초록 ▼

A fuel processor for producing a hydrogen-containing product stream from a fuel stream and an oxidant stream, comprises a mixing tube from which the combined fuel and oxidant stream is directed substantially axially into a reaction chamber. The reaction chamber comprises a turn-around chamber and a

A fuel processor for producing a hydrogen-containing product stream from a fuel stream and an oxidant stream, comprises a mixing tube from which the combined fuel and oxidant stream is directed substantially axially into a reaction chamber. The reaction chamber comprises a turn-around chamber and a turn-around wall at one end for re-directing the combined reactant stream, so that in the turn-around chamber the re-directed stream surrounds and is in contact with the combined reactant stream flowing substantially axially in the opposite direction. This design and opposing flow configuration creates a low velocity zone which stabilizes the location of a flame in the fuel processor and offers other advantages.

대표청구항 ▼

1. A fuel processor for producing a hydrogen-containing product stream from a fuel stream and an oxidant stream, said fuel processor comprising a fuel inlet port, an oxidant inlet port, a product outlet port, and an outer shell housing a reaction chamber, wherein said fuel processor further comprise

1. A fuel processor for producing a hydrogen-containing product stream from a fuel stream and an oxidant stream, said fuel processor comprising a fuel inlet port, an oxidant inlet port, a product outlet port, and an outer shell housing a reaction chamber, wherein said fuel processor further comprises: a mixing tube disposed within said reaction chamber, said mixing tube fluidly connected to receive said oxidant stream from said oxidant inlet port and said fuel stream from said fuel inlet port, said mixing tube capable of forming a combined reactant stream having a flame speed and directing said combined reactant stream substantially axially into said reaction chamber at a speed maintained above said combined reactant stream flame speed, wherein said reaction chamber further comprises:(i) a turn-around chamber;(ii) a turn-around wall at one end of said turn-around chamber, said turn-around wall being shaped to re-direct said combined reactant stream outwardly from a central axis and then back through said turn-around chamber in substantially the opposite direction, so that in said turn-around chamber the redirected stream surrounds and is in contact with said combined reactant stream flowing substantially axially in the opposite direction; and(iii) an annular section surrounding said mixing tube, located downstream of said turn-around chamber through which a product stream flows before exiting said fuel processor through said product outlet port;wherein said turn-around chamber and said turn-around wall are shaped to create a low velocity zone between the opposing reactant streams and to create eddies in said low velocity zone for stabilizing the location of a flame in the fuel processor during operation. 2. The fuel processor of claim 1 wherein said turn-around chamber is free of flow separation structures and flow impeding structures. 3. The fuel processor of claim 1 wherein said turn-around chamber does not contain a catalyst for promoting conversion of said fuel and oxidant streams. 4. The fuel processor of claim 3 wherein said fuel processor is a non-catalytic syngas generator. 5. The fuel processor of claim 1 wherein said oxidant inlet port is fluidly connected to receive exhaust gas from a combustion engine. 6. The fuel processor of claim 1 wherein the diameter of said turn-around chamber is about 3-7 times greater than the diameter of the outlet of said mixing tube. 7. The fuel processor of claim 1 wherein the diameter of said turn-around chamber is about 5 times greater than the diameter of the outlet of said mixing tube. 8. The fuel processor of claim 1 wherein the distance from the average plane of said turn-around wall to the outlet of said mixing tube is about 4-11 times the diameter of the outlet of said mixing tube. 9. The fuel processor of claim 1 wherein the distance from the average plane of said turn-around wall to the outlet of said mixing tube is about 7-8 times the diameter of the outlet of said mixing tube. 10. The fuel processor of claim 1 further comprising a critical flow venturi located upstream of said mixing tube. 11. The fuel processor of claim 1 wherein said reaction chamber comprises an annular particulate filter surrounding said mixing tube, located downstream of said turn-around chamber. 12. The fuel processor of claim 11 wherein said annular particulate filter is disposed substantially concentrically around said mixing tube. 13. The fuel processor of claim 12 further comprising a concentric sleeve type heat exchanger disposed within said shell housing. 14. The fuel processor of claim 1 wherein said turn-around wall is shaped with a central peak that protrudes towards said mixing tube and is aligned with the axis of said mixing tube. 15. The fuel processor of claim 1 further comprising more than one layer of thermal insulation wherein each layer of thermal insulation has thermal insulating property that differs from the thermal insulating property of each other layer of thermal insulation. 16. The fuel processor of claim 1 wherein said reaction chamber is formed by a layer of thermal insulation. 17. The fuel processor of claim 16 wherein said layer of thermal insulation is vacuum-formed. 18. The fuel processor of claim 1 further comprising a concentric sleeve type heat exchanger comprising an inner chamber fluidly connected to receive oxidant stream from said oxidant inlet port and direct it toward said mixing tube, and comprising a surrounding outer annular chamber fluidly connected to receive product stream from said reaction chamber and direct it toward said product outlet port. 19. The fuel processor of claim 18 wherein said heat exchanger is fluidly connected so that said oxidant stream and said product stream are directed through said concentric sleeve heat exchanger in a co-flow direction. 20. The fuel processor of claim 1 further comprising a glow plug. 21. The fuel processor of claim 20 wherein the tip of said glow plug is located in said low velocity zone. 22. The fuel processor of claim 20 wherein said glow plug is located in a lower portion of said turn-around chamber. 23. The fuel processor of claim 1 wherein said turn-around wall comprises one of a semi-horn torus, a semi-ring torus, a semi-cone torus, a semi-sphere and a pan-shaped structure.