SELECTIVE HEATING IN ADSORBENT SYSTEMS

• US 20080041226A1
• Filed: 08/29/2007
• Published: 02/21/2008
• Est. Priority Date: 09/23/2005
• Status: Abandoned Application

• Current Assignee: Clarence Clontz, Edward Tolles, Laurence Hiltzik, Roger Williams
• Original Assignee: Clarence Clontz, Edward Tolles, Laurence Hiltzik, Roger Williams
• Inventors: Williams, Roger, Clontz, Clarence, Hiltzik, Laurence, Tolles, Edward
• Application Number:
  US11/846,656
• Publication Number:
  US 20080041226A1
• Time in Patent Office: Days
• US Class Current: 95/90
• CPC Class Codes: B01D 2259/40086 by using a purge gas B01D2259/4009 takes precedence
• CPC Class Codes: B01D 53/0438 Cooling or heating systems
• CPC Class Codes: F02M 2025/0881 with means to heat or cool the canister
• CPC Class Codes: F02M 25/0854 Details of the absorption canister

Abstract

An invention is disclosed for efficiently improving the working capacity and useful service life of an adsorber system by selectively heating the adsorbent towards the purge outlet of the fluid path.

Claims

1. A method for increasing working capacity and maintaining working capacity over a service life of adsorber systems comprising steps of:

(i) contacting a purge flow through adsorbents unheated along a portion of a purge inlet of a fluid flow path length of the adsorbents; and

(ii) contacting the purge flow through a heat input means along a purge outlet of the fluid flow path length of the adsorbents, wherein the heat input means comprises at least one member selected from the group consisting of a heat input means located in the plenum, a heatable plenum, a heat input means associated with the adsorbent, and combinations thereof.

2. The method of claim 1, wherein the adsorber system is an evaporative emission control system.

3. The method of claim 2, wherein the purge inlet comprises at least one member selected from the group consisting of a path length with the main vapor recovery canister and an auxiliary canister in-series in purge flow with the main vapor recovery canister.

4. The method of claim 3, wherein the auxiliary canister includes at least one adsorbent selected from the group consisting of particulate form, monolith form, and combinations thereof.

5. The method of claim 3, wherein the auxiliary canister includes ceramic-bound carbon honeycomb adsorbent.

6. The method of claim 1, wherein the adsorbent comprises at least one member selected from the group consisting of zeolites, porous silicas, porous aluminas, pillared clays, molecular sieves, porous polymers, activated carbons, and combinations thereof.

7. The method of claim 6, wherein precursor of the activated carbon comprises at least one material selected from the group consisting of wood, peat, coal, coconut, lignite, petroleum pitch, petroleum coke, coal tar pitch, fruit pits, nut shells, sawdust, wood flour, synthetic polymer, and natural polymer having been activated by a process selected from the group consisting of chemical, thermal, and combined chemical/thermal activation methods.

8. The method of claim 1, wherein the adsorbent comprises at least one type of adsorbents.

9. The method of claim 1, wherein the adsorbent comprise at least one member selected from the group consisting of particulate form, monolith form, and combinations thereof.

10. The method of claim 9, wherein the particulate adsorbent comprises at least one member selected from the group consisting of irregular granular shapes, spherical shapes, cylindrical shapes, and combinations thereof.

11. The method of claim 9, wherein the monolith adsorbent comprises at least one form selected from the group consisting of extruded honeycomb with parallel cell passages, layered sheets with parallel passages, jelly-rolled sheets with parallel cell passages, bound aggregates of particulates with randomly distributed voidages for fluid flow, and combinations thereof.

12. The method of claim 1, wherein the heat input means comprises at least one member selected from the group consisting of electrical resistance heaters, positive temperature coefficient ceramics, heat exchangers, heat transfer fluids, and combinations thereof.

13. The method of claim 1, wherein the heat input means comprises at least one member selected from the group consisting of heaters located external to the adsorbent volumes, heaters internal to the adsorbent volumes, electrically conductive adsorbent volumes with heat applied by electrical current flow, and combinations thereof.

14. The method of claim 13, wherein the heat input means internal to the adsorbent volumes comprises at least one member selected from the group consisting of heaters in non-bonded contact with adsorbents, and heaters in bonded contact with the adsorbents.

15. The method of claim 13, wherein the electrically conductive adsorbent volume component comprises at least one conductive material selected from the group consisting of conductive adsorbents, conductive substrates, conductive additives, conductive binders, and combinations thereof

16. The method of claim 15, wherein the conductive component material is added at a step comprising at least one member selected from the group consisting of adsorbent preparation step, intermediate adsorbent shaping step, final adsorbent shaping step, and combinations thereof.

17. The method of claim 1, wherein the heat input means along the purge outlet flow path has same intensity throughout the path or has different local intensities.

18. The method of claim 1, wherein the heat input means comprises at least one member selected from the group consisting of heat applied after adsorption prior to purge flow and heat applied during purge flow.

19. An adsorber system comprising, in combination, an adsorber volume containing an initial volume of adsorbent material for temporarily adsorbing and storing adsorbate, a conduit for conducting adsorbate to the adsorbent, a conduit for expelling adsorbate-depleted fluid from the adsorber system, a conduit for conducting purge fluid to the adsorber system, and a conduit for conducting adsorbate-enriched purge fluid from the adsorber system, wherein the adsorber system is defined by an adsorbate-rich fluid flow path via the fluid inlet through adsorbent toward the conduit for expelling the adsorbate-depleted fluid, and, during operation in at least one subsequent step, purge fluid flow in a path to and through a conduit to the adsorbent system and along the fluid flow path in the adsorber system through the adsorbent volumes and the conduit from the adsorber system, the flow of purge fluid removing a portion of the adsorbate but leaving a residue of adsorbate in the adsorbent, and wherein:

(i) the purge flow is subjected through unheated adsorbents along a portion of the purge inlet of the fluid flow path length of the adsorbents; and

(ii) the purge flow is subjected through a heat input means along the purge outlet of the fluid flow path length of the adsorbents, wherein the heat input means comprises at least one member selected from the group consisting of a heat input means located in the plenum, a heatable plenum, a heat input means associated with the adsorbent, and combinations thereof.

20. The system of claim 19, wherein the adsorber system is an evaporative emission control system.

21. The system of claim 19, wherein the purge inlet comprises fluid flow path length within at least one volume of adsorbent.

22. The system of claim 19, wherein the adsorbent is of the form selected from the group consisting of particulate form, monolith form, and combinations thereof.

23. The system of claim 19, wherein the adsorbent includes ceramic-bound carbon honeycomb adsorbent.

24. The system of claim 19, wherein the adsorbent comprises at least one member selected from the group consisting of zeolites, porous silicas, porous aluminas, pillared clays, molecular sieves, porous polymers, activated carbons, and combinations thereof.

25. The system of claim 24, wherein precursor of the activated carbon comprises at least one material selected from the group consisting of wood, peat, coal, coconut, lignite, petroleum pitch, petroleum coke, coal tar pitch, fruit pits, nut shells, sawdust, wood flour, synthetic polymer, and natural polymer having been activated by a process selected from the group consisting of chemical, thermal, and combined chemical/thermal activation methods.

26. The system of claim 19, wherein the adsorbent comprises at least one type of adsorbents.

27. The system of claim 20, wherein the adsorbent comprise at least one member selected from the group consisting of particulate form, monolith form, and combinations thereof.

28. The system of claim 22, wherein the particulate adsorbent comprises at least one member selected from the group consisting of irregular granular shapes, spherical shapes, cylindrical shapes, and combinations thereof.

29. The system of claim 22, wherein the monolith adsorbent comprises at least one form selected from the group consisting of extruded honeycomb with parallel cell passages, layered sheets with parallel passages, jelly-rolled sheets with parallel cell passages, bound aggregates of particulates with randomly distributed voidages for fluid flow, and combinations thereof.

30. The system of claim 19, wherein the heat input means comprises at least one member selected from the group consisting of electrical resistance heaters, positive temperature coefficient ceramics, heat exchangers, heat transfer fluids, and combinations thereof.

31. The system of claim 19, wherein the heat input means associated with the adsorbent comprises at least one member selected from the group consisting of heaters located external to the adsorbent volumes, heaters internal to the adsorbent volumes, electrically conductive adsorbent volumes with heat applied by electrical current flow, and combinations thereof.

32. The system of claim 31, wherein the heat input means internal to the adsorbent volumes comprises at least one member selected from the group consisting of heaters in non-bonded contact with adsorbents, and heaters in bonded contact with the adsorbents.

33. The system of claim 31, wherein the electrically conductive adsorbent volume component comprises at least one conductive material selected from the group consisting of conductive adsorbents, conductive substrates, conductive additives, conductive binders, and combinations thereof

34. The system of claim 33, wherein the conductive component material is added at a step comprising at least one member selected from the group consisting of adsorbent preparation step, intermediate adsorbent shaping step, final adsorbent shaping step, and combinations thereof.

35. The system of claim 19, wherein the heat input means along the purge outlet flow path has same intensity throughout the path or has different local intensities.

36. The system of claim 19, wherein the heat input means comprises at least one member selected from the group consisting of heat applied after adsorption prior to purge flow and heat applied during purge flow.

37. An adsorber system operative for recovery of adsorbate defined by a adsorbate-laden fluid inlet to permit a fluid flow path through adsorbent volumes toward a conduit for expelling adsorbate-depleted fluid from the adsorber system and, during operation in at least one subsequent step, purge fluid flow is caused to flow in a path to and through a conduit opening to the adsorber system and along the fluid flow path in the adsorber system through the adsorbent volumes and the purge outlet conduit from the adsorber system, wherein the flow of fluid removing a portion of the adsorbate but leaving a residue of adsorbate in the adsorbent, and wherein:

(i) the purge flow is subjected through unheated adsorbents along a portion of the purge inlet of the fluid flow path length of the adsorbents; and

(ii) the purge flow is subjected through heat input means along the purge outlet of the fluid flow path length of the adsorbents, wherein the heat input means comprises at least one member selected from the group consisting of a heat input means located in the plenum, a heatable plenum, a heat input means associated with the adsorbent, and combinations thereof.

38. The adsorber system of claim 37, wherein the adsorber system is an evaporative emission control system.

39. The adsorber system operative of claim 37, wherein the purge inlet comprises fluid flow path length within at least one volume of adsorbent.

40. The adsorber system operative of claim 39, wherein the adsorbent volume includes at least one adsorbent selected from the group consisting of particulate form, monolith form, and combinations thereof.

41. The adsorber system operative of claim 39, wherein the adsorbent volume includes ceramic-bound carbon honeycomb adsorbent.

42. The adsorber system operative of claim 37, wherein the adsorbent comprises at least one member selected from the group consisting of zeolites, porous silicas, porous aluminas, pillared clays, molecular sieves, porous polymers, activated carbons, and combinations thereof.

43. The adsorber system operative of claim 42, wherein precursor of the activated carbon comprises at least one material selected from the group consisting of wood, peat, coal, coconut, lignite, petroleum pitch, petroleum coke, coal tar pitch, fruit pits, nut shells, sawdust, wood flour, synthetic polymer, and natural polymer having been activated by a process selected from the group consisting of chemical, thermal, and combined chemical/thermal activation methods.

44. The adsorber system operative of claim 37, wherein the adsorbent comprises at least one type of adsorbents.

45. The adsorber system operative of claim 37, wherein the adsorbent comprise at least one member selected from the group consisting of particulate form, monolith form, and combinations thereof.

46. The adsorber system operative of claim 45, wherein the particulate adsorbent comprises at least one member selected from the group consisting of irregular granular shapes, spherical shapes, cylindrical shapes, and combinations thereof.

47. The adsorber system operative of claim 45, wherein the monolith adsorbent comprises at least one form selected from the group consisting of extruded honeycomb with parallel cell passages, layered sheets with parallel passages, jelly-rolled sheets with parallel cell passages, bound aggregates of particulates with randomly distributed voidages for fluid flow, and combinations thereof.

48. The adsorber system operative of claim 37, wherein the heat input means comprises at least one member selected from the group consisting of electrical resistance heaters, positive temperature coefficient ceramics, heat exchangers, heat transfer fluids, and combinations thereof.

49. The adsorber system operative of claim 37, wherein the heat input means comprises at least one member selected from the group consisting of heaters located external to the adsorbent volumes, heaters internal to the adsorbent volumes, electrically conductive adsorbent volumes with heat applied by electrical current flow, and combinations thereof.

50. The adsorber system operative of claim 49, wherein the heat input means internal to the adsorbent volumes comprises at least one member selected from the group consisting of heaters in non-bonded contact with adsorbents, and heaters in bonded contact with the adsorbents.

51. The adsorber system operative of claim 49, wherein the electrically conductive adsorbent volume component comprises at least one conductive material selected from the group consisting of conductive adsorbents, conductive substrates, conductive additives, conductive binders, and combinations thereof

52. The adsorber system operative of claim 51, wherein the conductive component material is added at a step comprising at least one member selected from the group consisting of adsorbent preparation step, intermediate adsorbent shaping step, final adsorbent shaping step, and combinations thereof.

53. The adsorber system operative of claim 37, wherein the heat input means along the purge outlet flow path has same intensity throughout the path or has different local intensities.

54. The adsorber system operative of claim 37, wherein the heat input means comprises at least one member selected from the group consisting of heat applied after adsorption prior to purge flow and heat applied during purge flow.