Catalyst composition for oxidation of ethylene to ethylene oxide

• US 4,908,343 A
• Filed: 10/03/1988
• Issued: 03/13/1990
• Est. Priority Date: 02/20/1987
• Status: Expired due to Term

• Current Assignee: Dow Technology Investments LLC (Dow, Inc.)
• Original Assignee: Union Carbide Chemicals And Plastics Company, Inc.
• Inventors: Bhasin, Madan M.
• Primary Examiner(s): SHINE, WILLIAM
• Application Number:
  US07/251,573
• Time in Patent Office: 526 Days
• Field of Search: 502/208, 502/218, 502/317, 502/324, 502/340, 502/341, 502/347, 502/348, 549/536
• US Class Current: 502/218
• CPC Class Codes: B01J 23/66 Silver or gold
• CPC Class Codes: C07D 301/10 with catalysts containing silver or gold

Abstract

This invention relates to catalysts for the manufacture of ethylene oxide, especially at commercial concentrations in the presence of carbon dioxide gas recycle, which contains impregnated silver on a support and a mixture of cesium salt and one or more alkali metal and alkaline earth metal salts in which the anions thereof are halide or oxyanions of elements other than the oxygen therein having an atomic number of 7 or 15 to 83 and being from groups 3b through 7b, inclusive, and 3a through 7a, inclusive, of the Periodic Table of the Elements, at least a portion of said oxyanions are oxyanions of group 3b to 7b elements.

Claims

1. A catalyst for the manufacture of ethylene oxide by the epoxidation of ethylene containing an impregnated silver metal on an inert, refractory solid support and an efficiency-enhancing amount, relative to the amount of silver metal, of a mixture of (i) a cesium salt of an oxyanion of an element selected from Groups 3through 7b inclusive, of the Periodic Table of the Elements, and (ii) at least one of an alkali metal salt of lithium, sodium, potassium and rubidium and an alkaline earth metal salt, in which the anions of such salts are halides of atomic numbers of 9 to 53, inclusive, and oxyanions of elements other than the oxygen therein having an atomic number of 7 or 15 to 83, inclusive, and selected from Groups 3a to 7a, inclusive, and 3b through 7b, inclusive, of the periodic Table of the Elements.

2. The catalyst of claim 1, wherein the cesium salt (i) is a cesium salt of a titanate, tantalate, molybdate, chromate, zirconate, manqanate or vanadate oxyanion, and the salt (ii) is a lithium, sodium, potassium, rubidium, magnesium, calcium, strontium or barium salt of a manqanate, vanadate, titanate, tantalate, tungstate, molybdate, chromate, zirconate, phosphate or sulfate oxyanion.

3. The catalyst of claim 1, wherein the support is alpha alumina.

4. The catalyst of claim 3 which has been subjected to a process for making ethylene oxide by the reaction of ethylene and oxygen in which a stream comprising ethylene, oxygen, recycled carbon dioxide and a gas phase inhibitor is fed to a fixed bed of said catalyst and ethylene oxide is removed from the fixed bed of said catalyst.

5. The catalyst of claim 3, wherein said catalyst has been subjected to a process for making ethylene oxide at STANDARD ETHYLENE OXIDE PROCESS CONDITIONS under oxygen process conditions.

6. The catalyst of claim 4, wherein said catalyst has been subjected to a process for making ethylene oxide at STANDARD ETHYLENE OXIDE PROCESS CONDITIONS under air process conditions.

7. The catalyst of claim 4, wherein the mixture of metal salts (i) and (ii) is present in an amount, relative to the amount of silver metal, sufficient to provide an efficiency to ethylene oxide manufacture at a value of at least 79 percent, as determined at STANDARD ETHYLENE OXIDE PROCESS CONDITIONS measured under oxygen process conditions.

8. The catalyst of claim 4, wherein the gas phase inhibitor is an organic chloride.

9. The catalyst of claim 4, wherein the stream further comprises ethane.

10. The catalyst of claim 3 which comprises cesium salts and potassium salts.

11. The catalyst of claim 3 which comprises cesium salts and sodium salts.

12. The catalyst of claim 3 which comprises cesium salts and rubidium salts.

13. The catalyst of claim 3 which comprises sulfate anion.

14. The catalyst of claim 13 which comprises at least one of molybdate and tungstate anion.

15. The catalyst of claim 3 which comprises at least one of molybdate and tungstate anion.

16. The catalyst of claim 3 which comprises nitrate anion.

17. The catalyst of claim 3 which comprises as anion, at least one manqanate anion.

18. The catalyst of claim 3 which comprises vanadate.

19. The catalyst of claim 3 which comprises titanate.

20. The catalyst of claim 3 which comprises tantalate.

21. The catalyst of claim 3 which comprises molybdate.

22. The catalyst of claim 3 which comprises chromate.

23. The catalyst of claim 3 which comprises zirconate.

24. The catalyst of claim 3 which comprises tunqstate.

25. A catalyst for the manufacture of ethylene oxide by the epoxidation of ethylene containing an impregnated silver metal on an inert, refractory solid support and an efficiency-enhancing amount, relative to the amount of silver metal, of a mixture of (i) a cesium salt of an oxyanion of an element selected from Groups 3b through 7b inclusive, of the Periodic Table of the Elements;

and (ii) an alkali metal salt of lithium, sodium, potassium and rubidium, in which the anions of such salts are oxyanions of elements other than the oxygen therein having an atomic number of 15 or 83 and selected from Groups 3a to 7a, inclusive, and 3b through 7b, inclusive, of the Periodic Table of the Elements.

26. The catalyst of claim 25, wherein the cesium salt (i) is a cesium salt of a titanate, tantalate, molybdate, chromate, zirconate, manganate, tungstate, or vanadate oxyanion, and the alkali metal salt (ii) is a lithium, sodium, potassium, or rubidium salt of a manganate, vanadate, titanate, tantalate, tungstate, molybdate, chromate, zirconate, phosphate or sulfate oxyanion.

27. The catalyst of claim 25, wherein the support is alpha-alumina.

28. The catalyst of claim 27, wherein the catalyst comprises at least one manganate as oxyanion.

29. The catalyst of claim 27, wherein the catalyst comprises vanadate as oxyanion.

30. The catalyst of claim 27, wherein the catalyst comprises titanate as oxyanion.

31. The catalyst of claim 27, wherein the catalyst comprises tantalate.

32. The catalyst of claim 27, wherein the catalyst comprises molybdate.

33. The catalyst of claim 27, wherein the catalyst comprises chromate.

34. The catalyst of claim 27, wherein the catalyst comprises zirconate.

35. The catalyst of claim 27, wherein the catalyst comprises tungstate.

36. The catalyst of claim 27, wherein the catalyst comprises a mixture of cesium and rubidium salts.

37. The catalyst of claim 36, wherein the catalyst contains a molybdate as the oxyanion.

38. The catalyst of claim 27, wherein the catalyst contains a mixture of cesium and potassium salts.

39. The catalyst of claim 36, wherein the catalyst contains molybdate as the oxyanion.

40. The catalyst of claim 36, wherein the catalyst contains tungstate as the oxyanion.

41. A catalyst suitable for the manufacture of ethylene oxide comprising an impregnated silver metal on an inert, refractory solid support and an efficiency-enhancing amount, relative to the amount of silver metal, of a mixture of (i) a cesium salt of an oxyanion of an element other than the oxygen therein selected from Groups 3b through 7b, inclusive, of the Periodic Table of the Elements;

and (ii) an alkali metal salt of lithium, sodium, potassium and rubidium, in which the anions of such salts are oxyanions of elements other than the oxygen therein having an atomic number of at least 15 to 83 and being from Groups 3b to 7b, inclusive, and from 3a to 7a, inclusive of the Periodic Table of the Elements, which catalyst has been subjected to a process for making ethylene oxide by the reaction of ethylene and oxygen in which a stream comprising ethylene, oxygen, recycled carbon dioxide and a gas phase inhibitor is fed to a fixed bed of said catalyst and ethylene oxide is removed from the fixed bed of said catalyst.

42. The catalyst of claim 41, wherein the support is alpha-alumina.

43. The catalyst of claim 41 wherein the gas phase inhibitor is an organic chloride.

44. The catalyst of claim 41, wherein the cesium salt (i) is a cesium salt of a titanate, tantalate, molybdate, chromate, zirconate, manqanate or vanadate oxyanion, and the alkali metal salt (ii) is a lithium, sodium, potassium or rubidium salt of a manganate, vanadate, titanate, tantalate, tungstate, molybdate, chromate, zirconate, phosphate or sulfate oxyanion.