Supported nickel catalysts used as direct internal reforming catalyst in molten carbonate fuel cells

Patent metadata

Field	Value
Publication number	US-12255367-B2
Application number	US-202318108138-A
Country	US
Kind code	B2
Filing date	Feb 10, 2023
Priority date	Apr 11, 2016
Publication date	Mar 18, 2025
Grant date	Mar 18, 2025

Abstract

Disclosed here is a supported catalyst comprising a thermally stable core, wherein the thermally stable core comprises a metal oxide support and nickel disposed in the metal oxide support, wherein the metal oxide support comprises at least one base metal oxide and at least one transition metal oxide or rare earth metal oxide mixed with or dispersed in the base metal oxide. Optionally the supported catalyst can further comprise an electrolyte removing layer coating the thermally stable core and/or an electrolyte repelling layer coating the electrolyte removing layer, wherein the electrolyte removing layer comprises at least one metal oxide, and wherein the electrolyte repelling layer comprises at least one of graphite, metal carbide and metal nitride. Also disclosed is a molten carbonate fuel cell comprising the supported catalyst as a direct internal reforming catalyst.

First claim

What is claimed is:

1. A method of synthesizing a supported catalyst, the method comprising:
(a) forming a support comprising: (i) a base metal oxide selected from the group consisting of transition metal oxides, rare earth metal oxides, alkaline earth metal oxides, and post-transition metal oxides, and (ii) at least one transition metal oxide or rare earth metal oxide different from the base metal oxide;
(b) after (a), depositing nickel onto the support to form a thermally stable core;
(c) forming a catalyst tablet from the thermally stable core; and
(d) after (c), coating the catalyst tablet with an electrolyte repelling layer, the electrolyte repelling layer comprising at least one of graphite, a metal carbide, or a metal nitride, wherein the electrolyte repelling layer completely encapsulates the catalyst tablet.

2. The method of claim 1 , wherein the base metal oxide comprises at least one of alumina, CaO, or MgO.

3. The method of claim 1 , wherein the base metal oxide comprises at least one alkaline earth metal oxide or post-transition metal oxide.

4. The method of claim 1 , wherein the nickel is present within a range of 10 to 50 wt. % of the supported catalyst.

5. The method of claim 1 , wherein the supported catalyst is free of silicate.

6. The method of claim 1 , wherein the supported catalyst has a mean pore diameter within a range of 65 to 700 angstroms, as measured by mercury porosimetry of pelletized catalyst, and has a pore size distribution characterized by a standard deviation of less than 10% of the mean pore diameter.

7. The method of claim 1 , wherein the forming comprises extruding the thermally stable core to form the catalyst tablet.

8. A method of synthesizing a supported catalyst, the method comprising:
(a) forming a support comprising: (i) a base metal oxide selected from the group consisting of transition metal oxides, rare earth metal oxides, alkaline earth metal oxides, and post-transition metal oxides, and (ii) at least one transition metal oxide or rare earth metal oxide different from the base metal oxide;
(b) after (a), depositing nickel onto the support to form a thermally stable core;
(c) forming a catalyst tablet from the thermally stable core;
(d) coating the catalyst tablet with an electrolyte removing layer comprising at least one metal oxide, wherein the electrolyte removing layer completely encapsulates the catalyst tablet; and
(e) after (d), coating the electrolyte removing layer with an electrolyte repelling layer, comprising at least one of graphite, metal carbide, or metal nitride, wherein the electrolyte repelling layer completely encapsulates the electrolyte removing layer.

9. The method of claim 8 , wherein the base metal oxide comprises at least one of alumina, CaO, or MgO.

10. The method of claim 8 , wherein the base metal oxide comprises at least one alkaline earth metal oxide or post-transition metal oxide.

11. The method of claim 8 , wherein the nickel is present within a range of 10 to 50 wt. % of the supported catalyst.

12. The method of claim 8 , wherein electrolyte removing layer has a surface area of at least 50 m 2 /g.

13. The method of claim 8 , wherein the supported catalyst has a mean pore diameter within a range of 65 to 700 angstroms, as measured by mercury porosimetry of pelletized catalyst, and has a pore size distribution characterized by a standard deviation of less than 10% of the mean pore diameter.

14. The method of claim 8 , wherein the electrolyte removing layer comprises aluminum oxide, titanium oxide, zirconium oxide, tungsten oxide, doped aluminum oxide, doped titanium oxide, doped zirconium oxide, doped tungsten oxide, or a mixture thereof.

15. The method of claim 8 , wherein the supported catalyst is free of silicate.

16. The method of claim 8 , wherein the forming comprises extruding the thermally stable core to form the catalyst tablet.

17. A method of synthesizing a supported catalyst, the method comprising:
(a) forming a thermally stable core by co-precipitating nickel with: (i) a base metal oxide selected from the group consisting of transition metal oxides, rare earth metal oxides, alkaline earth metal oxides, and post-transition metal oxides, and (ii) at least one transition metal oxide or rare earth metal oxide different from the base metal oxide; and
(b) forming a catalyst tablet from the thermally stable core; and
(c) coating the catalyst tablet with an electrolyte repelling layer, the electrolyte repelling layer comprising at least one of graphite, a metal carbide, or a metal nitride, wherein the electrolyte repelling layer completely encapsulates the catalyst tablet.

18. The method of claim 17 , wherein the base metal oxide comprises at least one of alumina, CaO, or MgO.

19. The method of claim 17 , wherein the base metal oxide comprises at least one alkaline earth metal oxide or post-transition metal oxide.

20. The method of claim 17 , wherein the nickel is present within a range of 10 to 50 wt. % of the supported catalyst.

21. The method of claim 17 , wherein the supported catalyst is free of silicate.

22. The method of claim 17 , wherein the supported catalyst has a mean pore diameter within a range of 65 to 700 angstroms, as measured by mercury porosimetry of pelletized catalyst, and has a pore size distribution characterized by a standard deviation of less than 10% of the mean pore diameter.

23. The method of claim 17 , wherein the forming comprises extruding the thermally stable core to form the catalyst tablet.

Assignees

• Fuelcell Energy Inc

Inventors

• Wang Jin-Yun
• Farooque Mohammad
• Venkataraman Ramakrishnan
• Yuh Chao-Yi
• Corpuz April

Classifications

• H01M2008/147

  Fuel cells with molten carbonates · CPC title

• B01J21/066

  Zirconium or hafnium; Oxides or hydroxides thereof · CPC title

• B01J35/653

  500-1000 nm · CPC title

• B01J35/651

  50-500 nm · CPC title

• B01J35/647

  2-50 nm · CPC title