IP Library Granted Patent US 9,905,875
Granted Patent B2
US 9,905,875 · App. 14/368,086 · Granted Feb 27, 2018

Redox flow secondary battery and electrolyte membrane for redox flow secondary battery

Inventors: Akihiro Kato (Tokyo, JP); Naoto Miyake (Tokyo, JP)
Assignee: ASAHI KASEI KABUSHIKI KAISHA
H01M8/188C08J5/2287C08L27/18H01B1/122H01M8/0239H01M8/0241H01M8/0289H01M8/0293H01M8/1023H01M8/1039H01M8/1058H01M8/20C08J2327/18H01M2300/0082Y02E60/528
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Quick Facts
Patent No.
US 9,905,875
App. No.
14/368,086
Granted
Feb 27, 2018
Kind
B2
Abstract

This redox flow secondary battery has an electrolyte tank ( 6 ) containing: a positive electrode cell chamber ( 2 ) containing a positive electrode ( 1 ) comprising a carbon electrode; a negative electrode cell chamber ( 4 ) containing a negative electrode ( 3 ) comprising a carbon electrode; and an electrolyte membrane ( 5 ) as a barrier membrane that separates/isolates the positive electrode cell chamber ( 2 ) and the negative electrode cell chamber ( 4 ). The positive electrode cell chamber ( 2 ) contains a positive electrode electrolyte containing an active substance, the negative electrode cell chamber ( 4 ) contains a negative electrode electrolyte containing an active substance, and the redox flow secondary battery charges and discharges on the basis of the change in valency of the active substances in the electrolytes. The electrolyte membrane ( 5 ) contains an ion exchange resin composition that is primarily a polyelectrolyte polymer, and the electrolyte membrane ( 5 ) has a reinforcing material comprising a fluorine-based porous membrane.

Claims (27)

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 an active substance; and the negative electrode cell chamber comprises a negative electrode electrolyte solution comprising an active substance;

wherein the redox flow secondary battery charges and discharges based on changes in valences of the active substances in the electrolyte solutions;

wherein the electrolyte membrane comprises an ion-exchange resin composition comprising a polyelectrolyte polymer as a main component;

wherein the polyelectrolyte polymer is a perfluorocarbonsulfonic acid resin (PFSA) being a fluorine-based polyelectrolyte polymer having a structure represented by the following formula (2):

—[CF 2 CF 2 ] a —[CF 2 —CF (—O—(CF 2 ) m —X 4 )] g —  (2)

wherein a and g represent numbers satisfying 0≦a<1, 0<g≦1, and a+g=1; m represents an integer of 1 to 6; and X 4 represents SO 3 H; and

wherein the electrolyte membrane has a reinforcing material composed of at least one of a fluorine-based microporous membrane, a fluorine-based nonwoven fabric, and a fluorine-based woven fabric, wherein the reinforcing material has a structure in which the reinforcing material is impregnated with the polyelectrolyte polymer and the reinforcing material is impregnated at a rate of 95% or higher.

2. The redox flow secondary battery according to claim 1 , wherein an internal volume of the reinforcing material is substantially occluded.

3. The redox flow secondary battery according to claim 1 , wherein the redox flow secondary battery is a vanadium-type redox flow secondary battery using sulfuric acid electrolyte solutions comprising vanadium as the positive electrode electrolyte solution and the negative electrode electrolyte solution.

4. The redox flow secondary battery according to claim 1 , wherein the polyelectrolyte polymer has an equivalent weight EW (dry mass in grams per equivalent of ion-exchange groups) of 300 to 1,300 g/eq; and the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.

5. 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 polyelectrolyte polymer.

6. An electrolyte membrane for a redox flow secondary battery, comprising:

an ion-exchange resin composition comprising:

a polyelectrolyte polymer as a main component,

wherein the polyelectrolyte polymer is a perfluorocarbonsulfonic acid resin (PFSA) being a fluorine-based polyelectrolyte polymer having a structure represented by the following formula (2):

—[CF 2 CF 2 ] a —[CF 2 —CF (—O—(CF 2 ) m —X 4 )] g —  (2)

wherein a and g represent numbers satisfying 0≦a<1, 0<g≦1, and a+g=1; m represents an integer of 1 to 6; and X 4 represents SO 3 H, and

having a reinforcing material composed of at least one of a fluorine-based nonwoven fabric, a fluorine-based microporous membrane, and a fluorine-based woven fabric, wherein the reinforcing material has a structure in which the reinforcing material is impregnated with the polyelectrolyte polymer and the reinforcing material is impregnated at a rate of 95% or higher.

7. The electrolyte membrane for the redox flow secondary battery according to claim 6 , wherein an internal volume of the reinforcing material for the redox flow secondary battery is substantially occluded.

8. The electrolyte membrane for the redox flow secondary battery according to claim 6 , wherein the polyelectrolyte polymer has an equivalent weight EW (dry mass in grams per equivalent of ion-exchange groups) of 300 to 1,300 g/eq; and the electrolyte membrane has an equilibrium moisture content of 5 to 80% by mass.

9. The electrolyte membrane for the redox flow secondary battery according to claim 6 , 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 polyelectrolyte polymer.

10. The electrolyte membrane for the redox flow secondary battery according to claim 6 , wherein the electrolyte membrane for the redox flow secondary battery is subjected to a heat treatment at 130 to 200° C. for 1 to 60 min.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE CONVEYING PARTIES NAMES PREVIOUSLY RECORDED AT REEL: 038895 FRAME: 0337. ASSIGNOR(S) HEREBY CONFIRMS THE MERGER. Recorded Jun 21, 2016
From: ASAHI KASEI FIBERS CORPORATION; ASAHI KASEI CHEMICALS CORPORATION; ASAHI KASEI E-MATERIALS CORPORATION
To: ASAHI KASEI KABUSHIKI KAISHA
Reel/Frame 039097/0503 →
MERGER Recorded Jun 13, 2016
From: ASAHI KASEI E-MATERIALS CORPORATION
To: ASAHI KASEI KABUSHIKI KAISHA
Reel/Frame 038895/0337 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 22, 2014
From: KATO, AKIHIRO; MIYAKE, NAOTO
To: ASAHI KASEI E-MATERIALS CORPORATION
Reel/Frame 033785/0519 →
Priority Claims (2)
JP 2011-290020 · Dec 28, 2011 · national
JP 2012-010454 · Jan 20, 2012 · national
Continuity (1)
Related Publication 20140370404A1 · Dec 18, 2014