U.S. patents available from 1976 to present.
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Electrochemical cell apparatus having an integrated reformer-mixer nozzle-mixer diffuser

Patent 5047299 Issued on September 10, 1991. Estimated Expiration Date: Icon_subject July 25, 2010. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3718506

Fuel cell generator
Patent #: 4395468
Issued on: 07/26/1983
Inventor: Isenberg

High temperature solid electrolyte fuel cell configurations and interconnections
Patent #: 4490444
Issued on: 12/25/1984
Inventor: Isenberg

Reforming of fuel inside fuel cell generator
Patent #: 4729931
Issued on: 03/08/1988
Inventor: Grimble

Corner heating in rectangular solid oxide electrochemical cell generators Patent #: 4808491
Issued on: 02/28/1989
Inventor: Reichner

Inventor

Assignee

Application

No. 559111 filed on 07/25/1990

US Classes:

429/20, By heating or cooling429/30, Solid electrolyte429/34, Housing member, seal, spacer or fluid distributing or directing means429/39And fluid directing means

Examiners

Primary: Skapars, Anthony

Attorney, Agent or Firm

International Class

H01M 008/12

Abstract

An electrochemical apparatus (10) is made having a generator section (22) containing electrochemical cells (16), a fresh gaseous feed fuel inlet (28), a gaseous feed oxidant inlet (30), and at least one hot gaseous spent fuel recirculation channel (46), where the spent fuel recirculation channel (46), passes from the generator chamber (22) to combine with the fresh feed fuel inlet (28) to form a reformable mixture, where a reforming chamber (54) contains an outer portion containing reforming material (56), an inner portion preferably containing a mixer nozzle (50) and a mixer-diffuser (52), and a middle portion (64) for receiving spent fuel, where the mixer nozzle (50) and mixer-diffuser (52) are preferably both within the reforming chamber (54) and substantially exterior to the main portion of the apparatus, where the reformable mixture flows up and then backward before contacting the reforming material (56), and the mixer nozzle (50) can operate below 400° C.

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