Scalable shape- and size-controlled synthesis of metal nano-alloys

Patent metadata

Field	Value
Publication number	US-10493533-B2
Application number	US-201515326559-A
Country	US
Kind code	B2
Filing date	Jul 15, 2015
Priority date	Jul 17, 2014
Publication date	Dec 3, 2019
Grant date	Dec 3, 2019

Abstract

Embodiments of the present disclosure provide for a continuous-flow reactor, methods of making metal nano-alloys, and metal nano-alloys.

First claim

We claim:

1. A method of producing a metal nano-alloy, the method comprising:
contacting a solution comprising a reducible metal precursor and a reducing gas in a continuous-flow reactor to form a mixed solution; and
flowing the mixed solution through a coil reactor of a continuous-flow reactor for a residence time to form the metal nano-alloy;
wherein the reducible metal precursor is selected from the group consisting of a metal-based salt or a hydrated form thereof, a metal-based acid or a hydrated form thereof, a metal-based base or hydrated form thereof, an organometallic compound, and a combination thereof;
wherein the reducing gas is selected from the group consisting of hydrogen gas, carbon monoxide gas, ammonia gas, ozone gas, peroxide gas, hydrogen sulfide gas, and a combination thereof.

2. The method of claim 1 , including providing the continuous-flow reactor: with a first tubular component having a tubular inlet and a tubular outlet, and a heated tube-in-tube gas reactor fluidly connected to the first tubular component, wherein the heated tube-in-tube gas reactor is provided with an inner tube having a gas permeable surface and an outer tube.

3. The method of claim 2 , wherein the surface of the inner tube is made of a material that is impermeable to a fluid stream but is permeable or semi-permeable to one or more reducing gases, thereby providing for the flow of the one or more reducing gases between a volume of the inner tube and a volume of the outer tube.

4. The method of claim 1 , wherein the reducible metal precursor is selected from the group consisting of: PtCl 2 , PtCl 4 , K 2 PtCl 6 , K 2 PtCl 4 , H 2 PtCl 6 , H 2 PtBr 6 , Pt(NH 3 )Cl 2 , PtO 2 , Na 2 PdCl 4 , Pd(NO 3 ) 2 , HAuCl 4 , Ag(NO 3 ) 2 , NiCl 2 , CoCl 2 , CuCl 2 , and FeCl 3 .

5. The method of claim 1 , wherein the reducible metal precursor is selected from the group consisting of: a metal-acetylacetonate compound, a metal-fluoroacetylacetonate compound, a metal-acetate compound, a metal-cyclooctadien e compound, and a combination thereof.

6. The method of claim 1 , wherein the metal nano-alloy is a pure metal nano-alloy, wherein the metal nano-alloy comprises two or more metals selected from the group consisting of Ni, Pt, Pd, Ru, Rh, Ir, Cu, Co, Fe, Ag, Au, and Mn.

7. The method of claim 6 , wherein the metal nano-alloy is selected from the group consisting of PtNi, PtCu, PtCo, PtFe, PtPd, PtAg, PtAu, PtMn, PtRu, NiAg, NiPd, NiAgPd, CuRh, CuRu, NiRh, NiRu, and Ptlr alloys.

8. The method of claim 1 , including providing the continuous-flow reactor with two or more tubular components each having a tubular inlet and a tubular outlet, the tubular outlets being interconnected and configured to combine a fluid steam from each of the two or more tubular components and direct the combined fluid stream into a heated coil reactor, and a heated tube-in-tube gas reactor fluidly connected to at least one of the tubular components, wherein the heated tube-in-tube gas reactor comprises an inner tube having a gas permeable surface and an outer tube.

9. The method of claim 1 , wherein the solution of the reducible metal precursor further comprises a surfactant selected from the group consisting of oleylamine, octadecylamine, hexadecylamine, dodecylamine, octylamine, butylamine, oleic acid, adamantaneacetic acid, adamantinecarboxylic acid, polyvinylpyrrolidone (PVP), citrate acid, sodium citrate, cetylpyridinium chloride (CPC), tetractylammonium bromide (TTAB), cetyl trimethylammonium bromide (CTAB), cetyl trimethylammonium chloride (CTACI) and combinations thereof.

10. The method of claim 9 , wherein the reducing gas is carbon monoxide, the surfactant is adamantinecarboxylic acid or oleylamine, and the reducible metal precursor is a metal-acetylacetonate compound, PtCl 2 , PtCl 4 , K 2 PtCl 6 , K 2 PtCl 4 , H 2 PtCl 6 , H 2 PtBr 6 , Pt(NH 3 )Cl 2 , Na 2 PdCl 4 , HAuCl 4 , NiCl 2 , CoCl 2 , CuCl 2 , FeCl 3 , or a combination thereof.

Assignees

• Univ King Abdullah Sci & Tech

Inventors

• Bakr Osman M
• Knudsen Kristian Rahbek
• Lagrow Alec
• Alyami Noktan M
• Mehenni Hakim

Classifications

• B22F1/054

  Nanosized particles · CPC title

• B01J2219/00033

  Continuous processes · CPC title

• C22C5/04

  Alloys based on a platinum group metal · CPC title

• C22C19/03

  based on nickel · CPC title

• B22F9/26 Primary

  using gaseous reductors · CPC title