Apparatus and method for the photopromoted catalyzed degradation of compounds in a fluid stream

• US 5,516,492 A
• Filed: 06/30/1992
• Issued: 05/14/1996
• Est. Priority Date: 06/30/1992
• Status: Expired due to Fees

• Current Assignee: ClearFlow, Inc.
• Original Assignee: ClearFlow, Inc.
• Inventors: Dong, Junchang, Berman, Elliot
• Primary Examiner(s): Walsh, Donald P.
• Assistant Examiner(s): JENKINS, DANIEL J
• Application Number:
  US07/907,692
• Time in Patent Office: 1,414 Days
• Field of Search: 422/186.3, 422/900, 422/186, 422/186.06, 204/158.2, 210/748
• US Class Current: 422/186
• CPC Class Codes: B01D 2255/802 Photocatalytic
• CPC Class Codes: B01D 53/885 Devices in general for catalytic purification of waste gases
• CPC Class Codes: B01J 15/005 in the presence of catalytically active bodies, e.g. porous plates
• CPC Class Codes: B01J 16/005 in the presence of catalytically active bodies, e.g. porous plates
• CPC Class Codes: B01J 19/122 Incoherent waves gamma-radiation B01J19/082
• CPC Class Codes: B01J 19/24 Stationary reactors without moving elements inside B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02
• CPC Class Codes: B01J 2208/00451 Sunlight; Visible light
• CPC Class Codes: B01J 2208/00548 Flow
• CPC Class Codes: B01J 2208/0084 inside the bed, e.g. baffles
• CPC Class Codes: B01J 2219/0077 inclined
• CPC Class Codes: B01J 2219/00772 in a helix
• CPC Class Codes: B01J 8/02 with stationary particles, e.g. in fixed beds
• CPC Class Codes: B01J 8/0292 with stationary packing material in the bed, e.g. bricks, wire rings, baffles
• CPC Class Codes: C02F 1/325 Irradiation devices or lamp constructions
• CPC Class Codes: C02F 1/725 by catalytic oxidation
• CPC Class Codes: C02F 2201/3227 Units with two or more lamps
• CPC Class Codes: C02F 2201/328 Having flow diverters (baffles)
• CPC Class Codes: C02F 2305/10 Photocatalysts
• CPC Class Codes: Y02W 10/37 using solar energy

Abstract

In a reactor and process for the photopromoted catalytic decomposition of compounds in a fluid stream, the area of a catalyst support structure and/or the amount of catalyst on the support structure is varied as a function of distance from a light source to enhance quantum efficiency. In a preferred embodiment, the support structure has a surface area per unit of reaction chamber volume which increases with distance from the light source, or the amount of catalyst on the support structure per unit area increases with distance from the light source to maintain the light intensity on the catalyst within a desired range regardless of dispersion and/or absorption effects. In another embodiment, the support structure includes a plurality of curved plates which may, for example, be spherical, cylindrical or helical.

Claims

1. A reactor for use in the photopromoted catalyzed degradation of compounds in a fluid stream, comprising:

a light source;

a conduit for directing said fluid stream into optical proximity to the light source, said conduit defining a reaction chamber;

a solid catalyst; and

a structure for supporting the catalyst in a predetermined spatial distribution within said reaction chamber and in contact with said fluid stream so that light from the light source illuminates the catalyst at an intensity within a preselected range for degradation of said compounds;

said catalyst having a surface concentration on said supporting structure which increases with distance from the light source.

2. The reactor of claim 1 wherein:

said spatial distribution is selected so that the catalyst is illuminated at an intensity of between 10¹⁹ and 10²⁴ photons of actinic light per square meter per hour.

3. The reactor of claim 1 wherein:

the supporting structure defines a catalyst support surface having a surface area per unit of reaction chamber volume which increases with distance from the light source.

4. The reactor of claim 3 wherein:

said surface area per unit of reaction chamber volume increases in proportion to the distance from the light source.

5. The reactor of claim 3 wherein:

the supporting structure comprises at least one curved plate.

6. The reactor of claim 5 wherein:

said at least one curved plate is spherical.

7. The reactor of claim 5 wherein:

said at least one curved plate is cylindrical.

8. The reactor of claim 5 wherein:

said at least one curved plate is helical.

9. The reactor of claim 3 wherein:

the supporting structure comprises a plurality of curved plates.

10. The reactor of claim 3 wherein:

the supporting structure comprises a plurality of discrete support elements of different surface areas at different distances from the light source.

11. The reactor of claim 3 wherein:

the supporting structure comprises a plurality of fabric elements of different surface areas at different distances from the light source.

12. The reactor of claim 11 wherein:

said fabric elements at different distances from the light source have different weaves.

13. The reactor of claim 11 wherein:

said fabric elements at different distances from the light source have different thread diameters.

14. The reactor of claim 1 wherein:

said catalyst has a concentration per unit of reaction chamber volume which increases with distance from the light source.

15. The reactor of claim 14 wherein:

said concentration per unit of reaction chamber volume increases in proportion to the distance from the light source.

16. A reactor for use in the photopromoted catalyzed degradation of compounds in a fluid stream, comprising:

a light source;

a conduit for directing said fluid stream into optical proximity to the light source, said conduit defining a reaction chamber;

means for producing turbulent flow within said reaction chamber;

a solid catalyst; and

a structure for supporting the catalyst in a predetermined spatial distribution within said reaction chamber and in contact with said fluid stream so that light from the light source illuminates the catalyst at an intensity within preselected range for degradation of said compounds;

said catalyst having a surface concentration on said a supporting structure which increases with distance from the light source.

17. A method of fabricating a reactor for use in the photopromoted catalyzed degradation of compounds in a fluid stream, comprising:

providing a light source;

providing at least one conduit to direct said fluid stream into optical proximity to the light source, said conduit defining a reaction chamber;

disposing a solid catalyst on a supporting structure within said reaction chamber in contact with said fluid stream, at a surface concentration which increases with distance from the light source so that light from the light source illuminates the catalyst at an intensity within a preselected range for degradation of said compounds.

18. The method of claim 17 wherein:

said surface concentration is selected so that the catalyst is illuminated at an intensity of between 10¹⁹ and 10²⁴ photons per square meter per hour.

19. The method of claim 17 wherein:

the step of disposing a solid catalyst on a supporting structure within said reaction chamber comprises providing a catalyst support surface having a surface area per unit of reaction chamber volume which increases with distance from the light source.