Rare earth metals as oxidative dehydrogenation catalysts

• US 20040176656A1
• Filed: 03/23/2004
• Published: 09/09/2004
• Est. Priority Date: 10/08/2002
• Status: Abandoned Application

• Current Assignee: Conocophillips Company (ConocoPhillips)
• Original Assignee: Conocophillips Company (ConocoPhillips)
• Inventors: Ramani, Sriram, Chen, Zhen, Allison, Joe D., Gaffney, Anne, Chen, Shang Y., Carmichael, Lisa M., McDonald, Steve R.
• Application Number:
  US10/806,882
• Publication Number:
  US 20040176656A1
• Time in Patent Office: Days
• US Class Current: 585/658
• CPC Class Codes: B01J 23/10 of rare earths
• CPC Class Codes: B01J 23/63 with rare earths or actinides
• CPC Class Codes: C07C 11/02 Alkenes
• CPC Class Codes: C07C 11/04 Ethylene
• CPC Class Codes: C07C 2523/10 of rare earths
• CPC Class Codes: C07C 2523/56 Platinum group metals
• CPC Class Codes: C07C 5/48 with oxygen as an acceptor
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

Catalysts and methods useful for the production of olefins from alkanes via oxidative dehydrogenation (ODH) are disclosed. The ODH catalysts include a base metal selected from the group consisting of lanthanide metals, their oxides, and combinations thereof. The base metal is more preferably selected from the group consisting of samarium, cerium, praseodymium, terbium, their corresponding oxides and combinations thereof. The base metal loading is preferably between about 0.5 and about 20 weight percent and more preferably between about 2 and about 10 weight percent. Optionally, the ODH catalysts are further comprised of a Group VIII promoter metal present at trace levels. The Group VIII promoter metal is preferably platinum, palladium or a combination thereof and is preferably present at a promoter metal loading of between about 0.005 and about 0.1 weight percent. Optionally, the ODH catalyst is supported on a refractory support.

Claims

1. A method for oxidative dehydrogenation comprising

a) providing a reactant mixture comprising one or more hydrocarbons and an oxidant;

b) providing an ODH catalyst comprising a base metal selected from the group consisting of lanthanide metals, their oxides and combinations thereof;

c) exposing the reactant mixture to the ODH catalyst in a reactor under reaction promoting conditions; and

d) oxidatively dehydrogenating at least a fraction of the one or more hydrocarbons in the reactant mixture.

2. The method of claim 1 wherein the reactor is a short contact time reactor operated at a GHSV between about 20,000 hr⁻

1 and about 200,000,000 hr<sup>−

1</sup>.

3. The method of claim 1 wherein the reactor is a short contact time reactor operated at a GHSV between about 50,000 hr⁻

1 and about 50,000,000 hr<sup>−

1</sup>.

4. The method of claim 1 wherein the oxidant comprises a molecular oxygen-containing gas and the one or more hydrocarbons comprise one or more alkanes.

5. The method of claim 4 wherein the one or more alkanes comprise one or more paraffins with between 2 and 10 carbon atoms.

6. The method of claim 4 wherein the one or more alkanes comprise one or more paraffins with between 2 and 5 carbon atoms.

7. The method of claim 4 further comprising the step of pre-heating the reactant mixture to about 600°

C. or less.

8. The method of claim 4 further comprising the step of preheating the reactant mixture to about 300°

C. or less.

9. The method of claim 4 wherein the atomic oxygen-to-carbon ratio is between about 0.05:

1 and about 5;

1.

10. The method of claim 4 wherein the alkane conversion is at least about 40 percent and the alkene selectivity is at least about 35 percent.

11. The method of claim 4 wherein the alkane conversion is at least about 85 percent and the alkene selectivity is at least about 60 percent.

12. The method of claim 1 wherein the base metal is present at a base metal loading between about 0.5 and about 20 weight percent.

13. The method of claim 1 wherein the base metal is present at a base metal loading between about 2 and about 10 weight percent.

14. The method of claim 1 wherein the base metal is selected from the group consisting of samarium, cerium, praseodymium, terbium, their corresponding oxides and combinations thereof.

15. The method of claim 1 wherein the ODH catalyst further comprises a promoter metal selected from the group consisting of Group VIII metals, their oxides and combinations thereof and present at a promoter metal loading between about 0.005 and 0.10 weight percent.

16. The method of claim 1 wherein the ODH catalyst further comprises a promoter metal selected from the group consisting of rhodium, platinum, palladium, ruthenium or iridium and combinations thereof.

17. The method of claim 15 wherein the ODH catalyst has a molar ratio of base metal to promoter metal of about 10 or more.

18. The method of claim 15 wherein the ODH catalyst has a molar ratio of base metal to promoter metal of about 25 or more.

19. The method of claim 1 wherein the ODH catalyst further comprises a refractory support.

20. The method of claim 19 wherein the refractory support is comprised of a material selected from group consisting of zirconia, stabilized zirconias, alumina, stabilized aluminas, and combinations thereof.

21. The method of claim 19 wherein the ODH catalyst further comprises a promoter metal selected from the group consisting of Group VIII metals, their oxides and combinations thereof and present at a promoter metal loading between about 0.005 and 0.10 weight percent.

22. The method of claim 19 wherein the ODH catalyst further comprises a promoter metal selected from the group consisting of rhodium, platinum, palladium, ruthenium or iridium and combinations thereof.

23. The method of claim 21 wherein the ODH catalyst has a molar ratio of base metal to promoter metal of about 10 or more.

24. The method of claim 21 wherein the ODH catalyst has a molar ratio of base metal to promoter metal of about 25 or more.