin are based on tetrafluoroethylene. 7. The redox flow battery according to claim 5 , wherein the units based on a fluorine-containing monomer having a sulfonic acid functional group are represented by the formula (1): —[CF 2 —CF(-L-(SO 3 M) n )]— Formula (1): wherein L is a (n+1)-valent perfluorinated hydrocarbon group which may contain an oxygen atom, M is a hydrogen atom, an alkali metal or a quaternary ammonium cation, and n is 1 or 2. 8. The redox flow battery according to claim 7 , wherein the units represented by the formula (1) are units represented by the formula (1-4): —[CF 2 —CF 2 —(CF 2 ) x —(OCF 2 CFY) y —O—(CF 2 ) z —SO 3 M)]— Formula (1-4): wherein M is a hydrogen atom, an alkali metal or a quaternary ammonium cation, x is 0 or 1, y is an integer of 0 to 2, z is an integer of 1 to 4, and Y is F or CF 3 . 9. The redox flow battery according to claim 1 , which has a reinforcing material inside. 10. The redox flow battery according to claim 1 , wherein the ion exchange membrane does not contain a polymer other than the fluorinated polymer having sulfonic acid functional groups, and the fluorinated polymer having sulfonic acid functional groups consists of units based on a fluoroolefin and units based on a fluorine-containing monomer having a sulfonic acid functional group.
Fuel cells with polymeric electrolytes · CPC title
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes · CPC title
Homopolymers or copolymers of tetrafluoroethylene · CPC title
containing fluorine · CPC title
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