Method for producing carrier for electrode catalyst, precursor of carrier for electrode catalyst, and carrier for electrode catalyst, comprising same
US-12057587-B2 · Aug 6, 2024 · US
US2017033368A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017033368-A1 |
| Application number | US-201514815450-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 31, 2015 |
| Priority date | Jul 31, 2015 |
| Publication date | Feb 2, 2017 |
| Grant date | — |
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A carbon supported catalyst includes a carbon support having an average micropore diameter is less than about 70 angstroms and a platinum-group metal being disposed over the carbon support. A method for making the carbon supported catalyst includes a step of providing a first carbon supported catalyst having a platinum-group metal supported on a carbon support. The first carbon supported catalyst has a first average micropore diameter, and a first average surface area. The first carbon supported catalyst is contacted with an oxygen-containing gas at a temperature less than about 250° C. for a predetermined period of time to form a second carbon supported catalyst. The second carbon supported catalyst has a second average pore diameter and a second average surface area. Characteristically, the second average pore diameter is greater than the first average pore diameter, and the second average surface area is less than the first average surface area.
Opening claim text (preview).
What is claimed is: 1 . A carbon supported catalyst comprising: a carbon support having an average pore diameter that is greater than 50 angstroms, and an average surface area less than about 500 m 2 /g; and a platinum-group metal being disposed over the carbon support. 2 . The carbon supported catalyst of claim 1 wherein the average pore diameter is less than 150 angstroms. 3 . The carbon supported catalyst of claim 1 wherein the average surface area is greater than 50 m 2 /g, 4 . The carbon supported catalyst of claim 1 wherein the carbon support has an average pore volume that is less than about 0.6 cm 3 /g, 5 . The carbon supported catalyst of claim 4 wherein the average pore volume is from about 0.1 to about 0.5 cm 3 /g. 6 . The carbon supported catalyst of claim 1 wherein the platinum-group metal is selected from the group consisting of Pt, Pd, Au, Ru, Ir, Rh, and Os. 7 . The carbon supported catalyst of claim 1 wherein the platinum-group metal is Pt. 8 . The carbon supported catalyst of claim 1 wherein the carbon support is a carbon powder. 9 . The carbon supported catalyst of claim 1 wherein the carbon support includes particles selected from the group consisting of nano-rods, nanotubes, nano-rafts, non-electrically conducting particles, spherical particles, and combinations thereof. 10 . The carbon supported catalyst of claim 1 wherein the carbon support is a high surface area carbon (HSC) powder. 11 . A method for forming a carbon supported catalyst, the method comprising: providing a first carbon supported catalyst having a platinum-group metal supported on a first carbon support, the first carbon support having a first average pore diameter and a first average surface area; and contacting the first carbon supported catalyst with an oxygen-containing gas at a temperature less than about 250° C. for a predetermined period of time to form a second carbon supported catalyst, the second carbon supported catalyst including an altered carbon support having a second average pore diameter and a second average surface area, the second average pore diameter being greater than the first average pore diameter and the second average surface area being less than the first average surface area. 12 . The method of claim 11 wherein the first average pore diameter is less than 70 angstroms. 13 . The method of claim 11 wherein the second average pore diameter is greater than 70 angstroms. 14 . The carbon supported catalyst of claim 11 wherein the second average surface area is less than 500 m 2 /g, 15 . The method of claim 11 wherein the first carbon support has a first average pore volume and the altered carbon support has a second average pore volume, the second average pore volume being less than the first average pore volume. 16 . The method of claim 15 wherein the second average pore volume is from about 0.1 to about 0.5 cm 3 /g. 17 . The method of claim 11 wherein the platinum-group metal is selected from the group consisting of Pt, Pd, Au, Ru, Ir, Rh, and Os. 18 . The method of claim 11 wherein the platinum-group metal is Pt. 19 . The method of claim 11 wherein the carbon support is a carbon powder. 20 . The method of claim 11 wherein the second average pore diameter is more than 70 angstroms and the second average surface area is less than 500 m 2 /g.
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