Composite ion-exchange membranes for flow batteries
US-2024387848-A1 · Nov 21, 2024 · US
US2017271698A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017271698-A1 |
| Application number | US-201715617676-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 8, 2017 |
| Priority date | Dec 28, 2011 |
| Publication date | Sep 21, 2017 |
| Grant date | — |
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The problem addressed by the present invention is to obtain an electrolyte membrane that, as an electrolyte membrane for a redox flow secondary battery, is able to suppress the ion permeability of an active substance without detracting from proton (H+) permeability, has superior ion-selective permeability, has low electrical resistivity, and has superior current efficiency. The present invention solves the abovementioned problem by means of the electrolyte membrane for a redox flow secondary battery containing a perfluorocarbon sulfonic acid resin having a specific structure and an equivalent weight (EW), and the ion conductivity being adjusted to a predetermined range.
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1 . A redox flow secondary battery comprising an electrolytic bath comprising: a positive electrode cell chamber comprising a positive electrode composed of a carbon electrode; a negative electrode cell chamber comprising a negative electrode composed of a carbon electrode; and an electrolyte membrane as a diaphragm to separate the positive electrode cell chamber and the negative electrode cell chamber, wherein the positive electrode cell chamber comprises a positive electrode electrolyte solution comprising a positive electrode active substance; and the negative electrode cell chamber comprises a negative electrode electrolyte solution comprising a negative electrode active substance; wherein the redox flow secondary battery charges and discharges based on changes in valences of the positive electrode active substance and the negative electrode active substance in the electrolyte solutions; wherein the electrolyte membrane comprises an ion-exchange resin composition comprising a perfluorocarbonsulfonic acid resin having a structure represented by the following formula (1): —[CF 2 —CF 2 ] a —[CF 2 —CF(—O—(CF 2 ) m —SO 3 H)] g — (1) wherein a and g represent numbers satisfying 0≦a<1, 0<g≦1, and a+g=1; and m represents an integer of 1 to 6; wherein the perfluorocarbonsulfonic acid resin has an equivalent weight EW (a dry mass in grams per equivalent of ion-exchange groups) of 250 to 1,500 g/eq; and wherein the electrolyte membrane has an ionic conductivity at 110° C. at a relative humidity of 50% RH of 0.05 S/cm or higher, and wherein the electrolyte membrane does not comprise a reinforcing material. 2 . The redox flow secondary battery according to claim 1 , wherein the perfluorocarbonsulfonic acid resin has an equivalent weight EW (a dry mass in grams per equivalent of ion-exchange groups) of 250 to 700 g/eq. 3 . The redox flow secondary battery according to claim 1 , wherein the positive electrode electrolyte solution and the negative electrode electrolyte solution are sulfuric acid electrolyte solutions comprising vanadium. 4 . The redox flow secondary battery according to claim 1 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass. 5 . The redox flow secondary battery according to claim 2 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass. 6 . The redox flow secondary battery according to claim 1 , wherein the ion-exchange resin composition comprises 0.1 to 20 parts by mass of a polyphenylene ether resin and/or a polyphenylene sulfide resin with respect to 100 parts by mass of the perfluorocarbonsulfonic acid resin. 7 . The redox flow secondary battery according to claim 2 , wherein the ion-exchange resin composition comprises 0.1 to 20 parts by mass of a polyphenylene ether resin and/or a polyphenylene sulfide resin with respect to 100 parts by mass of the perfluorocarbonsulfonic acid resin.
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