Fuel processor for use with portable fuel cells
View Patent ↗The invention relates to a fuel processor that produces hydrogen from a fuel. The fuel processor comprises a reformer and a heater. The reformer includes a catalyst that facilitates the production of hydrogen from the fuel; the heater provides heat to the reformer. Multipass reformer and heater chambers are described that reduce fuel processor size. Single layer fuel processors include reformer and heater chambers in a compact form factor that is well suited for portable applications. Some fuel processors described herein place an electrically resistive material in contact with a thermally conductive material to heat fuel entering the fuel processor. This is particularly useful during start-up of the fuel processor. Fuel processors described may also include features that facilitate assembly.
1. A method for producing hydrogen in a fuel processor, the method comprising:
turning on an electrical heater;
passing fuel over a surface of the electrical heater;
vaporizing at least a portion of the fuel using the electrical heater to generate gaseous fuel; providing the gaseous fuel to a burner in the fuel processor;
combusting the gaseous fuel in the burner to generate heat;
transferring at least a portion of the heat from the burner to a reformer included in the fuel processor;
providing fuel to the reformer; and
catalytically processing the reformer fuel to produce hydrogen; and
wherein the fuel processor includes a monolithic structure having a common material included in walls that define the reformer and the burner, and wherein the reformer includes a first reformer chamber for outputting hydrogen and any unprocessed fuel and a second reformer chamber for receiving and processing fuel from the first reformer chamber, wherein the reformer is configured such that fuel flows through the first reformer chamber in a direction parallel to the fuel flow direction through the second reformer chamber.
2. The method of claim 1 , further comprising increasing a burner duty for the burner after the burner starts catalytically generating heat.
3. The method of claim 1 , further comprising varying combustion stoichiometry for the burner after the burner starts catalytically generating heat.
4. The method of claim 1 , further comprising turning off the electrical heater when the burner starts catalytically generating heat.
5. The method of claim 1 , further comprising providing oxygen to the burner.
6. The method of claim 1 , further comprising increasing fuel flow to the burner after the fuel is initially combusted in the burner to generate heat.
7. The method of claim 1 , wherein
the first reformer chamber including a first reformer chamber inlet configured to receive the fuel, including a catalyst capable of processing the fuel to produce hydrogen, and including a first reformer chamber outlet,
the second reformer chamber including a second reformer chamber inlet, including a catalyst capable of processing the portion of the fuel from the first reformer chamber to produce hydrogen, and including a second reformer chamber outlet configured to output hydrogen from the second reformer chamber,
wherein the reformer is configured such that fuel flows from the first reformer chamber inlet to the first reformer chamber outlet and from the second reformer chamber inlet to the second reformer chamber outlet.
8. The method of claim 7 , wherein fuel flows from the first reformer chamber inlet to the first reformer chamber outlet in a first direction, and wherein fuel flows from the second reformer chamber inlet to the second reformer chamber outlet in a second direction, wherein the first direction and the second direction are in about opposite directions.
9. The method of claim 8 , wherein the reformer further includes: a third reformer chamber including a third reformer chamber inlet that receives at least a portion of the fuel from the second reformer chamber, including a catalyst capable of processing the portion of the fuel from the second reformer chamber to produce hydrogen, and output the hydrogen and any unprocessed fuel from the third reformer chamber.
10. The method of claim 9 , wherein the reformer is configured such that the fuel flows through the third reformer chamber from the third reformer chamber inlet to the third reformer chamber outlet in a third direction,
the first direction and the third direction are in about the same direction, and
the second direction is in a direction that is about opposite to the first direction and the third direction.
11. The method of claim 10 , wherein the reformer or burner includes an internal wall with a chamfered corner or side.
12. The method of claim 10 , wherein the first reformer chamber includes a largest orthogonal dimension that is substantially parallel to a largest orthogonal dimension for the second reformer chamber.
13. The method of claim 10 , wherein the first reformer chamber includes a cross section that varies along a length of the first reformer chamber.
14. The method of claim 1 , wherein the fuel flows through the reformer in a direction that at least partially circles an outside cross-sectional perimeter for the burner.
15. The method of claim 1 , wherein the burner includes multiple burner chambers and the reformer at least bilaterally neighbors one burner chamber.
16. The method of claim 1 , wherein the reformer includes two reformer chambers that bilaterally neighbor the burner.
17. The method of claim 16 , wherein the reformer trilaterally neighbors the burner.
18. The method of claim 16 , wherein the reformer quadrilaterally neighbors the burner.
19. The method of claim 1 , wherein the fuel processor comprises a non-planar wall that is shared, by the reformer and the burner and permits conductive thermal communication from the burner to the reformer in orthogonal directions.