Catalysts for use in steam reforming processes

Patent metadata

Field	Value
Publication number	US-9511351-B2
Application number	US-201213981763-A
Country	US
Kind code	B2
Filing date	Feb 6, 2012
Priority date	Feb 14, 2011
Publication date	Dec 6, 2016
Grant date	Dec 6, 2016

Abstract

A method is described for preparing a catalyst suitable for use in a steam reforming process, including the steps of: (i) spraying a slurry containing a particulate catalyst compound, including one or more catalytic metals selected from the group consisting of Ni, Cu, Pt, Pd, Rh, Ru and Au, on to the surface of a shaped support in a pan coater to form a coated shaped support material having the catalytic metal in a surface layer, (ii) drying and optionally calcining the coated shaped support material to form a catalyst precursor, and (iii) optionally reducing the metal or metals in the catalyst precursor to a lower oxidation state to form the catalyst. The egg-shell catalyst is useful for performing a steam reforming reaction.

First claim

The invention claimed is:

1. A method for preparing a catalyst suitable for use in a steam reforming process, comprising the steps of:
(i) spraying a slurry containing a particulate catalyst compound, comprising one or more catalytic metals selected from the group consisting of Ni, Cu, Pt, Pd, Rh, Ru and Au, on to the surface of a shaped support in a pan coater to form a coated shaped support material having the catalytic metal in a surface layer, wherein the solids content of the slurry is in the range 1-60% by weight, and
(ii) drying the coated shaped support material to form a catalyst precursor,
wherein the shaped support comprises extrudates, pellets or granules having a length of 1 mm to 50 mm, a cross sectional width or diameter of 1 mm to 25 mm, and an aspect ratio of length/cross-section ≦2.

2. The method according to claim 1 wherein the catalytic metal in the particulate catalyst compound comprises Ni, optionally with one or more of Pt, Pd, Rh, Ru and Au.

3. The method according to claim 1 wherein the catalytic metal in the particulate catalyst compound comprises Pt, optionally with one or more of Pd, Rh, Ru and Au.

4. The method according to claim 1 wherein the catalytic metal in the particulate catalyst compound consists of Rh.

5. The method according to claim 1 wherein the particulate catalyst compound comprises an oxide, hydroxide or carbonate of the catalytically active metal.

6. The method according to claim 1 wherein the particulate catalyst compound comprises one or more metals selected from the group consisting of Ni, Cu, Pt, Pd, Rh, Ru and Au dispersed over the surface of a particulate catalyst support material.

7. The method according to claim 6 wherein the particulate catalyst support material is selected from the group consisting of alumina, titania or zirconia, zinc oxide, lanthana, magnesia, ceria, metal-aluminates and mixtures thereof.

8. The method according to claim 6 wherein the particulate catalyst support material comprises alumina and/or stabilised zirconia.

9. The method according to claim 1 wherein one or more intermediate layers are applied between the shaped support and the catalytic surface layer.

10. The method according to claim 1 wherein the shaped support units are multiholed-pellets or extrudates with a cross-section that is circular, lobed or fluted.

11. The method according to claim 1 wherein the shaped support is a refractory oxide comprising a support oxide selected from the group consisting of alumina, ceria, magnesia, titania or zirconia, calcium aluminate or magnesium aluminate; and mixtures thereof.

12. The method according to claim 1 wherein the shaped support is calcium aluminate, magnesium aluminate or alpha alumina.

13. The method according to claim 1 wherein the support is coated at a temperature in the range 30-60° C.

14. The method according to claim 1 wherein the thickness of the layer containing the catalytically active metal in the dried material is in the range 5 to 250 μm.

15. The method according to claim 1 wherein a polyethylene graft co-polymer is included in the slurry.

16. The method according to claim 1 wherein the dried coated support material is calcined.

17. The method according to claim 16 wherein the calcined coated support material is reduced.

18. The method according to claim 17 wherein the reduction is performed by passing a hydrogen-containing gas over the catalyst at a temperature in the range 200-600° C. for between 1 and 24 hours at atmospheric or higher pressures up to about 25 bar.

19. The method according to claim 17 wherein the reduced catalyst is passivated.

20. The method according to claim 1 wherein the catalytic metal in the particulate catalyst compound comprises Pt with Rh.

Assignees

• Feaviour Mark Robert
• Johnson Matthey Plc

Inventors

• Feaviour Mark Robert

Classifications

• B01J23/42 Primary

  Platinum · CPC title

• B01J23/464

  Rhodium · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title

• C01B3/40

  characterised by the catalyst · CPC title

• C01B2203/1217

  Alcohols · CPC title