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A layered catalyst member useful for catalytically generating a hydrogen-rich gas from a hydrocarbon feed. The layered catalyst member comprises a monolith substrate containing at least one layer of a steam reforming catalyst in contact with at least one layer of a catalytic partial oxidation cataly

A layered catalyst member useful for catalytically generating a hydrogen-rich gas from a hydrocarbon feed. The layered catalyst member comprises a monolith substrate containing at least one layer of a steam reforming catalyst in contact with at least one layer of a catalytic partial oxidation catalyst. The steam reforming catalyst comprises one or more platinum group metal components and the catalytic partial oxidation catalyst comprises palladium components.

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1. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with at least one graduated layer of a catalytic partial oxidation cataly

1. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with at least one graduated layer of a catalytic partial oxidation catalyst.2. The layered catalyst member of claim 1, wherein the monolith substrate contains on a surface thereof at least one layer of the steam reforming catalyst and at least one layer of the catalytic partial oxidation catalyst with said layer of the partial oxidation catalyst overlying, and in contact with, said steam reforming catalyst layer.3. The layered catalyst member of claim 1, wherein multiple steam reforming catalyst layers are present in the layered catalyst member, and each of such multiple layers comprises a different steam reforming catalyst composition.4. The layered catalyst member of claim 1, wherein multiple catalytic partial oxidation catalyst layers are present in the layered catalyst member, and each of such multiple layers comprises a different partial oxidation catalyst composition.5. The layered catalyst member of claim 1, wherein the catalytic partial oxidation layer is disposed in the catalyst member such that the hydrocarbon feed initially comes into contact with the catalytic partial oxidation catalyst layer.6. The layered catalyst member of claim 1, wherein the monolith substrate comprises a porous ceramic.7. The layered catalyst member of claim 6, wherein the porous ceramic is selected from the group consisting of alumina, alumina-silica, alumina-silica-titania, mullite, cordierite, zirconia, zirconia-ceria, zirconia-spinel, zirconia-mullite and silicon-carbide.8. The layered catalyst member of claim 6, wherein the porous ceramic is present in the form of a foam.9. The layered catalyst member of claim 1, wherein the monolith substrate comprises a heat and oxidation-resistant metal.10. The layered catalyst member of claim 9, wherein the metal is selected from the group consisting of stainless steel and iron/chromium alloy.11. The layered catalyst member of claim 9, wherein the metal is present in the form of a foam.12. The layered catalyst member of claim 1, wherein the catalytic partial oxidation catalyst layer comprises one or more platinum group metal components.13. The layered catalyst of claim 12, wherein the platinum group metal is selected from the group consisting of platinum, palladium, rhodium, iridium, osmium, ruthenium and mixtures thereof.14. The layered catalyst member of claim 1, wherein the steam reforming catalyst layer comprises one or more platinum group metal components.15. The layered catalyst member of claim 14, wherein the platinum group metal component is selected from the group consisting of platinum, palladium, rhodium, iridium, osmium, ruthenium and mixtures thereof.16. The layered catalyst member of claim 15, wherein the platinum group metal component comprises, on an elemental metal basis, about 10 to about 100% by weight of rhodium components and about 90 to about 0% by weight of platinum components.17. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein a surface of the monolith substrate contains a binder coating interposed between such surface and the steam reforming catalyst layer or the catalytic partial oxidation layer.18. The layered catalyst member of claim 17, wherein the binder comprises a high surface area alumina.19. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the steam reforming catalyst layer and the catalytic partial oxidation catalyst layer are present in the form of washcoats comprising alumina which has been impregnated with the steam reforming catalyst and alumina which has been impregnated with the catalytic partial oxidation catalyst.20. The layered catalyst member of claim 19, wherein the alumina comprises gamma-alumina mixed with one or more rare earth metal oxides and/or one or more alkaline earth metal oxides.21. The layered catalyst member of claim 20, wherein the gamma-alumina is mixed with one or more oxides for a metal selected from the group consisting of lanthanum, cerium, zirconium, praseodymium, yttrium, calcium, barium, strontium, magnesium and mixtures thereof.22. The layered catalyst member of claim 21, wherein the rare earth metal oxides and/or the alkaline earth metal oxides are present in an amount of about 2 to about 10 weight percent, based on the weight of the oxides plus gamma alumina.23. The layered catalyst member of claim 19, wherein each washcoat is present in an amount of about 0.02 to about 3.0 g/in3 of the monolith substrate.24. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the monolith substrate is present in the form of a heat exchanger.25. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the catalytic partial oxidation catalyst layer comprises one or more platinum group metal components wherein the platinum group metal components comprise a mixture of palladium and platinum components.26. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the catalytic partial oxidation catalyst layer comprises, on an elemental metal basis, at 10 to about 99% by weight of palladium components and about 10 to about 90% by weight of platinum components.27. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the catalytic partial oxidation catalyst layer is present in an amount of about 0.1 to about 3.0 g/in3 of monolith substrate.28. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the steam reforming catalyst comprises a nickel component, a cobalt component or a mixture of nickel and cobalt components.29. A layered catalyst member for generating a hydrogen-rich effluent from a hydrocarbon feed comprising a monolith substrate containing on a surface thereof at least one graduated layer of a steam reforming catalyst in contact with a graduated layer of a catalytic partial oxidation catalyst wherein the steam reforming catalyst layer is present in an amount of about 0.1 to about 5.0 g/in3 of the monolith substrate.