IP Library Granted Patent US 7,273,893
Granted Patent B2
US 7,273,893 · App. 10/683,974 · Granted Sep 25, 2007

Process for converting carbon dioxide to oxygenates

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Quick Facts
Patent No.
US 7,273,893
App. No.
10/683,974
Granted
Sep 25, 2007
Kind
B2
Abstract

A catalyst and process for converting carbon dioxide into oxygenates. The catalyst comprises copper, zinc, aluminum, gallium, and a solid acid.

Claims (83)

1. A process for converting a carbon dioxide-containing feed into oxygenates, said process comprising the steps of:

(a) contacting said carbon dioxide-containing feed with a catalyst composition comprising a solid acid in a reaction zone under reaction conditions sufficient to convert at least a portion of said feed stream into oxygenates, said carbon dioxide-containing feed comprising at least 90 volume percent carbon dioxide and hydrogen, said solid acid comprising a zeolite; and

(b) recovering at least a portion of said oxygenates from said reaction zone.

2. A process according to claim 1 ,

said catalyst composition comprising gallium.

3. A process according to claim 1 ,

said carbon dioxide-containing feed comprising at least 98 volume percent carbon dioxide and hydrogen.

4. A process according to claim 3 ,

said catalyst composition comprising gallium and copper.

5. A process according to claim 1 ,

said carbon dioxide-containing feed consisting essentially of carbon dioxide and hydrogen.

6. A process according to claim 5 ,

said catalyst composition comprising gallium, copper, zinc, and aluminum.

7. A process according to claim 1 ,

said feed comprising carbon dioxide and hydrogen in a volume ratio of about 1:1 to about 50:1.

8. A process according to claim 1 ,

said oxygenates comprising dimethyl ether.

9. A process for converting a carbon dioxide-containing feed into oxygenates, said process comprising the steps of:

(a) contacting said carbon dioxide-containing feed with a catalyst composition comprising copper, zinc, aluminum, gallium, and a solid acid comprising a zeolite in a reaction zone under reaction conditions sufficient to convert at least a portion of said carbon dioxide-containing feed into oxygenates; and

(b) recovering at least a portion of said oxygenates from said reaction zone.

10. A process according to claim 9 , said solid acid comprising ZSM-5.

11. A process according to claim 9 ,

said reaction conditions including a temperature of from about 50° C. to about 500° C. and a pressure of from about 200 psig to about 5,000 psig.

12. A process according to claim 9 ,

said carbon dioxide-containing feed being charged to said reaction zone at a GHSV of from about 100 to about 20,000 hr-1.

13. A process according to claim 9 ,

said carbon dioxide-containing feed consisting essentially of carbon dioxide and hydrogen.

14. A process according to claim 9 ,

said carbon dioxide-containing feed further comprising hydrogen.

15. A process according to claim 14 ,

said carbon dioxide-containing feed comprising said hydrogen and said carbon dioxide in amounts such that the volume ratio of said hydrogen to said carbon dioxide of said feed is in the range of from about 0.1:1 to about 100.1.

16. A process according to claim 15 ,

said carbon dioxide-containing feed comprising said carbon dioxide in an amount in the range of from about 1 to about 50 volume percent by volume of the total carbon dioxide-containing feed.

17. A process according to claim 16 ,

said carbon dioxide-containing feed comprising said hydrogen in an amount in the range of from about 50 to about 99 volume percent by volume of the total carbon dioxide-containing feed.

18. A process according to claim 17 ,

said carbon dioxide-containing feed comprising compounds other than carbon dioxide and hydrogen in an amount which is less than about 20 volume percent by volume of the total carbon dioxide-containing feed.

19. A process for converting a carbon dioxide-containing feed stream into oxygenates, said process comprising the steps of:

(a) contacting said feed stream with a catlyst composition comprising gallium and a solid acid comprising zeolite in a reaction zone under reaction conditions sufficient to convert at least a portion of said feed stream into oxygenates, said feed stream comprising carbon dioxide and hydrogen in a volume ration of about 0.1:1 to about 100:1, and said feed stream comprising less than about 20 volume percent of components other than hydrogen and carbon dioxide; and

(b) recovering at least a portion of said oxygenates from said reaction zone.

20. A process according to claim 19 ,

said feed stream comprising carbon dioxide and hydrogen in a volume ratio of about 1:1 to about 50:1.

21. A process according to claim 19 ,

said feed stream comprising carbon dioxide and hydrogen in a volume ration of 5:1 to 15:1.

22. A process according to claim 19 ,

said feed stream comprising less than about 10 volume percent of components other than carbon dioxide and hydrogen.

23. A process according to claim 19 ,

said feed stream comprising less than 2 volume percent of components other than carbon dioxide and hydrogen.

24. A process according to claim 19 ,

said feed stream consisting essentially of carbon dioxide and hydrogen.

25. A process according to claim 19 ,

step (a) including reacting carbon dioxide with hydrogen to thereby produce said oxygenates.

26. A process according to claim 19 ,

said oxygenates comprising dimethyl ether.

27. A process according to claim 19 ,

said catalyst composition comprising copper.

28. A process according to claim 27 ,

said catalyst composition comprising zinc.

29. A process according to claim 28 ,

said catalyst composition comprising aluminum.

30. A process for converting a carbon dioxide-containing feed into oxygenates, said process comprising the steps of:

(a) contacting said carbon dioxide-containing feed with a catalyst composition comprising a gallium and a solid acid comprising a zeolite in a reaction zone under reaction conditions sufficient to convert at least a portion of said feed stream into a product stream comprising dimethyl ether.

(b) recovering at least a portion of said dimethyl ether from said reaction zone.

31. A process according to claim 30 ,

said carbon dioxide-containing feed comprising at least about 80 volume percent carbon dioxide and hydrogen,

said product stream comprising at least about 20 carbon mole percent dimethyl ether.

32. A process according to claim 31 ,

said product stream comprising less than about 50 carbon mole percent methanol.

33. A process according to claim 30 ,

said carbon dioxide containing feed comprising at least 98 volume percent carbon dioxide and hydrogen,

said product stream comprising at least 60 carbon mole percent dimethyl ether.

34. A process according to claim 33 ,

said product stream comprising less than 25 carbon mole percent methanol.

35. A process according to claim 30 ,

said carbon dioxide-containing feed consisting essentially of carbon dioxide and hydrogen.

36. A process according to claim 30 ,

step (a) including converting carbon dioxide into said dimethyl ether.

37. A process according to claim 30 ,

said catalyst composition comprising copper.

38. A process according to claim 37 ,

said catalyst composition comprising zinc.

39. A process according to claim 38 ,

said catalyst composition comprising aluminum.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 15, 2012
From: CONOCOPHILLIPS COMPANY
To: PHILLIPS 66 COMPANY
Reel/Frame 028213/0824 →
CHANGE OF NAME Recorded Jun 8, 2009
From: PHILLIPS PETROLEUM COMPANY
To: CONOCOPHILLIPS COMPANY
Reel/Frame 022783/0989 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 10, 2003
From: YAO, JIANHUA; KIMBLE, JAMES B.
To: PHILLIPS PETROLEUM COMPANY
Reel/Frame 014597/0257 →