초록 ▼

A method is provided to inject liquid water into the normal stream of fuel, superheated air and superheated steam entering a primary reactor of a fuel processor. The injection location is in the steam supply line where superheated steam vaporizes a majority of the liquid water, preferably prior to i

A method is provided to inject liquid water into the normal stream of fuel, superheated air and superheated steam entering a primary reactor of a fuel processor. The injection location is in the steam supply line where superheated steam vaporizes a majority of the liquid water, preferably prior to injection into the primary reactor. Steam supplied by a vaporizer may temporarily lag desired steam production due to system up-power transients or startup conditions, coupled with vaporizer thermal lag time. Injection of liquid water overcomes this temporary deficit of steam. Additional air is also supplied as needed to improve reactance for a given steam volume/temperature. Injection rate or volume of the liquid water and air may also be based on one or more measured variables of the primary reactor.

대표청구항 ▼

1. A method of operating a primary reactor in a fuel processing system, the method comprising the steps of: generating a superheated steam stream; selectively injecting a water stream into said superheated steam stream to form a steam stream mixture; introducing said steam stream mixture to

1. A method of operating a primary reactor in a fuel processing system, the method comprising the steps of: generating a superheated steam stream; selectively injecting a water stream into said superheated steam stream to form a steam stream mixture; introducing said steam stream mixture to an inlet of a primary reactor; providing a hydrocarbon fuel stream to said inlet of said primary reactor; connecting an air stream to said inlet of said primary reactor; dissociating said steam stream, said fuel stream and said air stream in said primary reactor to form a hydrogen-containing reformate, wherein said water stream is selectively injected into said superheated steam stream based on an operating state of said primary reactor. 2. The method of claim 1 which comprises the further step of reducing injection of the water stream to a zero flow over a predetermined time period.3. The method of claim 1 which comprises the further steps of: preheating a source of the air stream; pressurizing the source of the air stream; and providing the preheated, pressurized air stream to the primary reactor inlet. 4. The method of claim 3 which comprises the further step of introducing a volumetric flow of said preheated, pressurized air stream to increase a rate of heat generation by the primary reactor.5. The method of claim 1 which comprises the further step of preheating a source of said liquid water stream prior to injecting said liquid water stream into the superheated steam stream.6. The method of claim 1 which comprises the further step of injecting said liquid water stream at a pre-selected spaced location in the first inlet stream, said location spaced from the primary reactor to permit the superheated steam stream to superheat at least a majority of a liquid water in the steam stream mixture prior to the mixture reaching the primary reactor inlet.7. The method of claim 1 which comprises the further step of preheating a source of said hydrocarbon fuel stream prior to introducing said fuel stream into the inlet of said primary reactor.8. A method of operating a primary reactor in a fuel processing system to produce a hydrogen containing reformate from a hydrocarbon fuel, the method comprising the steps of: supplying a first stream having a superheated steam to an inlet of the primary reactor; injecting a second stream having liquid water into said first stream, during a predetermined operating condition, to vaporize at least a majority of the liquid water in a liquid water/superheated steam mixture prior to the mixture reaching the primary reactor inlet; adding a third stream having a preheated fuel to the primary reactor inlet, for dissociation in the primary reactor; introducing a fourth stream having pressurized air to the primary reactor inlet; measuring an inlet temperature of the primary reactor; and controlling a net flow to the primary reactor, said net flow being a combination of the first, second, third and fourth streams to the primary reactor, based on the measured inlet temperature of the primary reactor. 9. The method of claim 8 which comprises the further step of temporarily increasing a flow of the pressurized air to the primary reactor to increase a primary reactor reaction temperature for vaporizing an unvaporized remainder of the liquid water/superheated steam mixture reaching the primary reactor inlet.10. The method of claim 8 which comprises the further step of adding the pressurized air over a continuous time period to control an oxygen/carbon (O/C) ratio and an outlet temperature of the primary reactor.11. The method of claim 8 which comprises the further step of controlling a volumetric flow rate of said fourth stream of pressurized air to the primary reactor inlet to increase an oxygen/carbon (O/C) ratio.12. The method of claim 9 which comprises the further step of adding a volumetric flow of the liquid water over a predetermined time period to increase a steam/carbon (S/C ) ratio.13. A method of operating a primary reactor in a fuel processing system over a semi-continuous time period to produce a hydrogen-containing reformate from a hydrocarbon fuel, the method comprising the steps of: supplying a first stream having a superheated steam to an inlet of the primary reactor; injecting a second stream having liquid water into said first stream; adding a third stream having a preheated fuel to the primary reactor inlet, for dissociation in the primary reactor; introducing a fourth stream having pressurized air to the primary reactor inlet; determining at least one threshold of liquid water volumetric flow above which an increased reaction heat of the primary reactor is required; and controlling a flow rate of the pressurized air to provide the increased reaction heat of the primary reactor. 14. The method of claim 13 which comprises the further step of controlling a volumetric flow of the liquid water injected during the semi-continuous time period to optimize a steam/carbon (S/C) ratio.15. The method of claim 13 which comprises the further step of temporarily increasing the reaction heat of the primary reactor by increasing the flow rate of the pressurized air to adjust an oxygen/carbon (O/C) ratio.16. The method of claim 13 which comprises the further step of temporarily increasing the reaction heat of the primary reactor by increasing the flow rate of the pressurized air to adjust an outlet temperature of the primary reactor.17. A fuel processing system for reforming a hydrocarbon fuel comprising a primary reactor having a reactor inlet and a reactor outlet; a superheater including a first portion having a first inlet, a second inlet, and a first outlet in fluid communication with said inlet of said primary reactor, and a second portion having a third inlet in fluid communication with said reactor outlet; a source of pressurized air in fluid communication with said second inlet; said superheater generating a superheated steam and air stream at the first outlet; and a water supply system including a source of water in fluid communication with said first inlet, an injector in fluid communication with said first outlet, and a controller coupled to said injector for selectively injecting water into said superheated steam and air stream based on an operating state of said primary reactor. 18. The fuel processor system of claim 17, further comprising a vaporizer interconnectably joining said source of water to said superheater, said vaporizer having a vaporizer inlet in fluid communication with said source of water, a vaporizer outlet in fluid communication with said first inlet, and a source of heat, said vaporizer receiving said source of water and utilizing said source of heat for generating a steam stream which is introduced into said first inlet.19. The fuel processor system of claim 18, further comprising a second injector in fluid communication with said first inlet and said water source, said second injector coupled to said controller for selectively injecting water into said steam stream based on an operating state of said primary reactor.20. The fuel processor of claim 17, wherein said source of water is preheated.