Claims
- 1. A method comprising
(a) providing at least one material having at least one major surface with an adjacent gas phase; (b) positioning a chamber in close proximity to said surface of said material to define a gap between said chamber and said surface, wherein said adjacent gas phase between said chamber and said surface define a region possessing an amount of mass; and (c) inducing transport of at least a portion of said mass from said region through said chamber, wherein M1 means total net time-average mass flow through said gap into said region and through said chamber resulting from pressure gradients, M2 means time-average mass flow from said at least one major surface of said material into said region, M3means total net time-average mass flow through said gap into said region resulting from motion of said material, and M4 means time-average rate of mass transport through said chamber such that M1+M2+M3=M4; and for the present method M1 has a value greater than zero but not greater than 0.25 kg/second/meter.
- 2. A method according to claim 1, wherein the temperature in said chamber is controlled to prevent phase change of components in said mass.
- 3. A method according to claim 1, wherein the material is a web.
- 4. A method according to claim 1, further comprising separating a vapor component from said mass transported through said chamber.
- 5. A method according to claim 4, wherein separation includes absorption, adsorption, membrane separation or condensation.
- 6. A method according to claim 4, wherein temperature of said vapor component is controlled to prevent condensation of vapor prior to separation.
- 7. A method according to claim 1, further comprising a destruction device in communication with said chamber for receiving said mass.
- 8. A method according to claim 1, wherein said gap is 3 cm or less.
- 9. A method according to claim 1, wherein said chamber includes at least one flame arresting mechanism.
- 10. A method according to claim 1, wherein M1 is no greater than 0.1 kg/second/meter.
- 11. A method according to claim 1, wherein the total net average velocity of M1 is no greater than 0.5 meters/second.
- 12. A method according to claim 1, wherein said material includes at least one evaporative component and energy is supplied to vaporize said evaporative component to form a vapor component in said mass of said adjacent gas phase.
- 13. A method according to claim 1, wherein one or more chambers are utilized to capture at least a portion of said vapor component.
- 14. A method according to claim 13, wherein each of said one or more chambers is independently controlled.
- 15. A method according to claim 12, wherein at least a portion of said vapor component is captured from said chamber at concentrations high enough to permit subsequent separation of said vapor component at a temperature of 0° C. or higher.
- 16. A method according to claim 1, wherein said time-average rate of mass transport through said region is at least 100% of said time-average mass flow from said at least one major surface of said material into said region.
- 17. A method according to claim 12, wherein said vapor component is flammable and is captured at a concentration of at least the upper flammability limit.
- 18. A method according to claim 1, wherein said chamber is in an enclosed environment.
- 19. A method comprising;
(a) providing at least one material having at least one major surface with an adjacent gas phase; (b) positioning a chamber in close proximity to said surface of said material to define a gap between said chamber and said surface, wherein said adjacent gas phase between said chamber and said surface define a region possessing an amount of mass; and (c) inducing transport of at least a portion of said mass from said region through said chamber, wherein M1 means total net time-average mass flow through said gap into said region resulting from pressure gradients, M2 means time-average mass flow from said at least one major surface of said material into said region, M3means total net time-average mass flow through said gap into said region resulting from motion of said material, and M4 means time-average rate of mass transport through said chamber such that M1+M2+M3=M4; and for the present method the total net average velocity of M1 is no greater than 0.5 meters/second.
- 20. A method according to claim 19, wherein M1 has a value greater than zero but not greater than 0.25 kg/second/meter.
- 21. A method according to claim 19, wherein the temperature in said chamber is controlled to prevent phase change of components in said mass.
- 22. A method according to claim 19, wherein the material is a web.
- 23. A method according to claim 19, further comprising separating a vapor component from said mass transported through said chamber.
- 24. A method according to claim 23, wherein separation includes absorption, adsorption, membrane separation or condensation.
- 25. A method according to claim 23, wherein temperature of said vapor component is controlled to prevent condensation of vapor prior to separation.
- 26. A method according to claim 19, wherein said gap is 3 cm or less.
- 27. A method according to claim 19, wherein said chamber includes at least one flame arresting mechanism.
- 28. A method according to claim 19, wherein said material includes at least one evaporative component and energy is supplied to vaporize said evaporative component to form a vapor component in said mass of said adjacent gas phase.
- 29. A method according to claim 19, wherein one or more chambers are utilized to capture at least a portion of said vapor component.
- 30. A method according to claim 29, wherein each of said one or more chambers is independently controlled.
- 31. A method according to claim 19, wherein said chamber is in an enclosed environment.
- 32. A method comprising;
(a) providing at least one material having at least one major surface with an adjacent gas phase, said material including at least one evaporative component; (b) positioning a chamber in close proximity to said surface of said material to define a gap between said chamber and said surface, wherein said adjacent gas phase between said chamber and said surface define a region possessing an amount of mass; (c) supplying energy to vaporize said at least one evaporative component to form a vapor component in said mass of said adjacent gas phase; and (d) inducing transport of at least a portion of said mass from said region through said chamber, wherein M1 means total net time-average mass flow through said gap into said region resulting from pressure gradients, M2 means time-average mass flow from said at least one major surface of said material into said region, M3means total net time-average mass flow through said gap into said region resulting from motion of said material, and M4 means time-average rate of mass transport through said chamber such that M1+M2+M3=M4; and for the present method M1 has a value greater than zero but not greater than 0.25 kg/second/meter.
- 33. A method according to claim 32, wherein said chamber is positioned at one or both of opposing ends of a gap drying apparatus.
- 34. A method according to claim 32, wherein said chamber is positioned within a gap drying apparatus.
- 35. A method according to claim 32, wherein said material is a web.
- 36. A method according to claim 32, further comprising sealing one end of said chamber in order to force said adjacent gas phase into said region.
- 37. A method according to claim 36, wherein said sealing is accomplished by forced gas or a mechanical seal.
- 38. A method according to claim 37, wherein said mechanical seal is moveable.
- 39. A method comprising:
(a) providing at least one material having at least one major surface with an adjacent gas phase; (b) positioning a chamber in close proximity to at least one end of a gap drying apparatus, internally to a gap drying apparatus, or combinations thereof, said chamber in close proximity to said surface of said material to define a gap between said chamber and said surface, wherein said adjacent gas phase between said chamber and said surface define a region possessing an amount of mass; and (c) inducing transport of at least a portion of said mass from said region through said chamber, wherein M1 means total net time-average mass flow through said gap into said region resulting from pressure gradients, M2 means time-average mass flow from said at least one major surface of said material into said region, M3means total net time-average mass flow through said gap into said region resulting from motion of said material, and M4 means time-average rate of mass transport through said chamber such that M1+M2+M3=M4; and for the present method M1 has a value greater than zero but not greater than 0.25 kg/second/meter.
- 40. An apparatus comprising;
(a) a support mechanism for supporting material, said material having at least one major surface with an adjacent gas phase; (b) a chamber positioned in close proximity to a surface of said material to define a gap between said chamber and said surface, wherein said adjacent gas phase between said chamber and said surface define a region possessing an amount of mass ; and (c) a mechanism in communication with said chamber to induce transport of at least a portion of said mass from said adjacent gas phase through said region, wherein M1 means total net time-average mass flow through said gap into said region resulting from pressure gradients, M2 means time-average mass flow from said at least one major surface of said material into said region, M3means total net time-average mass flow through said gap into said region resulting from motion of said material, and M4 means time-average rate of mass transport through said chamber such that M1+M2+M3=M4; and for the present method M1 has a value greater than zero but not greater than 0.25 kg/second/meter.
- 41. An apparatus according to claim 40, further comprising a separating mechanism in communication with said chamber for separating individual components from said mass transported through said chamber.
- 42. An apparatus according to claim 41, wherein separation occurs through absorption, adsorption, membrane separation or condensation.
- 43. An apparatus according to claim 40, wherein said material includes at least one evaporative component and said apparatus includes an energy source capable of providing sufficient energy to vaporize said at least one evaporative component to form a vapor component in said adjacent gas phase.
- 44. An apparatus according to claim 43, wherein said chamber includes a heating device to prevent condensation of said vapor component.
- 45. An apparatus according to claim 43, wherein energy is imparted to the material before being positioned near said chamber.
- 46. An apparatus according to claim 40, wherein said material is a web and said web is continuously conveyed past said chamber.
- 47. An apparatus according to claim 40, wherein the chamber includes a flame arresting device.
- 48. An apparatus according to claim 40, further comprising a sealing mechanism on one end of said chamber in order to force said adjacent gas phase into said region.
- 49. An apparatus according to claim 40, wherein said chamber is located on at least one opposing end of a gap drying system, internal to a gap drying system, or combinations thereof.
Parent Case Info
[0001] This application is claiming priority to U.S. Provisional Application Serial Nos. 60/235,214, filed Sep. 24, 2000, 60/235,221, filed on Sep. 24, 2000, and 60/274,050, filed on Mar. 7, 2001, all of which are hereby incorporated by reference in their entirety. The present invention relates to a vapor collection method, and more particularly to a method that enables the collection of gas phase components without substantial dilution.
Provisional Applications (3)
|
Number |
Date |
Country |
|
60235214 |
Sep 2000 |
US |
|
60235221 |
Sep 2000 |
US |
|
60274050 |
Mar 2001 |
US |