Palladium-copper chromite hydrogenation catalysts

• US 7,538,060 B2
• Filed: 02/14/2007
• Issued: 05/26/2009
• Est. Priority Date: 02/14/2007
• Status: Expired due to Fees

• Current Assignee: Eastman Chemical Company
• Original Assignee: Eastman Chemical Company
• Inventors: Worsham, Paul Randolph, Gustafson, Bruce LeRoy, Perri, Steven Thomas, Liu, Zhufang, Barnicki, Scott Donald
• Primary Examiner(s): Price; Elvis O
• Application Number:
  US11/674,831
• Publication Number:
  US 20080194397A1
• Time in Patent Office: 832 Days
• Field of Search: 502/104, 502/110, 502/117, 568/885, 568/833
• US Class Current: 502/104
• CPC Class Codes: B01J 23/868 copper and chromium
• CPC Class Codes: B01J 23/8993 with chromium, molybdenum or tungsten
• CPC Class Codes: B01J 37/0201 Impregnation
• CPC Class Codes: B01J 37/0205 in several steps
• CPC Class Codes: B01J 37/03 Precipitation; Co-precipitation
• CPC Class Codes: C07C 2601/14 The ring being saturated
• CPC Class Codes: C07C 29/149 with hydrogen or hydrogen-containing gases
• CPC Class Codes: C07C 29/157 containing platinum group metals or compounds thereof
• CPC Class Codes: C07C 31/04 Methanol
• CPC Class Codes: C07C 31/202 Ethylene glycol
• CPC Class Codes: C07C 31/276 with a six-membered ring
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

Disclosed are catalysts comprising copper chromite, palladium and lanthanum having hydrogenation activity. The combination of copper chromite with palladium and lanthanum enhances catalyst activity more than the presence of either palladium alone or palladium in combination with alkali or alkaline earth metals. The catalysts are useful for the preparation of methanol from carbon monoxide and hydrogen and for the hydrogenation of carbonyl compounds such as, for example, aldehydes, ketones, and esters, to their corresponding alcohols. The catalysts may be used for the preparation of cyclohexanedimethanols from dialkyl cyclohexanedicarboxylates or of ethylene glycol from alkyl glycolates.

Claims

1. A catalyst, comprising:

copper chromite, palladium, and lanthanum, wherein said palladium and lanthanum are deposited on said copper chromite.

2. The catalyst according to claim 1 which comprises about 0.1 to about 10 weight percent palladium, based on the total weight of said catalyst.

3. The catalyst according to claim 2 which comprises about 0.5 to about 5 weight percent palladium.

4. The catalyst according to claim 3 which comprises about 0.5 to about 2 weight percent palladium.

5. The catalyst according to claim 1 which comprises about 500 to about 8000 parts per million of said lanthanum, based on the total weight of said catalyst.

6. The catalyst according to claim 5 which comprises about 1000 to about 5000 parts per million of said lanthanum.

7. The catalyst according to claim 1 which comprises at least 60 weight percent weight percent of said copper chromite, based on the total weight of the catalyst.

8. The catalyst according to claim 1 wherein said copper chromite comprises about 15 to 60 weight percent copper and about 15 to 60 weight percent chromium, based on the weight of said copper chromite.

9. The catalyst according to claim 1 wherein said copper chromite comprises a gram-atom ratio of copper to chromium of about 1:

10 to about 10;

1.

10. The catalyst according to claim 9 wherein said copper chromite comprises a gram-atom ratio of copper to chromium of about 1:

5 to about 5;

1.

11. The catalyst according to claim 10 wherein said copper chromite comprises a gram-atom ratio of copper to chromium of about 1:

2 to about 2;

1.

12. A catalyst, comprising:

copper chromite having a gram-atom ratio of copper to chromium of about 1;

2 to about 2;

1, about 0.5 to about 1.5 weight percent palladium, and about 4000 to about 6000 ppm lanthanum, wherein said palladium and said lanthanum are deposited on said copper chromite.

13. A catalyst, consisting essentially of:

copper chromite having a gram-atom ratio of copper to chromium of about 1;

2 to about 2, about 0.5 to about 1.5 weight percent palladium, and about 4000 to about 6000 ppm lanthanum, wherein said palladium and said lanthanum are deposited on said copper chromite.

14. A process for the preparation of a catalyst, comprising:

contacting copper chromite with a solution of a palladium compound and a solution of a lanthanum compound;

drying said copper chromite, and calcining said dried copper chromite.

15. The process according to claim 14 wherein said catalyst comprises about 0.1 to about 10 weight percent palladium and about 500 to about 8000 parts per million of lanthanum deposited on said copper chromite, wherein said weight percentage and parts per million are based on the total weight of said hydrogenation catalyst.

16. The process according to claim 15 further comprising, (i) contacting copper chromite with a solution of a palladium compound;

(ii) drying said copper chromite;

(iii) calcining said dried copper chromite from step (ii);

(iv) contacting said calcined copper chromite from step (iii) with a solution of a lanthanum compound;

(v) drying said copper chromite from step (iv); and

(vi) calcining said dried copper chromite from step (v).

17. The process according to claim 16 wherein said drying steps (ii) and (v) independently are carried out at a temperature of about 40 to about 150°

C. and said calcination steps (iii) and (vi) independently are carried out at a temperature of about 400 to about 600°

C.

18. The process according to claim 16 wherein said catalyst comprises about 0.5 to about 2 weight percent palladium and about 1000 to about 5000 parts per million of lanthanum.

19. A process for the preparation of methanol, comprising:

contacting a gaseous feed comprising hydrogen, carbon monoxide, and optionally carbon dioxide, with a catalyst, comprising;

copper chromite, palladium, and lanthanum, wherein said palladium and lanthanum are deposited on said copper chromite.

20. The process according to claim 19 wherein said catalyst comprises about 0.1 to about 10 weight percent palladium, based on the total weight of said catalyst.

21. The process according to claim 20 wherein said catalyst comprises about 0.5 to about 5 weight percent palladium.

22. The process according to claim 19 wherein said catalyst comprises about 500 to about 8000 parts per million of said lanthanum, based on the total weight of said catalyst.

23. The process according to claim 22 wherein said catalyst comprises about 1000 to about 5000 parts per million of said lanthanum.

24. The process according to claim 19 wherein said copper chromite comprises a gram-atom ratio of copper to chromium of about 1:

2 to about 2;

1.

25. The process according to claim 19 wherein said catalyst comprises about 0.5 to about 1.5 weight percent palladium, about 4000 to about 6000 ppm lanthanum, and wherein said copper chromite comprises a gram-atom ratio of copper to chromium of about 1:

2 to about 2;

1.

26. The process according to claim 19 wherein said catalyst comprises about 85 to about 99.85 weight percent said copper chromite.

27. The process according to claim 19 wherein said copper chromite comprises about 15 to 60 weight percent copper and about 15 to 60 weight percent chromium, based on the weight of said copper chromite.

28. The process according to claim 19 wherein said contacting is at temperature of about 150 to about 350°

C. and at a pressure of about 10 to about 100 bara.

29. The process according to claim 28 wherein said contacting is at a temperature of about 180 to about 250°

C. and at a pressure of about 30 to about 70 bara.

30. The process according to claim 19 wherein said gaseous feed comprises about 1 to about 25 weight % carbon dioxide, based on the total volume of said gaseous feed.

31. The process according to claim 30 wherein said gaseous feed comprises about 1 to about 5 weight percent carbon dioxide.

32. The process according to claim 30 wherein said gaseous feed comprises about 10 to about 20 weight percent carbon dioxide.

33. The process according to claim 19 which comprises contacting said gaseous feed and said catalyst in a fixed bed or a liquid slurry phase reactor.

34. A process for hydrogenating an carbonyl compound to an alcohol, comprising contacting at least one carbonyl compound with hydrogen in the presence of a catalyst, comprising:

copper chromite, palladium, and lanthanum are, wherein said palladium and lanthanum deposited on said copper chromite.

35. The process according to claim 34 wherein said carbonyl compound comprises at least one aldehyde, ketone, carboxylic acid ester, or combinations thereof.

36. The process according to claim 35 wherein said carboxylic acid ester comprises at least one alkyl carboxylate comprising the residue of at least one hydroxy compound containing from 1 to about 40 carbon atoms.

37. The process according to claim 36 wherein said hydroxy compound is selected from methanol, ethanol, propanol, 1-butanol, 2-butanol, 2-ethylhexanol, 2,2-dimethyl-1,3-propanediol, ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,10-decanediol, cyclohexanol, 4-methylcyclohexanemethanol, diethylene glycol, glycerin, and trimethylol propane.

38. The process according to claim 36 wherein said alkyl carboxylate comprises the residue of at least one aliphatic, cycloaliphatic, aryl, or aralkyl carboxylic acid having from 1 to about 40 carbon atoms.

39. The process according to claim 38 wherein said alkyl carboxylate comprises an alkyl glycolate.

40. The process according to claim 39 wherein said alkyl glycolate comprises methyl glycolate.

41. The process according to claim 38 wherein said cycloaliphatic carboxylic acid is selected from 1,2-cyclohexanedicarboxylic acid, 1,3-cyclo-hexanedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, and combinations thereof.

42. A process for the preparation of a cyclohexanedimethanol comprising contacting at least one dialkyl cyclohexanedicarboxylate with hydrogen in the presence of a catalyst, comprising:

copper chromite, palladium, and lanthanum are, wherein said palladium and lanthanum deposited on said copper chromite.

43. The process according to claim 42 wherein said dialkyl cyclohexane-dicarboxylate is a dialkyl 1,4-cyclohexane dicarboxylate comprising residues of at least one hydroxy compound containing from 1 to about 20 carbon atoms.

44. The process according to claim 43 wherein said dialkyl 1,4-cyclohexane-dicarboxylate has a cis:

trans molar ratio of about 1;

1 to about 2;

1 and said 1,4-cyclohexanedimethanol has a cis;

trans molar ratio of 0.7;

1 to about 2;

1.

45. The process according to claim 43 wherein said hydroxy compound is selected from methanol, ethanol, propanol, 1-butanol, 2-butanol, 2-ethylhexanol, 2,2-dimethyl-1,3-propanediol, ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,10-decanediol, cyclohexanol, 4-methylcyclohexanemethanol, diethylene glycol, glycerin, and trimethylolpropane.

46. The process according to claim 42 which is a continuous process.

47. The process according to claim 46 which is conducted in the liquid phase, vapor phase, or a combination of liquid and vapor phase.

48. The process according to claim 47 which is at a temperature of about 150°

C. to about 350°

C. and at a pressure is about 40 to about 450 bara.

49. The process according to claim 48 wherein said dialkyl cyclohexane-dicarboxylate comprises dimethyl 1,4-cyclohexanedicarboxylate.

50. The process according to claim 49 wherein said contacting is at a temperature of about 180 to about 250°

C. and at a pressure of about 200 to about 350 bara.

51. The process according to claim 50 which comprises contacting said hydrogen said catalyst in a fixed bed or a liquid slurry phase reactor.