초록 ▼

The present invention discloses a hybrid combustor, such as an anode tailgas oxidizer (ATO), for fuel processing applications which combines both flame and catalytic type burners. The hybrid combustor of the present invention combines the advantages of both flame and catalytic type burners. The flam

The present invention discloses a hybrid combustor, such as an anode tailgas oxidizer (ATO), for fuel processing applications which combines both flame and catalytic type burners. The hybrid combustor of the present invention combines the advantages of both flame and catalytic type burners. The flame burner component of the hybrid combustor is used during start-up for the preheating of the catalytic burner component. As soon as the catalytic burner bed is preheated or lit off, the flame burner will be shut off. Optionally, the hybrid combustor may also include an integrated heat recovery unit located downstream of the catalytic burner for steam generation and for the preheating of the feed for a reformer, such as an autothermal reformer.

대표청구항 ▼

What is claimed is: 1. A hybrid combustor comprising: a first valve for allowing entrance of primary air into said hybrid combustor; a second valve for allowing entrance of fuel into said hybrid combustor; a third valve for allowing entrance of secondary air into said hybrid combustor; a flame burn

What is claimed is: 1. A hybrid combustor comprising: a first valve for allowing entrance of primary air into said hybrid combustor; a second valve for allowing entrance of fuel into said hybrid combustor; a third valve for allowing entrance of secondary air into said hybrid combustor; a flame burner with a spark ignitor for startup of said hybrid combustor; a high temperature deflectory plate; a fourth valve for allowing entrance of said fuel into said hybrid combustor wherein mixing point of said fuel, said primary air, and said secondary air is located right before combustion zone of said hybrid combustor; a reformate distributor; a catalytic burner wherein said catalytic burner comprises a catalyst bed; a heat exchanger; an integrated heat recovery unit located downstream of said catalytic burner wherein said integrated heat recovery unit comprises a cylindrical annulus wherein flue gas from said catalytic burner passes through said cylindrical annulus three times; a boiler wherein said boiler compromises both flow boiling and pool boiling; a bell shaped evaporator; big coils for gas further heating; small coils for steam superheating; and a rolled fin type heat exchanger. 2. The hybrid combustor of claim 1, further comprising a secondary air preheater. 3. The hybrid combustor of claim 1, further comprising an inline mixer located upstream of said fourth valve. 4. The hybrid combustor of claim 1, wherein combustion exhaust from said integrated heat recovery unit is piped to a reforming reactor for direct preheating of reformer bed and shift bed during start-up of said reforming reactor. 5. The hybrid combustor of claim 4, wherein said reforming reactor is an autothermal reforming reactor. 6. The hybrid combustor of claim 1, further comprising a secondary air preheater wherein combustion exhaust from said integrated heat recovery unit is piped to said secondary air preheater. 7. The hybrid combustor of claim 1, wherein exhaust from said flame burner preheats said catalyst bed by passing said catalyst bed directly. 8. The hybrid combustor of claim 7, wherein said flame burner automatically shuts off after said catalyst bed is preheated. 9. The hybrid combustor bf claim 1, wherein said reformate distributor is a sparger type reformate distributor. 10. The hybrid combustor of claim 1, wherein said catalyst bed is a monolith catalyst bed. 11. The. hybrid combustor of claim 1, wherein said heat exchanger is a rolled fin type heat exchanger. 12. The hybrid combustor of claim 1, wherein said hybrid combustor is a hybrid anode tailgas oxidizer. 13. The hybrid combustor of claim 1, wherein exhaust from said hybrid combustor preheats a reforming bed. 14. The hybrid combustor of claim 13, wherein said reforming bed is an autothermal reforming bed. 15. A method for operating a hybrid combustor comprising: opening a first valve to allow the entrance of primary air into said hybrid combustor to purge said hybrid combustor with said primary air; venting purged gas to an exhaust line while maintaining flow of said primary air; reducing flow of said primary air; allowing flow of fuel through said second valve; activating a spark ignitor of aflame burner immediately to light off said flame burner; monitoring a thermocouple for temperature change of said flame burner; opening a third valve to allow flow of secondary air after activation of said spark ignitor to cool flame down; controlling flow of said secondary air to prevent catalyst bed from sintering; running said flame burner with said secondary air to heat a heat exchanger and said catalyst bed; closing said second valve to stop flow of said fuel through said second valve automatically shutting off said flame burner; opening a fourth valve to let said fuel flow into a catalytic burner via a distributor wherein an integrated heat recovery unit is located downstream of said catalytic burner wherein said integrated heat recovery unit comprises a cylindrical annulus wherein flue gas from said catalytic burner passes through said cylindrical annulus three times; a boiler wherein said boiler compromises both flow boiling and pool boiling; a bell shaped evaporator; big coils for gas further heating; small coils for steam superheating; and a rolled fin type heat exchanger; and mixing said primary air, said secondary air, and said fuel at mixing point wherein said mixing point is right before combustion zone of said hybrid combustor. 16. The method for operating a hybrid combustor of claim 15, wherein flow of said natural gas, is determined based flow of said primary air and required oxygen to carbon ratio. 17. The method for operating a hybrid combustor of claim 15, further comprising preheating said natural gas by direct mixing with hot air from said heat exchanger. 18. The method for operating a hybrid combustor of claim 15, wherein exhaust from said hybrid combustor preheats a reforming bed. 19. The method for operating a hybrid combustor of claim 18, wherein said reforming bed is an autothermal reforming bed. 20. The method for operating a hybrid combustor of claim 15, wherein said hybrid combustor is a hybrid anode tailgas oxidizer.