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    • 2. 发明专利
    • Kompakte Brennstoffgas-Reformeranordnung
    • DE10083881B3
    • 2012-02-16
    • DE10083881
    • 2000-01-19
    • UTC FUEL CELLS LLC N D GES D STAATES DELAWARE
    • LESIEUR ROGER RCORRIGAN THOMAS J
    • C01B3/32F23D14/18B01J8/02B01J19/24C01B3/38C01B3/48C01B3/58H01M8/06
    • Kohlenwasserstoff-Brennstoffgas-Dampf-Reformeranordnung, aufweisend: a) eine Einlass-Verteilereinrichtung zum Lenken einer Mischung aus Brennstoffgas und Dampf in die Anordnung; b) einen Reformerabschnitt, der mit der Einlass-Verteilereinrichtung verbunden ist, um eine Strömung der Brennstoffgas- und Dampfmischung aufzunehmen, wobei der Reformerabschnitt aus einer ersten und einer zweiten voneinander beabstandeten Platte mit einem offenzelligen monolithischen Schaummaterial-Element, welches sandwichartig zwischen der ersten und zweiten Platte angeordnet ist, gebildet ist, wobei das monolithische, offenzellige Element einen diffusen Gasströmungsweg in den Reformerabschnitt liefert; c) einen Regenerator-Wärmetauscher-Abschnitt, der dem Reformerabschnitt benachbart ist, wobei der Regenerator-Wärmetauscher-Abschnitt aus der ersten Platte und einer dritten Platte, welche von der ersten Platte an deren der zweiten Platte entgegengesetzten Seite beabstandet ist, gebildet ist, wobei der Regenerator-Wärmetauscher-Abschnitt ferner ein monolithisches, offenzelliges Schaummaterial-Element beinhaltet, welches sandwichartig zwischen der ersten und der dritten Platte angeordnet ist, wobei das monolithische, offenzellige Element einen diffusen Gasströmungsweg in dem Regenerator-Wärmetauscher-Abschnitt bildet, wobei die erste Platte einen...
    • 5. 发明专利
    • DE19983854T5
    • 2008-08-28
    • DE19983854
    • 1999-12-17
    • UTC FUEL CELLS LLC N D GES D S
    • LESIEUR ROGER RBONVILLE LEONARD J JUNGAROW JAYCORRIGAN THOMAS JPRESTON JOHN L JUN
    • C01B3/32H01M8/04B01J20/02C01B3/38H01M8/00H01M8/06H01M8/10
    • A fuel gas processing system is operable to remove substantially all of the sulfur present in a hydrocarbon fuel supply used to power a fuel cell power plant in a mobile vehicular environment. The power plant fuel can be gasoline, diesel fuel, kerosene, fuel oil, natural gas, or another fuel which contains relatively high levels of organic sulfur compounds such as mercaptans, sulfides, disulfides, and the like. The hydrocarbon fuel supply is passed through a nickel reactant desulfurizer bed wherein essentially all of the sulfur in the organic sulfur compounds react with the nickel reactant, and are converted to nickel sulfide while the desulfurized fuel continues through the remainder of the fuel processing system. The fuel cell power plant and the processing system can be used to power a mobile vehicle, such an automobile, truck, bus, or the like. An auxiliary supply of hydrogen is provided in order to power the fuel cell power plant during start up of the fuel processing system. A second auxiliary supply of desulfurized fuel is also provided to operate the fuel cell power plant during an interim period until the highest temperature component of the fuel processing system is brought up to operational temperatures during the start up protocol.
    • 7. 发明专利
    • DE60031379T2
    • 2007-12-06
    • DE60031379
    • 2000-02-17
    • UTC FUEL CELLS LLC N D GES D S
    • CORRIGAN JBONVILLE JLESIEUR RHILDRETH WLUKIANOFF G
    • B01J35/04H01M8/06H01M8/24
    • A fuel gas catalyst bed for use in a fuel cell power plant is formed from a monolithic open cell foam component, the open cell lattice of which forms gas passages through the catalyst bed. The monolithic component has a lattice of internal open cells which are both laterally and longitudinally interconnected so as to produce a diffuse gas flow pattern through the catalyst bed. All areas of the monolithic component which form the gas flow pattern are provided with an underlying high porosity wash coat layer. The porous surface of the wash coat layer is provided with a nickel catalyst layer, or a noble metal catalyst layer, such as platinum, rhodium, palladium, or the like, over which the gas stream being treated flows. The base foam lattice can be a metal such as aluminum, stainless steel, a steel-aluminum alloy, a nickel alloy, a ceramic, or the like material which can be wash coated. The use of an open cell lattice as the basis of a catalyst bed enables the formation of very compact, light weight and high surface area catalyst bed with excellent gas flow-through characteristics.