초록 ▼

A CO-selective catalyst comprises a catalytic material, wherein the catalytic material is selected from the group consisting of Pt, Pd, Rh, Ir, Os, Ru, Ta, Zr, Y, Ce, Ni, Cu, and oxides, alloys, compounds, and combinations comprising at least one of the foregoing; a modifying agent selected from the

A CO-selective catalyst comprises a catalytic material, wherein the catalytic material is selected from the group consisting of Pt, Pd, Rh, Ir, Os, Ru, Ta, Zr, Y, Ce, Ni, Cu, and oxides, alloys, compounds, and combinations comprising at least one of the foregoing; a modifying agent selected from the group consisting of Pb, Bi, Ge, Si, Sb, As, P, and combinations comprising at least one of the foregoing; and a support. In one embodiment, the method for forming the CO selective catalyst comprises combining a catalytic material and a support with about 2 to about 25 atomic percent of a modifying agent, based on the total surface atoms of the catalytic material, to form a modified catalyst-containing support and disposing the modified catalyst-containing support on or into a substrate.

대표청구항 ▼

The invention claimed is: 1. A fuel cell system comprising: a fuel reformer for generating a feed stock comprising H2 and CO; a CO-selective oxidation reactor in fluid communication with said fuel reformer for treating said feed stock to oxidize CO, wherein said CO-selective oxidation reactor compr

The invention claimed is: 1. A fuel cell system comprising: a fuel reformer for generating a feed stock comprising H2 and CO; a CO-selective oxidation reactor in fluid communication with said fuel reformer for treating said feed stock to oxidize CO, wherein said CO-selective oxidation reactor comprises a housing disposed around a substrate comprising a CO-selective oxidation catalyst comprising: a catalytic material selected from the group consisting of Pt, Pd, Rh, Ir, Os, Ru, Ta, Zr, Y, Ce, Ni, Cu, and oxides, alloys, and compounds thereof, a modifying agent selected from the group consisting of Pb, and alloys, nitrates, sulfides, and chlorides thereof in an amount of about 2 to about 25 atomic percent based on the total surface atoms of said catalytic material, and a support; and a fuel cell in fluid communication with said CO-selective oxidation reactor. 2. The fuel cell system of claim 1, wherein said catalytic material is selected from the group consisting of Pt, Pd, Rh, Ir, and oxides, alloys, and compounds thereof. 3. The fuel cell system of claim 1, wherein said CO-selective catalyst comprises about 8 to about 15 atomic percent of said modifying agent. 4. The fuel cell system of claim 1, wherein said support is selected from the group consisting of alumina, titania, zirconia, and combinations comprising at least one of the foregoing supports. 5. The fuel cell system of claim 1, wherein the CO-selective oxidation catalyst comprises about 0.5 to about 5.0 wt % of said catalytic material, based upon a total weight of said catalytic material, said modifying agent, and said support. 6. The fuel cell system of claim 5, wherein the CO-selective oxidation catalyst comprises about 1.0 to about 3.5 wt % of said catalytic material. 7. The fuel cell system of claim 6, wherein the CO-selective oxidation catalyst comprises about 1.8 to about 2.5 wt 520 % of said catalytic material. 8. The fuel cell system of claim 1, wherein the CO-selective oxidation catalyst comprises about 0.01 to about 0.5 wt % of said modifying agent, based upon a total weight of said catalytic material, said modifying agent, and said support. 9. The fuel cell system of claim 8, wherein the CO-selective oxidation catalyst comprises about 0.05 to about 0.30 wt % of said modifying agent. 10. The fuel cell system of claim 9, wherein the CO-selective oxidation catalyst comprises about 0.10 to about 0.20 wt % of said modifying agent. 11. The fuel cell system of claim 1, wherein the wherein the CO-selective catalyst is capable of preferentially removing carbon monoxide over hydrogen removal. 12. The fuel cell system of claim 11, wherein the CO-selective catalyst is capable of the removal of the carbon monoxide in a feed stock while oxidizing less than about 3 mole % hydrogen in a feed from a reformer.