Scouring method

• US 8,048,306 B2
• Filed: 12/22/2005
• Issued: 11/01/2011
• Est. Priority Date: 12/20/1996
• Status: Expired due to Fees

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Siemens Industry Incorporated (Siemens AG)
• Inventors: McMahon, Robert J., Zha, Fufang, Johnson, Warren T., Kopp, Clinton V., Beck, Thomas W.
• Primary Examiner(s): SORKIN, DAVID L
• Application Number:
  US11/316,593
• Publication Number:
  US 20060131234A1
• Time in Patent Office: 2,140 Days
• Field of Search: 210/636, 210/760, 210/791, 210/798, 210/321.69, 210/321.79, 210/321.8, 210/321.89, 210/411, 210/500.23
• US Class Current: 210/636
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/16 Use of chemical agents
• CPC Class Codes: B01D 2321/168 Use of other chemical agents
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 2321/2058 by vibration of the membrane, e.g. with an actuator
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 63/022 Encapsulating hollow fibres
• CPC Class Codes: B01D 63/0221 using a mould
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 63/0241 being U-shaped
• CPC Class Codes: B01D 63/16 Rotary, reciprocated or vibrated modules
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation

Abstract

A method and apparatus for removing fouling materials from the surface of a plurality of porous membranes (9) arranged in a membrane module (4) by providing, from within the module, by means (10) other than gas passing through the pores of said membranes, gas bubbles in a uniform distribution relative to the porous membrane array such that the bubbles move past the surfaces of the membranes (9) to dislodge fouling materials therefrom. The membranes (9) are arranged in close proximity to one another and mounted to prevent excessive movement therebetween. The bubbles also produce vibration and rubbing together of the membranes to further assist removal of fouling materials.

Claims

1. A method of removing accumulated solids from outer surfaces of porous hollow fiber membranes arranged in close proximity to one another and mounted between potting heads with a cured potting material, wherein the membranes are situated in a vessel, the method comprising the steps of:

backwashing the membranes to dislodge accumulated solids from the outer surfaces of the membranes;

restricting movement of the membranes;

providing, through at least one porous tube disposed among and substantially parallel to the membranes, uniform gas bubbles which pass out among the membranes scouring solids on the outer surfaces of the membranes;

providing gas bubbles through a porous sheet and a plurality of gas distribution openings in a first potting head, the plurality of gas distribution openings each having a diameter from about 0.01 mm to about 5 mm, and the porous sheet having uniformly distributed pores and a smaller pore size relative to the gas distribution openings in the first potting head; and

removing dislodged accumulated solids from the vessel.

2. The method according to claim 1, wherein the removing step comprises draining down liquid from the vessel.

3. The method according to claim 2, wherein the draining down comprises a periodic draindown.

4. The method according to claim 1, wherein the removing step comprises using a clarifier.

5. The method according to claim 1, wherein the removing step comprises overflowing liquid from the vessel.

6. The method according to claim 5, wherein the overflowing comprises a periodic overflow.

7. The method according to claim 1, wherein the removing step comprises a continual bleed off.

8. The method according to claim 1, wherein the backwashing comprises backwashing with a gas.

9. The method according to claim 1, wherein the backwashing comprises backwashing with a liquid.

10. The method of claim 9, wherein the liquid comprises a permeate.

11. The method of claim 1, wherein the steps of backwashing and providing gas bubbles to the membrane occur simultaneously.

12. The method of claim 1, wherein the porous hollow fiber membranes extend longitudinally in an array to form a membrane module contained within the vessel.

13. The method of claim 1, wherein the membranes are mounted in a header in close proximity to one another so as to prevent excessive movement therebetween.

14. The method of claim 1, wherein the gas bubbles move past the outer surfaces of the membranes and vibrate the membranes to dislodge the accumulated solids therefrom.

15. The method of claim 1, wherein the membranes are mounted relative to one another so as to produce a rubbing effect between the membranes when vibrated.

16. The method of claim 1, wherein the hollow fiber membranes are arranged in at least one bundle.

17. The method of claim 1, wherein the hollow fiber membranes are surrounded by a perforated cage.

18. The method of claim 1, wherein the tube comprises a plurality of holes.

19. The method of claim 1, further comprising subjecting the membranes to a chemical cleaning.

20. The method of claim 1, further comprising subjecting the membranes to a chemical dosing.

21. The method of claim 1, wherein the gas bubbles are continuously provided.

22. The method of claim 1, wherein the gas bubbles are intermittently provided.

23. The method of claim 1, wherein backwashing the membranes occurs prior to providing gas bubbles to the membranes.

24. A membrane module, comprising:

a plurality of porous membranes, the membranes being arranged in close proximity to one another and mounted between potting heads with a cured potting material,

means for restricting membrane movement;

at least one porous tube located within the module;

a plurality of gas distribution openings in a first potting head each having a diameter from about 0.01 mm to about 5 mm; and

a porous sheet having uniformly distributed pores and a smaller pore size relative to the gas distribution openings in the first potting head;

the module constructed and arranged such that, in use, gas moves through the porous sheet, the gas distribution openings and the at least one porous tube but not through the pores of said membranes producing uniform bubbles which pass out among the membranes scouring solids on the membranes,

wherein the membranes comprise hollow fibre membranes and the at least one porous tube extends longitudinally between the potting heads among the membranes.