Aeration method

• US 7,361,274 B2
• Filed: 02/16/2005
• Issued: 04/22/2008
• Est. Priority Date: 08/21/2002
• Status: Expired due to Term

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Inventors: Lazaredes, Huw Alexander
• Primary Examiner(s): Drodge; Joseph
• Application Number:
  US11/060,106
• Publication Number:
  US 20050139538A1
• Time in Patent Office: 1,161 Days
• Field of Search: 210/321.69, 210/321.79, 210/321.8, 210/321.89, 210/321.9, 210/500.23, 210/636, 210/639, 210/650, 210/651, 210409-415, 210791-798, 554/31, 96/8
• US Class Current: 210/636
• CPC Class Codes: B01D 2201/087 using gas bubbles, e.g. air
• CPC Class Codes: B01D 2313/26 Specific gas distributors or gas intakes
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 29/114 arranged for inward flow filtration B01D29/15, B01D29/33 take precedence
• CPC Class Codes: B01D 29/62 Regenerating the filter material in the filter devices for taking out of action one or more units of multi-unit filters, e.g. for regeneration, B01D35/12
• CPC Class Codes: B01D 29/6438 nozzles
• CPC Class Codes: B01D 63/026 Wafer type modules or flat-surface type 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 filtration module (5) for providing gas bubbles within an array of vertically disposed porous hollow membranes (6) to clean the outer surfaces of said membranes (6) when the array is immersed in a liquid by feeding (10) the gas bubbles into the array transversely of the vertical axis of the array. In one preferred form, the gas bubbles are retained within the array using a sleeve (11) surrounding the array (6) at least along part of its length.

Claims

1. A method of cleaning outer surfaces of membranes for use in filtering a liquid, the method comprising the steps of:

providing a bundle of porous hollow fiber membranes mounted between upper and lower potting sleeves and immersed in the liquid; and

directing gas bubbles toward the bundle from around a circumference of the bundle transversely of a vertical axis of the bundle with one or more gas feeding rings fitted around the circumference of the bundle at locations spaced from the potting sleeves, the ring comprising a tube having an axis extending circumferentially around the bundle and having spaced openings formed to allow gas to be fed inwardly toward the bundle.

2. The method of claim 1, wherein the method further comprises the step of:

retaining the gas bubbles within the bundle with a sleeve surrounding the bundle along at least a part of a length of the bundle.

3. The method of claim 1, further comprising withdrawing filtrate from either or both of the upper and lower potting sleeves.

4. The method of claim 1, further comprising backwashing the module from either or both of the upper and lower potting sleeves.

5. A membrane filtration module comprising a bundle of porous hollow fiber membranes mounted in a lower potting sleeve and one or more gas feeding rings fitted around a circumference of the bundle at locations spaced from the lower potting sleeve, the ring comprising a tube having an axis extending circumferentially around the bundle and having spaced openings formed to allow gas to be fed inwardly toward the bundle.

6. The membrane filtration module according to claim 5, wherein the module further comprises a sleeve positioned about the bundle along at least a part of a length of the bundle, wherein the sleeve is impervious to the gas bubbles.

7. The membrane filtration module according to claim 6, wherein the sleeve extends along about 17% or greater of the length of the bundle.

8. The membrane filtration module according to claim 6, wherein the sleeve extends along a major portion of a length of the bundle.

9. The membrane filtration module according to claim 6, wherein the sleeve is situated adjacent to the gas feeding ring and above the gas feeding ring.

10. The membrane module according to claim 5, wherein the bundle is generally cylindrical.

11. The membrane filtration module according to claim 5, wherein the spaced openings of the gas feeding ring are positioned on an inner circumference of the gas feeding ring.

12. The membrane filtration module according to claim 11, wherein the gas feeding ring further comprises tube extensions positioned about the spaced openings.

13. The membrane filtration module according to claim 5, further comprising a plurality of gas feeding rings positioned along a length of the bundle.

14. The membrane filtration module according to claim 5, further comprising a screen positioned about the porous hollow membranes.

15. The membrane filtration module according to claim 5, wherein the porous hollow membranes are disposed vertically.

16. The module of claim 5, wherein the gas feeding ring is configured to direct gas bubbles toward the bundle from around the circumference of the bundle transversely of a vertical axis of the bundle.

17. The module of claim 5, wherein the gas feeding ring is configured to provide scouring bubbles independently of the lower potting sleeve or an upper potting sleeve.