Carbon supported catalyst

US9548500B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9548500-B2
Application numberUS-201214345754-A
CountryUS
Kind codeB2
Filing dateSep 19, 2012
Priority dateSep 28, 2011
Publication dateJan 17, 2017
Grant dateJan 17, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A catalyst includes (i) a primary metal or alloy or mixture including the primary metal, and (ii) an electrically conductive carbon support material for the primary metal or alloy or mixture including the primary metal, wherein the carbon support material: (a) has a specific surface area (BET) of 100-600 m 2 /g, and (b) has a micropore area of 10-90 m 2 /g.

First claim

Opening claim text (preview).

The invention claimed is: 1. An electrode comprising a gas diffusion layer and a catalyst, wherein the catalyst comprises: (i) a primary metal, or an alloy or mixture comprising the primary metal, and (ii) an electrically conductive carbon support material for said primary metal, alloy or mixture, wherein the carbon support material: (a) has a specific surface area (BET) of 300-600 m 2 /g, and (b) has a micropore area of 25-60 m 2 /g. 2. The electrode according to claim 1 , wherein the carbon support material loses 20% or less of its mass in an accelerated test involving a 1.2V potential hold over a 24 hour period at 80° C. 3. The electrode according to claim 1 , wherein the carbon support material has a specific corrosion rate of less than 65%. 4. The electrode according to claim 2 , wherein the carbon support material has a specific corrosion rate of less than 65%. 5. The electrode according to claim 1 , wherein the primary metal is selected from the group consisting of (i) the platinum group metals of platinum, palladium, rhodium, ruthenium, iridium and osmium, (ii) gold, silver, and (iii) a base metal or an oxide thereof. 6. The electrode according to claim 1 , wherein the primary metal has a gas phase metal area of at least 30 m 2 /g. 7. The electrode according to claim 1 , wherein the loading of primary metal particles on the carbon support material is in the range 5-95 wt %. 8. A catalysed membrane comprising a solid polymeric membrane and a catalyst, the catalyst comprising: (i) a primary metal, or an alloy or mixture comprising the primary metal, and (ii) an electrically conductive carbon support material for said primary metal, alloy or mixture, wherein the carbon support material: (a) has a specific surface area (BET) of 300-600 m 2 /g, (b) has a micropore area of 25-60 m 2 /g. 9. A catalysed transfer substrate comprising a transfer substrate and the catalyst as defined in claim 1 . 10. A membrane electrode assembly comprising the electrode as claimed in claim 1 . 11. A fuel cell comprising the membrane electrode assembly as claimed in claim 10 . 12. A fuel cell comprising the electrode according to claim 1 . 13. The electrode according to claim 1 , wherein the primary metal is platinum. 14. The fuel cell according to claim 11 , wherein the fuel cell is a proton exchange membrane fuel cell and the loading of primary metal particles on the carbon support material is in the range of 35-75 wt %. 15. The fuel cell according to claim 11 , wherein the fuel cell is a phosphoric acid fuel cell and the loading of primary metal particles on the carbon support material is in the range 5-25 wt %. 16. The catalyzed membrane according to claim 8 , wherein the carbon support material loses 20% or less of its mass in an accelerated test involving a 1.2V potential hold over a 24 hour period at 80° C. 17. The catalyzed membrane according to claim 8 , wherein the carbon support material has a specific corrosion rate of less than 65%. 18. The catalyzed membrane according to claim 8 , wherein the primary metal is selected from the group consisting of (i) the platinum group metals of platinum, palladium, rhodium, ruthenium, iridium and osmium, (ii) gold, silver, and (iii) a base metal or an oxide thereof. 19. The catalyzed membrane according to claim 8 , wherein the primary metal has a gas phase metal area of at least 30 m 2 /g. 20. The catalyzed membrane according to claim 8 , wherein the loading of primary metal particles on the carbon support material is in the range 5-95 wt %. 21. A membrane electrode assembly comprising the catalyzed membrane according to claim 8 . 22. A fuel cell comprising the membrane electrode assembly according to claim 21 . 23. A fuel cell comprising the catalyzed membrane according to claim 8 . 24. The catalyzed membrane according to claim 8 , wherein the primary metal is platinum. 25. The fuel cell according to claim 22 , wherein the fuel cell is a proton exchange membrane fuel cell and the loading of primary metal particles on the carbon support material is in the range of 35-75 wt %. 26. The fuel cell according to claim 22 , wherein the fuel cell is a phosphoric acid fuel cell and the loading of primary metal particles on the carbon support material is in the range 5-25 wt %. 27. The electrode according to claim 1 , wherein the electrically conductive carbon support material comprises carbon black, and the carbon black has been treated with at least one gas selected from the group consisting of oxygen, ozone, hydrogen peroxide, nitrogen dioxide, air, carbon dioxide and steam. 28. The electrode according to claim 27 , wherein the carbon black is treated at a temperature between 800° C. and 1100° C. 29. The electrode according to claim 27 , wherein the carbon black is treated for a time ranging between 30 minutes and 4 hours. 30. The catalyzed membrane according to claim 8 , wherein the electrically conductive carbon support material comprises carbon black, and the carbon black has been treated with at least one gas selected from the group consisting of oxygen, ozone, hydrogen peroxide, nitrogen dioxide, air, carbon dioxide and steam. 31. The catalyzed membrane according to claim 30 , wherein the carbon black is treated at a temperature between 800° C. and 1100° C. 32. The catalyzed membrane according to claim 30 , wherein the carbon black is treated for a time ranging between 30 minutes and 4 hours.

Assignees

Inventors

Classifications

  • Fuel cells with polymeric electrolytes · CPC title

  • H01M4/9083Primary

    on carbon or graphite · CPC title

  • Surface area · CPC title

  • H01M4/926Primary

    on carbon or graphite · CPC title

  • Metals or alloys (H01M4/92 takes precedence) · CPC title

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What does patent US9548500B2 cover?
A catalyst includes (i) a primary metal or alloy or mixture including the primary metal, and (ii) an electrically conductive carbon support material for the primary metal or alloy or mixture including the primary metal, wherein the carbon support material: (a) has a specific surface area (BET) of 100-600 m 2 /g, and (b) has a micropore area of 10-90 m 2 /g.
Who is the assignee on this patent?
Johnson Matthey Fuel Cells Ltd, Timcal Ltd, Imerys Graphite & Carbon Switzerland Ltd
What technology area does this patent fall under?
Primary CPC classification H01M4/9083. Mapped technology areas include Electricity.
When was this patent published?
Publication date Tue Jan 17 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).