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A hydrogen generation system is disclosed that includes an integrated steam reforming reactor. The reactor has an overall cylindrical shape, receives a reformate and separately receiving a combustion gas mixture. The reactor includes a plurality of reforming stages arranged in a stacked series of di

A hydrogen generation system is disclosed that includes an integrated steam reforming reactor. The reactor has an overall cylindrical shape, receives a reformate and separately receiving a combustion gas mixture. The reactor includes a plurality of reforming stages arranged in a stacked series of disc shaped stage configuration, wherein each reforming stage has a disc shaped combustion portion adjacent a disc shaped catalyst pack through which the reformate passes, wherein the reformate is directed axially between stages and radially within each stage; and the combustion mixture is directed radially between groups of stages and circumferentially within each stage.

대표청구항 ▼

1. A hydrogen generation system comprising: a hydrocarbon fuel supply;a water supply;a combustion gas mixture; andan integrated reforming reactor receiving a portion of the fuel supply for processing as a reformate and separately receiving the combustion mixture, the reactor comprising: a plurality

1. A hydrogen generation system comprising: a hydrocarbon fuel supply;a water supply;a combustion gas mixture; andan integrated reforming reactor receiving a portion of the fuel supply for processing as a reformate and separately receiving the combustion mixture, the reactor comprising: a plurality of reforming stages arranged in a stacked series configuration, wherein each reforming stage has a disc shaped combustion portion adjacent a disc shaped catalyst pack through which the reformate passes, wherein the reformate is directed axially between stages and radially within each stage; and the combustion mixture is directed radially between groups of stages and circumferentially within each stage. 2. The system according to claim 1 wherein the combustion portion of each stage comprises a pair of opposing disc shaped plates each having a flat heat exchange surface and an opposite surface having a plurality of arcuate concentric ribs formed thereon and a central axial bore therethrough, and wherein the pair of disc shaped plates are mated together with the concentric ribs interleaved to form arcuate concentric passages extending from a first side edge of the pair of plates to an opposite side edge of the pair of plates. 3. The system according to claim 2 further comprising a tapered entrance passage and an opposite tapered exit passage formed between the side edges and the ends of the interleaved ribs for receiving and exhausting the combustion gas. 4. The system according to claim 2 wherein end surfaces of each of the ribs contacts the opposite plate surface so as to seal each of the arcuate passages. 5. The system according to claim 1 wherein the catalyst pack comprises a flat disc shaped diverter plate sandwiched between two catalyst screens. 6. The system according to claim 5 wherein each catalyst pack has a series of catalyst screens sandwiching the diverter plate. 7. The system according to claim 5 wherein the combustion portion has a central bore therethrough through which reformate passes to axially enter an adjacent catalyst pack. 8. The system according to claim 7 wherein reformate is directed radially through the catalyst first outwardly from the central bore to an outer edge of the diverter plate, around the outer edge of the diverter plate, and radially inward to the central bore of another combustion portion of an adjacent stage. 9. The system according to claim 1 wherein the integrated reformer reactor has a plurality of stages arranged in groups of three and wherein combustion gas flows through each group of stages in parallel and between sequential groups in series. 10. The system according to claim 9 wherein the integrated reformer reactor has at least 12 stages and includes a manifold attached to the stages to direct combustion gas between groups of stages. 11. An integrated reforming reactor for use in a hydrogen generation system, the reactor receiving a reformate and separately receiving a combustion gas mixture, the reactor comprising: a plurality of reforming stages arranged in a stacked series configuration, wherein each reforming stage has a disc shaped combustion portion adjacent a disc shaped catalyst pack through which the reformate passes, wherein the reformate is directed axially between stages and radially within each stage; and the combustion mixture is directed radially between groups of stages and circumferentially within each stage. 12. The reactor according to claim 11 wherein the combustion portion of each stage comprises a pair of opposing disc shaped plates each having a flat heat exchange surface and an opposite surface having a plurality of arcuate concentric ribs formed thereon and a central axial bore therethrough, and wherein the pair of disc shaped plates are mated together with the concentric ribs interleaved to form arcuate concentric passages extending from a first side edge of the pair of plates to an opposite side edge of the pair of plates. 13. The reactor according to claim 12 further comprising a tapered entrance passage and an opposite tapered exit passage formed between the side edges and the ends of the interleaved ribs for receiving and exhausting the combustion gas. 14. The reactor according to claim 12 wherein end surfaces of each of the ribs contacts the opposite plate surface so as to seal each of the arcuate passages. 15. The reactor according to claim 11 wherein the catalyst pack comprises a flat disc shaped diverter plate sandwiched between two catalyst screens. 16. The reactor according to claim 15 wherein each catalyst pack has a series of catalyst screens sandwiching the diverter plate. 17. The reactor according to claim 15 wherein the combustion portion has a central bore therethrough through which reformate passes to axially enter an adjacent catalyst pack. 18. The reactor according to claim 17 wherein reformate is directed radially through the catalyst first outwardly from the central bore to an outer edge of the diverter plate, around the outer edge of the diverter plate, and radially inward to the central bore of another combustion portion of an adjacent stage. 19. The reactor according to claim 11 wherein the integrated reformer reactor has a plurality of stages arranged in groups of three and wherein combustion gas flows through each group of stages in parallel and between sequential groups in series. 20. The reactor according to claim 19 wherein the integrated reformer reactor has at least 12 stages and includes a manifold attached to the stages to direct combustion gas between groups of stages.