Method for producing fine catalyst particles and method for producing carbon-supported catalyst
US-2017117554-A1 · Apr 27, 2017 · US
US2016218370A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016218370-A1 |
| Application number | US-201514979292-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 22, 2015 |
| Priority date | Jan 22, 2015 |
| Publication date | Jul 28, 2016 |
| Grant date | — |
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Disclosed is a method for producing a catalyst, wherein the method comprises: a supplying step of supplying a dispersion containing a palladium-containing fine particle from a supplying part into a reaction container; a preparing step of preparing a copper-palladium-containing complex in which at least part of a surface of the palladium-containing fine particle is covered with copper, by passing the dispersion through a reacting part and bringing the palladium-containing fine particle in the dispersion into contact with a copper-containing member in the reacting part; and a substituting step of substituting the copper in the copper-palladium-containing complex emitted from an emitting part with platinum by bringing the complex into contact with a platinum-containing solution.
Opening claim text (preview).
The invention claimed is: 1 . A method for producing a catalyst comprising a fine catalyst particle which comprises a palladium-containing fine particle and a platinum-containing outermost layer covering at least part of the palladium-containing fine particle, wherein a reaction container comprising (1) a supplying part, (2) a reacting part inside which one or more copper-containing members are provided, and (3) an emitting part is used; wherein at least part of a surface of the copper-containing member contains at least one copper-containing material selected from the group consisting of copper, a copper alloy and a copper compound; and wherein the method comprises: a supplying step of supplying a dispersion containing the palladium-containing fine particle from the supplying part into the reaction container; a preparing step of preparing a copper-palladium-containing complex in which at least part of a surface of the palladium-containing fine particle is covered with copper, by passing the dispersion through the reacting part and bringing the palladium-containing fine particle in the dispersion into contact with the copper-containing member in the reacting part; and a substituting step of substituting the copper in the copper-palladium-containing complex emitted from the emitting part with platinum by bringing the complex into contact with a platinum-containing solution. 2 . The method for producing the catalyst according to claim 1 , wherein the dispersion and an inert gas are supplied from the supplying part into the reaction container. 3 . The method for producing the catalyst according to claim 2 , wherein at least the reacting part is a microreactor. 4 . The method for producing the catalyst according to claim 1 , wherein the dispersion contains the palladium-containing fine particle and an acid solution. 5 . The method for producing the catalyst according to claim 1 , wherein the catalyst is a catalyst for fuel cells. 6 . A device for producing a catalyst comprising a fine catalyst particle which comprises a palladium-containing fine particle and a platinum-containing outermost layer covering at least part of the palladium-containing fine particle, wherein the device comprises a reaction container and a reaction vessel; wherein the reaction container comprises: a supplying part for supplying a dispersion containing the palladium-containing fine particle into the reaction container; a reacting part for preparing a copper-palladium-containing complex in which at least part of a surface of the palladium-containing fine particle is covered with copper, by bringing the palladium-containing fine particle in the dispersion supplied from the supplying part into contact with one or more copper-containing members provided inside the reacting part; and an emitting part for emitting the copper-palladium-containing complex to the reaction vessel; wherein at least part of a surface of the copper-containing member contains at least one copper-containing material selected from the group consisting of copper, a copper alloy and a copper compound; and wherein, in the reaction vessel, the copper in the copper-palladium-containing complex emitted from the emitting part is substituted with platinum by bringing the complex into contact with a platinum-containing solution. 7 . The device for producing the catalyst according to claim 6 , wherein the dispersion and an inert gas are supplied from the supplying part into the reaction container. 8 . The device for producing the catalyst according to claim 7 , wherein at least the reacting part is a microreactor. 9 . The device for producing the catalyst according to claim 6 , wherein the dispersion contains the palladium-containing fine particle and an acid solution. 10 . The device for producing the catalyst according to claim 6 , wherein the catalyst is a catalyst for fuel cells.
Metals of platinum group (H01M4/94 {, H01M4/9058} take precedence) · CPC title
Stationary reactors without moving elements inside · CPC title
Feeding or evacuation · CPC title
Microreactors, e.g. miniaturised or microfabricated reactors (laboratory containers with capillary fluid transport in microfabricated channels or chambers B01L3/5027) · CPC title
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
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