The present invention relates to solid-oxide fuel cells, and more specifically, to solid-oxide fuel cells that comprise a ferritic support.
Known solid-oxide fuel cells comprise a first electrode that acts as an anode, a second electrode that acts as a cathode and an electrolyte. Depending on the support used in these cells, there are cathodic support cells, anodic support cells and electrolyte support cells. There are also cells that comprise a metallic support.
U.S. Pat. No. 6,794,075 describes a solid-oxide fuel cell with a metallic support, more specifically a stainless steel ferritic support. It discloses a solid-oxide fuel cell with an intermediate temperature, its working temperature being around 500° C. The sintering process of this type of cell takes place at temperatures no higher than 1000° C.
In the solid-oxide fuel cells are used fuels such as natural gas, liquefied petroleum gas and diesel. In order to be used in this type of cell, said fuels must be converted by a reforming process into a mixture that comprises hydrogen, carbon monoxide and dioxide, and water. These reforming processes require high temperatures (from 600° C. to 900° C.).
It is an object of this invention to provide a solid-oxide fuel cell that comprises a metallic support, and which has a sufficiently low working temperature to prevent oxidation problems in the metallic support, and sufficiently high to have a sufficient thermal level to produce reformed gas with the minimum external heat contribution.
The inventive fuel cell thus comprises a metallic support, more specifically a ferritic support, a first electrode deposited on said ferritic support, an electrolyte deposited on said first electrode, and a second electrode deposited on said electrolyte. The inventive fuel cell also comprises, between the first electrode and the ferritic support, a diffusion barrier that comprises cerium oxide.
The inventive fuel cell must have a sintering temperature of over 1100° C. in order to densify the electrolyte, and the sintering atmosphere must be reductive or inert. If the diffusion barrier of cerium oxide is not used, at said temperatures the chrome and iron of the ferritic support will melt the first electrode, seriously affecting the stability and the catalytic activity of said first electrode.
The cerium oxide barrier prevents the diffusion of chrome and iron and also has the following characteristics:
Therefore, the inventive fuel cell comprises a metallic support instead of a ceramic support, thereby reducing costs, and it also has a working temperature that is sufficiently high to prevent the need for additional heating means to reform the fuel, and all this without diffusion problems being created during the sintering process.
These and other advantages and characteristics of the invention will be made evident in the light of the drawing and the detailed description thereof.
As shown in
In an inventive embodiment, the first electrode 3 is the anode and the second electrode 5 is the cathode. In a preferred embodiment, said first electrode 3 comprises Ni-YSZ and the electrolyte 4 comprises YSZ. The ferritic support 2 must have a thermal expansion coefficient similar to the thermal expansion coefficient of the electrolyte 4, which comprises YSZ in this case, said ferritic support 2 having a percentage of chrome of between 16% and 30% in weight. The thickness of said ferritic support 2 must be preferably comprised between 100 micron and 1 millimetre, and must have a porosity of between 20% and 55%.
During the cell manufacturing process, on said ferritic support 2, to which the diffusion barrier 6 has previously been added, is deposited NiO—YSZ with a percentage of NiO of between 30% and 60% in volume, preferably of around 50%, and with a final porosity of between 20% and 50%. The thickness of the resulting electrode 3 can vary between 5 and 30 micron. On said electrode 3 is deposited the electrolyte, the thickness of which may vary between 5 and 20 micron, being preferably 10 micron. During the sintering process, which is performed in a reductive or inert atmosphere, the NiO—YSZ is converted into Ni—YSZ.
The electrode 3 of the inventive cell 1 may comprise, instead of Ni—YSZ, an equivalent material such as Ni—ScsZ, Ni—YDC or Ni—SDC. Similarly, electrolyte 4 may comprise, instead of YSZ, an equivalent material such as SsZ, YDC or SDC.
In a first embodiment of the invention, the diffusion barrier 6 comprises cerium oxide doped with rare earth elements. Preferably, the cerium oxide doped with rare earth elements comprises Ce1−XRExO2−x/2, where RE is a rare earth element and X may vary between 0.05 and 0.3. Said rare earth element is preferably Yttrium, Samarium or Gadolinium.
In a second embodiment of the invention, the cerium oxide of the diffusion barrier 6 is not doped with rare earth elements, said diffusion barrier 6 comprising cerium oxide.
The thickness of the diffusion barrier of cerium oxide is comprised between 1 micron and 20 micron. In a preferred embodiment said thickness is approximately 5 micron.
Number | Date | Country | Kind |
---|---|---|---|
200502329 | Sep 2005 | ES | national |
Number | Name | Date | Kind |
---|---|---|---|
7297436 | Hori | Nov 2007 | B2 |
20020048699 | Steele et al. | Apr 2002 | A1 |
20070009784 | Pal et al. | Jan 2007 | A1 |
Number | Date | Country |
---|---|---|
546714 | Jun 1993 | EP |
546714 | Aug 1999 | EP |
1263067 | Dec 2002 | EP |
07153469 | Jun 1995 | JP |
0022689 | Apr 2000 | WO |
2005122300 | Dec 2005 | WO |
2006082057 | Aug 2006 | WO |
Number | Date | Country | |
---|---|---|---|
20070072057 A1 | Mar 2007 | US |