Hydrogen generation and energy production assemblies

• US 20060090397A1
• Filed: 10/31/2005
• Published: 05/04/2006
• Est. Priority Date: 10/31/2004
• Status: Abandoned Application

• Current Assignee: IdaTech LLC (IdaTech Ltd.)
• Original Assignee: IdaTech LLC (IdaTech Ltd.)
• Inventors: Edlund, David J., Studebaker, R. Todd
• Application Number:
  US11/263,726
• Publication Number:
  US 20060090397A1
• Time in Patent Office: Days
• US Class Current: 48/61
• CPC Class Codes: B01J 19/249 Plate-type reactors
• CPC Class Codes: B01J 2219/2453 Plates arranged in parallel
• CPC Class Codes: B01J 2219/2458 Flat plates, i.e. plates which are not corrugated or otherwise structured, e.g. plates with cylindrical shape
• CPC Class Codes: B01J 2219/2462 the reactants being in indirect heat exchange with a non reacting heat exchange medium
• CPC Class Codes: B01J 2219/2464 Independent temperature control in various sections of the reactor
• CPC Class Codes: B01J 2219/2465 Two reactions in indirect heat exchange with each other
• CPC Class Codes: B01J 2219/2466 The same reactant stream undergoing different reactions, endothermic or exothermic
• CPC Class Codes: B01J 2219/2467 Additional heat exchange means, e.g. electric resistance heaters, coils
• CPC Class Codes: B01J 2219/247 Feeding means for the reactants
• CPC Class Codes: B01J 2219/2475 Separation means, e.g. membranes inside the reactor
• CPC Class Codes: B01J 2219/2479 Catalysts coated on the surface of plates or inserts
• CPC Class Codes: B01J 2219/2481 Catalysts in granular from between plates
• CPC Class Codes: B01J 2219/2482 Catalytically active foils; Plates having catalytically activity on their own
• CPC Class Codes: B01J 2219/2493 Means for assembling plates together, e.g. sealing means, screws, bolts
• CPC Class Codes: B01J 2219/2495 the plates being assembled interchangeably or in a disposable way
• CPC Class Codes: B01J 2219/2496 Means for assembling modules together, e.g. casings, holders, fluidic connectors
• CPC Class Codes: C01B 2203/0233 the reforming step being a steam reforming step
• CPC Class Codes: C01B 2203/0244 the reforming step being an autothermal reforming step, e.g. secondary reforming processes
• CPC Class Codes: C01B 2203/0261 containing a catalytic partial oxidation step [CPO]
• CPC Class Codes: C01B 2203/0266 containing a decomposition step
• CPC Class Codes: C01B 2203/0405 : Purification by membrane separation
• CPC Class Codes: C01B 2203/043 : Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration
• CPC Class Codes: C01B 2203/0445 : Selective methanation
• CPC Class Codes: C01B 2203/047 : the impurity being carbon monoxide
• CPC Class Codes: C01B 2203/066 : with fuel cells
• CPC Class Codes: C01B 2203/0811 : by combustion of fuel
• CPC Class Codes: C01B 2203/1076 : Copper or zinc-based catalysts
• CPC Class Codes: C01B 2203/146 : At least two purification steps in series
• CPC Class Codes: C01B 2203/1604 : Starting up the process
• CPC Class Codes: C01B 3/384 : the catalyst being continuously externally heated
• CPC Class Codes: C01B 3/501 : by diffusion
• CPC Class Codes: C01B 3/56 : by contacting with solids; Regeneration of used solids C01B3/508 takes precedence
• CPC Class Codes: H01M 2250/30 : Fuel cells in portable systems, e.g. mobile phone, laptop
• CPC Class Codes: H01M 8/04022 : Heating by combustion
• CPC Class Codes: H01M 8/04201 : Reactant storage and supply, e.g. means for feeding, pipes
• CPC Class Codes: H01M 8/04373 : of auxiliary devices, e.g. reformers, compressors, burners
• CPC Class Codes: H01M 8/04776 : at auxiliary devices, e.g. reformer, compressor, burner
• CPC Class Codes: H01M 8/04955 : Shut-off or shut-down of fuel cells
• CPC Class Codes: H01M 8/0612 : from carbon-containing material
• CPC Class Codes: H01M 8/0631 : Reactor construction specially adapted for combination reactor/fuel cell hydrogen C01B3/00; reactors for physicochemical processes B01J19/00
• CPC Class Codes: H01M 8/0668 : Removal of carbon monoxide or carbon dioxide
• CPC Class Codes: H01M 8/0687 : Reactant purification by the use of membranes or filters
• CPC Class Codes: Y02B 90/10 : Applications of fuel cells in buildings
• CPC Class Codes: Y02E 60/50 : Fuel cells

Abstract

Hydrogen generation assemblies, components thereof, and fuel cell systems containing the same. In some embodiments, the hydrogen generation assembly includes a heater assembly having separate startup and primary burner assemblies that utilize different fuels. In some embodiments, the heating assembly is adapted to utilize a volume of liquid fuel to startup the hydrogen generation assembly, while in other embodiments a gaseous fuel is used. In some embodiments, the fuel used during start up includes at least 25 vol % water. In some embodiments, the fuel cell system has a rated power output in the range of 100-1000 watts. In some embodiments, the hydrogen generation assembly is a portable system.

Claims

1. A hydrogen generation assembly, comprising:

a fuel processing assembly, comprising;

a hydrogen-producing region adapted to receive at least a feed stream containing at least a carbon-containing feedstock and to produce a mixed gas steam containing hydrogen gas as a majority component therefrom;

at least one purification region adapted to receive the mixed gas stream and to separate the mixed gas stream into at least one product hydrogen stream and at least one byproduct stream;

a heating assembly adapted to combust a fuel stream to produce a heated exhaust stream for heating at least the hydrogen-producing region, wherein the heating assembly is adapted to receive and combust the byproduct stream when the hydrogen-producing region is producing hydrogen gas;

a flow restrictor between the hydrogen-producing region and the heating assembly, wherein the flow restrictor is adapted to create backpressure in a fluid conduit through which the byproduct stream flows to the heating assembly;

a feedstock delivery system adapted to deliver the feed stream containing at least a carbon-containing feedstock to the hydrogen-producing region of the fuel processing assembly, wherein the feedstock delivery system is in communication with a liquid supply containing the carbon-containing feedstock, wherein the feedstock delivery system comprises;

a pump assembly adapted to draw from the supply a liquid inlet stream containing at least the carbon-containing feedstock and to emit a liquid outlet stream;

an outlet conduit in fluid communication with a delivery conduit and with a recycle conduit, wherein the delivery conduit is in fluid communication with the hydrogen-producing region of the hydrogen-producing fuel processing assembly, and the recycle conduit is in fluid communication with at least one of the liquid supply and an inlet conduit through which the inlet stream is drawn to the pump assembly;

wherein the outlet conduit is adapted to receive the liquid outlet stream and to define a flow path for the liquid outlet stream to the delivery conduit and the recycle conduit;

a flow restrictor adapted to create backpressure in the recycle conduit; and

a pressure-actuated valve adapted to selectively permit liquid in the recycle conduit to bypass the flow restrictor; and

wherein the fuel processing assembly is adapted to produce at least 3 and no more than 20 slm of hydrogen gas when opening at fill capacity.

2. The hydrogen generation assembly of claim 1, wherein the pressure-actuated valve is in fluid communication with a bypass conduit that extends in fluid communication with portions of the recycle conduit upstream and downstream of the flow restrictor.

3. The hydrogen generation assembly of claim 2, wherein the pressure-actuated valve is adapted to be selectively configured between a closed configuration, in which the pressure-actuated valve restricts flow of the liquid outlet stream through the bypass conduit, and an actuated configuration, in which the pressure-actuated valve permits flow of the liquid outlet stream through the bypass conduit, and further wherein the pressure-actuated valve is biased to the closed configuration.

4. The hydrogen generation assembly of claim 3, wherein the pressure-actuated valve is adapted to transition to the actuated configuration when the pressure of the liquid outlet stream in the delivery conduit exceeds a threshold recycle pressure.

5. The hydrogen generation assembly of claim 4, wherein the hydrogen-producing region has a threshold delivery pressure for the portion of the liquid outlet stream delivered thereto, and further wherein the threshold recycle pressure corresponds to the threshold delivery pressure.

6. The hydrogen generation assembly of claim 5, wherein the threshold recycle pressure is less than the threshold delivery pressure.

7. The hydrogen generation assembly of claim 4, wherein the pressure-actuated valve is further adapted to automatically return to the closed configuration.

8. The hydrogen generation assembly of claim 1, wherein the flow restrictor includes a restrictive orifice.

9. The hydrogen generation assembly of claim 1, wherein the feed stream contains water and a carbon-containing feedstock.

10. The hydrogen generation assembly of claim 1, wherein the hydrogen-producing region is adapted to receive up to a threshold flow rate of the outlet stream through the delivery conduit, and further wherein the pump assembly is adapted to emit a liquid outlet stream having a greater flow rate than the threshold flow rate.

11. The hydrogen generation assembly of claim 10, wherein when the hydrogen-producing region is receiving a portion of the liquid outlet stream and producing hydrogen gas therefrom, the pump assembly is adapted to emit a flow rate of the liquid outlet stream that exceeds the threshold flow rate.

12. The hydrogen generation assembly of claim 1, wherein the hydrogen-producing region and at least one purification region are housed within a sealed shell.

13. The hydrogen generation assembly of claim 1, in combination with a fuel cell stack adapted to produce an electric current from an oxidant and at least a portion of the product hydrogen stream, wherein the fuel cell stack has a rated power output in the range of 100-1000 watts.

14. The hydrogen generation assembly of claim 13, wherein the fuel processing assembly is adapted to produce less than 10 slm of hydrogen gas when operating at full capacity, and further wherein the fuel cell stack has a rated power output of 600 watts or less.

15. The hydrogen generation assembly of claim 13, wherein the fuel processing assembly is adapted to produce less than 5 slm of hydrogen gas when operating at full capacity, and further wherein the fuel cell stack has a rated power output of 300 watts or less.

16. The hydrogen generation assembly of claim 1, wherein the heating assembly is in thermal communication with the hydrogen-producing region, wherein the heating assembly comprises at least one fuel chamber and at least one heating and ignition source;

wherein the at least one fuel chamber is adapted to receive at least one fuel stream at a first temperature, the at least one fuel stream comprising a liquid, combustible, carbon-containing fuel having an ignition temperature greater than said first temperature, and further wherein the at least one heating and ignition source is adapted to heat at least a portion of the fuel chamber to raise the temperature of at least a portion of the carbon-containing fuel to a second temperature at least as great as the ignition temperature and to ignite the carbon-containing fuel.

17. The hydrogen generation assembly of claim 16, wherein the feedstock delivery system is further adapted to deliver the at least one fuel stream to the at least one fuel chamber.

18. The hydrogen generation assembly of claim 17, wherein the feed stream and the fuel stream each comprise at least one common carbon-containing component.

19. The hydrogen generation assembly of claim 17, wherein the feed stream and the fuel stream each comprise at least 25 vol % water and at least one water-miscible carbon-containing component.

20. The hydrogen generation assembly of claim 17, wherein the heating and ignition source comprises an electrical resistance heating element adapted to be heated to a heating element ignition temperature at which the heating element is adapted to ignite the carbon-containing fuel in the chamber.

21. The hydrogen generation assembly of claim 17, wherein the fuel chamber includes an at least substantially open reservoir adapted to receive and at least temporarily store a volume of the liquid combustible carbon-containing fuel.

22. The hydrogen generation assembly of claim 17, wherein the heating assembly further comprises a transport medium disposed in the fuel chamber.

23. The hydrogen generation assembly of claim 22, wherein the transport medium is adapted to at least temporarily absorb the liquid combustible carbon-containing fuel.

24. The hydrogen generation assembly of claim 22, wherein the transport medium is adapted to define a flame-holding surface for the fuel.

25. In a hydrogen generation assembly having a hydrogen-producing region having a minimum hydrogen-production temperature and adapted to receive at least one feed stream comprising at least a carbon-containing feedstock and to produce an output stream comprising hydrogen gas as a majority component, a method of starting up and operating the hydrogen generation assembly, the method comprising:

delivering at least one fuel stream comprising a liquid, combustible, carbon-containing fuel to a heating assembly at a first temperature, wherein the carbon-containing fuel has an ignition temperature greater than the first temperature;

heating said fuel stream in the heating assembly with at least one heating and ignition source to a second temperature at least as great as the ignition temperature;

igniting said fuel stream in the heating assembly with the at least one heating and ignition source to produce a combustion stream;

heating the hydrogen-producing region of the hydrogen generation assembly with the combustion stream to a predetermined temperature related to the minimum hydrogen-production temperature of the hydrogen-producing region;

drawing a liquid feed stream from a supply containing at least one carbon-containing feedstock for the hydrogen-producing region of a hydrogen-producing fuel cell system;

pumping a flow of the liquid feed stream through an outlet conduit that is in fluid communication with a delivery conduit and a first portion of a recycle conduit, wherein the delivery conduit is in fluid communication with the hydrogen-producing region of the hydrogen generation assembly, wherein the recycle conduit is adapted to provide a flow path to return the liquid feed stream to at least one of the supply and a location upstream from a delivery mechanism that is adapted to propel the liquid stream to the outlet conduit, and further wherein the pumping step produces a flow of the liquid stream that exceeds the capacity of the delivery conduit, with an excess portion of the flow flowing into the recycle conduit;

regulating the distribution of the flow between the delivery conduit and the recycle conduit, wherein the regulating includes creating backpressure in the recycle conduit with a flow restrictor that separates the recycle conduit into at least a first portion that extends between the outlet conduit and the flow restrictor and a second portion that extends from the flow restrictor, wherein the regulating further includes selectively permitting the excess portion of the flow to bypass the flow restrictor by flowing through a bypass conduit in fluid communication with portions of the recycle conduit upstream and downstream of the flow restrictor; and

receiving at least a portion of the flow in the hydrogen-producing region and producing the output stream containing hydrogen gas therefrom.

26. The method of claim 25, wherein the drawing step occurs after the hydrogen-producing region is heated to at least the predetermined temperature.

27. The method of claim 25, wherein the hydrogen-producing region is a reforming region that contains a reforming catalyst.

28. The method of claim 25, wherein the method further includes producing an electrical power output from an oxidant and at least a portion of the stream containing hydrogen gas.