Facile control of pore structure in carbon-supported PGM-based catalysts

Patent metadata

Field	Value
Publication number	US-9947935-B1
Application number	US-201615282080-A
Country	US
Kind code	B1
Filing date	Sep 30, 2016
Priority date	Sep 30, 2016
Publication date	Apr 17, 2018
Grant date	Apr 17, 2018

Abstract

A method for forming a carbon supported catalyst includes a step of providing a first carbon supported catalyst having a platinum-group metal supported on a first carbon support. Characteristically, the first carbon support has a first average micropore diameter and a first average carbon surface area. The first carbon supported catalyst is contacted with an oxygen-containing gas at a temperature less than about 450° C. for a predetermined period of time to form a second carbon supported catalyst, wherein the first carbon support or the second carbon supported catalyst is acid leached.

First claim

What is claimed is:

1. A method for forming a carbon supported catalyst, the method comprising:
a) 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;
b) contacting the first carbon supported catalyst with an oxygen-containing gas at a temperature less than about 450° C. for a predetermined period of time to form a second carbon supported catalyst, wherein the first carbon support or the second carbon supported catalyst is acid leached.

2. The method of claim 1 wherein the first carbon support is acid leached and then contacted with the oxygen-containing gas at a temperature less than about 300° C. to form the second carbon supported catalyst.

3. The method of claim 2 wherein the first carbon supported catalyst is dried prior to being contacted with the oxygen-containing gas.

4. The method of claim 3 further comprising contacting the second carbon supported catalyst with molecular hydrogen.

5. The method of claim 1 wherein the first carbon support is contacted with the oxygen-containing gas and then acid leached to form the second carbon supported catalyst.

6. The method of claim 5 further comprising contacting the second carbon supported with molecular hydrogen.

7. The method of claim 1 wherein the second carbon supported catalyst includes an altered carbon support having a second average pore diameter and a second average carbon surface area, the second average micropore diameter being greater than the first average micropore diameter and the second average carbon surface area being less than the first average carbon surface area.

8. The method of claim 7 wherein the first average micropore diameter is less than 40 angstroms.

9. The method of claim 7 wherein the second average micropore diameter is greater than 40 angstroms.

10. The carbon supported catalyst of claim 7 wherein the second average carbon surface area is decreased by more than 2% and a second average carbon amount is decreased by more than 1%.

11. The method of claim 7 wherein the first carbon support has a first average pore volume and the altered carbon support has a second average pore volume for pore size in a range of 40-100 angstroms, the second average pore volume being greater than the first average pore volume.

12. The method of claim 1 wherein the platinum-group metal is selected from the group consisting of Pt, Pd, Au, Ru, Ir, Rh, and Os.

13. The method of claim 1 wherein the platinum-group metal is Pt.

14. The method of claim 1 wherein the first carbon support is a carbon powder.

15. A method for forming a carbon supported catalyst, the method comprising:
a) 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 micropore diameter and a first average carbon surface area;
b) contacting the first carbon supported catalyst with an oxygen-containing gas at a temperature less than about 450° C. for a predetermined period of time to form a second carbon supported catalyst;
c) contacting the second carbon supported with molecular hydrogen to form a third carbon supported catalyst; and
d) acid leaching the third carbon supported catalyst to form a fourth carbon supported catalyst having depleted non-noble metal catalyst particles disposed thereon.

16. The method of claim 15 wherein the carbon supported catalyst is dried prior to being contacted with the oxygen-containing gas.

17. The method of claim 15 wherein the second carbon supported catalyst includes an altered carbon support having a second average micropore diameter and a second average carbon surface area, the second average micropore diameter being greater than the first average micropore diameter and the second average carbon surface area being less than the first average carbon surface area.

18. The method of claim 15 wherein the platinum-group metal is selected from the group consisting of Pt, Pd, Au, Ru, Ir, Rh, and Os.

19. The method of claim 15 wherein the platinum-group metal is Pt.

Assignees

• Gm Global Tech Operations Llc

Inventors

• Kongkanand Anusorn
• Carpenter Michael K

Classifications

• H01M4/8878

  Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body · CPC title

• H01M4/8882 Primary

  Heat treatment, e.g. drying, baking · CPC title

• H01M4/926 Primary

  on carbon or graphite · CPC title

• H01M4/9083

  on carbon or graphite · CPC title

• H01M2008/1095

  Fuel cells with polymeric electrolytes · CPC title