Hydrogen generation catalysts and methods for hydrogen generation

• US 20060292067A1
• Filed: 06/28/2005
• Published: 12/28/2006
• Est. Priority Date: 06/28/2005
• Status: Abandoned Application

• Current Assignee: Millennium Cell Inc.
• Original Assignee: Millennium Cell Inc.
• Inventors: Wu, Ying, Binder, Michael, Zhang, Qinglin, Smith, Gregory M.
• Application Number:
  US11/167,607
• Publication Number:
  US 20060292067A1
• Time in Patent Office: Days
• US Class Current: 423/648.1
• CPC Class Codes: B01J 23/892 Nickel and noble metals
• CPC Class Codes: B01J 37/0225 of metal substrates
• CPC Class Codes: C01B 3/065 from a hydride
• CPC Class Codes: Y02E 60/36 Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Abstract

Supported catalyst methods are provided to promote hydrogen generation from the hydrolysis of boron hydrides. The methods use a supported catalyst which is a supported metallic mixture comprising a first transition metal selected from the group consisting of cobalt, ruthenium, zinc, molybdenum, manganese, titanium, tin, cadmium, and iridium, in an amount of from about 0.1 to about 20% by weight, and a second metal selected from the group consisting of cobalt, ruthenium, zinc, molybdenum, manganese, titanium, tin, cadmium, boron, and iridium, in an amount of from about 0.05 to about 25% by weight of the supported catalyst.

Claims

1. A method of generating hydrogen gas, comprising:

providing an aqueous fuel solution comprising a material selected from the group consisting of boranes, polyhedral boranes, borohydride salts, and polyhedral borane salts; and

contacting the aqueous fuel solution with a hydrogen generation catalyst comprising a support, a first metal selected from the group consisting of cobalt, ruthenium, zinc, molybdenum, manganese, titanium, tin, cadmium, and iridium, the first metal being present in an amount of about 0.05 to about 20% by weight of the hydrogen generation catalyst; and

a second metal selected from the group consisting of cobalt, ruthenium, zinc, molybdenum, manganese, titanium, tin, cadmium, boron, and iridium to produce hydrogen gas, the second metal being present in an amount of about 0.01 to about 25% by weight of the hydrogen generation catalyst.

2. The method of claim 1, wherein the first metal is cobalt and the second metal is ruthenium.

3. The method of claim 1, wherein the first metal is present in an amount of about 1 to about 10% by weight.

4. The method of claim 1, wherein the first metal is present in an amount of about 1 to about 5% by weight.

5. The method of claim 1, wherein the second metal is present in an amount of about 0.1 to about 2% by weight.

6. The method of claim 1, wherein conversion of the aqueous fuel solution with the hydrogen generation catalyst is conducted with a conversion rate of at least 80%.

8. The method of claim 1, wherein the second metal is present in an amount of about 0.1 to about 2% by weight of the supported catalyst.

9. The method of claim 1, wherein the first metal is cobalt.

10. The method of claim 9, wherein the second metal is selected from the group consisting of ruthenium, manganese, molybdenum, and zinc.

11. The method of claim 1, wherein the support contains a material selected from the group consisting of activated carbon, coke, and charcoal.

12. The method of claim 1, wherein the support contains at least one refractory inorganic oxide.

13. The method of claim 1, wherein the support contains a metal in the form of a foam, sintered particle, fiber, monolith, or a mixture thereof.

14. The method of claim 1, wherein the support is in the form of a perovskite of the formula ABO₃, wherein A is a metallic atom with a valence of +2 and B is a metallic atom with a valence of +4.

15. The method of claim 1, wherein the catalyst has a BET surface area of about 5 to about 25 m²/g.

16. The method of claim 1, wherein the catalyst has a BET surface area of about 10 m²/g .

17. The method of claim 1, wherein the supported catalyst has pores and an average pore radius of about 5 to about 50 Angstroms.

18. The method of claim 1, wherein the supported catalyst has pores having a volume of about 5 to 100 mL/g.