Redox flow battery
US-2016013506-A1 · Jan 14, 2016 · US
US10826100B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10826100-B2 |
| Application number | US-201615536867-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 7, 2016 |
| Priority date | Apr 8, 2015 |
| Publication date | Nov 3, 2020 |
| Grant date | Nov 3, 2020 |
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The present specification relates to a polymer electrolyte membrane, an electrochemical battery including the polymer electrolyte membrane, an electrochemical battery module including the electrochemical battery, a flow battery including the polymer electrolyte membrane, a method for manufacturing a polymer electrolyte membrane, and an electrolyte solution for a flow battery.
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The invention claimed is: 1. A polymer electrolyte membrane comprising: an ion conductive polymer having a thickness, wherein a cross-over prevention layer is present inside the ion conductive polymer at 10% or more and 90% or less of the thickness of the ion conductive polymer, wherein the cross-over prevention layer has a thickness of 1 μm or more and 100 μm or less; wherein the cross-over prevention layer comprises a nitrate of a cationic metal, wherein the cationic metal comprises at least one of tin (Sn), lead (Pb), mercury (Hg), and silver (Ag). 2. The polymer electrolyte membrane of claim 1 , wherein the cross-over prevention layer is parallel to a surface perpendicular to a thickness direction of the polymer electrolyte membrane. 3. An electrochemical battery comprising: a first electrode; a second electrode; and the polymer electrolyte membrane according to claim 1 provided between the first electrode and the second electrode. 4. The electrochemical battery of claim 3 , wherein a cross-over prevention layer of the polymer electrolyte membrane comprises a cationic metal, and the cationic metal comprises a metal having a standard electrode potential which ranges from a lower standard electrode potential of standard electrode potentials of the first and second electrodes to a higher standard electrode potential of standard electrode potentials of the first and second electrodes. 5. An electrochemical battery module comprising the electrochemical battery of claim 3 as a unit cell. 6. A flow battery comprising: a first electrode which a first electrolyte solution comprising a first electrode active material is capable of being injected into and discharged from; a second electrode which a second electrolyte solution comprising a second electrode active material is capable of being injected into and discharged from; and the polymer electrolyte membrane according to claim 1 which is disposed between the first electrode and the second electrode. 7. The flow battery of claim 6 , wherein at least one of the second electrolyte solution and the first electrolyte solution comprises a cationic metal salt. 8. The flow battery of claim 7 , wherein the cationic metal salt comprises at least one of a nitrate of molybdenum (Mo), tin (Sn), lead (Pb), copper (Cu), mercury (Hg), silver (Ag), or palladium (Pd); a chloride salt of molybdenum (Mo), tin (Sn), lead (Pb), copper (Cu), mercury (Hg), silver (Ag), or palladium (Pd); a sulfide salt of molybdenum (Mo), tin (Sn), lead (Pb), copper (Cu), mercury (Hg), silver (Ag), or palladium (Pd); a sulfate of molybdenum (Mo), tin (Sn), lead (Pb), copper (Cu), mercury (Hg), silver (Ag), or palladium (Pd); and a carbonate of molybdenum (Mo), tin (Sn), lead (Pb), copper (Cu), mercury (Hg), silver (Ag), or palladium (Pd). 9. The flow battery of claim 6 , wherein the first electrode and the second electrode each comprise a carbon felt or a carbon felt comprising a cationic inorganic salt on a surface thereof. 10. The flow battery of claim 9 , wherein when a cationic inorganic salt is provided on a surface of the first electrode carbon felt, a content of the cationic inorganic salt is 0.01 wt % or more and 10 wt % or less based on a weight of the first electrode carbon felt, and when a cationic inorganic salt is provided on a surface of the second electrode carbon felt, a content of the cationic inorganic salt is 0.01 wt % or more and 10 wt % or less based on a weight of the second electrode carbon felt. 11. A method for manufacturing a polymer electrolyte membrane, the method comprising: installing an electrochemical battery comprising a first electrode, a second electrode, and a polymer electrolyte membrane provided between the first electrode and the second electrode; injecting a first electrolyte solution comprising a first electrode active material into a side of the first electrode and injecting a second electrolyte solution comprising a second electrode active material into a side of the second electrode, wherein at least one of the first electrolyte solution and the second electrolyte solution comprises metal cations; and manufacturing a polymer electrolyte membrane comprising a cross-over prevention layer formed therein, by operating the electrochemical battery to allow the metal cations to permeate into the polymer electrolyte membrane, wherein the polymer electrolyte membrane comprises: an ion conductive polymer having a thickness, wherein a cross-over prevention layer is present inside the ion conductive polymer at 10% or more and 90% or less of the thickness of the ion conductive polymer, wherein the cross-over prevention layer has a thickness of 1 μm or more and 100 μm or less, wherein the cross-over prevention layer comprises a nitrate of a cationic metal, wherein the cationic metal comprises at least one of tin (Sn), lead (Pb), mercury (Hg), and silver (Ag). 12. The method of claim 11 , wherein the metal cation comprises a metal having a standard electrode potential which ranges from a lower standard electrode potential of standard electrode potentials of the first and second electrodes to a higher standard electrode potential of standard electrode potentials of the first and second electrodes. 13. The method of claim 11 , wherein the metal cation comprises at least one of a cation of molybdenum (Mo), a cation of tin (Sn), a cation of lead (Pb), a cation of copper (Cu), a cation of mercury (Hg), a cation of silver (Ag), and a cation of palladium (Pd). 14. The method of claim 11 , further comprising: operating an electrochemical battery comprising a polymer electrolyte membrane comprising a cross-over prevention layer formed therein immediately after the manufacturing of the polymer electrolyte membrane comprising the cross-over prevention layer formed therein. 15. The method of claim 11 , wherein the electrochemical battery is a flow battery in which a first electrolyte comprising a first electrode active material is injected into and discharged from the first electrode and a second electrolyte comprising a second electrode active material is injected into and discharged from the second electrode. 16. A method for manufacturing a polymer electrolyte membrane, the method comprising: impregnating a polymer electrolyte membrane with a solution comprising metal cations; installing an electrochemical battery comprising a first electrode, a second electrode, and the polymer electrolyte membrane provided between the first electrode and the second electrode; and manufacturing a polymer electrolyte membrane comprising a cross-over prevention layer formed therein by operating the electrochemical battery, wherein the polymer electrolyte membrane comprises: an ion conductive polymer having a thickness, wherein a cross-over prevention layer is present inside the ion conductive polymer at 10% or more and 90% or less of the thickness of the ion conductive polymer, wherein the cross-over prevention layer has a thickness of 1 μm or more and 100 μm or less, wherein the cross-over prevention layer comprises a nitrate of a cationic metal, wherein the cationic metal comprises at least one of tin (Sn), lead (Pb), mercury (Hg), and silver (Ag).
comprising ion-exchange membranes in or on which electrode material is embedded · CPC title
Ion-conducting additives, e.g. ion-conducting particles, heteropolyacids, metal phosphate or polybenzimidazole with phosphoric acid · CPC title
characterised by their physical properties, e.g. porosity, ionic conductivity or thickness · CPC title
in the form of layered or coated products · CPC title
Inorganic layers on the polymer electrolytes, e.g. inorganic coatings · CPC title
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