초록 ▼

A method of preparing catalyst agglomerates for electrochemical devices is provided. The method comprises dispersing particles of a catalyst in a non-aqueous solvent to form a dispersion of the catalyst, adding an ion conducting polymer in a dilute solution to the dispersion of the catalyst under ag

A method of preparing catalyst agglomerates for electrochemical devices is provided. The method comprises dispersing particles of a catalyst in a non-aqueous solvent to form a dispersion of the catalyst, adding an ion conducting polymer in a dilute solution to the dispersion of the catalyst under agitation to form catalyst agglomerates, and stirring the dispersion of the catalyst and the catalyst agglomerates to control the growth of the agglomerates. A directly applicable catalyst composition is also provided. The catalyst composition comprises the catalyst agglomerates prepared according to the present invention, a solvent to plasticize surfaces of the catalyst agglomerates and the membrane, and a non-aqueous carrier solvent.

대표청구항 ▼

1. A method of preparing catalyst agglomerates for use in a membrane electrode assembly comprising:dispersing particles of a catalyst in a non-aqueous solvent to form a dispersion of said catalyst; adding an ion conducting polymer to said dispersion of said catalyst under agitation to form catalyst

1. A method of preparing catalyst agglomerates for use in a membrane electrode assembly comprising:dispersing particles of a catalyst in a non-aqueous solvent to form a dispersion of said catalyst; adding an ion conducting polymer to said dispersion of said catalyst under agitation to form catalyst agglomerates; and stirring said catalyst agglomerates and said dispersion of said catalyst in an attritor to control growth of said catalyst agglomerates. 2. The method of claim 1 wherein said attritor has a ratio of bead to slurry from about 30:70 to 70:30 by volume and a bead size from about 1 to 20 mm in diameter.3. The method of claim 2 wherein said particles of said catalyst are dispersed in an attritor having a ratio of bead to slurry of about 50:50 by volume and a bead size from about 2 to 5 mm in diameter.4. The method of claim 1 wherein said dispersion of said catalyst has a concentration of said catalyst from about 2 to 25 percent by weight.5. The method of claim 1 wherein said ion conducting polymer is added to said dispersion of said catalyst in an amount from about 5 to 25 percent by weight of said catalyst.6. The method of claim 5, wherein particles of platinum ruthenium are dispersed in a non-aqueous solvent to form a dispersion of platinum ruthenium, and said ion conducting polymer is added to said dispersion of platinum ruthenium in an amount from about 5 to 15 percent by weight of platinum ruthenium.7. The method of claim 6, wherein said ion conducting polymer added to said dispersion of platinum ruthenium is diluted in an aqueous solution to a concentration from about 0.5 to 5 percent by weight of platinum ruthenium.8. The method of claim 5, wherein particles of platinum are dispersed in a non-aqueous solvent to form a dispersion of platinum, and said ion conducting polymer is added to said dispersion of platinum in an amount from about 5 to 10 percent by weight of platinum.9. The method of claim 8 wherein said ion conducting polymer added to said dispersion of platinum is diluted in an alcoholic solution to a concentration from about 0.5 to 5 percent by weight of platinum.10. The method of claim 9 wherein said ion conducting polymer is diluted in an alcoholic solution with a ratio of alcohol to water from about 0.01 to 100 by weight of platinum.11. The method of claim 10 wherein said ion conducting polymer is diluted in an alcoholic solution with a ratio of alcohol to water of about 1 by weight.12. The method of claim 1 wherein said ion conducting polymer is added to said dispersion of said catalyst at a level from about 33 to 100 percent of said polymer needed to make up a final catalyst layer.13. The method of claim 12 wherein said ion conducting polymer is added to said dispersion of said catalyst at a level from about 75 to 95 percent of said polymer needed to make up a final catalyst layer.14. The method of claim 1 wherein said catalyst agglomerates and said dispersion of said catalyst are stirred in an attritor having a ratio of bead to slurry from about 30:70 to 70:30 by volume and a bead size from about 1 to 20 mm in diameter.15. The method of claim 11 wherein said catalyst agglomerates and said dispersion of said catalyst are stirred in an attritor having a ratio of bead to slurry of about 50:50 by volume and a bead size from about 2 to 5 mm in diameter.16. The method of claim 14 or 15 wherein said catalyst agglomerates and said dispersion of said catalyst are stirred in said attritor at a temperature from about 0 to 100° C. and at an angular velocity of rotation of said attritor from about 10 to 150 cm/s.17. The method of claim 1 further comprising adding silinized fume silica to said dispersion of said catalyst.18. The method of claim 1 further comprising drying said catalyst agglomerates at a temperature from about 25 to 100° C.19. The method of claim 1 wherein said catalyst agglomerates have a porosity from about 25 to 70 percent by volume of the volume of said catalyst agglomerates.20. A catalyst composition comprising the catalyst agglomerates prepared according to claim 1;a solvent to plasticize surfaces of said catalyst agglomerates and surfaces of said membranes; and a non-aqueous carrier solvent comprising ketones, aliphatic or aromatic hydrocarbons, and acetate. 21. The catalyst composition of claim 20 wherein said solvent to plasticize surfaces of said catalyst agglomerates and surfaces of said membranes comprises alcohol, water, and acetamides.22. The catalyst composition of claim 21 wherein said solvent to plasticize surfaces of said catalyst agglomerates and surfaces of said membranes comprises methoxyethanol, butoxyethanol, isopropylalcohol, and water.23. The catalyst composition of claim 20 wherein said non-aqueous carrier solvent comprises acetone, xylene, and n-butylacetate.24. The catalyst composition of claim 20 further comprising additives to modify performance characteristics of said catalyst composition.25. The catalyst composition of claim 24 wherein said additives comprise carbon, electrochemically inert nonionic surfactants, or cross-linking agents.26. The catalyst composition of claim 20 further comprising an ionomer.27. The catalyst composition of claim 20 wherein said composition comprises 10-70 percent by weight of said catalyst agglomerates, 1-20 percent by weight of said solvent to plasticize surfaces of said catalyst agglomerates and surfaces of said membrane, and 30-89 percent by weight of said non-aqueous carrier solvent.