AU2003254384B2 - Aeration method - Google Patents
Aeration method Download PDFInfo
- Publication number
- AU2003254384B2 AU2003254384B2 AU2003254384A AU2003254384A AU2003254384B2 AU 2003254384 B2 AU2003254384 B2 AU 2003254384B2 AU 2003254384 A AU2003254384 A AU 2003254384A AU 2003254384 A AU2003254384 A AU 2003254384A AU 2003254384 B2 AU2003254384 B2 AU 2003254384B2
- Authority
- AU
- Australia
- Prior art keywords
- bundle
- membrane filtration
- filtration module
- module according
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000000034 method Methods 0.000 title claims description 12
- 238000005273 aeration Methods 0.000 title 1
- 239000012528 membrane Substances 0.000 claims description 32
- 239000000835 fiber Substances 0.000 claims description 18
- 238000005374 membrane filtration Methods 0.000 claims description 17
- 238000004140 cleaning Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 description 5
- 238000004382 potting Methods 0.000 description 5
- 238000009991 scouring Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000003491 array Methods 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Description
00 -1- TECHNICAL FIELD The present invention relates to membrane filtration systems and more particularly Sto an improved backwash method and apparatus.
BACKGROUND OF THE INVENTION Any discussion of the prior art throughout the specification should in no way be 00 Mc, considered as an admission that such prior art is widely known or forms part of common in general knowledge in the field.
The use of membrane filtration systems is growing rapidly. The success of such systems is largely dependant on employing effective and efficient membrane cleaning methods. Commonly used physical cleaning methods include backwash (backpulse, backflush) using liquid permeate or a gas, and membrane scrubbing or scouring using a gas in the form of bubbles in a liquid. Examples of this second type of method are illustrated in United States Patent No. 5,192,456 to Ishida et al, United States Patent No.
5,248,424 to Cote et al, United States Patent No. 5,639,373 to Henshaw et al, United States Patent No. 5,783,083 to Henshaw et al and our PCT Application Nos W098/28066 and W00O/18498.
These prior art systems use a variety of techniques to introduce gas bubbles into the membrane arrays to produce effective and efficient surface cleaning. It has been found that effective cleaning is achieved by introducing bubbles into the array in a uniform manner and retaining the bubbles within the array as much as possible to produce efficient cleaning of the membrane surfaces.
SUMMARY OF THE INVENTION One object of the present invention is to provide an improved method and apparatus for introducing gas into membrane array which overcomes or at least ameliorates one or more of the disadvantages of the prior art or at least provides a useful alternative.
According to a first aspect, the present invention provides a method of cleaning outer surfaces of membranes for use in filtering a liquid, the method comprising the steps of: 00- 0 providing a bundle of porous hollow membranes mounted between upper and b lower potting sleeves and immersed into liquid; and directing gas bubbles toward the bundle from around a circumference of the IN bundle transversely of a vertical axis of the bundle with a gas feeder spaced from the potting sleeves.
00 Preferably, said method includes the step of retaining said gas bubbles within said bundle using a sleeve surrounding said bundle at least along part of its length.
According to a further aspect, the present invention provides a membrane filtration module including a bundle of porous hollow membrane and a gas feeder fitted around the circumference of the bundle.
According to another aspect, the present invention provides a membrane filtration module comprising a bundle of porous hollow membrane mounted between headers, and gas feeding means for directing gas bubbles toward a bundle from around a circumference of the bundle transversely of a vertical axis of the bundle independently of the headers.
For preference, said module further includes a sleeve surrounding said bundle at least along part of its length for retaining said gas bubbles within the bundle. Preferably, the sleeve extends along 17% or greater of the length of the array.
Preferably, said porous hollow membranes comprise hollow fibre membranes. For preference, the fibre membranes are formed in a generally cylindrical bundle. For further preference, said sleeve is located adjacent and above the gas feeder. Preferably, the gas feeder comprises a tube adapted to extend around the periphery of the bundle of membranes, the tube having a plurality of openings located on its inner surface adjacent the bundle of membranes for feeding gas into the membrane bundle. For preference, a number of gas feeders are provided along the length of the bundle. Preferably, the openings in the tube include extensions in the form of tubes adapted to extend into the bundle. For preference, the sleeve extends along a major portion of the length of said membranes.
Unless the context clearly requires otherwise, throughout the description and the claims, the words "comprise", "comprising", and the like are to be construed in an 00 2a- 0 O inclusive sense as opposed to an exclusive or exhaustive sense; that is to say, in the sense of"including, but not limited to".
BRIEF DESCRIPTION OF THE DRAWINGS A preferred embodiment of the invention will now be described, by way of example only, with reference to the accompanying drawings in which: 00 Mc, Figure 1 shows a broken side elevation view of a hollow fibre membrane module n with a gas feeding ring according to an embodiment of the invention; Figure 2 shows a perspective view of the gas feeding ring of Figure 1; Figure 3 shows a cutaway perspective view of the gas feeding ring of Figure 2; and Figure 4 shows a graph of transmembrane pressure (TMP) vs time running of a filtration module for different percentage lengths of the wrapping of the module.
DESCRIPTION OF PREFERRED EMBODIMENT The preferred embodiment relates to porous hollow fibre membranes, however, it will be appreciated that the invention is not limited to such an application and is equally applicable to other similar arrays of membranes.
Referring to the drawings, a fibre membrane module 5 is shown in figure 1 comprising a bundle of hollow fibre membranes 6 extending between an upper and lower potting sleeves 7 and 8, respectively. The fibre membranes 6 are supported by a screen 9 also extending between the sleeves 7 and 8.
WO 2004/018084 PCT/AU20031001068 -3- The gas feeding ring 10 is fitted around the circumference of the fibre bundle 6 at a location spaced from the lower potting sleeve 8. A tube or sleeve 11 is placed around the bundle 6 above the gas feeding ring 10 and extends along the length of the bundle 6.
The tube 11 may be formed as a solid tube or by wrapping a suitable sheet material around the fibre bundle 6. The tube material should be impervious to the gas bubbles so they are retained within the fibre bundle but need not be liquid impervious. A region 12 above and below the potting sleeves is left uncovered by the tube 11 to allow entry of feed to the fibre membranes as well as removal of material backwashed from the membranes by usual processes as well as bubbles fed into the bundle by the gas feeding ring Figures 2 and 3 show the gas feeding ring 10 in more detail. The ring is an annular tube 15 having spaced holes or openings 16 formed around its inner circumference to allow gas to be fed into the fibre array when the ring is placed around the bundle as shown in Figure 1. Gas or air may be supplied to the ring 10 through a port 17 in one side ofthering.
The system provides a number of advantages. Air or gas can be fed into the membrane bundle at a number of locations along its length by use of a number of gas feeding rings. This enables more uniform provision of gas scouring bubbles within the bundles. Retention of bubbles within the bundle by the tube or sleeve 11 produces a more efficient scouring of the fibre surfaces. Provision of scouring bubbles in this way, independent of the fibre headers, allows filtrate to withdrawn from either of both ends of the fibre module and allows reverse filtration from either or both ends of the fibre module when backwashing.. Figure 4 illustrates the reduction in increase of TMP with increased sleeve or wrapping length along the fibre bundle.
It will also be appreciated that further embodiments and exemplifications of the invention are possible without departing from the spirit or scope of the invention described.
Claims (9)
- 3. A membrane filtration module including a bundle of porous hollow membranes and a gas feeder fitted around the circumference of the bundle.
- 4. A membrane filtration module comprising a bundle of porous hollow membranes mounted between headers, and gas feeding means for directing gas bubbles toward a bundle from around a circumference of the bundle transversely of a vertical axis of the bundle independently of the headers. A membrane filtration module according to claim 3 or claim 4 wherein said module further includes a sleeve positioned about said bundle at least along part of the length of the bundle for retaining said gas bubbles within the bundle.
- 6. A membrane filtration module according to claim 5 wherein the sleeve extends along about 17% or greater of the length of the array.
- 7. A membrane filtration module according to claim 5 wherein the sleeve extends along a major portion of the length of said membranes.
- 8. A membrane filtration module according to any one of claims 5 to 7 wherein said sleeve is located adjacent to the gas feeder and above the gas feeder.
- 9. A membrane filtration module according to any one of claims 3 to 8 wherein said porous hollow membranes comprise hollow fibre membranes. 00 A membrane filtration module according to claim 9 wherein the bundle is generally cylindrical.
- 11. A membrane filtration module according to any one of claims 3 to 10 wherein the N gas feeder comprises a tube defining a plurality of openings located on an inner circumference of the gas feeder. 00 12. A membrane filtration module according to claim 11 wherein the openings in the tube include extensions in the form of tubes adapted to extend into the array. Cc 13. A membrane filtration module according to any one of claims 3 to 12 further including a number of gas feeders positioned along the length of the bundle.
- 14. A membrane filtration module according to any one of claims 3 to 13 further including a screen positioned about said porous hollow membranes. A membrane filtration module substantially as herein described with reference to any one of the embodiments of the invention illustrated in the accompanying drawings.
- 16. A method of cleaning the outer surfaces of membranes substantially as herein described with reference to any one of the embodiments of the invention illustrated in the accompanying drawings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2003254384A AU2003254384B2 (en) | 2002-08-21 | 2003-08-21 | Aeration method |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2002950934A AU2002950934A0 (en) | 2002-08-21 | 2002-08-21 | Aeration method |
AU2002950934 | 2002-08-21 | ||
PCT/AU2003/001068 WO2004018084A1 (en) | 2002-08-21 | 2003-08-21 | Aeration method |
AU2003254384A AU2003254384B2 (en) | 2002-08-21 | 2003-08-21 | Aeration method |
Publications (2)
Publication Number | Publication Date |
---|---|
AU2003254384A1 AU2003254384A1 (en) | 2004-03-11 |
AU2003254384B2 true AU2003254384B2 (en) | 2008-09-25 |
Family
ID=34275475
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2003254384A Expired AU2003254384B2 (en) | 2002-08-21 | 2003-08-21 | Aeration method |
Country Status (1)
Country | Link |
---|---|
AU (1) | AU2003254384B2 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4876006A (en) * | 1985-10-08 | 1989-10-24 | Ebara Corporation | Hollow fiber filter device |
JPH07236819A (en) * | 1994-02-25 | 1995-09-12 | Nok Corp | Air bubble disperser |
JP2000317276A (en) * | 1999-05-12 | 2000-11-21 | Zenken:Kk | Filtering device |
US20020070157A1 (en) * | 2000-08-18 | 2002-06-13 | Yosuke Yamada | Filter device |
-
2003
- 2003-08-21 AU AU2003254384A patent/AU2003254384B2/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4876006A (en) * | 1985-10-08 | 1989-10-24 | Ebara Corporation | Hollow fiber filter device |
JPH07236819A (en) * | 1994-02-25 | 1995-09-12 | Nok Corp | Air bubble disperser |
JP2000317276A (en) * | 1999-05-12 | 2000-11-21 | Zenken:Kk | Filtering device |
US20020070157A1 (en) * | 2000-08-18 | 2002-06-13 | Yosuke Yamada | Filter device |
Also Published As
Publication number | Publication date |
---|---|
AU2003254384A1 (en) | 2004-03-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FGA | Letters patent sealed or granted (standard patent) | ||
MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |