Method for producing a catalyst for fuel cells
US-2015318560-A1 · Nov 5, 2015 · US
US10326147B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10326147-B2 |
| Application number | US-201314784115-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 18, 2013 |
| Priority date | Apr 18, 2013 |
| Publication date | Jun 18, 2019 |
| Grant date | Jun 18, 2019 |
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The present invention is to provide a catalyst for fuel cells, which is able to inhibit gas diffusion resistance and shows high IV characteristics far more than conventional fuel cell catalysts, and a method for producing the catalyst. Disclosed is a catalyst for fuel cells, comprising fine catalyst particles, each of which comprises a palladium-containing particle and an outermost layer containing platinum and covering the palladium-containing particle, and a carrier on which the fine catalyst particles are supported, wherein the catalyst for fuel cells satisfies 0.9×S1≤S2 in which S1 is a BET specific surface area of a material for the carrier, and S2 is a BET specific surface area of the carrier in the catalyst for fuel cells.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a catalyst for fuel cells, the catalyst comprising fine catalyst particles, each of which comprises a palladium-containing particle and an outermost layer containing platinum and covering the palladium-containing particle, and a carrier on which the fine catalyst particles are supported, wherein the method comprises: preparing a carrier on which palladium-containing particles are supported; covering the palladium-containing particles with a monatomic layer; synthesizing the fine catalyst particles by substituting the monatomic layer with the outermost layer containing platinum in the presence of an additive; and washing a catalyst precursor in which the fine catalyst particles are supported on the carrier with water more than one time until a ratio of the total mass of the additive and a derivative thereof, both of which remain in the catalyst for fuel cells after the washing, to a total mass of the additive used for the synthesis of the fine catalyst particles, becomes 2.5% by mass or less determined by measuring the water. 2. The method for producing a catalyst for fuel cells according to claim 1 , wherein the catalyst precursor is dispersed and washed in water by at least one method selected from a group consisting of an ultrasonic dispersion method, a method for pulverizing the catalyst precursor with a ball mill and then adding it to water, and a method for dispersing the catalyst precursor with a device that uses shear stress, when the catalyst precursor is washed with water. 3. The method for producing a catalyst for fuel cells according to claim 1 , wherein a temperature of the water used for the washing is 30° C. or more and less than 100° C. 4. The method for producing a catalyst for fuel cells according to claim 1 , wherein the additive is at least one surfactant selected from the group consisting of citric acid and ethylenediaminetetraacetic acid (EDTA), and sodium salts and potassium salts thereof. 5. The method for producing a catalyst for fuel cells according to claim 1 , wherein an acid is further used when the monatomic layer is substituted with the outermost layer. 6. The method for producing a catalyst for fuel cells according to claim 1 , wherein, the carrier on which the palladium-containing particles are supported is subjected to an acid treatment. 7. The method for producing a catalyst for fuel cells according to claim 1 , wherein the ratio of the total mass of the additive and the derivate thereof, both of which remain in the catalyst for fuel cells after the washing, to the total mass of the additive used for the synthesis of the fine catalyst particles, is calculated based on a result of measuring a conductivity of the water used for washing. 8. The method for producing a catalyst for fuel cells according to claim 1 , wherein the catalyst for fuel cells satisfies 0.9×S1≤S2 in which S1 is a BET specific surface area of a material for the carrier, and S2 is a BET specific surface area of the carrier in the catalyst for fuel cells. 9. The method for producing a catalyst for fuel cells according to claim 1 , wherein the method comprises firing the catalyst precursor at a temperature of 80° C. or more and less than 200° C. in a reducing gas atmosphere, after washing the catalyst precursor. 10. The method for producing a catalyst for fuel cells according to claim 9 , wherein the catalyst has a mass activity of 450 (A/g Pt ) or more and a specific activity of a 4.0 (A/m2) or more.
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