IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
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출원번호 |
US-0880105
(2007-07-19)
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등록번호 |
US-8435683
(2013-05-07)
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발명자
/ 주소 |
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출원인 / 주소 |
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대리인 / 주소 |
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인용정보 |
피인용 횟수 :
2 인용 특허 :
6 |
초록
▼
The present teachings relate to solid oxide fuel cells with internal reforming capability. The solid oxide fuel cell generally includes a cathode, an electrolyte, an anode, and a catalyst layer in contact with the anode. The catalyst layer can include a support membrane and a reforming catalyst laye
The present teachings relate to solid oxide fuel cells with internal reforming capability. The solid oxide fuel cell generally includes a cathode, an electrolyte, an anode, and a catalyst layer in contact with the anode. The catalyst layer can include a support membrane and a reforming catalyst layer associated with the support membrane. In some embodiments, the reforming catalyst can include one or more partial oxidation reforming catalysts. The present teachings also provide methods of making and operating the solid oxide fuel cells described above.
대표청구항
▼
1. A fuel cell comprising: a cathode;an electrolyte;an anode; anda catalyst layer in contact with the anode, wherein the catalyst layer comprises a reforming catalyst associated with a support membrane, the support membrane comprising coria, zirconia, lanthana, and alumina, and one or more metal oxi
1. A fuel cell comprising: a cathode;an electrolyte;an anode; anda catalyst layer in contact with the anode, wherein the catalyst layer comprises a reforming catalyst associated with a support membrane, the support membrane comprising coria, zirconia, lanthana, and alumina, and one or more metal oxides selected from lanthanum strontium oxide, molybdenum oxide, calcium titanium oxide, lanthanum strontium chromite, and lanthanum calcium chromite. 2. The fuel cell of claim 1, wherein the reforming catalyst comprises at least one of Pt, Ni, W, Ru, Au, Pd, Mo, Cu, Sn, Rh, and V. 3. The fuel cell of claim 1, wherein the reforming catalyst comprises at least one of Pt and Pd. 4. The fuel cell of claim 1, wherein the reforming catalyst comprises Ru. 5. The fuel cell of claim 1, wherein the support membrane further comprises one or more metal oxides selected from titanium oxide and zinc oxide. 6. The fuel cell of claim 1, wherein the anode is partially covered by the catalyst layer. 7. The fuel cell of claim 1, wherein the anode is substantially covered by the catalyst layer. 8. The fuel cell of claim 1, wherein the reforming catalyst is impregnated in the support membrane. 9. The fuel cell of claim 1, wherein the catalyst layer has a thickness between about 5μm and about 50μm. 10. The fuel cell of claim 1, wherein zirconia and ceria are included with alumina in a ratio of about 0.1 to about 0.9. 11. The fuel cell of claim 1, wherein the support membrane comprises ceria and zirconia in a range of about 10% to about 50% by weight of the total weight of the support membrane. 12. The fuel cell of claim 11, wherein the support membrane comprises lanthana in a range of about 10% to about 20% by weight of the total weight of the support membrane. 13. A fuel cell comprising: a cathode;an electrolyte;an anode; anda catalyst layer in contact with the anode, wherein the catalyst layer comprises a reforming catalyst associated with a support membrane, the support membrane comprising alumina ceria, zirconia, and one or more metal oxides selected from lanthanum strontium oxide, molybdenum oxide, calcium titanium oxide, lanthanum strontium chromite, and lanthanum calcium chromite. 14. The fuel cell of claim 13, wherein zirconia and ceria are included with alumina in a ratio of about 0.1 to about 0.9. 15. The fuel cell of claim 13, wherein the support membrane further comprises one or more metal oxide elected from titanium oxide, lanthanum oxide, and zinc oxide. 16. A method of making an internally reforming fuel cell, the method comprising: depositing a support slurry onto at least a portion of an anode of a fuel cell, wherein the support slurry comprises a plurality of metal oxides in a solvent, wherein the plurality of metal oxides comprise alumina, ceria and zirconia;drying the support slurry and calcining the fuel cell at a temperature between about 800° C. and about 1200° C. to form a support membrane; andassociating a reforming catalyst with the support membrane. 17. The method of claim 16, wherein the support slurry farther comprises one or more metal oxides selected from titanium oxide, lanthanum oxide, lanthanum strontium oxide, molybdenum oxide, zinc oxide, calcium titanium oxide, lanthanum strontium chromite, and lanthanum calcium chromite. 18. The method of claim 16, wherein the-reforming catalyst comprises at least one of Pt, Ni, W, Ru, Au, Pd, Mo, Cu, Sn, Rh, and V. 19. The method of claim 16, wherein the support slurry is deposited by slip-coating, dip coating, or spin-coating. 20. The method of claim 16, wherein associating a reforming catalyst with the support membrane comprises depositing a catalyst composition comprising a reforming catalyst in a solvent onto the support membrane and calcining the fuel cell at a temperature between about 800° C. and about 1200° C. to associate the support membrane with the reforming catalyst.
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