Module cleaning method

• US 8,808,540 B2
• Filed: 11/12/2004
• Issued: 08/19/2014
• Est. Priority Date: 11/14/2003
• Status: Expired due to Fees

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Evoqua Water Technologies LLC
• Inventors: Johnson, Warren Thomas
• Primary Examiner(s): Savage, Matthew O
• Assistant Examiner(s): Behrendt, Benjamin J
• Application Number:
  US10/595,841
• Publication Number:
  US 20070075021A1
• Time in Patent Office: 3,567 Days
• Field of Search: 210/321.69, 210/321.8, 210/321.89, 210/636, 210/321.6, 210/106, 210/167.09, 210/167.14, 210/355, 210/391, 210/393, 210/409, 210/760, 210/333.01, 210/333.1, 210/233.1, 134/166.R, 134/101.1, 1341021-1023, 15/17, 151/040.4
• US Class Current: 210/321.69
• CPC Class Codes: B01D 2313/02 Specific tightening or locking mechanisms
• CPC Class Codes: B01D 2313/20 Specific housing
• CPC Class Codes: B01D 2313/2011 Pressure vessels
• CPC Class Codes: B01D 2313/26 Specific gas distributors or gas intakes
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2317/04 Elements in parallel
• CPC Class Codes: B01D 2321/02 Forward flushing
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/12 Use of permeate
• CPC Class Codes: B01D 2321/14 Use of concentrate
• CPC Class Codes: B01D 2321/18 Use of gases
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• CPC Class Codes: B01D 63/046 in separate housings
• 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

An aeration/backwash device (16) for use with a porous membrane filtration module (5) including one or more membranes (6) extending longitudinally between vertically spaced upper (7) and lower headers (8) into which the ends of the membranes are potted. The membranes (6) having a permeable wall which, in use, is subjected to a filtration operation wherein feed containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall. The aeration/backwash device (16) adapted to at least partially surround a portion of said membrane module (5) and including a communication chamber (17) having spaced through-openings (18, 19) in fluid communication with the chamber (17) and the membrane module (5). In use, gas is supplied to the chamber (17) and communicated to the membrane module (5) through the through-openings (18, 19) to aerate the membranes within the membrane module and liquid backwash is withdrawn from and/or fed into the membrane module (5) through the throughopenings into the chamber (17).

Claims

1. An aeration/backwash device configured for use with a membrane filtration module comprising one or more membranes and opposing potted ends, comprising:

a communication chamber including a closed internal volume defined by an inner wall, an outer wall, an upper wall coupling the inner wall to the outer wall, and a lower wall coupling the inner wall to the outer wall, the communication chamber at least partially surrounding a circumference of the membrane filtration module, the inner wall having upper through-openings and lower through-openings vertically spaced apart from the upper through-openings, the upper and lower through-openings spaced circumferentially about the inner wall, each through-opening having a longitudinal axis substantially perpendicular to the one or more membranes;

a source of gas in fluid communication with the internal volume of the communication chamber; and

a source of backwash liquid in fluid communication with the internal volume of the communication chamber,

wherein the source of gas and the source of backwash liquid share a common inlet to the internal volume of the communication chamber.

2. The aeration/backwash device according to claim 1, wherein the upper and lower through-openings are configured to allow selective fluid communication of the gas and backwash liquid between the communication chamber and the membrane filtration module through the same upper or lower through-openings.

3. The aeration/backwash device according to claim 1, wherein the upper and lower through-openings are configured to allow the gas to fluidly communicate through at least the upper through-openings into the membrane filtration module and to allow the backwash liquid to fluidly communicate through the lower through-openings.

4. The aeration/backwash device according to claim 3, wherein the upper and lower through-openings are configured to allow the backwash liquid or a source of feed liquid in fluid communication with the communication chamber to fluidly communicate from the communication chamber to the membrane filtration module through the lower through-openings or through the upper and lower through-openings.

5. The aeration/backwash device according to claim 4, wherein the upper and lower through-openings are configured to allow the backwash or feed liquid to fluidly communicate from the membrane filtration module to the communication chamber through the lower through-openings or through the upper and lower through-openings.

6. The aeration/backwash device according to claim 1, wherein the upper through-openings are smaller than the lower through-openings.

7. The aeration/backwash device according to claim 1, wherein the upper and lower through-openings are axially spaced around the periphery of the chamber.

8. The aeration/backwash device according to claim 1, wherein both the upper and lower through-openings are configured to allow the backwash liquid to fluidly communicate from the membrane filtration module to the communication chamber or from the communication chamber to the membrane filtration module through the upper and lower through-openings.

9. The aeration/backwash device according to claim 1, wherein the device is formed as an annulus.

10. A porous membrane filtration module comprising:

an upper and lower header vertically spaced from each other;

one or more membranes having a permeable wall and an upper and lower end extending longitudinally between the upper and lower headers, into which the ends of the one or more membranes are potted, wherein at least one of the upper or lower ends of the membranes is in fluid communication with the upper or lower header, and the permeable wall is configured to allow feed containing contaminant matter to be applied to one side of the wall and to allow filtrate to be withdrawn from the other side of the wall;

at least one filtrate collection chamber in fluid communication with at least one of the upper and lower header; and

an aeration/backwash device comprising;

a communication chamber including a closed internal volume defined by an inner wall, an outer wall, an upper wall coupling the inner wall to the outer wall, and a lower wall coupling the inner wall to the outer wall, the communication chamber at least partially surrounding a circumference of the membrane filtration module, the inner wall having upper through-openings and lower through-openings vertically spaced apart from the upper through-openings, the upper and lower through-openings spaced circumferentially about the inner wall, each through-opening having a longitudinal axis substantially perpendicular to the one or more membranes;

a source of gas in fluid communication with the internal volume of the communication chamber; and

a source of backwash liquid in fluid communication with the internal volume of the communication chamber,

wherein the source of gas and the source of backwash liquid share a common inlet to the internal volume of the communication chamber.

11. The porous membrane filtration module according to claim 10, wherein the upper and lower through-openings are configured to allow the gas to fluidly communicate through at least the upper through-openings into the membrane filtration module and to allow the backwash liquid to fluidly communicate through the lower through-openings.

12. The porous membrane filtration module according to claim 10, further comprising a filtrate connection pipe in fluid communication with and configured to withdraw filtrate from the at least one filtrate collection chamber.

13. The porous membrane filtration module according to claim 10, wherein the aeration/backwash device is located adjacent the lower header.

14. The porous membrane filtration module according to claim 10, wherein the at least one filtrate collection chamber further comprises at least one collection cup adapted to detachably receive and engage in a fluid-tight manner with the upper or lower header.

15. The porous membrane filtration module according to claim 14, wherein the upper or lower header is engaged with the at least one collection cup by means of a bayonet-type fitting.

16. The porous membrane filtration module according to claim 10, further comprising a screen that at least partially surrounds the one or more membranes.

17. The porous membrane filtration module according to claim 16, wherein the screen is a sleeve which extends along part of the length of the one or more membranes.

18. The porous membrane filtration module according to claim 16, wherein the screen is solid.

19. The porous membrane filtration module according to claim 18, wherein the screen extends along the full length of the membrane filtration module and comprises one or more openings adjacent the upper and lower through-openings of the aeration/backwash device to allow communication with the membranes and one or more additional openings at or adjacent a top of the module and configured to allow flow of a gas or a liquid therethrough.

20. The porous membrane filtration module according to claim 19, having one or more further openings in the screen at or adjacent to the aeration/backwash device and configured to allow bypass of a backwash flow.

21. The porous membrane filtration module according to claim 16, wherein the screen is located above the aeration/backwash device.

22. A membrane filtration system comprising:

at least one membrane filtration module comprising one or more membranes and opposing potted ends;

a feed tank in fluid communication with the at least one membrane filtration module;

at least one filtrate manifold in fluid communication with the at least one membrane filtration module and a source of filtrate;

at least one aeration/backwash device comprising;

a communication chamber including a closed internal volume defined by an inner wall, an outer wall, an upper wall coupling the inner wall to the outer wall, and a lower wall coupling the inner wall to the outer wall, the communication chamber at least partially surrounding a circumference of the membrane filtration module, the inner wall having upper through-openings and lower through-openings vertically spaced apart from the upper through-openings, the upper and lower through-openings spaced circumferentially about the inner wall, each through-opening having a longitudinal axis substantially perpendicular to the one or more membranes; and

a source of gas in fluid communication with the internal volume of the communication chamber;

at least one aeration/backwash manifold in fluid communication with the aeration/backwash device; and

a source of backwash liquid in fluid communication with the aeration/backwash manifold, wherein the source of gas and the source of backwash liquid share a common inlet to the internal volume of the communication chamber.

23. The membrane filtration system according to claim 22, wherein the source of gas is in fluid communication with the at least one aeration/backwash manifold.

24. The membrane filtration system according to claim 22, further comprising at least one gas manifold in fluid communication with the at least one aeration/backwash device.

25. The membrane filtration system according to claim 24, wherein the source of gas is in fluid communication with the at least one gas manifold.

26. The membrane filtration system according to claim 22, wherein the at least one filtrate and aeration/backwash manifolds are arranged along a bottom of the feed tank.

27. The membrane filtration system according to claim 22, wherein the at least one filtrate and aeration/backwash manifolds are installed near a base of the at least one membrane filtration module.

28. The membrane filtration system according to claim 22, wherein the at least one aeration/backwash device is formed as an annulus that surrounds a base of the at least one filtration module.

29. The membrane filtration system according to claim 22, wherein the upper and lower through-openings are configured to allow the gas to fluidly communicate through at least the upper through-openings into the membrane filtration module and to allow the backwash liquid to fluidly communicate through the lower through-openings.

30. The membrane filtration system according to claim 29, wherein the lower through-openings are in fluid communication with a source of feed liquid.

31. The membrane filtration system according to claim 29, wherein the upper and lower through-openings are axially spaced around the periphery of the communication chamber.

32. The membrane filtration system according to claim 22, wherein the source of filtrate is fluidly communicated to the at least one filtrate manifold from a top or a bottom of the at least one membrane filtration module.

33. The membrane filtration system according to claim 22, wherein both the upper and lower through-openings are configured to allow the backwash liquid to fluidly communicate from the membrane filtration module to the communication chamber or from the communication chamber to the membrane filtration module through the upper and lower through-openings.