REDOX FLOW SECONDARY BATTERY AND ELECTROLYTE MEMBRANE FOR REDOX FLOW SECONDARY BATTERY
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.
1 - 10 . (canceled)
11 . 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.
12 . The redox flow secondary battery according to claim 11 , 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.
13 . The redox flow secondary battery according to claim 11 , wherein the positive electrode electrolyte solution and the negative electrode electrolyte solution are sulfuric acid electrolyte solutions comprising vanadium.
14 . The redox flow secondary battery according to claim 11 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.
15 . The redox flow secondary battery according to claim 12 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.
16 . The redox flow secondary battery according to claim 11 , 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.
17 . The redox flow secondary battery according to claim 12 , 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.
18 . An electrolyte membrane for a redox flow secondary battery, comprising 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.
19 . The electrolyte membrane for the redox flow secondary battery according to claim 18 , 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.
20 . The electrolyte membrane for the redox flow secondary battery according to claim 18 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.
21 . The electrolyte membrane for the redox flow secondary battery according to claim 19 , wherein the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.
22 . The electrolyte membrane for the redox flow secondary battery according to claim 18 , 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.
23 . The electrolyte membrane for the redox flow secondary battery according to claim 19 , 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.
24 . The electrolyte membrane for the redox flow secondary battery according to claim 20 , 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.
25 . The electrolyte membrane for the redox flow secondary battery according to claim 18 , wherein the ion-exchange resin composition has been subjected to a heat treatment at 130 to 200° C. for 1 to 60 min.
26 . The electrolyte membrane for the redox flow secondary battery according to claim 19 , wherein the ion-exchange resin composition has been subjected to a heat treatment at 130 to 200° C. for 1 to 60 min.
27 . The electrolyte membrane for the redox flow secondary battery according to claim 20 , wherein the ion-exchange resin composition has been subjected to a heat treatment at 130 to 200° C. for 1 to 60 min.
28 . The electrolyte membrane for the redox flow secondary battery according to claim 22 , wherein the ion-exchange resin composition has been subjected to a heat treatment at 130 to 200° C. for 1 to 60 min.