초록 ▼

A fuel processor for producing a hydrogen-rich product gas suitable for direct use in fuel cell applications includes a housing, an annular shift/methanator reactor vessel at least one reactor vessel wall disposed within the housing and forming an outer annular space between the at least one reactor

A fuel processor for producing a hydrogen-rich product gas suitable for direct use in fuel cell applications includes a housing, an annular shift/methanator reactor vessel at least one reactor vessel wall disposed within the housing and forming an outer annular space between the at least one reactor vessel wall and the housing. A combustion chamber having at least one combustion chamber wall and forming a first inner annular space between the at least one combustion chamber wall and the at least one reactor vessel wall is disposed in the interior space formed by the annular shift/methanator reactor vessel, and a reformer reactor vessel having at least one reformer vessel wall and forming a second inner annular space between the at least one reformer vessel wall and the at least one combustion chamber wall is disposed within the combustion chamber.

대표청구항 ▼

1. A method for reforming a hydrocarbon fuel comprising the steps of:mixing said hydrocarbon fuel with water, forming a fuel/water mixture; introducing said fuel/water mixture into a heat exchange zone of a fuel processor, said heat exchange zone comprising at least one steam vaporizing coil, said a

1. A method for reforming a hydrocarbon fuel comprising the steps of:mixing said hydrocarbon fuel with water, forming a fuel/water mixture; introducing said fuel/water mixture into a heat exchange zone of a fuel processor, said heat exchange zone comprising at least one steam vaporizing coil, said at least one steam vaporizing coil heated with products of combustion from a combustor disposed within said fuel processor, forming a preheated mixture comprising steam; introducing said preheated mixture into an input end of a reformer section disposed within said fuel processor, said reformer section comprising a cylindrical housing having said input end and an output end, said input end disposed proximate a middle region of said fuel processor and said output end disposed proximate a bottom region of said fuel processor, and said reformer section heated by said combustor, said combustor comprising a combustion catalyst bed disposed around an exterior surface of said reformer section and filling at least a portion of an annular space disposed between said exterior surface and a cylindrical flue gas shaft disposed at a central axis of said fuel processor, thereby forming a reformer section effluent comprising hydrogen, carbon monoxide, carbon dioxide and steam; passing said reformer section effluent into a shift/methanator reactor vessel, said shift/methanator reactor vessel comprising an annular cylindrical structure having a shift/methanator reactor inlet end in fluid communication with said output end of said reformer section and a shift/methanation reactor outlet end, said annular cylindrical structure forming an inner annular region between said annular cylindrical structure and said combustor and an outer annular region between said annular cylindrical structure and a fuel processor housing enclosing said combustor, said reformer section, said heat exchange zone and said shift/methanation reactor vessel, and said annular structure filled with a shift catalyst proximate said shift/methanator reactor inlet end and a methanation catalyst proximate said shift/methanator outlet end, forming a hydrogen-rich product gas. 2. A method in accordance with claim 1, wherein said outer annular region and said inner annular region are filled with an insulating material.3. A method in accordance with claim 2, wherein said insulating material is one of a castable refractory and a moldable ceramic insulating foam.4. A method in accordance with claim 1, wherein a flue gas exhausted from said fuel processor has a temperature in a range of about 300° F. to about 600° F.5. A method in accordance with claim 1, wherein said reformer section effluent exits from said reformer section at a temperature in a range of about 500° F. to about 1300° F.6. A method in accordance with claim 1, wherein said hydrogen-rich product gas exiting from said shift/methanator reactor vessel is in the range of about 200° F. to about 600° F.7. An apparatus comprising:at least one housing wall, said at least one housing wall forming a reformable fuel inlet, a product gas outlet, a combustible fuel inlet and a flue gas outlet; a shift/methanator reactor vessel comprising at least one reactor vessel wall disposed within said housing and forming an outer annular space between said at least one reactor vessel wall and said at least one housing wall; a combustion chamber comprising at least one combustion chamber wall and forming a first inner annular space between said at least one combustion chamber wall and said at least one reactor vessel wall, said combustion chamber having a combustion products outlet in fluid communication with said flue gas outlet; and a reformer reactor vessel comprising at least one reformer vessel wall and forming a second inner annular space between said at least one reformer vessel wall and said at least one combustion chamber wall. 8. An apparatus in accordance with claim 7 further comprising at least one combustion catalyst disposed in said second inner annular space.9. An apparatus in accordance with claim 7, wherein at least one methanator cooling coil having a fuel/water inlet and a fuel/water outlet is disposed in a downstream region of said shift/methanator reactor vessel.10. An apparatus in accordance with claim 9, wherein a shift cooling coil having a shift gas inlet in fluid communication with said fuel/water outlet and having a shift gas outlet is disposed in an downstream region of said shift/methanator reactor vessel.11. An apparatus in accordance with claim 10 further comprising at least one steam coil having a pre-reformed gas inlet and a pre-reformed gas outlet disposed within said combustion chamber, said pre-reformed gas inlet in fluid communication with said shift gas outlet and said pre-reformed gas outlet in fluid communication with an interior of said reformer reactor vessel.12. An apparatus in accordance with claim 11, wherein said at least one reformer vessel wall forms a reformed gas outlet, said reformed gas outlet in fluid communication with an interior of said shift/methanator reactor vessel.13. An apparatus in accordance with claim 7, wherein said at least one reformer vessel wall forms a reformed gas outlet, said reformed gas outlet in fluid communication with an interior of said shift/methanator reactor vessel.14. An apparatus in accordance with claim 7, wherein said shift/methanator reactor vessel comprises a shift region in which is disposed at least one shift catalyst and a methanation region in which is disposed at least one methanation catalyst, said shift catalyst disposed upstream of said methanation catalyst.15. An apparatus in accordance with claim 7, wherein one of a castable refractory and a moldable ceramic insulating foam is disposed in said outer annular space and said first inner annular space.16. An apparatus in accordance with claim 7, wherein at least one reformer catalyst is disposed within said reformer reactor vessel.17. An apparatus in accordance with claim 7, wherein said housing is cylindrical in shape.18. An apparatus in accordance with claim 17, wherein said shift/methanator reactor vessel is cylindrical in shape and coaxially aligned with said housing.19. An apparatus in accordance with claim 18, wherein said reformer reactor vessel is cylindrical in shape and coaxially aligned with said housing.20. An apparatus in accordance with claim 7 further comprising a ceramic start-up burner adapted to fire into said combustion chamber.21. An apparatus in accordance with claim 7 further comprising an air humidification section disposed within said apparatus proximate said flue gas outlet.22. An apparatus comprising:a cylindrical fuel processor housing having a reformable fuel inlet, a product gas outlet, a combustible fuel inlet and a flue gas outlet; a cylindrical annular shift/methanator reactor vessel having a reformed fuel inlet end corresponding to a shift zone, a product gas outlet end corresponding to a methanation zone and an inner cylindrical wall and an outer cylindrical wall concentrically disposed within said cylindrical fuel processor housing and forming an annular region between said cylindrical fuel processor housing and said outer cylindrical wall, said inner cylindrical wall enclosing a concentrically disposed core region; a combustion chamber wall enclosing a cylindrical combustion chamber concentrically disposed within said concentrically disposed core region and forming an outer annular region between said inner cylindrical wall and said combustion chamber wall, said cylindrical combustion chamber having a combustion end and an exhaust end, said combustion end oriented toward said reformed fuel inlet end of said shift/methanator reactor vessel; a cylindrical reformer vessel concentrically disposed within said cylindrical combustion chamber and forming an inner annular region between an outer surface of said reformer vessel and said combustion chamber wall, said cylindrical reformer vessel having a reformed fuel outlet end oriented toward said reformed fuel inlet end in fluid communication with said reformed fuel inlet end and a reformable fuel inlet end in fluid communication with said reformable fuel inlet of said housing; a shift catalyst disposed in said shift zone of said shift/methanator reactor vessel and a methanation catalyst disposed in said methanation zone of said shift/methanator reactor vessel; a reformer catalyst disposed in said cylindrical reformer vessel; and heat exchange means disposed within said housing for controlling the temperature of a process stream passing through said apparatus. 23. An apparatus in accordance with claim 22, wherein a combustion catalyst bed is disposed in said inner annular region.24. An apparatus in accordance with claim 22, wherein said heat exchange means comprises a steam coil disposed in said combustion chamber proximate said exhaust end, said steam coil having a steam coil inlet end and a steam coil outlet end, said steam coil outlet end in fluid communication with said reformable fuel inlet end of said cylindrical reformer vessel.25. An apparatus in accordance with claim 24, wherein said heat exchange means further comprises a methanator cooling coil disposed in said methanation zone of said shift/methanator reactor vessel and having a methanator cooling coil inlet end and a methanator cooling coil outlet end, said methanator cooling coil outlet end in fluid communication with said steam coil inlet end.26. An apparatus in accordance with claim 25, wherein said heat exchange means further comprises a shift cooling coil disposed between said steam coil and said methanation cooling coil in said shift zone of said shift/methanator reactor vessel and having a shift cooling coil inlet end and a shift cooling coil outlet end, said shift cooling coil inlet end in fluid communication with said methanation cooling coil outlet end and said shift cooling coil outlet end in fluid communication with said steam coil inlet end.27. An apparatus in accordance with claim 22 further comprising a ceramic start-up burner adapted to burn a fuel in said combustion end of said combustion chamber.28. An apparatus in accordance with claim 22, wherein said reformer catalyst comprises a plurality of alternating layers of larger and smaller particles.29. An apparatus in accordance with claim 22 further comprising an air humidification section disposed within said cylindrical fuel processor housing proximate said flue gas outlet.