초록 ▼

Embodiments of a compact pressure swing reformer are disclosed. Certain embodiments have a construction comprising multiple rotating reformer beds, high temperature rotary valves at the bed ends, and E-seals to seal the beds to the valves. Several possible designs for introducing reactants into the

Embodiments of a compact pressure swing reformer are disclosed. Certain embodiments have a construction comprising multiple rotating reformer beds, high temperature rotary valves at the bed ends, and E-seals to seal the beds to the valves. Several possible designs for introducing reactants into the beds also are disclosed. The multiple reformer beds are configured to provide for pressure equalization and ‘steam push’. The compact pressure swing reformer is suitable for use in fuel cell vehicle applications.

대표청구항 ▼

1. A pressure swing reformer, comprising: a reformer bed assembly comprising greater than two reactor beds, wherein each of the reactor beds has a feed end and a product end, wherein at least one of the reactor beds contains a reforming catalyst;one or more valves located at the feed end of each of

1. A pressure swing reformer, comprising: a reformer bed assembly comprising greater than two reactor beds, wherein each of the reactor beds has a feed end and a product end, wherein at least one of the reactor beds contains a reforming catalyst;one or more valves located at the feed end of each of the reactor beds;one or more valves located at the product end of each of the reactor beds; andone or more interconnections between the one or more valves located at the feed end and the one or more valves located at the product end of each of the reactor beds, wherein the one or more interconnections are configured to provide for pressure equalizations between the reactor beds. 2. The pressure swing reformer of claim 1 wherein the one or more interconnections allow for an interconnection between the product ends of one or more pairs of the reactor beds. 3. The pressure swing reformer of claim 1 wherein the one or more interconnections allow for an interconnection between the product ends of more than two of the reactor beds. 4. The pressure swing reformer of claim 1 wherein the one or more interconnections allow for interconnection between the feed ends of more than two reactor beds. 5. The pressure swing reformer of claim 1 wherein the reformer bed assembly comprises nine reactor beds. 6. The pressure swing reformer of claim 1 further comprising one or more feed end rotary valves, wherein the one or more valves located at the feed end of each of the reactor beds are incorporated into the one or more feed end rotary valves. 7. The pressure swing reformer of claim 1 further comprising one or more product end rotary valves, wherein the one or more valves located at the product end of each of the reactor beds are incorporated into the one or more product end rotary valves. 8. The pressure swing reformer of claim 1, further comprising one or more equalization ports operatively located between the one or more valves located at the feed end of each of the reactor beds and the product end, wherein the one or more interconnections are configured to provide for pressure equalizations between the reactor beds. 9. A method of pressure swing reforming fuel and water, the method comprising: providing a pressure swing reformer comprising:a reformer bed assembly comprising greater than two reactor beds, wherein each of the reactor beds has a feed end and a product end;one or more valves located at the feed end of each of the reactor beds;one or more valves located at the product end of each of the reactor beds; andone or more interconnections between the one or more valves located at the feed end and the one or more valves located at the product end of each of the reactor beds, wherein the one or more interconnections are configured to provide for pressure equalizations between the reactor beds; and sequentially performing in each reactor bed of the reformer bed assembly the repeated steps of:pressurizing a first one of the reactor beds at its feed end with fuel and water while the one or more valves located at the product end thereof is kept closed;reforming fuel and water in the first one of the reactor beds while continuing to admit fuel and water at the feed end thereof and while the one or more valves located at the product end thereof is kept open, thereby preserving a syngas product from the product end thereof;supply equalizing from the first one of the reactor beds, wherein a product gas from one of the ends of the first one of the reactor beds is supplied to one of the ends of a second one of the reactor beds, wherein the product gas from the first one of the reactor beds has a higher pressure than a pressure of the second one of the reactor beds;exhausting a remaining portion of the product gas from the first one of the reactor beds from its feed end;regenerating the first one of the reactor beds by supplying fuel and oxidant to the product end thereof while the one or more valves located at the feed end thereof is open, thereby exhausting regeneration fuel gas from the feed end thereof; andpressure equalizing the first one of the reactor beds, wherein a product gas from one of the ends of a third one of the reactor beds is provided to one of the ends of the first one of the reactor beds, wherein the product gas from the third one of the reactor beds has a higher pressure than a pressure of the first one of the reactor beds. 10. The method of claim 9 wherein the supply equalizing step further comprises supplying the product gas from the product end of the first one of the reactor beds-to the product end of the second one of the reactor beds. 11. The method of claim 9 wherein the pressure equalizing step further comprises providing the product gas from the product end of the third one of the reactor beds to the product end of the first one of the reactor beds. 12. The method of claim 9, further comprising: supply purging from the first one of the reactor beds following the supply equalizing step wherein product gas from the product end of the first one of the reactor beds is supplied to the product end of a fourth one of the reactor beds wherein the at least one valve located at the product end of the fourth one of the reactor beds is open to ambient; andpurging the first one of the reactor beds following the regenerating step, wherein a product gas from the product end of a fifth one of the reactor beds is provided to the product end of the first one of the reactor beds while the valves located at the feed end of the first one of the reactor beds is open to ambient. 13. The method of claim 9 further comprising a steam pushing step comprising pushing syngas out of the first one of the reactor beds with high pressure steam following the reforming step, whereby the supply and pressure equalizing steps reduce the amount of high pressure steam employed. 14. The method of claim 9 wherein the exhausting step further comprises any of: opening the feed end of the first one of the reactor beds to ambient,externally purging the first one of the reactor beds, andevacuating the first one of the reactor beds. 15. The method of claim 9 further comprising additional supply equalizing and pressure equalizing steps comprising acts comprising purging, regeneration, and removal of one or more gases from at least one of the reactor beds. 16. The method of claim 9 further comprising providing a pressure swing reformer comprising nine reactor beds. 17. The method of claim 9 further comprising providing a pressure swing reformer comprising: a feed end rotary valve, wherein the one or more valves located at the feed ends of each of the reactor beds are incorporated into the feed end rotary valve; anda product end rotary valve, wherein the one or more valves located at the product ends of each of the reactor beds are incorporated into the product end rotary valve.