Advanced filtration technique for fluid purification

• US 5,589,078 A
• Filed: 06/07/1995
• Issued: 12/31/1996
• Est. Priority Date: 06/07/1995
• Status: Expired due to Term

• Current Assignee: Purifics Environmental Technologies Incorporated
• Original Assignee: Anthony L. Powell, Brian E. Butters
• Inventors: Powell, Anthony L., Butters, Brian E.
• Primary Examiner(s): McCarthy, Neil
• Application Number:
  US08/478,226
• Time in Patent Office: 573 Days
• Field of Search: 210/510.1, 210/748, 210/650, 210/651, 210/323.1, 210/323.2, 210/490, 210/500.25, 210/104, 210/257.1, 250/432 R, 250/435, 250/436, 204/158.2, 422/186.3, 422/24
• US Class Current: 210/748.11
• CPC Class Codes: B01D 39/02 Loose filtering material, e.g. loose fibres
• CPC Class Codes: B01J 19/123 Ultraviolet light
• CPC Class Codes: C02F 1/20 by degassing, i.e. liberation of dissolved gases degasification of liquids in general B01D19/00; arrangement of degassing apparatus in boiler feed supply F22D
• CPC Class Codes: C02F 1/32 with ultraviolet light
• CPC Class Codes: C02F 1/725 by catalytic oxidation
• CPC Class Codes: C02F 2305/10 Photocatalysts

Abstract

A method and system for fluid purification is disclosed herein. In accordance with the present invention, an improved technique for recovering a decontaminated effluent after photocatalytic decontamination of a contaminated fluid is achieved. A slurry is formed by mixing a contaminated fluid with photocatalytic particles having an agglomeration property, and the photocatalytic particles are excited to render a treated slurry that includes a decontaminated fluid and the photocatalytic particles. The treated slurry is directed into a filter unit that includes at least one separation element. Each separation element has an inner surface defined by a channel extending through a substrate, and a plurality of pores which derive from the inner surface and extend through the substrate. The treated slurry is passed through the separation element and the agglomerated photocatalytic particles are allowed to form a layer at or near the inner surface of the separation element. Decontaminated effluent can then be recovered through the plurality of pores of the separation element. The treated slurry is preferably degassified in a tank before it is presented to the filter unit. Further, the amounts of recovered decontaminated effluent is preferably limited based on the level of treated slurry in the tank.

Claims

1. A method for recovering a decontaminated effluent after photocatalytic decontamination of a contaminated fluid, comprising:

forming a slurry by mixing a contaminated fluid with photocatalytic particles having an agglomeration property;

exciting the photocatalytic particles of the slurry to render a treated slurry that includes a decontaminated fluid and agglomerated photocatalytic particles;

directing the treated slurry into a filter unit that includes at least one separation element, each separation element having an inner surface defined by a channel extending through a substrate, each separation clement having a plurality of pores which derive from the inner surface and extend through the substrate;

passing the treated slurry through a separation element under certain conditions designed to induce the agglomerated photocatalytic particles to accumulate and form a layer at or near the inner surface of the separation element; and

recovering the decontaminated fluid through the plurality of pores of the separation element.

2. The method of claim 1, wherein:

the photocatalytic particles have a primary particle size, each of the plurality of pores is greater than the primary particle size of the photocatalytic particles.

3. The method of claim 1, wherein:

the agglomerated photocatalytic particles are TiO₂.

4. The method of claim 3, wherein:

the diameter of each of the plurality of pores is greater than 21 nm.

5. The method of claim 3, wherein:

the diameter of each of the plurality of pores is at least 200 nm.

6. The method of claim 1, wherein:

the layer of agglomerated photocatalytic particles is operable to capture foulants therein.

7. The method of claim 1, further comprising:

periodically removing the layer of agglomerated photocatalytic particles.

8. The method of claim 7, wherein:

the removal of the layer of agglomerated photocatalytic particles occurs at least once every 5 minutes.

9. The method of claim 7, wherein:

the removal of the layer of agglomerated photocatalytic particles occurs at least once every 1 minute.

10. The method of claim 1, further comprising:

substantially minimizing the shear stresses to which the inner surface of each separation element is subjected.

11. The method of claim 10, wherein:

the treated slurry passes through the separation element at a laminar flow.

12. The method of claim 1, wherein:

the treated slurry is passed through the filter unit at a linear velocity of less than 5 m/s.

13. The method of claim 1, wherein:

the treated slurry is passed through the filter unit at a linear velocity of less than 3 m/s.

14. The method of claim 1, wherein:

the treated slurry is passed through the filter unit at a linear velocity of less than 1 m/s.

15. The method of claim 1, wherein:

each separation element is subjected to a transmembrane pressure less than 50 psi.

16. The method of claim 1, wherein:

each separation element is subjected to a transmembrane pressure less than 20 psi.

17. The method of claim 1, wherein:

each separation element is subjected to a transmembrane pressure less than 10 psi.

18. The method of claim 1, wherein:

the photocatalytic particles are excited by irradiating the photocatalytic particles with ultraviolet light.

19. The method of claim 1, further comprising:

substantially degassifying the treated slurry.

20. A system for fluid purification, comprising:

a system for treating contaminated fluids by a photocatalytic process, the system being operable to render a treated slurry which includes a decontaminated effluent and photocatalytic particles having an agglomeration property;

a filter unit including at least one separation element, each separation element having an inner surface defined by a channel extending through a substrate and a plurality of pores which derive from the inner surface and extend through the substrate, each of the plurality of pores being larger than individual ones of the photocatalytic particles, the filter unit being operable to separate the treated slurry into decontaminated effluent and a residual slurry, the decontaminated effluent being recovered after passing through the plurality of pores of a separation element; and

a pump to return the residual slurry to the treatment system.

21. The system for fluid purification of claim 20, further comprising:

a tank interposed between the treatment system and the filter unit for storage of the treated slurry;

a level detector for measuring the amount of treated slurry in the tank; and

an electronic control unit which limits the recovery of decontaminated effluent based on the measurements of the level detector.

22. The system of fluid purification of claim 21, wherein:

the tank is subjected to atmospheric pressure and releases treated slurry directed to the filter unit towards the bottom of the tank such that the released treated slurry is substantially degassified.