Abstract: Described are SCR catalyst systems comprising a first SCR catalyst composition and a second SCR catalyst composition arranged in the system, the first SCR catalyst composition having a faster DeNOx response time when exposed to ammonia than the second catalyst composition and the second SCR catalyst composition has a higher steady state DeNOx performance than the first catalyst composition. The SCR catalyst systems are useful in methods and systems to catalyze the reduction of nitrogen oxides in the presence of a reductant.

Abstract: Described are SCR catalyst systems comprising a first SCR catalyst composition and a second SCR catalyst composition arranged in the system, the first SCR catalyst composition having a faster DeNOx response time when exposed to ammonia than the second catalyst composition and the second SCR catalyst composition has a higher steady state DeNOx performance than the first catalyst composition. The SCR catalyst systems are useful in methods and systems to catalyze the reduction of nitrogen oxides in the presence of a reductant.

Abstract: The invention relates to a reformer for reacting fuel and oxidant into reformate, comprising a reforming zone (12) which can receive a supply of fuel, and from an upstream oxidation zone, a mixture of oxidant and at least partially oxidized fuel for catalytic reaction into the reformate. To boost the reforming efficiency it is proposed that the reforming zone (12) now comprises a first (32) and second (48) catalytic reaction zone in the streaming direction of the gas flow, each arranged separately from the other and interposed by a non-catalytic active homogenization zone (44) for homogenizing gas components emerging from the first reaction zone (32). The configuration in accordance with the invention now achieves that after first partial reforming the gas is homogenized to achieve a more efficient second partial reforming.

Abstract: The invention relates to a reformer for reacting fuel and oxidant to a gaseous reformate, comprising an oxidation zone, an evaporation zone and a zone for catalytic H2 generation, the oxidation zone being capable of receiving a supply of a gaseous mixture of fuel and oxidant for oxidation in generating an oxidant-containing exhaust gas, the evaporation zone being capable of receiving a supply of fuel and an evaporator gas for generating an evaporator gas mixture containing fuel, and the zone for catalytic H2 generation being capable of receiving a supply of an ignitable reforming gas mixture containing evaporated fuel and an oxidant-containing exhaust gas to generate the gaseous reformate.

Abstract: The invention relates to a method for regenerating a reformer fed with a mixture of fuel and an oxidant having a mean air number ?1 in continuous reformer operation, the air number being varied for the purpose of regenerating the reformer. In accordance with the invention it is provided for that regeneration occurs in a shutoff phase of the reformer in that the reformer is operated during several successive time intervals with an air number ?2 higher than in reformer operation (?2>?1). Again in accordance with the invention it may be provided for that regeneration occurs in a starting phase of the reformer in that the reformer is continually operated with an air number increased as compared to reformer operation ?2>?1 until a critical temperature threshold is attained. The invention relates furthermore to a system including a reformer and a controller for implementing a method in accordance with the invention.

Abstract: The invention relates to a reformer (10) comprising a first media feeder portion (12) for receiving a supply of fuel (14) and oxidant (16), following the first media feeder portion an oxidation zone (18) in which the media supplied to the first media feeder portion react at least in part into flue gas (20), a second media feeder portion (22) for receiving at least a supply of fuel (24), a mixture formation zone following the oxidation zone (18) and the second media feeder portion and in which a fuel/flue gas mixture (28) can be generated, and following the mixture formation zone (26) a reforming zone in which the fuel/flue gas mixture (28) is catalytically reformable. In accordance with the invention it is provided for that the volume of the mixture formation zone is in the range of 20 to 90 cm3.

Abstract: The invention relates to a reformer system for generating a hydrogen-rich reformate comprising a reformer to which fuel and an oxidising agent can be supplied. According to the invention it is contemplated that the fuel supplied to the reformer is at least partly coolable by a fluid having other functions in addition to the function of cooling the fuel in the reformer system or a parent system into which the reformer system is integrated. The invention further relates to a method for generating a hydrogen-rich reformate as well as a fuel cell system comprising a reformer system according to the invention.

Abstract: The invention relates to a reformer for a fuel cell system for generating a reformate comprising a plurality of function units for treating the fuel, at least one function unit being adapted to a first type of fuel. In this arrangement the invention is characterized to advantage in that the function unit adapted to the first type of fuel can be releasably coupled to the reformer as a module by means of an interface which is also designed to couple a replacement function unit instead of the function unit adapted to the first type of fuel, the replacement function unit being adapted to a second type of fuel different from the first type of fuel. The invention relates furthermore to a function unit for such a reformer, to a fuel cell system having such a reformer and to a motor vehicle having such a fuel cell system.

Abstract: A reformer (10) for reacting fuel (12, 14) and oxidizer (16, 18) into reformate (20), with a plurality of reaction zones (22, 24) to which the fuel (12) and oxidizer (16) are supplied and in each which the fuel and oxidizer are reacted into reformate. The process for reacting fuel and oxidizer into reformate separately adjusting the fuel and/or oxidizer supplied to the reaction zones for varying the reformate output produced.

Abstract: A device for providing a homogenous mixture of fuel and oxidant including an arrangement (5) for feeding liquid fuel to an evaporator, an arrangement (4) for feeding gaseous oxidant into a mixing zone (12) downstream of the evaporator, and a reaction zone downstream of the mixing zone in which a packed structure (3) is arranged. The packed structure can be a ceramic cylindrical molding having a diameter in the range 25 to 35 mm and an axial length in the range 15 to 50 mm or it can have flow conduits that are square in cross-section and have a cell density in the range 400 to 1200 cpsi.

Abstract: A reformer (10) for reacting fuel (12, 14) and oxidizer (16, 18) into reformate (20), with a plurality of reaction zones (22, 24) to which the fuel (12) and oxidizer (16) are supplied and in each which the fuel and oxidizer are reacted into reformate. The process for reacting fuel and oxidizer into reformate separately adjusting the fuel and/or oxidizer supplied to the reaction zones for varying the reformate output produced.