초록 ▼

A catalytic reactor comprises a plurality of fluid-impermeable plates defining flow channels between them. Tight fitting within each flow channel is a sheet of corrugated material whose surfaces are coated with catalytic material. At each end of the flow channels are headers to supply gas mixtures t

A catalytic reactor comprises a plurality of fluid-impermeable plates defining flow channels between them. Tight fitting within each flow channel is a sheet of corrugated material whose surfaces are coated with catalytic material. At each end of the flow channels are headers to supply gas mixtures to the flow channels, the headers communicating with adjacent channels being separate. The reactor enables different gas mixtures to be supplied to adjacent channels, which may be at different pressures, and the corresponding chemical reactions are also different. Where one of the reactions is endothermic while the other reaction is exothermic, heat is transferred through the wall of the tube separating the adjacent channels, from the exothermic reaction to the endothermic reaction.

대표청구항 ▼

The invention claimed is: 1. A catalytic reactor comprising a plurality of metal sheets arranged for defining first gas flow channels between adjacent sheets, means for defining second gas flow channels in proximity to said first gas flow channels, arranged for ensuring good thermal contact between

The invention claimed is: 1. A catalytic reactor comprising a plurality of metal sheets arranged for defining first gas flow channels between adjacent sheets, means for defining second gas flow channels in proximity to said first gas flow channels, arranged for ensuring good thermal contact between gases in said first and said second gas flow channels; catalytic material on at least some surfaces within each flow channel, and header means for supplying gas mixtures to said gas flow channels, said header means being arranged for supplying different gas mixtures to said first and said second gas flow channels, said metal sheets being substantially flat and said gas flow channels being defined by grooves therein such that gases in said first and said second gas flow channels may differ in pressure by several atmospheres; portions of said sheet between said grooves being in contact with the adjacent metal sheet for providing thermal contact, and said metal sheets being bonded together as a stack; characterized by corrugated metal foils provided in gas flow channels, said foils being of an aluminium-bearing ferritic steel that forms an adherent oxide coating of alumina on surfaces of said foils when heated in air, and having said catalytic material on said surfaces. 2. A catalytic reactor as claimed in claim 1 wherein said corrugated metal foils are compressed within said flow channels. 3. A catalytic reactor as claimed in claim 1 wherein corrugations in said metal foils are of different pitch, wavelength or pattern at successive positions along said flow channel. 4. A catalytic reactor as claimed in claim 1 wherein said corrugated foils are shaped for promoting mixing of said gases within said flow channel. 5. A catalytic reactor as claimed in claim 1 wherein at least some of said gas flow channels vary in width or depth along their length. 6. A catalytic reactor comprising a series of metal sheets arranged as a stack and bonded together, said sheets being shaped and arranged for defining a plurality of first fluid flow channels between adjacent sheets and a plurality of second fluid flow channels between adjacent sheets, said first fluid flow channels alternating with said second fluid flow channels in the stack, and portions of each channel-defining sheet between flow channels being in contact with the adjacent metal sheet for providing good thermal contact between fluids in the first and the second flow channels, and providing structural support such that fluids in the first and the second flow channels may differ in pressure; header means for supplying fluids to the flow channels, said header means enabling different fluids to be supplied to the first and the second flow channels; and catalyst-carrying metal sheets in at least some of the flow channels, each catalyst-carrying metal sheet being shaped for subdividing a respective flow channel into a multiplicity of parallel flow sub-channels, and each catalyst-carrying metal sheet having the catalytic material on its surface. 7. A catalytic reactor as claimed in claim 6 wherein each catalyst-carrying metal sheet is a corrugated metal foil, and is not structural. 8. A catalytic reactor as claimed in claim 6 wherein said parallel flow sub-channels are of different pitch, wavelength or pattern at successive positions along the flow channel. 9. A catalytic reactor as claimed in claim 6 wherein each catalyst-carrying metal sheet is of an aluminium-bearing ferritic steel that forms an adherent oxide coating of alumina when heated in air. 10. A catalytic reactor as claimed in claim 6 wherein at least some of the flow channels vary in width or depth along their length. 11. A catalytic reactor as claimed in claim 6 wherein both said first and second flow channels are less than 5 mm wide in at least one direction transverse to the flow direction. 12. A catalytic reactor as claimed in claim 6 wherein the flow direction of the first flow channels is transverse to the flow direction of the second flow channels. 13. A catalytic reactor comprising a series of metal sheets arranged as a stack and bonded together, said sheets being shaped and arranged for defining a plurality of first flow channels between adjacent sheets and a plurality of second flow channels between adjacent sheets, first flow channels alternating with second flow channels in the stack, and portions of each channel-defining sheet between flow channels being in contact with the adjacent metal sheet and so providing thermal contact, such that there is good thermal contact between fluids in the first and the second flow channels, and providing structural support such that fluids in the first and the second flow channels may differ in pressure; headers for supplying fluids to the flow channels, said headers enabling different fluids to be supplied to the first and the second flow channels; and catalyst-carrying metal substrates in at least some of the flow channels; wherein the flow direction of the first flow channels is transverse to the flow direction of the second flow channels. 14. A catalytic reactor as claimed in claim 13 wherein at least some of the flow channels vary in width or depth along their length. 15. A catalytic reactor as claimed in claim 13 wherein both the first and the second flow channels are less than 5 mm wide in at least one direction transverse to the flow direction. 16. A catalytic reactor comprising a plurality of metal sheets arranged as a stack and bonded together; said sheets being shaped for defining first gas flow channels between adjacent sheets and second gas flow channels between further adjacent sheets wherein said first gas flow channels alternate with said second gas flow channels within said stack; header means for supplying different fluids to said first and second gas flow channels; said first and second gas flow channels being arranged for providing good thermal contact between said different fluids flowing in flow paths along said first and second flow channels; metal foil means disposed within said first gas flow channels and said second gas flow channels and having catalyst material carried thereon; said catalyst material, at least in said first gas flow channels, having catalytic activity varied along the flow path for providing low catalytic activity initially and higher catalytic activity further along said flow path. 17. The catalytic reactor as defined in claim 16 wherein said catalytic activity is varied by adjusting the loading of said catalytic material along said flow path. 18. The catalytic reactor as defined in claim 16 wherein said metal foil means include a ceramic coating thereon, and said catalytic material is incorporated into said ceramic coating. 19. The catalytic reactor as defined in claim 18 wherein said ceramic coating is of thickness in the range 10-50 μm. 20. The catalytic reactor as defined in claim 18 wherein said ceramic coating in at least some of said gas flow channels is comprised of alumina. 21. The catalytic reactor as defined in claim 16 wherein said metal foils are corrugated and are comprised of aluminum-bearing ferritic steel. 22. The catalytic reactor as defined in claim 16 wherein at least some of said flow channels vary in width or depth along their length. 23. The catalytic reactor as defined in claim 16 wherein both said first flow channels and said second flow channels are less than 5 mm wide in at least one direction transverse to the flow direction.