Adsorptive gas separation employing steam for regeneration

1. An adsorptive gas separation process for separating at least a first component from a multi-component fluid mixture, the process comprising:

(a) admitting said multi-component fluid mixture comprising at least said first component, at a pressure equal to or greater than a first pressure threshold as a feed stream into an adsorptive gas separator comprising at least one adsorbent material in at least one contactor and an adsorption zone of said at least one contactor, adsorbing at least a portion of said first component on said at least one adsorbent material in said adsorption zone of said at least one contactor to form a first product stream depleted in said first component relative to said feed stream, and recovering said first product stream from said at least one contactor;

(b) admitting a second regeneration stream, at a sub-ambient pressure, having a second component into said adsorptive gas separator and a second regeneration zone of said at least one contactor, adsorbing at least a portion of said second component of said second regeneration stream on said at least one adsorbent material, desorbing at least a portion of said first component adsorbed on said at least one adsorbent material to form a fifth product stream enriched in at least one of said first component and said second component relative to said feed stream, and recovering said fifth product stream from said second regeneration zone of said at least one contactor;

(c) admitting a first regeneration stream comprising said second component into said adsorptive gas separator and a first regeneration zone of said at least one contactor, desorbing at least a portion of said first component adsorbed on said at least one adsorbent material in said first regeneration zone to form a second product stream enriched in at least one of said first component and said second component relative to said feed stream, recovering said second product stream from said first regeneration zone of said at least one contactor and said adsorptive gas separator, admitting at least a portion of said second product stream into at least a first condenser, causing at least a portion of said second component in said second product stream to condense, to form a purified second product stream and a first condensate stream, fluidly connecting said first condenser to said adsorptive gas separator and inducing a reduction in pressure in at least said first regeneration zone of said at least one contactor to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream and said first condensate stream from said condenser; and

(d) admitting a conditioning stream into a conditioning zone of said at least one contactor, increasing a pressure of said conditioning zone of said at least one contactor to a pressure greater than said second pressure threshold to form a third product stream and recovering said third product stream from said at least one contactor.

2. The process of claim 1 , further comprising, prior to step (c), admitting at least a pre-regeneration stream into said adsorptive gas separator and into a pre-regeneration zone of said at least one contactor, desorbing a portion of the first component adsorbed on the at least one adsorbent material in said pre-regeneration zone of said at least one contactor, to form a reflux stream enriched in said first component relative to said feed stream, recovering said reflux stream from said at least one contactor, admitting said reflux stream into a reflux zone of at least one contactor, adsorbing at least a portion of said first component in said reflux stream on said at least one adsorbent material in said reflux zone of at least one contactor to form a fourth product stream, and recovering said fourth product stream from said reflux zone of at least one contactor.

3. The process of claim 2 , further comprising admitting said pre-regeneration stream into said adsorptive gas separator and said pre-regeneration zone of said at least one contactor at a pressure equal to or greater than a third pressure threshold.

4. The process of claim 3 , wherein said third pressure threshold is equal to or greater than said second pressure threshold.

5. The process of claim 2 , wherein a pressure in said reflux zone of said at least one contactor is less than a third pressure threshold immediately prior to admitting said reflux stream.

6. The process of claim 2 , wherein said pre-regeneration stream is enriched in said second component relative to said feed stream.

7. The process of claim 2 , wherein said pre-regeneration stream comprises at least a portion of said first regeneration stream.

8. The process of claim 2 , further comprising after step (c), admitting a third regeneration stream into a third regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material to form a sixth product stream, and recovering said sixth product stream from said third regeneration zone of said at least one contactor.

9. The process of claim 2 , further comprising prior to step (d), admitting a fourth regeneration stream into a fourth regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material in said fourth regeneration zone of said at least one contactor to form a seventh product stream, and recovering said seventh product stream from said fourth regeneration zone of said at least one contactor.

10. The process of claim 2 , wherein said multi-component fluid mixture comprises a post-combustion gas stream produced by a fuel combustor.

11. The process of claim 2 , wherein in step (c), said reduction in pressure is induced by at least one of said first condenser and/or a pump.

12. The process of claim 11 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

13. The process of claim 2 , further comprising in step (c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than said second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

14. The process of claim 13 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

15. The process of claim 2 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

16. The process of claim 2 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

17. The process of claim 2 , wherein said third pressure threshold is equal to or greater than said second pressure threshold.

18. The process of claim 1 , further comprising prior to step (a), admitting said multi-component fluid mixture comprising said first component into a steam generator, admitting a water stream into said steam generator, transferring heat from said multi-component fluid mixture to said steam generator and converting said water stream into a high pressure steam stream, recovering at least a portion of said multi-component fluid mixture and said high pressure steam stream from said steam generator, admitting said high pressure steam stream into a first steam turbine and expanding said high pressure steam stream in said first steam turbine forming at least one low pressure steam stream, and recovering said at least one low pressure steam stream from said first steam turbine.

19. The process of claim 18 , further comprising employing said at least one low pressure steam stream as at least a portion of said first regeneration stream, or a pre-regeneration stream.

20. The process of claim 1 , further comprising, after step a) and prior to step d), fluidly connecting a depressurization zone of said at least one contactor with a pressurization zone of said at least one contactor to reduce the pressure of said depressurization zone of said at least one contactor to a pressure of less than said first pressure threshold and to increase the pressure of said pressurization zone of said at least one contactor to a pressure greater than said second pressure threshold.

21. The process of claim 20 , further comprising, prior to step c), admitting at least a pre regeneration stream into said adsorptive gas separator and into a pre-regeneration zone of said at least one contactor, desorbing a portion of the first component adsorbed on the at least one adsorbent material in said pre-regeneration zone of said at least one contactor, to form a reflux stream enriched in said first component relative to said feed stream, recovering said reflux stream from said at least one contactor, admitting said reflux stream into a reflux zone of at least one contactor, adsorbing at least a portion of at least one component adsorbed on said at least one adsorbent material in said reflux zone of at least one contactor to form a fourth product stream, and recovering said fourth product stream from said reflux zone of at least one contactor.

22. The process of claim 21 , further comprising admitting said pre-regeneration stream into said adsorptive gas separator and said pre-regeneration zone of said at least one contactor at a pressure equal to or greater than a third pressure threshold.

23. The process of claim 22 , wherein said third pressure threshold is equal to or greater than said second pressure threshold.

24. The process of claim 21 , wherein a pressure in said reflux zone of said at least one contactor is less than a third pressure threshold immediately prior to admitting said reflux stream.

25. The process of claim 24 , wherein said third pressure threshold is equal to or greater than said second pressure threshold.

26. The process of claim 21 , wherein said pre-regeneration stream is enriched in said second component relative to said feed stream.

27. The process of claim 21 , wherein said pre-regeneration stream comprises at least a portion of said first regeneration stream.

28. The process of claim 20 , further comprising, after step c), admitting a third regeneration stream into a third regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material to form a sixth product stream, and recovering said sixth product stream from said third regeneration zone of said at least one contactor.

29. The process of claim 20 , further comprising, prior to step d), admitting a fourth regeneration stream into a fourth regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material in said fourth regeneration zone of said at least one contactor to form a seventh product stream, and recovering said seventh product stream from said fourth regeneration zone of said at least one contactor.

30. The process of claim 20 , further comprising, prior to step a), admitting said multi-component fluid mixture comprising said first component into a steam generator, admitting a water stream into said steam generator, transferring heat from said multi-component fluid mixture to said steam generator and converting said water stream into a high pressure steam stream, recovering at least a portion of said multi-component fluid mixture and said high pressure steam stream from said steam generator, admitting said high pressure steam stream into a first steam turbine and expanding said high pressure steam stream in said first steam turbine forming at least one low pressure steam stream, and recovering said at least one low pressure steam stream from said first steam turbine.

31. The process of claim 30 , further comprising employing said at least one low pressure steam stream as at least a portion of said first regeneration stream.

32. The process of claim 20 , wherein said multi-component fluid mixture comprises a post-combustion gas stream produced by a fuel combustor.

33. The process of claim 20 , wherein in step c), said reduction in pressure is induced by at least one of said first condenser and/or a pump.

34. The process of claim 33 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

35. The process of claim 20 , further comprising in step c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

36. The process of claim 35 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

37. The process of claim 20 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

38. The process of claim 20 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

39. The process of claim 20 , further comprising fluidly connecting said depressurization zone of said at least one contactor with a plurality of said pressurization zones of said at least one contactor to reduce the pressure of said depressurization zone of said at least one contactor to a pressure of less than said first pressure threshold and increase the pressure of said plurality of said pressurization zones of said at least one contactor to a pressure greater than said second pressure threshold.

40. The process of claim 1 , further comprising, after step c), admitting a third regeneration stream into a third regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material to form a sixth product stream, and recovering said sixth product stream from said third regeneration zone of said at least one contactor.

41. The process of claim 40 , further comprising, prior to step d), admitting a fourth regeneration stream into a fourth regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material in said fourth regeneration zone of said at least one contactor to form a seventh product stream, and recovering said seventh product stream from said fourth regeneration zone of said at least one contactor.

42. The process of claim 40 , further comprising, prior to step a), admitting said multi-component fluid mixture comprising said first component into a steam generator, admitting a water stream into said steam generator, transferring heat from said multi-component fluid mixture to said steam generator and converting said water stream into a high pressure steam stream, recovering said at least a portion of multi-component fluid mixture and said high pressure steam stream from said steam generator, admitting said high pressure steam stream into a first steam turbine and expanding said high pressure steam stream in said first steam turbine forming at least one low pressure steam stream, and recovering said at least one low pressure steam stream from said first steam turbine.

43. The process of claim 42 , further comprising employing said at least one low pressure steam stream as at least a portion of said first regeneration stream.

44. The process of claim 40 , wherein said multi-component fluid mixture comprises a post-combustion gas stream produced by a fuel combustor.

45. The process of claim 40 , wherein in step c), said reduction in pressure is induced by at least one of said first condenser and/or a pump.

46. The process of claim 45 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

47. The process of claim 40 , further comprising in step c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

48. The process of claim 47 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

49. The process of claim 40 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

50. The process of claim 40 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

51. The process of claim 1 , further comprising, prior to step d), admitting a fourth regeneration stream into a fourth regeneration zone of said at least one contactor, desorbing at least a portion of said second component adsorbed on said at least one adsorbent material in said fourth regeneration zone of said at least one contactor to form a seventh product stream, and recovering said seventh product stream from said fourth regeneration zone of said at least one contactor.

52. The process of claim 1 , further comprising, prior to step a), admitting said multi-component fluid mixture comprising said first component into a steam generator, admitting a water stream into said steam generator, transferring heat from said multi-component fluid mixture to said steam generator and converting said water stream into a high pressure steam stream, recovering said at least a portion of multi-component fluid mixture and said high pressure steam stream from said steam generator, admitting said high pressure steam stream into a first steam turbine and expanding said high pressure steam stream in said first steam turbine forming at least one low pressure steam stream, and recovering said at least one low pressure steam stream from said first steam turbine.

53. The process of claim 52 , further comprising employing said at least one low pressure steam stream as at least a portion of said first regeneration stream.

54. The process of claim 52 , wherein said multi-component fluid mixture comprises a post-combustion gas stream produced by a fuel combustor.

55. The process of claim 52 , wherein in step c), said reduction in pressure is induced by at least one of said first condenser and/or a pump.

56. The process of claim 55 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

57. The process of claim 52 , further comprising in step c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

58. The process of claim 57 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

59. The process of claim 52 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

60. The process of claim 50 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

61. The process of claim 1 , wherein said multi-component fluid mixture comprises a post-combustion gas stream produced by a fuel combustor.

62. The process of claim 1 , wherein in step c), said reduction in pressure is induced by at least one of said first condenser and/or a pump.

63. The process of claim 62 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

64. The process of claim 62 , further comprising in step c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

65. The process of claim 64 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

66. The process of claim 62 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

67. The process of claim 62 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

68. The process of claim 1 , further comprising in step c), admitting said purified second product stream into at least one of a pump and a valve to maintain a pressure in said first regeneration zone of said at least one contactor, to a pressure of equal to or less than a second pressure threshold, and recovering said purified second product stream from at least one of said pump and said valve.

69. The process of claim 68 , wherein said pump comprises at least one of an ejector, a vacuum pump, and a compressor.

70. The process of claim 68 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

71. The process of claim 68 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

72. The process of claim 1 , further comprising admitting said purified second product stream into a second condenser, condensing said second component from said purified second product stream and recovering said purified second product stream from said second condenser.

73. The process of claim 72 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.

74. The process of claim 1 , further comprising admitting said purified second product stream into a water ring vacuum pump, separating at least a portion of said second component from said purified second product stream.