FUEL CELL ELECTRODE STRUCTURE AND METHOD OF MAKING IT

Abstract: An electrode provided with an alkali or alkaline earth hydroxide constituent which upon heat treatment in the presence of carbon dioxide is converted to a carbonate constituent.

Description: ELECTRODE STRUCTURE AND METHOD OF MAKING SAME Background of the Invention This invention pertains to electrodes and, in particular, to electrodes for use with molten carbonate fuel cells. In the design of electrodes for molten carbonate fuel cells, it is essential that the electrodes be provided with carbonate constituent to provide the needed bridge with the carbonate electrolyte tile. In present structures, one technique for providing the needed carbonate constituent is to fill the electrolyte tile with excess carbonate and allow some of the excess to drain into the electrodes. The electrolyte becomes depleted in the tile and electrodes during the course of fuel cell operation and limits the useful life of the fuel cell. A storage of excess carbonate electrolyte can be provided in the electrolyte tile by increasing its thickness. However, increasing the tile thickness decreases the fuel cell output and, thus, is undesirable. To avoid having to increase the tile thickness, other practices have been used in which carbonate electrolyte is supplied directly to the electrodes. SMile this requires increased electrode thickness, such #increased thickness is not detrimental to cell performance. Present techniques for adding carbonate electrolyte to the electrodes, however, are inefficient and could have an adverse effect on the electrode characteristics. In particular, carbonate electrolyte is usually added by melting the electrolyte directly into the electrode at high temperatures (e.g., 6O0#C). When this is carried out using gases that the fuel electrode would normally be subjected to during fuel cell operation, wetting of the electrode is poor and inhibits electrolyte absorption. Thus, in this case, the high temperatures used can adversely affect the electrode characteristics and the degree of added electrolyte is not substantial. Moreover, while the amount of electrolyte can be increased by using a different gas during the heating, the change in gas composition can also adversely affect the electrode characteristics. It is therefore an object of the present invention to provide a practice for incorporating carbonate electrolyte into an electrode which does not suffer from the above disadvantages. It is a further object of the present invention to provide an improved electrode for molten carbonate fuel cells. Summary of the Invention In accordance with the principles of the present invention, the above and other objectives are realized in an electrode provided with an alkali and or alkaline earth hydroxide constituent. Such constituent is added to the electrode at room temperature and the electrode is subsequently heat treated in a carbon dioxide environment either in or out of cell to convert the hydroxide constituent to a carbonate. The resultant electrode thereby includes the desired carbonate electrolyte in an amount which can be readily controlled and selected by the initial selection and introduction of the hydroxide constituent at room temperature. In a further aspect of the present invention, a ceramic oxide constituent is also included in the electrode. This constituent also reacts with the hydroxide constituent during heating to provide a stable component which affords sintering resistance and greater carbonate retaining capability. Brief Description of the Drawings The above and other features and aspects of the present invention will become more apparent upon reading the following detailed description in conjunction with the accompanying drawings, in which: FIG. 1 shows an electrode in accordance with the principles of the present invention; and FIG. 2 illustrates a flow diagram for fabricating electrodes in accordance with the invention. Detailed Description In Fig. 1, an electrode in accordance with the principles of the invention is shown. The electrode is to be used in a fuel cell employing a carbonate electrolyte tile. The cation of the tile may be any alkaline constituent, such as, for example, Li, K, Na, etc. The electrode 1 comprises a base metallic structure preferably formed of a nickel or a nickel alloy such as, for example, Ni-Co, Ni-Cr, Ni and other metals, etc. In accordance with the invention, the electrode 1 is additionally filled or impregnated with an alkali and/or alkaline earth hydroxide having a preselected cation component similar to the cation of the carbonate tile with which the electrode is to be used. This impregnation is carried out at room temperature by a conventional technique, such as, for example, dipping, spraying or vacuum filtration, using a solution of desired hydroxide. Depending upon the particular process used and type of electrode, a suitable organic or inorganic solvent may be used to form the hydroxide solution. Preferable solvents are water, methanol, ethanol and isopropanol. The amount of hydroxide impregnated should be such as to provide the needed contact and bridge between the electrode and the electrolyte tile during fuel cell operation and, moreover, should be such as to provide an inventory for replenishing electrolyte depleted during operation. Preferably the amount of impregnated hydroxide should be such as to result in electrolyte in the electrode which fills from 5 to 85 percent of the electrode pore volume. Subsequent to impregnating the electrode with the desired hydroxide constituent, the hydroxide is converted to carbonate electrolyte by exposure to a carbon dioxide atmosphere at a temperature above 1000C. This treatment can be carried out out-of-cell or in-cell and provides the resultant electrode with the desired carbonate constituent make-up. In a further aspect of the invention, the hydroxide added to the electrode 1, in addition to providing the carbonate electrolyte upon heat treatment, also converts any ceramic oxides or hydroxides in the electrode to stabilizing components. In accordance with this aspect of the invention, ceramic oxides, such as, for example, alumina, zirconia, iron oxide, etc., may be added by any conventional process to the electrode subsequent to sintering, these oxides then being converted by the hydroxides to the desired stablizing components. In this case, the amount of hydroxide added should be selected to be sufficient to convert the ceramic oxides, as well as to convert the hydroxide to the desired amount of carbonate electrolyte. In preferred construction, the hydroxide added to the electrode contains lithium hydroxide for reacting with the ceramic oxides. For ceramic oxides such as, for example, Or02, A1203 and We203 respective components Li2Zro3, Lilo2 and LiFeO2 having extremely high sintering resistance and stability are produced. These components, furthermore, fill the pores of the electrode and enhance the electrolyte storage and wicking properties. Preferably, the added ceramic oxide includes A1203 or A1(OH)3 so that the reaction with lithium hydroxide produces highly stable lithium aluminate. The invention will be further illustrated by the following examples and tables. Example I A nickel-cobalt anode for a fuel cell was impregnated with alkali hydroxides of Li-K composition similar to that of the electrolyte tile of the cell (identified as Cell 149 in Table 1 below). The amount of hydroxide was equivalent to filling approximately 10% of the electrode pore volume with carbonates. The conversion of hydroxides to carbonates was performed in-cell in the presence of C02 during the early cell heat up cycle. As can be seen from Table 1, the performance of the cell was 35 mV higher at 115 mA/cm2 than that of a cell (identified as cell 151) assembled with similar com-ponents and no hydroxide treatment. TABLE 1 RESULTS OF HYDROXIDE (LiKOH) WETTED ANODE STRUCTURES IN FUEL CELLS EMI5.1 <tb> <SEP> Hydroxide <SEP> Performance <SEP> at <tb> <SEP> 2 <tb> Cell <SEP> No. <SEP> Treatment <SEP> 115 <SEP> mA/cm <SEP> (mV) <SEP> Comment <tb> 149 <SEP> Yes <SEP> 860 <SEP> Improvement <tb> <SEP> of <SEP> 35 <SEP> mv <tb> 151 <SEP> No <SEP> 825 <tb> Example 2 In this example, both hydroxide components and -eramic oxide components were added to nickel-based carbonate fuel cell anodes to provide carbonate electrolyte and stable sintering retardant constituents. The flow diagram of the procedure followed is shown in Fig. 2 which also provides desirable porosity ranges for the initial and final anode structures and desirable weight gain ranges due to the addition of the hydroxide and ceramic oxide components. A total of four cells were assembled with the alkali hydroxide and aluminum hydroxide treatment. The anodes were first electrochemically impregnated with Al (OH)3. The amount of A1(OH)3 was determined based upon a desired final electrode porosity. After impregnation, the electrodes were sprayed with an alkali hydroxide (Li-K-OH) solution in methanol. The reaction of lithium hydroxide with aluminum hydroxide produced lithium aluminate and the presence of carbon dioxide caused the conversion of the remainder of the alkali hydroxides to alkali carbonates. Performance of the fuel cells assembled with these hydroxide-treated anodes are compared with cells assembled with untreated anodes in Table 2. All the cells treated with hydroxides displayed significantly better performance (40-75 mV higher at 115 mA/cm2). Also, cell endurance with the stabilized anodes was better than that of cells assembled with conventional nickel- anodes. This can be attributed to the sintering resistance imparted by lithium aluminate. An additional advantage is also derived from the fine particle structure of lithium aluminate formed in the electrode pores. This fine particle structure improves the capability of the cell to withstand high differential pressures across the fuel and oxidant chambers. TABLE 2 RESULTS OF A1(OH)3 IMPREGNATION FOLLOWED BY HYDROXIDE TREATMENT IN FUEL CELLS EMI7.1 <tb> <SEP> Al(OH)3 <SEP> Performance <tb> <SEP> at <SEP> <SEP> at115 <tb> <SEP> Treat <tb> Cell <SEP> Nos. <SEP> nent <SEP> Cell <SEP> Design <SEP> 11w <SEP> <SEP> Comments <SEP> <tb> 57-7, <SEP> 7-14, <SEP> No <SEP> Standard <SEP> 770-820 <SEP> Significant <SEP> per <tb> 7-18, <SEP> 7-31 <SEP> formance <SEP> <SEP> losses <tb> <SEP> observed <SEP> during <tb> <SEP> first <SEP> 300 <SEP> hours <tb> <SEP> of <SEP> <SEP> cell <SEP> <SEP> operation <tb> <SEP> 7-38 <SEP> Yes <SEP> Standard <SEP> 850870 <SEP> <SEP> 4050 <SEP> <SEP> 11w <SEP> <SEP> improve- <SEP> <tb> <SEP> 7-40 <SEP> ment <SEP> <SEP> and <SEP> stable <tb> <SEP> for <SEP> 4000 <SEP> hours <tb> <SEP> 7-35 <SEP> Yes <SEP> Nickel <SEP> - <SEP> cobalt <SEP> <SEP> 880 <SEP> 60 <SEP> mV <SEP> inprwement <SEP> <tb> <SEP> anode <SEP> and <SEP> stable <SEP> for <tb> <SEP> 750 <SEP> <SEP> hours <SEP> (volun- <SEP> <tb> <SEP> tary <SEP> termination) <tb> <SEP> IR7-1 <SEP> Yes <SEP> Nickel <SEP> current <SEP> 895 <SEP> 75 <SEP> Mw <SEP> <SEP> inprocement <SEP> <tb> <SEP> collectors <SEP> for <tb> <SEP> anode <tb> In all cases it is understood that the above-described arrangements are merely illustrative of the many possible specific embodiments which represent applications of the present invention. Numerous and varied other arrangements can readily be devised without departing from the spirit and scope of the invention.

Claims: What We Claim Is 1. Apparatus comprising: an electrode; and an alkaline hydroxide constituent incorporated into said electrode. 2. Apparatus in accordance with claim 1 wherein: said alkaline hydroxide constituent comprises one of an alkali hydroxide and an alkaline earth hydroxide. 3. Apparatus in accordance with claim 2 wherein: said hydroxide comprises one of lithium, sodium and potassium hydroxide. 4. Apparatus in#accordance with claim 2 wherein: said hydroxide comprises lithium and potassium hydroxide. 5. Apparatus in accordance with claim 2 wherein: said electrode comprises nickel. 6. Apparatus in accordance with claim 1, 2, 3, 4 or 5 further comprising: a ceramic oxide incorporated into said electrode. 7. Apparatus in accordance with claim 6 wherein: said ceramic oxide is such that during heating in the presence of carbon dioxide said ceramic oxide reacts with said hydroxide and other components to produce components having increased stability. 8. Apparatus in accordance with claim 7 wherein: said ceramic oxide comprises one of alumina, zirconia and iron oxide. 9. Apparatus in accordance with claim 7 wherein: said ceramic is A1(OH)3. 10. Apparatus in accordance with claim 9 wherein: said hydroxide is lithium hydroxide. 11. Apparatus in accordance with claim 1 wherein: the amount of hydroxide added is such that upon heat treating said electrode in the presence of carbon dioxide carbonate constituent filling about 5 to 85 percent of the electrode pore vol lume is produced 12. Apparatus in accordance with claim 1 wherein: said alkaline hydroxide constituent com prises an alkali hydroxide and an alkaline earth hydroxide. 13. A method of fabricating an electrode for use in a molten carbonate fuel cell comprising: incorporating an alkaline hydroxide into an electrode structure at room temperature; heating the electrode structure carrying the hydroxide in the presence of carbon dioxide to convert the hydroxide to a carbonate constituent. 14. A method in accordance with claim 13 wherein: said incorporating is by impregnation. 15. A method in accordance with claim 14 wherein: said impregnation is by one of spraying, dipping and vacuum filtration. 16. A method in accordance with claim 13 wherein: said heating is subsequent to said electrode being incorporated into a fuel cell. 17. A method in accordance with claim 13 wherein: said heating is prior to said electrode being incorporated into a fuel cell. 18. A method in accordance with claim 13 wherein: said hydroxide is one of an alkali hydroxide and an alkaline earth hydroxide. 19. A method in accordance with claim 18 wherein: said hydroxide is one of lithium, potassium and sodium hydroxide. 20. A method in accordance with claim 13 or 18 further comprising: incorporating a ceramic oxide into said electrode prior to said heating. 21. A method in accordance with claim 20 wherein: said ceramic oxide incorporation is by impregnation. 22. A method in accordance with claim 20 wherein: said ceramic oxide incorporation is prior to said hydroxide incorporation. 23. A method in accordance with claim 20 wherein: said ceramic oxide is one of alumina, zirconia and iron oxide. 24. A method in accordance with claim 20 wherein: said hydroxide is lithium hydroxide. 25. A method in accordance with claim 13 wherein: the amount of hydroxide added in such that the resultant carbonate constituent fills about 5 to 85 percent of the electrode pore volume. 26; A method in accordance with claim 13 wherein: said alkaline hydroxide constituent com prises an alkali hyrdoxide and an alkaline earth hydroxide.

Inventors: PAETSCH, LAWRENCE M., PATEL, PINAKIN S.
Applicants: ENERGY RESEARCH CORPORATION
Application year: 1983
Main classification: H01M8
IPC codes: H01M8, H01M4