Abstract: The plant (1) with high-temperature fuel cells (7) includes a clamping device for a cell stack (5) and axially aligned chambers (7) for an after-burning. Clamping bars (60) of the clamping device are disposed between the afterburning chambers. Exhaust gas passages connect the after-burning chambers to a heat exchanger (20a) acting as a heat sink. A clamping element (62) of the clamping device is in heat conducting connection with the heat exchanger. Compression springs (63) are respectively mounted on the clamping bars between an end of the clamping bar and a lug (622) of the clamping element. In this arrangement they exert a clamping force onto the clamping bars. The compression springs are shielded by the clamping element from the cell stack so that, thanks to the heat sink, the compression springs are only exposed to moderate temperature at which the clamping force is maintained.

Abstract: Please substitute the following version of the Abstract, with changes shown by strikethrough (for deletions) or underlining (for added matter). The heat exchanger (I) is provided for a heating system with integrated fuel cells (Z) for the production of electricity and with an additional burner (B). Electrical and thermal energy (E, Q) can be produced in this heating system from a gaseous fuel or from a fuel brought into the gas form by means of the fuel cells, and/or thermal energy (Q) can be produced by means of the additional burner. One part of the thermal energy present in the form of hot exhaust gases can be transferred in the heat exchanger to a liquid heat transfer medium, in particular water or an oil. The heat transfer medium is provided for heat transport for the purpose of room heating and/or process water heating. The heat exchanger forms a compact unit which is also made of a material of good thermal conductivity.

Abstract: The plant (1) with high-temperature fuel cells (7) includes a clamping device for a cell stack (5) and axially aligned chambers (7) for an after-burning. Clamping bars (60) of the clamping device are disposed between the afterburning chambers. Exhaust gas passages connect the after-burning chambers to a heat exchanger (20a) acting as a heat sink. A clamping element (62) of the clamping device is in heat conducting connection with the heat exchanger. Compression springs (63) are respectively mounted on the clamping bars between an end of the clamping bar and a lug (622) of the clamping element. In this arrangement they exert a clamping force onto the clamping bars. The compression springs are shielded by the clamping element from the cell stack so that, thanks to the heat sink, the compression springs are only exposed to moderate temperature at which the clamping force is maintained.

Abstract: The fuel cell battery (1) has an integrated heat exchanger (4) which is arranged between a heat insulating jacket (12) and a stack (10) of high temperature fuel cells (2). There is a chamber (3), preferably at least two chambers for afterburning, between a periphery (14) of the cell stack and the heat exchanger. The heat exchanger is provided for a heat transfer from an exhaust gas (7) to a gaseous oxygen carrier (5). There are arranged on the stack periphery (14), outside or inside the chamber or chambers respectively, inlet points (25a) for the oxygen carrier, on the one hand, and outlet points (25b, 26b) for non-converted educts, namely a fuel gas (6) and the oxygen carrier, on the other hand. The heat exchanger (4) includes a passage system (4) through which the exhaust gas (7) and the oxygen carrier (5) flow largely in transverse planes disposed perpendicular to the axis of the cell stack (10) in one operating state of the battery.

Abstract: The heat exchanger (1) is provided for a heating system with integrated fuel cells (Z) for the production of electricity and with an additional burner (B). Electrical and thermal energy (E, Q) can be produced in this heating system from a gaseous fuel or from a fuel brought into the gas form by means of the fuel cells and/or thermal energy (Q) can be produced by means of the additional burner. One part of the thermal energy present in the form of hot exhaust gases can be transferred in the heat exchanger to a liquid heat transfer medium, in particular water or an oil. The heat transfer medium is provided for heat transport for the purpose of room heating and/or process water heating. The heat exchanger forms a compact unit which is also made of a material of good thermal conductivity. Two separate passages (12, 13) are arranged in the heat exchanger inside a double-walled jacket (10). The jacket has a structured inner space (11) which forms a communicating vessel.

Abstract: The method for the reformation of fuels, in particular of heating oil (20?) and of another liquid fuel is carried out using an oxygen containing gas (5a, 5b, 21?, 22?). The method includes the following steps: formation of a fuel/gas mixture by dispersing of the fuel in a jet of the oxygen containing gas (21?); additionally an admixture of gas of a return flow (3b) and vaporization of the dispersed fuel; generation of synthesized gas from the gas mixture by means of partial oxidation and also reformation processes by heterogeneous catalysis; branching off of the produced synthesized gas into a product flow (3a) and the return flow (3b) for a recirculation; and a regulated extraction of heat from the return flow for the setting of a predetermined temperature of a catalyst support (10) on which the heterogeneous catalysis takes place.

Abstract: The fuel cell battery (1) has an integrated heat exchanger (4) which is arranged between a heat insulating jacket (12) and a stack (10) of high temperature fuel cells (2). There is a chamber (3), preferably at least two chambers, for afterburning, between a periphery (14) of the cell stack and the heat exchanger. The heat exchanger is provided for a heat transfer from an exhaust gas (7) to a gaseous oxygen carrier (5). There are arranged on the stack periphery (14), outside or inside the chamber or chambers respectively, inlet points (25a) for the oxygen carrier, on the one hand, and outlet points (25b, 26b) for non-converted educts, namely a fuel gas (6) and the oxygen carrier, on the other hand. The heat exchanger (4) includes a passage system (4) through which the exhaust gas (7) and the oxygen carrier (5) flow largely in transverse planes disposed perpendicular to the axis of the cell stack (10) in one operating state of the battery.

Abstract: The invention relates to a device for reforming educts containing hydrocarbons, having a radiation burner and a reforming reactor, which contains, at least in part, metal honeycomb bodies having a catalyst coating, and which can in particular be used to produce hydrogen from fossil energy carriers. The invention should thereby be able to convert educts containing hydrocarbons into synthesis gases with high efficiency, in particular in a low-power range. For this purpose, a radiation burner is used that heats a two-part reforming reactor by radiation and convection. The radiation burner and the two parts of the reforming reactor are thereby arranged and constructed in such a way that the radiation burner surrounds the two parts of the reforming reactor, and the educt gas and smoke gas can be conducted in counter-current between the two parts of the reforming reactor.

Abstract: The method for the reformation of fuels, in particular of heating oil (20′) and of another liquid fuel is carried out using an oxygen containing gas (5a, 5b, 21′, 22′).

Abstract: The invention relates to a method and a device for autothermally reforming hydrocarbons. According to the invention, the fuel is fed to a reforming reactor via a feeding device. The resulting reformate is conveyed to the reforming starting materials in a heat exchanger in a reverse direction flow, in such a way that heat is exchanged, said starting materials being conveyed from the outside inwards. The fuel supplied by the feeding device is delivered directly to the reaction zone together with the starting material. Said reaction zone has a catalyst. The combustion and reforming or catalysis processes are then carried out simultaneously and in the same area in the reaction zone.

Abstract: The plant (1) contains high temperature fuel cells (20) which are arranged with planar design in a centrally symmetrical stack (2). A supply point (5) is provided for a gaseous or liquid fuel (50). In a reformer (4) following the supply point the fuel can be catalytically converted at least partially into CO and H2 in the presence of H2O and with process heat being supplied. An afterburner chamber (6) follows the output points of the fuel cells (20). A feedback connection (61) exists between the supply point and the afterburner chamber via which the exhaust gas (60′, 70′) can be fed back to the supply point. In case no gas is provided as a fuel, the supply point comprises a means for feeding in a liquid fuel, such as using an atomizer.

Abstract: The (1) contains high temperature fuel cells (20) which are arranged with planar design in a centrally symmetrical stack (2). A supply point (5) is provided for a gaseous or liquid fuel (50). In a reformer (4) following the supply point the fuel can be catalytically converted at least partially into CO and H2 in the presence of H2O and with process heat being supplied. Along the stack axis a central cavity (25) is arranged via which the fuel which is treated in the reformer can be fed into the fuel cells. The reformer is arranged in the central cavity and is formed in such a manner that the heat required for the endothermic reforming processes can be transferred at least partially via radiation from the fuel cells to the reformer.

Abstract: The fuel cell battery (1) for liquid fuels has the following components: a cell stack (2) which is arranged along an axis (2a) and within a periphery (2b); a distributor passage (21) on the stack axis (2a) via which a reformed fuel gas can be fed in into cells (20) of the stack (2); afterburner chambers (22) at the stack periphery (2b); furthermore an auxiliary burner (3) for a start-up operation. A reaction device (3) is in connection with the cell stack and is provided for the treatment of the liquid fuel by reforming with partial oxidation to form a fuel gas which contains CO and H2. A heat exchanger system (4) is integrated into the reaction device, by means of which, in a current delivering operation of the battery (1)—using hot exhaust gas from the afterburning chambers—the liquid fuel can be vaporized and a gaseous oxygen carrier can be heated up.

Abstract: A hot water heater has an inlet for liquid fuels, a plurality of inlets for resh air, an inlet for a fluid to be heated, at least two combustion stages traversed by the fuel-air mixture with catalytic combustion chambers surrounded at least partially by at least one fluid chamber filled with fluid and with an offgas heat exchanger for fluid to be heated. The heat exchanger is traversed by the offgas escaping from the combustion chambers. The first combustion stage has an evaporation chamber that has on its outside surface, at least a partial catalyst layer.

Abstract: A water heater has a gas inlet (8) for a mixture of gas and air and an in for a fluid (2) to be heated. The gas-air mixture passes through a combustion chamber (11,18) which is at least partly surrounded by at least one fluid chamber (4,7) filled with the fluid (2). The exhaust gas leaving the combustion chamber(s) (11,18) passes through an exhaust gas heat exchanger together with the fluid (2). Here there are two combustion stages, the first (16) being a catalytic gap burner (11) and the second being a monolithic burner (18,19). Owing to the two-stage arrangement, about 80% of the combustion gas is burned in the combustion stage (16) while the remainder is consumed even at the low partial pressures in the second combustion stage (20) virtually without any residue, and especially without emission of NO.sub.x.