Active Support for Cathode Catalysts
US-2015380741-A1 · Dec 31, 2015 · US
US10693146B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10693146-B2 |
| Application number | US-201414787196-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 16, 2014 |
| Priority date | May 1, 2013 |
| Publication date | Jun 23, 2020 |
| Grant date | Jun 23, 2020 |
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Provided is a method for efficiently manufacturing fine metal particles applicable as a fuel cell electrode catalyst. Provided is a method of manufacturing fine metal particles, including the step of: a hydrogen bubbling step to perform bubbling to a reaction solution, wherein: the reaction solution is prepared by allowing seeds of fine metal particles in a dispersed state and a water soluble noble metal precursor to co-exist in a water-containing solvent; and the bubbling is performed with a reaction gas containing a hydrogen gas, is provided.
Opening claim text (preview).
The invention claimed is: 1. A method of manufacturing fine metal particles, comprising the step of: a hydrogen bubbling step to perform bubbling to a reaction solution, wherein: the reaction solution is prepared by allowing seed fine metal particles in a dispersed state and a water-soluble noble metal precursor to co-exist in a water-containing solvent; the seed fine metal particles are not soluble in the water-containing solvent; the seed fine metal particles are an alloy of noble metal and non-noble metal; the water-soluble noble metal precursor is selected from the group consisting of an acid of noble metal, a salt of noble metal, and a complex of noble metal; the bubbling is performed with a reaction gas containing a hydrogen gas, and a noble metal skin layer is formed so as to cover the seed fine metal particles. 2. The method of claim 1 , wherein an average particle diameter of the seed fine metal particles is 1 to 8 nm. 3. The method of claim 1 , wherein the seed fine metal particles are supported on a carrier and are dispersed. 4. The method of claim 1 , wherein a value of pH of the reaction solution when the bubbling is started is 0 or higher. 5. The method of claim 1 , further comprising the step of: a boiling step to boil the reaction solution before the hydrogen bubbling step. 6. The method of claim 1 , wherein the water-containing solvent is removed after the hydrogen bubbling step, followed by addition of the water-soluble noble metal precursor and the water-containing solvent, and then the hydrogen bubbling is performed again. 7. The method of claim 1 , wherein the reaction gas has a hydrogen gas concentration of 0.1 to 100%. 8. The method of claim 1 , wherein the hydrogen bubbling step is terminated when a concentration of the water-soluble noble metal precursor in the reaction solution becomes 10% or lower. 9. The method of claim 1 , further comprising the step of: a thermal treatment step to perform a thermal treatment with the seed fine metal particles under reductive atmosphere before adding the seed fine metal particles to the reaction solution. 10. The method of claim 1 , wherein: the noble metal of the seed fine metal particles comprises at least one metal selected from the group consisting of platinum, palladium, rhodium, iridium, ruthenium, and gold; and the non-noble metal of the seed fine metal particles comprises at least one metal selected from the group consisting of iron, cobalt, nickel, manganese, chromium, vanadium, titanium, niobium, molybdenum, lead, and tungsten. 11. The method of claim 1 , wherein the noble metal in the acid of noble metal, salt of noble metal, and complex of noble metal comprises at least one noble metal selected from the group consisting of platinum, palladium, rhodium, iridium, ruthenium, and gold. 12. The method of claim 1 , wherein the water-soluble noble metal precursor is selected from the group consisting of chloroplatinic acid, chloroplatinate salt, and platinum ammine complex. 13. The method of claim 1 , wherein: the seed fine metal particles are supported on an electron conductive carrier; and the seed fine metal particles are an electrode catalyst of fuel cell.
Nanosized particles · CPC title
Catalytic material supported on carriers, e.g. powder carriers (H01M4/8807, H01M4/881, H01M4/8814, H01M4/925 take precedence) · CPC title
using gaseous reductors · CPC title
Fuel cells · CPC title
using gaseous reductors · CPC title
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