Fuel cell system with interconnect
US-9525181-B2 · Dec 20, 2016 · US
US10411266B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10411266-B2 |
| Application number | US-201515542321-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 4, 2015 |
| Priority date | Jan 7, 2015 |
| Publication date | Sep 10, 2019 |
| Grant date | Sep 10, 2019 |
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Provided are: a dry reforming catalyst, in which a noble metal (M) is doped in a nickel yttria stabilized zirconia complex (Ni/YSZ) and an alloy (M-Ni alloy) of the noble metal (M) and nickel is formed at Ni sites on a surface of the nickel yttria stabilized zircona (YSZ); a method for producing the dry reforming catalyst using the noble metal/glucose; and a method for performing dry reforming using the catalyst. The present invention can exhibit a significantly higher dry reforming activity as compared with Ni/YSZ catalysts. Furthermore, the present invention can have an improved long-term performance by suppressing or preventing the deterioration. Furthermore, the preparing method is useful in performing the alloying of noble metal with Ni at Ni sites on the Ni/YSZ surface and can simplify the preparing process, and thus is suitable in mass production.
Opening claim text (preview).
What is claimed is: 1. A dry reforming catalyst, wherein the dry reforming catalyst comprises a noble metal (M) that is doped to a nickel yttria stabilized zirconia complex (Ni/YSZ) and an alloy (M-Ni alloy) of the noble metal (M) and nickel is formed at Ni sites on a surface of the nickel yttria stabilized zircona (YSZ). 2. The dry reforming catalyst according to claim 1 , wherein the noble metal (M) is Pd, Pt, Ru, Rh, Au, or Ag. 3. The dry reforming catalyst according to claim 1 , wherein the noble metal (M) is Pd. 4. The dry reforming catalyst according to claim 1 , wherein an electrical structure of Ni is changed by the alloying of noble metal with Ni at the Ni sites. 5. The dry reforming catalyst according to claim 1 , wherein during the alloying of noble metal with Ni at the Ni sites, a charge transfer occurs from the noble metal particles to the Ni side. 6. The dry reforming catalyst according to claim 1 , wherein the alloying of noble metal with Ni at the Ni sites changes an oxidation state of nickel into a reduced state. 7. The dry reforming catalyst according to claim 1 , wherein the alloying of noble metal with Ni at the Ni sites increases resistance to oxidation of nickel. 8. The dry reforming catalyst according to claim 1 , wherein the alloying of noble metal with Ni at the Ni sites suppresses carbon growth or carbon deposit formation. 9. The dry reforming catalyst according to claim 1 , wherein the alloyed noble metal-nickel alloy (M-Ni alloy) at the Ni sites promotes both CH 4 cracking and CO 2 mediated carbon oxidation. 10. The dry reforming catalyst according to claim 1 , wherein the alloyed noble metal-nickel alloy (M-Ni alloy) at the Ni sites promotes the oxidation of cracked carbon and promotes methane activation. 11. The dry reforming catalyst according to claim 1 , wherein the catalyst is used for dry reforming at a temperature of 750° C. or more. 12. The dry reforming catalyst according to claim 1 , wherein the catalyst is used for dry reforming at a temperature of 800° C. or more. 13. The dry reforming catalyst according to claim 1 , wherein the catalyst is used for dry reforming at a temperature of 750° C. to 900° C. or 800° C. to 900° C. 14. The dry reforming catalyst according to claim 1 , wherein the catalyst is a dry reforming catalyst for improving dry reforming performance and long-term stability of a nickel yttria stabilized zirconia (Ni/YSZ). 15. The dry reforming catalyst according to claim 1 , wherein the catalyst maintains an initial activity after being operated for 120 hours or more. 16. The dry reforming catalyst according to claim 1 , wherein the catalyst is a dry reforming catalyst of a solid oxide fuel cell. 17. A solid oxide fuel cell comprising the dry reforming catalyst according to claim 1 . 18. The solid oxide fuel cell according to claim 17 , wherein the catalyst is a fuel electrode catalyst of the solid oxide fuel cell.
Negative electrodes · CPC title
Direct internal reforming at the anode of the fuel cell · CPC title
of noble metals or noble-metal based alloys · CPC title
specially used in fuel cell operating at high temperature, e.g. SOFC · CPC title
consisting of more than one material, e.g. consisting of composites · CPC title
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