Fuel cell with segregated electrolyte distribution and method for making the same
US-2018331368-A1 · Nov 15, 2018 · US
US11462745B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11462745-B2 |
| Application number | US-202017114920-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 8, 2020 |
| Priority date | Dec 10, 2019 |
| Publication date | Oct 4, 2022 |
| Grant date | Oct 4, 2022 |
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The present disclosure relates to a fuel cell catalyst, a fuel cell electrode including the same, and a membrane-electrode assembly including the same. In one embodiment, the fuel cell catalyst includes: a support including a titanium oxynitride represented by the following Formula 1: TiO1-yNy, wherein 0.05<y<0.9; and an active material supported on the support.
Opening claim text (preview).
What is claimed is: 1. A fuel cell catalyst comprising: a support comprising a titanium oxynitride represented by the following Formula 1; and an active material supported on the support: TiO1-yNy [Formula 1] wherein 0.05<y<0.9, wherein the titanium oxynitride of Formula 1 is comprised in an amount of 2.4 to 20 wt % based on the total weight of the support. 2. The fuel cell catalyst of claim 1 , wherein the titanium oxynitride of Formula 1 is comprised in an amount of 2.5 to 19 wt % based on the total weight of the support. 3. The fuel cell catalyst of claim 1 , comprising 100 parts by weight of the support and 10 to 60 parts by weight of the active material. 4. The fuel cell catalyst of claim 1 , wherein the active material has an average size of 2 to 10 nm. 5. The fuel cell catalyst of claim 1 , wherein the support has a BET specific surface area of 20 to 50 m2/g and an electrical conductivity of 20 to 40 S/cm. 6. The fuel cell catalyst of claim 1 , wherein the support has an average pore size of 50 to 80 nm. 7. The fuel cell catalyst of claim 1 , wherein the support is prepared by a method comprising steps of: preparing an intermediate by heat-treating titanium dioxide (TiO2) to a temperature of 400 to 900° C. while introducing a nitrogen-containing gas thereto; and cooling the intermediate. 8. The fuel cell catalyst of claim 7 , wherein the heat- treating is performed by heating to a temperature of 400 to 900° C. at a heating rate of 1 to 15° C/second. 9. The fuel cell catalyst of claim 1 , wherein the active material includes one or more precious metals selected from among platinum (Pt), palladium (Pd), iridium (Ir) and ruthenium (Ru). 10. The fuel cell catalyst of claim 9 , wherein the active material further comprises one or more transition metals selected from among copper (Cu), cobalt (Co), nickel (Ni) and iron (Fe). 11. A fuel cell electrode comprising the fuel cell catalyst of claim 1 . 12. A membrane-electrode assembly comprising: a cathode; an anode; and an electrolyte membrane interposed between the cathode and the anode, wherein one or more of the cathode and the anode comprise the fuel cell catalyst of claim 1 . 13. A fuel cell comprising the fuel cell catalyst of claim 1 .
supported on carriers, e.g. powder carriers · CPC title
as mixture · CPC title
on carbon or graphite · CPC title
Catalytic material supported on carriers, e.g. powder carriers (H01M4/8807, H01M4/881, H01M4/8814, H01M4/925 take precedence) · CPC title
Alloys or mixtures with metallic elements · CPC title
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