Chemistry: electrical current producing apparatus – product – and – With pressure equalizing means for liquid immersion operation
Reexamination Certificate
1999-03-03
2003-07-08
Ryan, Patrick (Department: 1745)
Chemistry: electrical current producing apparatus, product, and
With pressure equalizing means for liquid immersion operation
C429S010000, C429S006000, C429S047000
Reexamination Certificate
active
06589680
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a method for preparation of anodes for use in solid oxide fuel cells. More particularly, this invention relates to a method for preparation of an anode for a solid oxide fuel cell in which metals and catalytic materials employed in such anodes are added in a separate step compared to conventional methods of anode preparation.
2. Description of Prior Art
Solid oxide fuel cells have grown in recognition as a viable high temperature fuel cell technology. There is no liquid electrolyte with its attending metal corrosion and electrolyte management problems. Rather, the electrolyte of the cells is made primarily from solid ceramic materials so as to survive the high temperature environment. The operating temperature of greater than about 600° C. allows internal reforming, promotes rapid kinetics with non-precious materials, and produces high quality by-product heat for cogeneration or for use in a bottoming cycle. The high temperature of the solid oxide fuel cell, however, places stringent requirements on its materials. Because of the high operating temperatures of conventional solid oxide fuel cells (approximately 1000° C.), the materials used in the cell components are limited by chemical stability in oxidizing and reducing environments, chemical stability of contacting materials, conductivity, and thermomechanical compatibility.
The most common anode materials for solid oxide fuel cells are nickel (Ni)-cermets prepared by high-temperature calcination of NiO and yttria-stabilized zirconia (YSZ) powders. High-temperature calcination is essential in order to obtain the necessary ionic conductivity in the YSZ. These Ni-cermets perform well for hydrogen (H
2
) fuels and allow internal steam reforming of hydrocarbons if there is sufficient water in the feed to the anode. Because Ni catalyzes the formation of graphite fibers in dry methane, it is necessary to operate anodes at steam/methane ratios greater than 3. However, there are significant advantages to be gained by operating under dry conditions. Progress in this area has been made using an entirely different type of anode, either based on ceria (See Eguchi, K, et al.,
Solid State Ionics
, 52, 165 (1992); Mogensen, G.,
Journal of the Electrochemical Society
, 141, 2122 (1994); and Putna, E. S., et al.,
Langmuir
, 11 4832 (1995)) or perovskite anodes (See Baker, R. T., et al.,
Solid State Ionics
, 72, 328 (1994); Asano, K., et al.,
Journal of the Electrochemical Society
, 142, 3241 (1995); and Hiei, Y., et al.,
Solid State Ionics
, 86-88, 1267 (1996).). These oxides do not, however, provide sufficient electronic conductivity. Replacement of Ni for other metals, including Co (See Sammes, N. M., et al.,
Journal of Materials Science
, 31, 6060 (1996)), Fe (See Bartholomew, C. H.,
Catalysis Review
-
Scientific Engineering
, 24, 67 (1982)), Ag or Mn (See Kawada, T., et al.,
Solid State Tonics
, 53-56, 418 (1992)) has been considered; however, with the possible exception of Ag, these are likely to react with hydrocarbons in a way similar to that of Ni. Substitution of Ni with Cu would also be promising but for the fact that CuO melts at the calcination temperatures which are necessary for establishing the YSZ matrix in the anodes.
It is also well known that the addition of ceria to the anode improves performance. However, the high-temperature calcination utilized in conventional anode preparation causes ceria to react with YSZ, as a result of which performance is not enhanced to the extent which could be possible if formation of ceria-zirconia did not occur.
SUMMARY OF THE INVENTION
Accordingly, it is one object of this invention to provide a method for preparation of solid oxide fuel cell anodes which enables the use of lower melting temperature materials than employed by conventional solid oxide fuel cell anodes.
It is another object of this invention to provide a process for solid oxide fuel cell anode preparation which enables efficient operation using dry natural gas as a fuel.
It is yet another object of this invention to provide a method for a solid oxide fuel cell anode preparation which enables the use of ceria to improve anode performance while avoiding the formation of ceria-zirconia which reduces the extent of performance enhancement in conventional solid oxide fuel cell anodes.
These and other objects of this invention are addressed by a method for preparation of an anode for a solid oxide fuel cell in which a plurality of zircon fibers or other porous matrix material is mixed with a yttria-stabilized-zirconia (YSZ) powder, thereby forming a fiber/powder mixture. The fiber/powder mixture is then formed into a porous YSZ layer and calcined. The calcined porous YSZ layer is then impregnated with a metal-containing salt solution. Accordingly, contrary to conventional methods for solid oxide fuel cell anode preparation, the method of this invention results in a YSZ layer which remains highly porous following high-temperature calcination to which any suitable metal, including Cu and Ni is then added by impregnation of the salt solution, after the high temperature calcination of the YSZ layer. In addition to enabling the use of metals whose oxides have a low melting temperature, the method of this invention also allows catalytic materials, such as ceria and/or palladium (Pd) to be added in controlled amounts in a separate step.
Cells prepared in accordance with the method of this invention with Ni perform in a very similar manner to those cells prepared using conventional means. With Cu used in place of Ni, there is a possibility of oxidizing hydrocarbons directly, particularly since Cu is inert in dry methane. Even without direct conversion, the Cu-YSZ anode allows the use of dryer gases (partially reformed methane), because Cu is inert to methane. To convert methane, it is necessary to add a catalytic component. Ceria, particularly when doped with noble metals like Pd, Pt, or Rh, is active for this process.
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CRC Handbook of Chemistry and Physics, The Chemical Rubber Co., 1972-1973, pp. B-89 and B-114.*
K. Eguchi et al.:Electrical properties of ceria-based oxides and their application to solid oxide fuel cells, Solid State Ionics, 52, pp. 165-172, 1992.
M. Mogensen et al.:Physical Properties of Mixed Conductor Solid Oxide Fuel Cell Anodes of Doped CeO2, J. Electrochem. Soc., vol. 141, No. 8, pp. 2122-2128, Aug. 1994.
E.S. Putna et al.:Ceria-Based Anodes for the Direct Oxidation of Methane in Solid Oxide Fuel Cells, Langmuir, vol. 11, No. 12, pp. 4832-4837, 1995.
R.T. Baker et al.:Evaluation of perovskite anodes for the complete oxidation of dry methane in solid oxide fuel cells, Solids State Ionics, pp. 328-333, 1994.
K. Asano et al.:A novel Solid Oxide Fuel Cell System Using the Partial Oxidation of Methane, J. Electrochem. Soc., vol. 142, No. 10, pp. 3241-3245, Oct. 1995.
Y. Hiei et al.:Partial oxidation of methane for internally reformed solid oxide fuel cell, Solid State Ionics, vol. 86-88, pp. 1267-1272, 1996.
N.M. Sammes et al.:Synthesis and properties of dense nickel and cobait zirconia cermet anodes for solid oxide fuel cells, J. Mat. Sci, 31, pp. 6069-6072, 1996.
C.H. Bartholomew:Carbon Deposition in Stream Reforming and Methanation, Catal. Rev.—Sci. Eng., 24(1), pp. 67-112, 1982.
T. Kawada et al:Electrical properties of transition-metal-doped YSV, Solid State Ionics, vol. 53-56, pp. 418-425, 1992.
T. Tsai et al.:Effect of Mixed-Conducting Interfacial Layers on Solid Oxide Fuel Cell Anode Performance, J. Elect
Craciun Radu
Gorte Raymond J.
Vohs John M.
Fejer Mark E.
Mercado Julian
Ryan Patrick
The Trustees of the University of Pennsylvania
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