초록 ▼

A fuel processor for rapid start and operational control. The fuel processor includes a reformer, a shift reactor, and a preferential oxidation reactor for deriving hydrogen for use in creating electricity in a plurality of H2?O2 fuel cells. A heating and cooling mechanism is coupled to at least the

A fuel processor for rapid start and operational control. The fuel processor includes a reformer, a shift reactor, and a preferential oxidation reactor for deriving hydrogen for use in creating electricity in a plurality of H2?O2 fuel cells. A heating and cooling mechanism is coupled to at least the shift reactor for controlling the critical temperature operation of the shift reactor without the need for a separate cooling loop. This heating and cooling mechanism produces or removes thermal energy as a product of the temperature of the combustion of air and fuel. Anode effluent and cathode effluent or air are used to control the temperature output of the heating mechanism. A vaporizer is provided that heats the PrOx reactor to operating temperature.

대표청구항 ▼

1. A reforming fuel cell system comprising:a reformer converting a hydrogen-containing fuel to produce an H2-containing reformate having a level of carbon monoxide; a first reactor operable to reduce said level of carbon monoxide of said reformate; a fuel cell stack generating electrical energy from

1. A reforming fuel cell system comprising:a reformer converting a hydrogen-containing fuel to produce an H2-containing reformate having a level of carbon monoxide; a first reactor operable to reduce said level of carbon monoxide of said reformate; a fuel cell stack generating electrical energy from said reformate and discharging an H2-containing anode effluent and an O2-containing cathode effluent; a combustor having a catalyst bed disposed therein for burning said anode effluent to generate an exhaust gas; a heat exchanger thermally coupled to said first reactor to control the temperature thereof, said heat exchanger having an input fluidly coupled to said combustor to receive said exhaust gas; and a controller operable for metering air flow to said combustor to control the combustion temperature thereof. 2. The system of claim 1 wherein said controller comprises:a cathode control valve system disposed between said fuel cell stack and said combustor, said cathode control valve system operable to direct said cathode effluent to said combustor to control the temperature of said combustor as a function of the H2 content of said anode effluent. 3. The system of claim 2 wherein said cathode control valve system comprises:a first control valve fluidly coupled between said fuel cell stack and said combustor, said first control valve selectively actuated between an opened position to enable flow of said cathode effluent to said combustor and a closed position to prevent flow of said cathode effluent to said combustor; and a second control valve fluidly coupled between said fuel cell stack and an exhaust passage, said second control valve selectively actuated between an opened position to enable exhausting of said cathode effluent and a closed position to provide a back pressure to facilitate flow of said cathode effluent through said first control valve. 4. The system of claim 1, further comprising:a second reactor disposed between said first reactor and said fuel cell stack, said second reactor being operable to further reduce carbon monoxide levels of said reformate exiting said first reactor; a combustion heater outputting a heated exhaust stream; and a start vaporizer disposed downstream from said combustion heater, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam, said steam from said start vaporizer being directed to a heat exchanger element associated with said second reactor for heating said second reactor. 5. The system of claim 4, further comprising:a spray vaporizer selectively injecting a cooling fluid into said heated exhaust stream to reduce the fluid temperature thereof. 6. The system of claim 4, further comprising:a run vaporizer exposed to an exhaust flow from a heat exchanger element of said first reactor for vaporizing an inlet fluid to produce a steam, said steam from said run vaporizer being directed to an inlet of said reformer. 7. The system of claim 1, further comprising:a second reactor disposed between said first reactor and said fuel cell stack, said second reactor being operable to further reduce carbon monoxide levels of said reformate exiting said first reactor; a combustion heater outputting a heated exhaust stream; a spray vaporizer selectively injecting a cooling fluid into said heated exhaust-stream to control the fluid temperature thereof; and a start vaporizer fluidly coupled to said combustion heater, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam stream, said steam stream being directed to a heat exchanger element of said second reactor for heating said second reactor; wherein a flow through said combustion heater, said spray vaporizer, said start vaporizer, said first reactor, and said combustor is reversible so as to alternatively position said combustion heater, said spray vaporizer, and said start vaporizer upstream and downstream from said first reactor. 8. A fuel processor for rapid start and operational control, said fuel processor comprising:a plurality of fuel cells discharging an H2-containing anode effluent and an O2-containing cathode effluent; a reformer converting a hydrogen-containing fuel selected from the group consisting of alcohol and hydrocarbons to H2 to produce a reformate for fueling said plurality of fuel cells; a shift reactor disposed between said plurality of fuel cells and said reformer, said shift reactor having a catalytic region operable to reduce carbon monoxide levels of said reformate and a heat exchange region; a preferential oxidation reactor disposed between said shift reactor and said plurality of fuel cells, said preferential oxidation reactor being operable to further reduce carbon monoxide levels of said reformate exiting said shift reactor; a combustor providing hot exhaust gas to said heat exchange region of said shift reactor, said combustor having a catalyst bed disposed therein for burning said anode effluent and said cathode effluent to generate said hot exhaust gas; a combustion burner operably coupled to said combustor, said combustion burner outputting a heated exhaust stream; and a cathode control valve system disposed between said plurality of fuel cells and said combustor, said cathode control valve system operable to direct said cathode effluent to said combustor to control a temperature of said combustor when the H2 content of said anode effluent increases. 9. The fuel processor according to claim 8 wherein said cathode control valve system comprises:a first control valve fluidly coupled between said plurality of fuel cells and said combustor, said first control valve selectively actuated between an opened position to enable flow of said cathode effluent to said combustor and a closed position to prevent flow of said cathode effluent to said combustor; and a second control valve fluidly coupled between said plurality of fuel cells and an exhaust passage, said second control valve selectively actuated between an opened position to enable exhausting of said cathode effluent and a closed position to provide a back pressure to facilitate flow of said cathode effluent through said first control valve. 10. The fuel processor according to claim 9, further comprising:a spray vaporizer selectively injecting a cooling fluid into said heated exhaust stream to reduce the fluid temperature thereof; and a start vaporizer disposed downstream from said combustion burner, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam, said steam from said start vaporizer being directed to a heat exchanger element associated with said preferential oxidation reactor for heating said preferential oxidation reactor. 11. The fuel processor according to claim 10, further comprising:a run vaporizer exposed to an exhaust flow of said heat exchanger region of said shift reactor for vaporizing an inlet fluid to produce a steam, said steam from said run vaporizer being directed to an inlet of said reformer. 12. The fuel processor according to claim 8, further comprising:a spray vaporizer selectively injecting a cooling fluid into said heated exhaust stream to control the fluid temperature thereof; and a start vaporizer fluidly coupled to said combustion burner, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam stream, said steam stream from said start vaporizer being directed to a heat exchanger element of said preferential oxidation reactor for heating said preferential oxidation reactor; wherein a flow through said combustion burner, said spray vaporizer, said start vaporizer, said shift reactor, and said combustor is reversible so as to alternatively position said combustion burner, said spray vaporizer, and said start vaporizer upstream and downstream from said shift reactor. 13. A fuel processor for rapid start and operational control, said fuel processor comprising:a plurality of fuel cells discharging an H2-containing anode effluent and an O2-containing cathode effluent; a reformer converting a hydrogen-containing fuel selected from the group consisting of alcohol and hydrocarbons to H2 to produce a reformate for fueling said plurality of fuel cells; a shift reactor disposed between said plurality of fuel cells and said reformer, said shift reactor being operable to reduce carbon monoxide levels of said reformate; a preferential oxidation reactor disposed between said shift reactor and said plurality of fuel cells, said preferential oxidation reactor being operable to further reduce carbon monoxide levels of said reformate exiting said shift reactor; a combustor providing hot exhaust gas to said shift reactor, said combustor being fueled by said fuel and said anode effluent, said combustor having a catalyst bed disposed therein for burning said fuel and said anode effluent to generate said hot exhaust gas; a combustion burner operably coupled to said combustor, said combustion burner outputting a heated exhaust stream; a spray vaporizer selectively injecting a cooling fluid into said heated exhaust stream to reduce the fluid temperature thereof; and a controller operable for metering air flow to said combustor to control the combustion temperature of said combustor. 14. The fuel processor according to claim 13, further comprising:a cathode control valve system disposed between said plurality of fuel cells and said combustor, said cathode control valve system operable to direct said cathode effluent to said combustor to limit a temperature of said combustor when the H2 content of said anode effluent increases. 15. The fuel processor according to claim 14 wherein said cathode control valve system comprises:a first control valve fluidly coupled between said plurality of fuel cells and said combustor, said first control valve selectively actuated between an opened position to enable flow of said cathode effluent to said combustor and a closed position to prevent flow of said cathode effluent to said combustor; and a second control valve fluidly coupled between said plurality of fuel cells and an exhaust passage, said second control valve selectively actuated between an opened position to enable exhausting of said cathode effluent and a closed position to provide a back pressure to facilitate flow of said cathode effluent through said first control valve. 16. The fuel processor according to claim 13, further comprising:a start vaporizer disposed downstream from said combustion burner, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam, said steam from said start vaporizer being directed to a heat exchanger element associated with said preferential oxidation reactor for heating said preferential oxidation reactor. 17. The fuel processor according to claim 16, further comprising:a run vaporizer exposed to an exhaust flow from a heat exchanger element of said shift reactor for vaporizing an inlet fluid to produce a steam, said steam from said run vaporizer being directed to an inlet of said reformer. 18. The fuel processor according to claim 13, further comprising:a start vaporizer fluidly coupled to said combustion burner, said start vaporizer being exposed to said heated exhaust stream for vaporizing an inlet fluid to produce a steam stream, said steam stream from said start vaporizer being directed to a heat exchanger element of said preferential oxidation reactor for heating said preferential oxidation reactor; wherein a flow through said combustion burner, said spray vaporizer, said start vaporizer, said shift reactor, and said combustor is reversible so as to alternatively position said combustion burner, said spray vaporizer, and said start vaporizer upstream and downstream from said shift reactor.