Method for producing core-shell catalyst particles
US-2016359173-A1 · Dec 8, 2016 · US
US10998556B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10998556-B2 |
| Application number | US-201716329362-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 7, 2017 |
| Priority date | Oct 10, 2016 |
| Publication date | May 4, 2021 |
| Grant date | May 4, 2021 |
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The present invention relates to a catalyst for a solid polymer fuel cell, including platinum, cobalt, and zirconium supported as a catalytic metal on a carbon powder carrier, in which the supporting ratio of platinum, cobalt, and zirconium on the carbon powder carrier is Pt:Co:Zr=3:0.5 to 1.5:0.1 to 3.0 by molar ratio. In the present invention, it is preferable that the peak position of Pt 3 Co seen in the X-ray diffraction pattern of catalyst particles is 2θ=41.10° or more and 42.00° or less, and moderate alloying has occurred in the catalytic metal.
Opening claim text (preview).
The invention claimed is: 1. A catalyst for a solid polymer fuel cell, comprising a catalytic metal dispersed and supported on a surface of a carbon powder carrier, wherein the catalytic metal is an alloy of platinum, cobalt, and zirconium and is in the form of catalyst particles having an average particle size of 2 to 20 nm, wherein a supported ratio of the platinum, cobalt, and zirconium constituting the catalytic metal is Pt:Co:Zr=3:0.5 to 1.5:0.1 to 3.0 by molar ratio, and wherein a supporting density of the catalytic metal is 30 mass % or more and 70 mass % or less. 2. The catalyst for a solid polymer fuel cell according to claim 1 , wherein the supported ratio of platinum, cobalt, and zirconium on the carbon powder carrier is Pt:Co:Zr=3:0.5 to 1.5:0.2 to 1.8 by molar ratio. 3. The catalyst for a solid polymer fuel cell according to claim 1 , wherein in a diffraction pattern obtained from the X-ray diffraction analysis of catalyst particles, the peak position of Pt 3 Co that appears in a region of 2θ=40.0° or more and 42.0° or less is 2θ=41.10° or more and 42.00° or less. 4. The catalyst for a solid polymer fuel cell according to claim 1 , wherein in the diffraction pattern obtained from the X-ray diffraction analysis of catalyst particles, the ratio (I o /I a ) of the peak intensity of ZrO 2 (I o ) that appears in a region of 2θ=28.0° or more and 28.4° or less to the peak intensity of Pt 3 Co (I a ) that appears in a region of 2θ=40.0° or more and 42.0° or less is 1.3 or less. 5. The catalyst for a solid polymer fuel cell according to claim 1 , wherein the catalyst particles have a surface and a core, and wherein the catalyst particles are configured such that the concentrations of cobalt and zirconium at the catalyst particle surface are lower than the concentrations of cobalt and zirconium at the catalyst particle core. 6. A method for producing the catalyst for a solid polymer fuel cell defined in claim 1 , comprising: a step of supporting cobalt and zirconium on a platinum catalyst including platinum particles supported on a carbon powder carrier; a step of heat-treating the platinum catalyst having cobalt and zirconium supported thereon in the supporting step at 900° C. or more and 1,200° C. or less; and a step of bringing the heat-treated catalyst into contact with an oxidizing solution at least once to elute at least part of the supported cobalt and zirconium. 7. The method for producing a catalyst for a solid polymer fuel cell according to claim 6 , wherein the oxidizing solution is a solution of sulfuric acid, nitric acid, phosphorous acid, potassium perzirconate, hydrogen peroxide, hydrochloric acid, chloric acid, hypochlorous acid, or chromic acid. 8. The method for producing a catalyst for a solid polymer fuel cell according to claim 6 , wherein the contact treatment with the oxidizing solution is such that the treatment temperature is 40° C. or more and 90° C. or less, and the contact time is 1 hour or more and 10 hours or less. 9. The catalyst for a solid polymer fuel cell according to claim 2 , wherein in a diffraction pattern obtained from the X-ray diffraction analysis of catalyst particles, the peak position of Pt 3 Co that appears in a region of 2θ=40.0° or more and 42.0° or less is 2θ= 41 . 10 ° or more and 42 . 00 ° or less. 10. The catalyst for a solid polymer fuel cell according to claim 2 , wherein in the diffraction pattern obtained from the X-ray diffraction analysis of catalyst particles, the ratio (I o /I a ) of the peak intensity of ZrO 2 (I o ) that appears in a region of 2θ=28.0° or more and 28.4° or less to the peak intensity of Pt 3 Co (I a ) that appears in a region of 2θ=40.0° or more and 42.0° or less is 1.3 or less. 11. The catalyst for a solid polymer fuel cell according to claim 3 , wherein in the diffraction pattern obtained from the X-ray diffraction analysis of catalyst particles, the ratio (I o /I a ) of the peak intensity of ZrO 2 (I o ) that appears in a region of 2θ=28.0° or more and 28.4° or less to the peak intensity of Pt 3 Co (I a ) that appears in a region of 2θ=40.0° or more and 42.0° or less is 1.3 or less. 12. The catalyst for a solid polymer fuel cell according to claim 2 , wherein the catalyst particles are configured such that the concentrations of cobalt and zirconium at the catalyst particle surface are lower than the concentrations of cobalt and zirconium at the catalyst particle core. 13. The catalyst for a solid polymer fuel cell according to claim 3 , wherein the catalyst particles are configured such that the concentrations of cobalt and zirconium at the catalyst particle surface are lower than the concentrations of cobalt and zirconium at the catalyst particle core. 14. The catalyst for a solid polymer fuel cell according to claim 4 , wherein the catalyst particles are configured such that the-concentrations of cobalt and zirconium at the catalyst particle surface are lower than the concentrations of cobalt and zirconium at the catalyst particle core. 15. A method for producing the catalyst for a solid polymer fuel cell defined in claim 2 , comprising: a step of supporting cobalt and zirconium on a platinum catalyst including platinum particles supported on a carbon powder carrier; a step of heat-treating the platinum catalyst having cobalt and zirconium supported thereon in the supporting step at 900° C. or more and 1,200° C. or less; and a step of bringing the heat-treated catalyst into contact with an oxidizing solution at least once to elute at least part of the supported cobalt and zirconium. 16. A method for producing the catalyst for a solid polymer fuel cell defined in claim 3 , comprising: a step of supporting cobalt and zirconium on a platinum catalyst including platinum particles supported on a carbon powder carrier; a step of heat-treating the platinum catalyst having cobalt and zirconium supported thereon in the supporting step at 900° C. or more and 1,200° C. or less; and a step of bringing the heat-treated catalyst into contact with an oxidizing solution at least once to elute at least part of the supported cobalt and zirconium. 17. The method for producing a catalyst for a solid polymer fuel cell according to claim 7 , wherein the contact treatment with the oxidizing solution is such that the treatment temperature is 40° C. or more and 90° C. or less, and the contact time is 1 hour or more and 10 hours or less. 18. The method for producing a catalyst for a solid polymer fuel cell according to claim 6 , wherein the particulate catalyst metal is formed by being subjected to reduction and precipitation from a metal salt solution of platinum, cobalt, and zirconium and then subjected to alloying by heat treatment. 19. The catalyst for solid polymer fuel cell according to claim 1 , wherein the carbon powder carrier is a carbon powder having a specific surface area of 50 to 1,200 m 2 /g.
Selection of catalytic material · CPC title
Alloys or mixtures with metallic elements · CPC title
Fuel cells with solid oxide electrolytes · CPC title
Positive electrodes · CPC title
Inert electrodes with catalytic activity, e.g. for fuel cells · CPC title
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