Planar high-temperature fuel cell
AssigneeSiemens Aktiengesellschaft
InventorsRobert Fleck, Horst Greiner, Alessandro Zampieri
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AssigneeSiemens Aktiengesellschaft
InventorsRobert Fleck, Horst Greiner, Alessandro Zampieri
Estimating the term…
A planar high temperature fuel cell, a use and a method of manufacture are discloses. The planar high-temperature fuel cell with includes a layer structure. The layer structure includes a cathode layer, an anode layer and a solid electrolyte layer disposed between the cathode layer and the anode layer. Each of the layers are planar. A porous metal structure is used as the support for the layer structure and is also planar.
A planar high-temperature fuel cell, comprising:
A planar high-temperature fuel cell, comprising:
Dependencies are inferred from the claim text.
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From the US filing history. Foreign family members aren’t listed.
Porous and characterised by the material: metals or alloys
Composites: in the form of layered or coated products
Characterised by the electrode/electrolyte combination or the supporting material: characterised by the supporting layer
Operating at high temperature, e.g. with stabilised ZrO2 electrolyte: fuel cells with solid oxide electrolytes
About 5 years 7 months of term left · ends 16 May 2032 (estimated)
This application is the US National Stage of International Application No. PCT/EP2009/062366, filed Sep. 24, 2009, and claims the benefit thereof. The International Application claims the benefits of German application No. 102008049712.6 filed Sep. 30, 2008. All of the applications are incorporated by reference herein in their entirety.
The invention relates to a planar high-temperature fuel cell. The invention also relates to the fuel cell system comprised of same and to a method for the production thereof.
Solid electrolyte high-temperature fuel cells are essentially characterized by a solid ceramic electrolyte which is generally implemented as an oxide ceramic layer between two electrodes. A fuel cell of this kind (SOFC=Solid Oxide Fuel Cell) generally has an operating temperature of 600 to 1000° C. At this temperature, the electrochemical reaction is optimized. Low operating temperatures tend to reduce the costs of a fuel cell system.
Further details and advantages of the invention will emerge from the following description of exemplary embodiments with reference to the accompanying drawings and associated claims.
In highly schematic form,
FIG. 1 shows a perspective view of a planar fuel cell,
In the figures, identical parts are provided with the same reference characters in each case. Some of the figures are described jointly.
FIG. 1 shows a perspective view of a planar fuel cell and FIG. 2 an associated section. Reference numeral 5 denotes the metal support made of a sintered material which has a predefined porosity, functional layers for the SOFC being deposited on the upper side of the support structure. The functional layers consist specifically of the cathode K, the solid electrolyte El and the anode A. The layer structure as a whole is denoted by 100.
In the layer structure 100, the solid electrolyte El of known composition is disposed as a thin layer between cathode K and anode A. The layered electrodes on the one hand and the layered solid electrolyte on the other can be formed from sub-layers interspersed with adaptation layers, for which reference is made to the prior art.