초록 ▼

Provided are improved carbon monoxide removal articles and processes for treating hydrogen gas streams to achieve very low threshold levels of carbon monoxide. The articles have a substrate with an inlet end, an outlet end, a length extending between the inlet end to the outlet end, wall elements an

Provided are improved carbon monoxide removal articles and processes for treating hydrogen gas streams to achieve very low threshold levels of carbon monoxide. The articles have a substrate with an inlet end, an outlet end, a length extending between the inlet end to the outlet end, wall elements and a plurality of cells defined by the wall elements. A first layer is deposited on the wall elements from the inlet end and extending at least partially toward the outlet end. The first layer has a preferential carbon monoxide oxidation catalyst. A second layer contains a methanation catalyst, and is deposited on at least part of the first layer from the outlet end. The second layer has a length that is about 10-70% of the substrate length.

대표청구항 ▼

What is claimed is: 1. An apparatus for supplying a hydrogen stream to a fuel cell, said apparatus comprising a hydrocarbon reformer reactor, a water-gas shift reactor, and an article for removing carbon monoxide in the hydrogen stream, wherein the article comprises: a substrate comprising an inlet

What is claimed is: 1. An apparatus for supplying a hydrogen stream to a fuel cell, said apparatus comprising a hydrocarbon reformer reactor, a water-gas shift reactor, and an article for removing carbon monoxide in the hydrogen stream, wherein the article comprises: a substrate comprising an inlet end, an outlet end, a length extending between the inlet end to the outlet end, wall elements and a plurality of cells defined by the wall elements; a first layer deposited on the wall elements from the inlet end and extending at least partially toward the outlet end, wherein the first layer comprises a preferential carbon monoxide oxidation catalyst; and a second layer deposited on at least part of the first layer from the outlet end and having a length that is about 10-70% of the wall elements' length, the second layer overlaying the first layer for a length of at least about 10% of the wall elements' length, wherein the second layer comprises a methanation catalyst; wherein the hydrocarbon reformer reactor is upstream and in train with the water-gas shift reactor, and the article for removing the carbon monoxide is downstream and in train with the water-gas shift reactor. 2. The apparatus of claim 1, wherein the substrate is a honeycomb substrate having a plurality of parallel, axially enclosed cells. 3. The apparatus of claim 1, wherein the substrate is an open-celled foam substrate. 4. The apparatus of claim 1, wherein the second layer has a length of about 30% to about 60% of the wall elements' length. 5. The apparatus of claim 1, wherein the preferential carbon monoxide oxidation catalyst comprises platinum. 6. The apparatus of claim 5, wherein the preferential carbon monoxide oxidation catalyst further comprises an iron component. 7. The apparatus of claim 1, wherein the methanation catalyst comprises ruthenium on an alumina support. 8. The apparatus of claim 1, wherein the preferential carbon monoxide oxidation catalyst comprises about 3 to 5 wt. % of platinum and about 0.1 to 0.5 wt. % iron in the platinum-based, iron-promoted catalyst. 9. The apparatus of claim 1, wherein the methanation catalyst comprises about 1 to 10 wt. % of ruthenium. 10. The apparatus of claim 1, wherein the second layer overlays the first layer for a length of at least about 30% of the wall elements' length. 11. The apparatus of claim 1, wherein the preferential carbon monoxide oxidation catalyst comprises a platinum group metal. 12. The apparatus of claim 1, wherein the preferential carbon monoxide oxidation catalyst comprises about 5 wt. % of platinum.