Thermally primed hydrogen-producing fuel cell system
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
H01M-008/00
H01M-008/04
출원번호
UP-0229365
(2005-09-16)
등록번호
US-7659019
(2010-04-02)
발명자
/ 주소
Edlund, David J.
출원인 / 주소
Idatech, LLC
대리인 / 주소
Dascenzo Intellectual Property Law, P.C.
인용정보
피인용 횟수 :
12인용 특허 :
48
초록▼
Thermally primed fuel processing assemblies and hydrogen-producing fuel cell systems that include the same. The thermally primed fuel processing assemblies include at least one hydrogen-producing region housed within an internal compartment of a heated containment structure. In some embodiments, the
Thermally primed fuel processing assemblies and hydrogen-producing fuel cell systems that include the same. The thermally primed fuel processing assemblies include at least one hydrogen-producing region housed within an internal compartment of a heated containment structure. In some embodiments, the heated containment structure is an oven. In some embodiments, the compartment also contains a purification region and/or heating assembly. In some embodiments, the containment structure is adapted to heat and maintain the internal compartment at or above a threshold temperature, which may correspond to a suitable hydrogen-producing temperature. In some embodiments, the containment structure is adapted to maintain this temperature during periods in which the fuel cell system is not producing power and/or not producing power to satisfy an applied load to the system. In some embodiments, the fuel cell system is adapted to provide backup power to a power source, which may be adapted to power the containment structure.
대표청구항▼
The invention claimed is: 1. A thermally primed hydrogen-producing fuel cell system, comprising: a fuel processing assembly comprising a hydrogen-producing region that contains a reforming catalyst, wherein the hydrogen-producing region is adapted to receive a feed stream containing at least a carb
The invention claimed is: 1. A thermally primed hydrogen-producing fuel cell system, comprising: a fuel processing assembly comprising a hydrogen-producing region that contains a reforming catalyst, wherein the hydrogen-producing region is adapted to receive a feed stream containing at least a carbon-containing feedstock and water and, when the hydrogen-producing region is at least within a hydrogen-producing temperature range, to produce from the feed stream a reformate stream containing hydrogen gas as a majority component; a fuel cell stack adapted to receive an oxidant and a fuel stream containing hydrogen gas produced in the hydrogen-producing region, wherein the fuel cell stack is further adapted to generate a fuel cell power output from the fuel stream and the oxidant to satisfy an applied load from an energy-consuming device when a primary power source that is normally adapted to satisfy the applied load is not providing a primary power output to satisfy the applied load; a containment structure including an enclosure that defines an internal compartment containing at least the hydrogen-producing region of the fuel processing assembly; a first heating assembly adapted to heat and maintain at least the internal compartment of the containment structure at or above a threshold temperature within the hydrogen-producing temperature range during periods in which there is no demand for the fuel cell system to generate the fuel cell power output, the fuel processing assembly is not producing the reformate stream, and the primary power source is providing the primary power output to satisfy the applied load; and a second heating assembly adapted to provide heat to at least the hydrogen-producing region of the fuel processing assembly when the fuel processing assembly is producing hydrogen gas and the primary power source is not providing the primary power output to satisfy the applied load; wherein the thermally primed hydrogen-producing fuel cell system is adapted to have a thermally biased response time to produce hydrogen gas with the fuel processing assembly upon a demand for the fuel cell system to generate the fuel cell power output, wherein the thermally biased response time is shorter than a startup response time of a comparative hydrogen-producing fuel cell system that includes the second heating assembly but that does not include the first heating assembly. 2. The fuel cell system of claim 1, wherein the first heating assembly is adapted to be powered by the primary power source when the primary power source is configured to satisfy the applied load from the energy-consuming device. 3. The fuel cell system of claim 2, wherein the primary power source includes an electrical grid. 4. The fuel cell system of claim 1, wherein the first heating assembly is adapted to stop heating the internal compartment when the fuel processing assembly is producing hydrogen gas. 5. The fuel cell system of claim 1, wherein the second heating assembly is positioned within the enclosure and is adapted to receive and combust a gaseous fuel stream to provide heat to at least the hydrogen-producing region of the fuel processing assembly when the fuel processing assembly is producing hydrogen gas. 6. The fuel cell system of claim 1, wherein the hydrogen-producing region is adapted to produce hydrogen gas from the feed stream, if delivered thereto, when the hydrogen-producing region is at or above the threshold temperature. 7. The fuel cell system of claim 6, wherein the carbon-containing feedstock is methanol and the threshold temperature is at least 350° C. 8. The fuel cell system of claim 6, wherein the carbon-containing feedstock is a hydrocarbon and the threshold temperature is at least 700° C. 9. The fuel cell system of claim 1, wherein the enclosure is an insulated enclosure having an internal surface, which defines at least in part the internal compartment, and an exterior surface, and further wherein the enclosure is adapted to maintain the exterior surface at a temperature that is less than 100° C when the threshold temperature is at least 350° C. 10. The fuel cell system of claim 9, wherein the enclosure is adapted to maintain the exterior surface at a temperature that is less than 50° C when the threshold temperature is at least 350° C. 11. The fuel cell system of claim 1, wherein the fuel processing assembly further comprises at least one purification region adapted to receive at least a portion of the reformate stream and to produce a product hydrogen stream having at least one of a greater concentration of hydrogen gas and a lower concentration of at least one of the other gases present in the reformate stream. 12. The fuel cell system of claim 11, wherein the fuel processing assembly includes at least one purification region within the internal compartment. 13. The fuel cell system of claim 11, wherein the fuel processing assembly includes at least one purification region external the enclosure. 14. The fuel cell system of claim 1, wherein the fuel cell system further includes an energy storage device adapted to satisfy an applied load from at least one of the fuel cell system and an energy-consuming device. 15. The fuel cell system of claim 14, wherein, the energy storage device has a maximum charge that is adapted to satisfy an applied load for a time period, and further wherein the time period is greater than the thermally biased response time. 16. The fuel cell system of claim 15, wherein the time period is less than the startup response time of the comparative hydrogen-producing fuel cell system. 17. The fuel cell system of claim 1, wherein the thermally biased response time is less than two minutes. 18. The fuel cell system of claim 1, wherein the thermally biased response time is less than one minute. 19. The fuel cell system of claim 1, wherein the thermally biased response time is less than forty-five seconds. 20. A thermally primed hydrogen-producing fuel cell system, comprising: a fuel processing assembly comprising a hydrogen-producing region that contains a reforming catalyst, wherein the hydrogen-producing region is adapted to receive a feed stream containing at least a carbon-containing feedstock and water and, when the hydrogen-producing region is at least within a hydrogen-producing temperature range, to produce from the feed stream a reformate stream containing hydrogen gas as a majority component; a fuel cell stack adapted to receive an oxidant and a fuel stream containing hydrogen gas produced in the hydrogen-producing region, wherein the fuel cell stack is further adapted to generate a fuel cell power output from the fuel stream and the oxidant to satisfy an applied load from an energy-consuming device when a primary power source that is normally adapted to satisfy the applied load is not providing a primary power output to satisfy the applied load; a containment structure including an enclosure that defines an internal compartment containing at least the hydrogen-producing region of the fuel processing assembly; a first heating assembly adapted to heat and maintain at least the internal compartment of the containment structure at or above a threshold temperature within the hydrogen-producing temperature range during periods in which there is no demand for the fuel cell system to generate the fuel cell power output, the fuel processing assembly is not producing the reformate stream, and the primary power source is providing the primary power output to satisfy the applied load; and a second heating assembly adapted to provide heat to at least the hydrogen-producing region of the fuel processing assembly when the fuel processing assembly is producing hydrogen gas and the primary power source is not providing the primary power output to satisfy the applied load; wherein the thermally primed hydrogen-producing fuel cell system is adapted to have a thermally biased response time to produce hydrogen gas with the fuel processing assembly upon a demand for the fuel cell system to generate the fuel cell power output, wherein the thermally biased response time is shorter than a startup response time of a comparative hydrogen-producing fuel cell system that does not heat and maintain a respective hydrogen-producing region within a respective hydrogen-producing temperature range during periods in which there is no demand for the comparative hydrogen-producing fuel cell system to generate a respective fuel cell power output. 21. A thermally primed hydrogen-producing fuel cell system, comprising: a fuel processing assembly comprising a hydrogen-producing region that contains a reforming catalyst, wherein the hydrogen-producing region is adapted to receive a feed stream containing at least a carbon-containing feedstock and water and, when the hydrogen-producing region is at least within a hydrogen-producing temperature range, to produce from the feed stream a reformate stream containing hydrogen gas as a majority component; a fuel cell stack adapted to receive an oxidant and a fuel stream containing hydrogen gas produced in the hydrogen-producing region, wherein the fuel cell stack is further adapted to generate a fuel cell power output from the fuel stream and the oxidant to satisfy an applied load from an energy-consuming device when a primary power source that is normally adapted to satisfy the applied load is not providing a primary power output to satisfy the applied load; means for heating and maintaining the hydrogen-producing region within the hydrogen-producing temperature range during periods in which there is no demand for the fuel cell system to generate the fuel cell power output, the fuel processing assembly is not producing the reformate stream, and the primary power source is providing the primary power output to satisfy the applied load; wherein the thermally primed hydrogen-producing fuel cell system is adapted to have a thermally biased response time to produce hydrogen gas with the fuel processing assembly upon a demand for the fuel cell system to generate the fuel cell power output, wherein the thermally biased response time is shorter than a startup response time of a comparative hydrogen-producing fuel cell system that does not include the means for heating and maintaining.
연구과제 타임라인
LOADING...
LOADING...
LOADING...
LOADING...
LOADING...
이 특허에 인용된 특허 (48)
Palmer Ian (Cumbria GBX) Seymour Clive M. (Cumbria GBX) Dams Robert A. J. (West Sussex GBX), Application of fuel cells to power generation systems.
Ishimaru Kimio (Nara JPX) Nakashiba Akio (Katano JPX) Koga Masahiro (Kawasaki JPX) Ohnishi Hisao (Osaka JPX) Kawahara Hideaki (Yao JPX), Energy supply system for optimizing energy cost, energy consumption and emission of pollutants.
Misage Robert (Manchester CT) Scheffler Glenn W. (Tolland CT) Setzer Herbert J. (Ellington CT) Margiott Paul R. (Manchester CT) Parenti ; Jr. Edmund K. (Manchester CT), Heat exchanger for fuel cell power plant reformer.
Matsubayashi Takaaki,JPX ; Oda Katsuya,JPX ; Miyake Yasuo,JPX, Hydrogen production apparatus and method operable without supply of steam and suitable for fuel cell systems.
David J. Edlund ; Charles R. Hill ; William A. Pledger ; R. Todd Studebaker, Hydrogen purification devices, components and fuel processing systems containing the same.
Watkins David S. (Coquitlam) Dircks Kenneth W. (North Vancouver) Epp Danny G. (Tsawwassen) Merritt Robert D. (Vancouver) Gorbell Brian N. (Vancouver CAX), Integrated fuel cell power generation system.
Chen Jeffrey S. ; Huang Wenhua ; Acker William P., Integrated full processor, furnace, and fuel cell system for providing heat and electrical power to a building.
Fletcher Nicholas J.,CAX ; Boehm Gustav A.,DEX ; Pow Eric G.,CAX, Method and apparatus for commencing operation of a fuel cell electric power generation system below the freezing temper.
Ankersmit Jan H. (Schiedam NLX) Hendriks Rudolf (Velp NLX) Blomen Leo J. M. J. (Vooreschoten NLX), Process and installation for the combined generation of electrical and mechanical energy.
Krumm Hagen (Frankfurt am Main DT) Jockel Heinz (Klein-Gerau DT) VON Walter Klaus (Arnoldshain DT) Restin Kurt (Berlin DT) Kuhn Robert (Berlin DT), Process for supplying heat to chemical reactions.
Wilkinson David P. (Vancouver CAX) Voss Henry H. (West Vancouver CAX) Watkins David S. (Coquitlam CAX) Prater Keith B. (Vancouver CAX), Solid polymer fuel cell systems incorporating water removal at the anode.
Isomura Manabu,JPX ; Soma Takao,JPX ; Takahashi Tomonori,JPX, System for production of high-purity hydrogen, process for production of high-purity hydrogen, and fuel cell system.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.