초록 ▼

Described herein is a fuel processor that produces hydrogen from a fuel source. The fuel processor comprises a reformer and burner. The reformer includes a catalyst that facilitates the production of hydrogen from the fuel source. Voluminous reformer chamber designs are provided that increase the a

Described herein is a fuel processor that produces hydrogen from a fuel source. The fuel processor comprises a reformer and burner. The reformer includes a catalyst that facilitates the production of hydrogen from the fuel source. Voluminous reformer chamber designs are provided that increase the amount of catalyst that can be used in a reformer and increase hydrogen output for a given fuel processor size. The burner provides heat to the reformer. One or more burners may be configured to surround a reformer on multiple sides to increase thermal transfer to the reformer. Dewars are also described that increase thermal management of a fuel processor and increase burner efficiency. A dewar includes one or more dewar chambers that receive inlet air before a burner receives the air. The dewar is arranged such that air passing through the dewar chamber intercepts heat generated in the burner before the heat escapes the fuel processor.

대표청구항 ▼

What is claimed is: 1. A fuel processor for producing hydrogen from a fuel source, the fuel processor comprising: a reformer including two or more reformer chambers in a cross section that are configured to receive the fuel source and configured to output hydrogen, each of the two or more reformer

What is claimed is: 1. A fuel processor for producing hydrogen from a fuel source, the fuel processor comprising: a reformer including two or more reformer chambers in a cross section that are configured to receive the fuel source and configured to output hydrogen, each of the two or more reformer chambers including a reformer catalyst that facilitates the production of hydrogen, wherein the two or more reformer chambers are configured such that reactants move through the two or more reformer chambers in series; a boiler configured to heat the fuel source before the reformer receives the fuel source; a burner including two or more burner chambers in a cross section, each of the two or more burner chambers including a burner catalyst, the two or more burner chambers configured to provide heat to the reformer, wherein the two or more burner chambers are configured such that reactants move through the two or more burner chambers in series; and a dewar that contains the reformer, contains the burner and includes a set of dewar walls that form a dewar chamber that is configured to receive the fuel source or oxygen before one of the two or more burner chambers receives the fuel source or oxygen, wherein the fuel processor includes a monolithic structure having a common material included in walls that define the two or more reformer chambers, the two or more burner chambers and the boiler, wherein the monolithic structure comprises a wall comprising copper that is shared by one of the two or more reformer chambers and one of the two or more burner chambers and the fuel processor is configured to permit conductive thermal communication from the burner catalyst, through the wall, to one of the two or more reformer chambers. 2. The fuel processor of claim 1 wherein the two or more reformer chambers surrounds greater than 50 percent of the two or more burner chamber cross-sectional perimeter. 3. The fuel processor of claim 2 wherein the two or more reformer chambers surrounds greater than 75 percent of the two or more burner chamber cross-sectional perimeter. 4. The fuel processor of claim 3 wherein the two or more reformer chambers surrounds greater than 90 percent of the two or more burner chamber cross-sectional perimeter. 5. The fuel processor of claim 1 wherein the two or more burner chambers bilaterally neighbors the two or more reformer chambers. 6. The fuel processor of claim 5 wherein the two or more burner chambers trilaterally neighbors the two or more reformer chambers. 7. The fuel processor of claim 6 wherein the two or more burner chambers quadrilaterally neighbors the two or more reformer chambers. 8. The fuel processor of claim 1 wherein the two or more burner chambers each has a non-planar cross-sectional shape. 9. The fuel processor of claim 1 wherein the two or more burner chambers each has a non-quadrilateral cross-sectional shape. 10. The fuel processor of claim 1 wherein the dewar includes a radiative layer disposed on an inner wall of the set of dewar walls that improves radiative heat reflectance of the inner wall. 11. The fuel processor of claim 1 wherein the dewar is configured such that air passing through the dewar chamber receives heat generated in one of the two or more burner chambers. 12. The fuel processor of claim 1 wherein the dewar annularly surrounds the two or more burner chambers in the cross section. 13. The fuel processor of claim 1 wherein the dewar includes a second dewar chamber. 14. The fuel processor of claim 13 wherein the second dewar chamber is configured to receive heat from the two or more burner chambers. 15. The fuel processor of claim 1 wherein the common material comprises a metal. 16. The fuel processor of claim 15 wherein the monolithic structure is formed in a single extrusion or casting. 17. The fuel processor of claim 1 wherein the wall permits conductive thermal communication between the two or more burner chambers and the two or more reformer chambers in orthogonal directions. 18. The fuel processor of claim 17 wherein the boiler is configured to receive heat from one of the two or more burner chambers. 19. The fuel processor of claim 18 further comprising a second boiler that is configured to heat the fuel source before one of the two or more burner chambers receives the fuel source. 20. A fuel processor for producing hydrogen from a fuel source, the fuel processor comprising: a reformer including two or more reformer chambers in a cross section that are configured to receive the fuel source and configured to output hydrogen, each of the two or more reformer chambers are configured such that reactants move through the two or more reformer chambers in series and including a catalyst that facilitates the production of hydrogen, each of the two or more reformer chambers having a volume greater than about 0.1 cubic centimeters and less than about 50 cubic centimeters, and each of the two or more reformer chambers is characterized by a cross sectional width and a cross sectional height that is greater than one-third the cross sectional width; a boiler configured to heat the fuel source before the reformer receives the fuel source; a burner including two or more burner chambers in a cross section, each of the burner chambers including a burner catalyst, each of the two or more burner chambers are configured to provide heat to the reformer, wherein the two or more burner chambers are configured such that reactants move through the two or more burner chambers in series; a dewar that contains the reformer, contains the burner and includes a set of dewar walls that form a dewar chamber that is configured to receive the fuel source or oxygen before one of the two or more burner chambers receives the fuel source or oxygen, wherein the fuel processor includes a monolithic structure comprising copper that forms a wall of one of the two or more reformer chambers, a wall of one of the two or more burner chambers, and a wall of the boiler. 21. The fuel processor of claim 20 wherein the two or more reformer chambers each are substantially non-quadrilateral in cross section. 22. The fuel processor of claim 20 wherein the two or more reformer chambers each includes a substantially elliptical cross section. 23. The fuel processor of claim 22 wherein the two or more reformer chambers each include a substantially circular cross section. 24. The fuel processor of claim 20 wherein the two or more reformer chambers each comprises a volume between about 0.5 cubic centimeters and about 2.5 cubic centimeters. 25. The fuel processor of claim 20 wherein the cross sectional height is greater than one-half the cross sectional width. 26. The fuel processor of claim 20 wherein the cross sectional height is greater than the cross sectional width. 27. The fuel processor of claim 20 wherein the two or more burner chambers each has a non-quadrilateral cross-sectional shape. 28. The fuel processor of claim 27 wherein the two or more burner chambers bilaterally neighbors the two or more reformer chambers. 29. The fuel processor of claim 28 wherein the two or more burner chambers collectively quadrilaterally neighbor the two or more reformer chambers. 30. The fuel processor of claim 20 wherein the two or more reformer chambers surrounds greater than 90 percent of the two or more burner chamber perimeter. 31. The fuel processor of claim 20 wherein the boiler is configured to receive heat from at least one of the two or more burner chambers. 32. The fuel processor of claim 20 wherein the fuel processor includes a monolithic structure having a common material included in walls that define the two or more reformer chambers, the two or more burner chambers and the boiler. 33. The fuel processor of claim 32 wherein the common material comprises a metal. 34. The fuel processor of claim 33 wherein the monolithic structure is formed in a single extrusion. 35. The fuel processor of claim 20 wherein the catalyst comprises pellets. 36. The fuel processor of claim 35 wherein the pellets have a diameter ranging from about 300 microns to about 1500 microns. 37. A fuel processor for producing hydrogen from a fuel source, the fuel processor comprising: a reformer including two or more reformer chambers in a cross section that are configured to receive the fuel source and configured to output hydrogen, each of the two or more reformer chambers including a reformer catalyst that facilitates the production of hydrogen, wherein the two or more reformer chambers are configured such that reactants move through the two or more reformer chambers in series; a boiler configured to heat the fuel source before the reformer receives the fuel source; a burner, including two or more burner chambers in a cross section, each of the two or more burner chambers include a burner catalyst, each of the two or more burner chambers configured to provide heat to the reformer; a dewar that contains the reformer, contains the burner and includes a set of dewar walls that form a dewar chamber that is configured to receive the fuel source or oxygen before one of the two or more burner chambers receives the fuel source or oxygen, wherein the fuel processor includes a monolithic structure comprising copper that forms a wall of at least one of the two or more reformer chambers, a wall of at least one of the two or more burner chambers, and a wall of the boiler. 38. The fuel processor of claim 20 wherein the two or more reformer chambers surrounds greater than 50 percent of the two or more burner chamber cross-sectional perimeter. 39. The fuel processor of claim 20 wherein the two or more reformer chambers surrounds greater than 75 percent of the two or more burner chamber cross-sectional perimeter. 40. The fuel processor of claim 37 wherein the two or more burner chambers are configured such that reactants move through the two or more burner chambers in series.