Simultaneous removal of mercury and water from fluids

• US 4,892,567 A
• Filed: 08/15/1988
• Issued: 01/09/1990
• Est. Priority Date: 08/15/1988
• Status: Expired due to Term

• Current Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Yan, Tsoung Y.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US07/232,194
• Time in Patent Office: 512 Days
• Field of Search: 55/31, 55/33, 55/35, 55/72, 55/75, 55/389, 210/688, 210/914, 423/99, 423/210, 502/75, 502/344, 502/347, 502/348
• US Class Current: 95/126
• CPC Class Codes: B01D 53/02 by adsorption, e.g. preparative gas chromatography solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury
• CPC Class Codes: B01J 20/186 Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
• CPC Class Codes: C10G 25/05 Removal of non-hydrocarbon compounds, e.g. sulfur compounds
• CPC Class Codes: C10G 33/04 with chemical means
• CPC Class Codes: C10K 1/32 with selectively adsorptive solids, e.g. active carbon
• CPC Class Codes: Y10S 210/914 Mercury
• CPC Class Codes: Y10S 95/902 Molecular sieve

Abstract

A regenerable molecular sieve comprises 0.001-15% elemental silver or gold in or on zeolite A. The molecular sieve is capable of simultaneously removing mercury and water from a fluid. A method for impregenating zeolite A with elemental silver or gold comprising treating the zeolite A with a solution of a silver or gold salt of a carboxylic acid and heating the impregnated zeolite A at a temperature sufficient to decompose the salt is also provided. A method for simultaneously and repeatedly removing mercury and water from a hydrocarbon fluid by contacting the fluid with an effective amount of a molecular sieve comprising zeolite A and 0.001-15% elemental silver or gold and regenerating the zeolite A at elevated temperatures is also provided.

Claims

1. A method for simultaneously removing mercury and water from a fluid comprising contacting the fluid with an effective amount of a molecular sieve comprising zeolite A containing on its surface 0.001-15% weight of elemental silver or gold and regenerating the molecular sieve for simultaneous water and mercury removal at elevated temperatures.

2. The method according to claim 1 wherein the fluid is a hydrocarbon fluid.

3. The method according to claim 2 wherein the hydrocarbon fluid is a gas.

4. The method according to claim 3 wherein the gas is natural gas.

5. The method according to claim 1 wherein the hydrocarbon fluid is contacted with the zeolite A at a temperature between 0°

and 300°

C. and a gas hourly space velocity between 1000 and ten million v/v hr.

6. The method according to claim 1 wherein the zeolite A is regenerated at temperatures between 100°

C. and 600°

C.

7. The method according to claim 1 wherein the molecular sieve comprises zeolite A and elemental silver.

8. The method according to claim 1 wherein the molecular sieve consists essentially of zeolite A and elemental silver.

9. The method according to claim 1 wherein the zeolite A contains 0.001-10% elemental silver.

10. The method according to claim 1 wherein the zeolite A contains 0.01-1% elemental silver.

11. The method according to claim 1 wherein the zeolite A is zeolite 4A.

12. The method according to claim 1 wherein the elemental silver is impregnated onto zeolite A by treating zeolite A with an aqueous solution of silver acetate and heating the silver acetate at temperatures between 100°

-600°

C.

13. A method for simultaneously removing mercury and water from a fluid comprising contacting the fluid with an effective amount of a molecular sieve comprising zeolite A containing in its cavities 0.001-5% by weight of elemental silver or gold and regenerating the molecular sieve for simultaneous water and mercury removal at elevated temperatures.

14. The method according to claim 13 wherein the fluid is a hydrocarbon fluid.

15. The method according to claim 14 wherein the hydrocarbon fluid is a gas.

16. The method according to claim 15 wherein the gas is natural gas.

17. The method according to claim 13 wherein the hydrocarbon fluid is contacted with the zeolite A at a temperature between 0°

and 300°

C. and a gas hourly space velocity between 1000 and ten million v/v hr.

18. The method according to claim 13 wherein the zeolite A is regenerated at temperatures between 100°

C. and 600°

C.

19. The method according to claim 13 wherein the molecular sieve comprises zeolite A and elemental silver.

20. The method according to claim 13 wherein the molecular sieve consists essentially of zeolite A and elemental silver.

21. The method according to claim 13 wherein the zeolite A contains 0.001-1% elemental silver.

22. The method according to claim 13 wherein the zeolite A is zeolite 4A.

23. A method for simultaneously removing mercury and water from a gas comprising contacting the gas with an effective amount of a molecular sieve comprising zeolite 4A containing on its surface 0.001-15% by weight of elemental silver and regenerating the molecular sieve for simultaneous water and mercury removal at elevated temperatures.

24. A method for simultaneously removing mercury and water from a gas comprising contacting the gas with an effective amount of a molecular sieve comprising zeolite 4A containing ion its cavities 0.001-5% by weight of elemental silver and regenerating the molecular sieve for simultaneous water and mercury removal at elevated temperatures.

25. The method according to claim 24 wherein the zeolite 4A contains 0.001-1% by weight of elemental silver.

26. A regenerable molecular sieve capable of simultaneously removing mercury and water from a fluid, comprising zeolite A containing on its surface about 0.001-15% by weight of elemental silver or gold.

27. A molecular sieve according to claim 26, which consists essentially of zeolite A containing on its surface about 0.001-15% by weight elemental silver or gold.

28. A molecular sieve according to claim 26, which comprises zeolite A containing elemental silver.

29. A molecular sieve according to claim 28 wherein the silver is impregnated onto the zeolite A by treating the zeolite A with an aqueous solution of a silver salt of a carboxylic acid and heating the zeolite A so treated in the absence of oxygen at a temperature capable of decomposing the silver acetate.

30. A molecular sieve according to claim 29 wherein the silver salt is silver acetate.

31. A molecular sieve according to claim 29 wherein the treated zeolite A is heated in flowing hot gas.

32. A molecular sieve according to claim 31 wherein the gas is natural gas.

33. A molecular sieve according to claim 29 wherein the zeolite A treated with silver salt solution is heated to a temperature between about 100°

C.-600°

C.

34. A molecular sieve according to claim 26 wherein the zeolite A is zeolite 4A.

35. A molecular sieve according to claim 34 wherein the zeolite A is zeolite 5A.

36. A molecular sieve according to claim 34 wherein the zeolite A is zeolite 3A.

37. A molecular sieve according to claim 26 wherein the zeolite A is capable of being regenerated for the purpose of simultaneously removing mercury and water from a fluid more than 100 times by heating at 340°

C. for one hour.

38. A molecular sieve capable of simultaneously removing mercury and water from a fluid, consisting essentially of zeolite A containing on its surface 0.001-10% elemental silver, wherein the zeolite A is capable of being regenerated more than 100 times for such simultaneous removal by heating at 340°

C. for one hour.

39. A bed of regenerable zeolite A containing on its surface 0.001-15% by weight of elemental silver or gold capable of simultaneously removing mercury and water from a fluid wherein the zeolite A is substantially uniformly coated with the silver or gold throughout the bed.

40. A bed of regenerable zeolite A containing on its surface 0.001-15% by weight of elemental silver or gold capable of simultaneously removing mercury and water from a fluid wherein the silver or gold is more heavily concentrated at the end of the bed away from the direction of fluid flow.

41. A bed of regenerable zeolite A according to claim 40 wherein the silver or gold is present in the 2/3 of the bed away from the direction of fluid flow.

42. A bed of regenerable zeolite A according to claim 40 wherein the silver or gold is present in the 1/2 of the bed away from the direction of fluid flow.

43. A bed of regenerable zeolite A according to claim 40 wherein the silver or gold is present in 1/3 of the bed away from the direction of fluid flow.

44. A regenerable molecular sieve capable of simultaneously removing mercury and water from a gas comprising zeolite 4A containing on its surface about 0.001-15% by weight of elemental silver.

45. A molecular sieve according to claim 44 wherein the zeolite A is capable of being regenerated for the purpose of simultaneously removing mercury and water from a fluid more than 100 times by heating at 340°

C. for one hour.

46. A molecular sieve capable of simultaneously removing mercury and water from a gas, consisting essentially of zeolite 4A containing on its surface 0.001-10% elemental silver, wherein the zeolite 4A is capable of being regenerated more than 100 times for such simultaneous removal by heating at 340°

C. for one hour.

47. A regenerable molecular sieve capable of simultaneously removing mercury and water from a liquid, comprising zeolite A containing in its cavities about 0.001-5% by weight of elemental silver or gold.

48. A molecular sieve according to claim 47, which consists essentially of zeolite A containing about 0.001-1% by weight elemental silver or gold.

49. A molecular sieve according to claim 47, which comprises zeolite A containing elemental silver.

50. A molecular sieve according to claim 47 wherein the zeolite A is zeolite 4A.

51. A molecular sieve according to claim 47 wherein the zeolite A is zeolite 5A.

52. A molecular sieve according to claim 47 wherein the zeolite A is zeolite 3A.

53. A molecular sieve according to claim 47 wherein the zeolite A is capable of being regenerated for the purpose of simultaneously removing mercury and water from a fluid more than 100 times by heating at 340°

C. for one hour.

54. A regenerable molecular sieve capable of simultaneously removing mercury and water from a gas, comprising zeolite 4A containing ion its cavities about 0.001-1% by weight of elemental silver.

55. A molecular sieve according to claim 54 wherein the zeolite 4A is capable of being regenerated for the purpose of simultaneously removing mercury and water from a gas more than 100 times by heating at 340°

C. for one hour.

56. A method for impregnating zeolite A with elemental silver comprising treating zeolite A with a solution of a silver salt capable of decomposing directly to elemental silver and heating the impregnated zeolite A in the absence of oxygen at a temperature sufficient to decompose the silver salt.

57. The method according to claim 56 wherein the impregnated zeolite A is heated at a temperature of 180°

C.-500°

C.

58. The method according to claim 56 wherein the salt is a salt of a carboxylic acid.

59. The method according to claim 58 wherein the salt is silver acetate.

60. The method according to claim 56 wherein the salt is impregnated onto zeolite that is on-line in a dryer vessel.

61. A method for adding elemental silver to zeolite A comprising impregnating zeolite A with a solution of a silver salt and reducing the silver salt impregnated on the zeolite A to elemental silver.

62. The method according to claim 61 wherein the salt is silver nitrate.