MEMBRANE MODULE PROTECTION

• US 20100051545A1
• Filed: 04/04/2008
• Published: 03/04/2010
• Est. Priority Date: 04/04/2007
• Status: Abandoned Application

• Current Assignee: Siemens Industry Incorporated (Siemens AG)
• Original Assignee: Siemens Industry Incorporated (Siemens AG)
• Inventors: Zha, Fufang, Beck, Thomas William, Johnson, Warren Thomas
• Application Number:
  US12/594,376
• Publication Number:
  US 20100051545A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2313/21 Specific headers, end caps
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 63/043 with separate tube sheets
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: C02F 1/44 by dialysis, osmosis or reverse osmosis general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268

Abstract

A filtration system for removing fine solids from a liquid suspension comprising a vessel for containing the liquid suspension, one or more permeable, membranes (9) within the vessel, means for providing a pressure differential across walls of the membranes (9) such that some of the liquid suspension passes through the walls of the membranes (9) to be drawn off as permeate and means for withdrawing the permeate from the membranes. A screen (8) is positioned in a flow path of the liquid suspension through to the membrane walls.

Claims

1. A filtration system for removing fine solids from a liquid suspension comprising:

a vessel for containing said liquid suspension;

one or more permeable, membranes within the vessel;

means for providing a pressure differential across walls of said membranes such that some of the liquid suspension passes through the walls of the membranes to be drawn off as permeate;

a screen positioned in a flow path of the liquid suspension through to said membrane walls; and

means for withdrawing permeate from the membranes.

7. A filtration system according to claim 1 wherein said screen is a fine screen.

8. A filtration system according to claim 7 wherein the aperture size of the screen is between about 625 μ

m² to about 25×

10⁶ μ

m².

9. A filtration system according to claim 8 wherein the aperture size is between about 1×

10⁴ μ

m² to about 1×

10⁶ m².

11. A filtration system according to claim 1 wherein the membranes are sealed at the first end and open at the second end to allow removal of a filtrate.

12. A filtration system according to claim 1 wherein the membranes comprise hollow fibre membranes.

13. A filtration system according to claim 12 wherein the fibres are arranged in close proximity to one another and mounted in a bundle in a substantially taut manner between an upper potting head and a lower potting head to prevent excessive movement therebetween.

14. A filtration system according to claim 13 wherein the fibres are substantially uniformly mounted in the lower potting head relative to a distributed array of aeration holes in the lower potting head, wherein the aeration holes are sized and located such that bubbles, formed by a gas passing therethrough when the module is immersed in a liquid, pass substantially uniformly between the fibres.

15. A filtration system according to claim 14 wherein the vessel includes a plenum chamber beneath the lower potting head through which the pressurized gas is introduced, and wherein the plenum chamber includes an aperture substantially beneath the aeration holes for allowing egress of contaminants.

16. A filtration system according to claim 14 wherein the lower potting head is connected to a source of the pressurized gas, and the fibres and screen are arranged to be vibrated by the gas bubbles.

23. A membrane module according to claim 16 wherein the membranes are sealed at the first end and open at the second end to allow removal of a filtrate.

2. A filtration system comprising:

a membrane module comprising a plurality of permeable membranes, each of the membranes having a first end and a second end, the membranes having one of said ends extending from and mounted to at least one potting head, and

a screen surrounding the membranes.

3. A filtration system comprising:

a membrane module comprising a plurality of permeable membranes, each of the membranes having a first end and a second end, the membranes having one of said ends extending from and mounted to at least one potting head,

said module having an upper and a lower end;

a screen surrounding the membranes and extending between said upper and lower ends of said module; and

an opening being provided in said screen at or adjacent said upper end of the module.

4. A filtration system according to claim 3, wherein said opening is provided by peripherally spacing an end of said screen from said upper end of the module.

5. A filtration system according to claim 3, wherein said opening is provided by extending said screen to below said upper end of the module.

6. A filtration system according to claim 5, wherein the upper end of said module comprises said at least one potting head.

10. A filtration system according to claim wherein the screen is connected to and extends from said potting head.

17. A membrane module, comprising:

a plurality of permeable membranes, said membranes being arranged in close proximity to one another to form an array, the module having a header in which one end of each of the membranes is mounted and

a screen surrounding said array of membranes.

18. A membrane module according to claim 17 wherein the screen extends from said header.

19. A membrane module according to claim 18 wherein the screen is connected to the header.

20. A membrane module according to claim 17 wherein said screen is a fine screen.

21. A membrane module according to claim 20 wherein the aperture size of the screen is between about 625 μ

m² to about 25×

10⁶ μ

m².

22. A membrane module according to claim 21 wherein the aperture size is between about 1×

10⁴ μ

m² to about 1×

10⁶ μ

m².

24. A membrane module according to claim 17 wherein the membranes comprise hollow fibre membranes.

25. A membrane module according to claim 24 the fibre membranes are arranged in bundles surrounded by the screen.

26. A membrane module according to claim 17 wherein the header is connected to a source of pressurized gas so as to permit formation of gas bubbles such that, in use, the bubbles move past the surfaces of and vibrate said membranes and said screen to dislodge fouling materials therefrom.

27. A method for filtering a feed liquid comprising the steps of:

providing a vessel;

providing a membrane module, the membrane module comprising;

a plurality of permeable membranes, and

a fine screen surrounding the plurality of membranes,

wherein the membrane module is contained within the vessel; and

the membranes comprising a plurality of pores and an outer surface,

providing a feed liquid to the vessel;

applying a transmembrane pressure to the membranes in the module, whereby a filtrate passes through pores in the membranes, thereby producing a concentrated feed comprising a fouling material in the vessel; and

removing the fouling material from the vessel.

28. A method for filtering a feed liquid according to claim 27 wherein the membranes are mounted in a header in close proximity to one another so as to prevent excessive movement therebetween.