JPS61192309A - Hollow yarn type module - Google Patents
Hollow yarn type moduleInfo
- Publication number
- JPS61192309A JPS61192309A JP3154285A JP3154285A JPS61192309A JP S61192309 A JPS61192309 A JP S61192309A JP 3154285 A JP3154285 A JP 3154285A JP 3154285 A JP3154285 A JP 3154285A JP S61192309 A JPS61192309 A JP S61192309A
- Authority
- JP
- Japan
- Prior art keywords
- hollow
- hollow yarn
- gas
- hollow fiber
- fixed part
- 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.)
- Pending
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、中空系型モジュールを使用しで、汚染物を含
む原水等の口過を外圧法で行うとき、中空系の外面に付
着するコロイド等の汚染物を容易に取り除くことができ
るようになした中空糸型モジュールに関する。Detailed Description of the Invention (Field of Industrial Application) The present invention uses a hollow system module to filter raw water containing contaminants using an external pressure method. The present invention relates to a hollow fiber module that allows contaminants such as colloids to be easily removed.
(従来技術とその問題点)
金属コロイド等のコロイド状物質を含む原水或はその他
の汚染物を含む原水等を中空糸型モ゛ジュールを用いて
外圧法で口過する場合、中空糸の外面にはコロイド物質
等の汚染物が付着するので、口過水量は次第に低下し、
また−1中空糸の耐用年数も短かくなる欠点がある。そ
こで、中空糸の外面に付着したコロイド等を取り除くた
めに逆洗等が行なわれているが十分な効果は得られてい
ない。(Prior art and its problems) When raw water containing colloidal substances such as metal colloids or raw water containing other contaminants is filtered using a hollow fiber module using an external pressure method, the outer surface of the hollow fiber As contaminants such as colloidal substances adhere to the water, the amount of water passing through the mouth gradually decreases.
Moreover, the -1 hollow fiber has the disadvantage that its service life is shortened. Therefore, backwashing and the like have been carried out to remove colloids and the like adhering to the outer surface of the hollow fibers, but sufficient effects have not been obtained.
本発明者はこの問題の解決のために、別途、中空糸型モ
ジュール下部における中空糸束を接着固定した接着固定
部に、該接着固定部を貫通するスリットを設け、口過水
量が低下したとき、該スリッI・より気体又は気体を含
む液体を導入することによって、中空糸に付着したコロ
イド物質等を取り除くことを提案した。この提案によれ
ば、コロイド等の除去に効果はあるが一方スリ・ント製
作時に中空糸を傷つけ易く、また、スリットの数が少な
いと、コロイド物質が除去されるのは、スリット近傍の
中空糸に限定され、スリットの数を多くすると作業が大
変である等の問題点がある。In order to solve this problem, the inventor separately provided a slit that penetrates the adhesive fixing part in which the hollow fiber bundle is adhesively fixed at the bottom of the hollow fiber type module, so that when the amount of water passing through the mouth decreases. proposed that colloidal substances adhering to the hollow fibers be removed by introducing gas or a liquid containing gas through the slit I. According to this proposal, it is effective in removing colloids, etc., but on the other hand, the hollow fibers are easily damaged when making slits, and if the number of slits is small, the colloidal substances are removed only by the hollow fibers near the slits. However, if the number of slits is increased, the work becomes difficult.
(発明の目的)
本発明は、前記した問題点を解決するために、中空糸の
外部に付着したコロイド等の汚染物を簡単にしかも効率
的に除去できる中空糸型モジュールを提供するものであ
る。(Object of the Invention) In order to solve the above-mentioned problems, the present invention provides a hollow fiber module that can easily and efficiently remove contaminants such as colloids attached to the outside of the hollow fibers. .
(発明の構成)
本発明は、上部は開口し、下部は閉止した多数の中空糸
の上下両端を接着剤によって固定した中空系型モジュー
ルにおいて、下部接着固定部を貫通して、両端開口の送
気管を中空糸束内に分散して埋設し、場合によっては、
更に上部接着固定部に少なくとも一端を閉lヒした隔離
管を中空糸束内に分散して埋設したことを特徴とする。(Structure of the Invention) The present invention provides a hollow type module in which the upper and lower ends of a large number of hollow fibers, each of which is open at the upper part and closed at the lower part, are fixed with an adhesive. The trachea is dispersed and buried within a hollow fiber bundle, and in some cases,
Furthermore, it is characterized in that isolation tubes with at least one end closed are embedded in the upper adhesive fixing part and are dispersed within the hollow fiber bundle.
(実施態様)
次に、本発明の中空糸型モジュールを図面によって説明
する。(Embodiment) Next, the hollow fiber type module of the present invention will be explained with reference to the drawings.
第1〜第3図は、本発明の中空糸型モジュールの一例を
示す。中空系束はハウジング(1)内に上下両端を接着
剤で固定して収容されている。各中空糸(2)は−F端
が開口し、下端は閉止しており、」一端は上部接着固定
部(3)で、また下端は下記接着固定部(3)によって
固定されている。下部接着固定部(3)には、該固定部
を貫通して該接着固定部の厚みより長い、両端が開口し
た多数の送気管(5)が中空糸束内に分散して埋設され
ている(第2図)。一方、上部接着固定部(3)には、
中空糸の両端又は一端を閉止した隔離管(4)が中空糸
束内に分散して埋設しである(第3図)。1 to 3 show an example of a hollow fiber type module of the present invention. The hollow bundle is housed in a housing (1) with its upper and lower ends fixed with adhesive. Each hollow fiber (2) is open at the -F end and closed at the lower end; one end is fixed by an upper adhesive fixing part (3) and the lower end is fixed by an adhesive fixing part (3) described below. In the lower adhesive fixing part (3), a large number of air supply pipes (5), which penetrate the fixing part and are longer than the thickness of the adhesive fixing part and are open at both ends, are dispersed and buried within the hollow fiber bundle. (Figure 2). On the other hand, in the upper adhesive fixing part (3),
Isolation tubes (4) with both ends or one end of the hollow fibers closed are dispersed and embedded within the hollow fiber bundle (Fig. 3).
原水入口(6)よりモジュール内に加圧導入された原水
は、ハウジング内の各中空糸(2)の外側に入り、原水
中に含まれるコロイド等の汚染物は中空糸(2)の外側
に残り、中空糸壁を通って口過された清浄水は、上部接
着固定部を経て口過水出口(7)から排出される。Raw water pressurized into the module from the raw water inlet (6) enters the outside of each hollow fiber (2) in the housing, and contaminants such as colloids contained in the raw water are removed to the outside of the hollow fibers (2). The remaining clean water passed through the hollow fiber wall passes through the upper adhesive fixing part and is discharged from the passed water outlet (7).
中空糸の外壁にコロイド等が次第に付着し、口過効率が
低下した際には、原水の送給を中空して、送気管(5)
を通して気体又は気体を含む液体を送入する。送入され
た気体によってコロイド等の汚染物は中空糸壁からはが
れて中空糸の活性は回復する。送入された気体は汚染物
除去後、上部接着固定部の下部に集まる。更に上部、接
着固定部(3)内に隔離管(4)を分散埋設しておけば
、各中空糸は十分な間隔を保っているので、送入された
気体は中空糸束内を均一に上昇流動し、除去性能が一層
向上する。隔離管(4)は両端又は一端が閉止されてい
るので、気体が口過水に混入することはない。中空糸壁
から除去された汚染物は、コロイド液抜き出し口(8)
から、また、気体は気体抜き出し口(8)から間けつ的
に排出除去し、中空糸の活性が回復した後、口過を再開
する。When colloids etc. gradually adhere to the outer wall of the hollow fiber and the filtration efficiency decreases, the raw water is fed through the air pipe (5).
A gas or a liquid containing gas is introduced through the Contaminants such as colloids are peeled off from the walls of the hollow fibers by the introduced gas, and the activity of the hollow fibers is restored. The injected gas collects at the bottom of the upper adhesive fixing part after removing contaminants. Furthermore, if isolation tubes (4) are dispersed and buried in the adhesive fixing part (3) in the upper part, each hollow fiber will maintain sufficient spacing, so the injected gas will be distributed uniformly within the hollow fiber bundle. It flows upward, further improving removal performance. Since the isolation tube (4) is closed at both ends or at one end, gas will not be mixed into the drinking water. Contaminants removed from the hollow fiber wall are removed from the colloid liquid outlet (8).
Then, the gas is discharged and removed intermittently from the gas outlet (8), and after the activity of the hollow fibers is restored, the filtration is restarted.
送気管の径としては、内径0.1〜10fflI11程
度が好ましい。0.1mm未満では送気管を通って導入
される気体又は気体を含む液体の量が不足するため、中
空糸外面に付着したコロイド等の除去が不十分となり、
また10mmを越えると、導入された気体が十分分散さ
れないとか、中空糸の本数が少なくなり、口過効率が低
下する等の問題が生ずる。The diameter of the air pipe is preferably about 0.1 to 10 fflI11 in inner diameter. If it is less than 0.1 mm, the amount of gas or gas-containing liquid introduced through the air pipe will be insufficient, and colloids etc. adhering to the outer surface of the hollow fibers will be insufficiently removed.
Moreover, if it exceeds 10 mm, problems such as the introduced gas not being sufficiently dispersed or the number of hollow fibers decreasing will occur, such as a decrease in filtration efficiency.
送気管は気体が好適に送入されるようにその長さを任意
に調節できる。送気管の本数は、送気管の直径や使用す
るモジュールの直径によって異なり、本数が多い程コロ
イド等の除去には効果があるが、中空糸膜面積が減少す
るので、これらの点を配慮して適当に決定する必要があ
る。The length of the air supply pipe can be adjusted arbitrarily so that gas can be suitably introduced. The number of air pipes varies depending on the diameter of the air pipe and the diameter of the module used. The larger the number, the more effective it is in removing colloids, etc., but the hollow fiber membrane area will decrease, so please take these points into consideration. It is necessary to decide appropriately.
(発明の効果)
本発明の中空糸型モジュールは、汚染、物の除去が容易
で、口過効率を高く保持できる。(Effects of the Invention) The hollow fiber module of the present invention allows easy removal of contamination and substances, and can maintain high filtration efficiency.
第1図は、本発明の中空糸型モジュールの一部を縦断し
て示した概念的説明図。
第2図は、第1図のA−A’線による断面図で、送気管
と中空糸の関係を概念的に拡大して示したもの、第3図
は、第1図のB−B’線による断面図で、中空系と隔離
管の関係を概念的に拡大して示したものである。
1ハウジング 5送気管
2中空糸 6原水入口
3接着固定部 70過水出ロ
4隔離管 8気体抜き出しロ9コロイド液抜
き出し口FIG. 1 is a conceptual explanatory diagram showing a part of the hollow fiber type module of the present invention in longitudinal section. FIG. 2 is a cross-sectional view taken along line AA' in FIG. 1, conceptually enlarging the relationship between the air pipe and the hollow fibers, and FIG. 3 is a cross-sectional view taken along line AA' in FIG. 1. This is a cross-sectional view drawn by lines, conceptually enlarging the relationship between the hollow system and the isolation tube. 1 Housing 5 Air supply pipe 2 Hollow fiber 6 Raw water inlet 3 Adhesive fixing part 70 Super water outlet 4 Isolation pipe 8 Gas extraction outlet 9 Colloid liquid outlet
Claims (2)
上下両端を接着剤によって固定した中空糸型モジュール
において、下部接着固定部を貫通して、両端開口の送気
管を、中空糸束内に分散して、埋設したことを特徴とす
る中空糸型モジュール。(1) In a hollow fiber module in which the upper and lower ends of a large number of hollow fibers are fixed with adhesive, the upper part is open and the lower part is closed, the hollow fibers pass through the lower adhesive fixing part and connect the air pipe with both ends open. A hollow fiber module characterized by being dispersed and buried within a bundle.
下両端を接着剤によって固定した中空糸型モジュールに
おいて、下部接着固定部を貫通して、両端開口の送気管
を、中空糸束内に分散して埋設すると共に、上部接着固
定部には少なくとも一端を閉止した隔離管を中空糸束内
に分散して埋設したことを特徴とする中空糸型モジュー
ル。(2) In a hollow fiber module in which both the upper and lower ends of a large number of hollow fibers, which are open at the upper end and closed at the lower end, are fixed with an adhesive, the air supply tube with both ends open is inserted into the hollow fiber bundle by passing through the lower adhesive fixing part. What is claimed is: 1. A hollow fiber module characterized in that isolation tubes with at least one end closed are dispersed and buried within the hollow fiber bundle in the upper adhesive fixing part.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3154285A JPS61192309A (en) | 1985-02-21 | 1985-02-21 | Hollow yarn type module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3154285A JPS61192309A (en) | 1985-02-21 | 1985-02-21 | Hollow yarn type module |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61192309A true JPS61192309A (en) | 1986-08-26 |
Family
ID=12334075
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3154285A Pending JPS61192309A (en) | 1985-02-21 | 1985-02-21 | Hollow yarn type module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61192309A (en) |
Cited By (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002525197A (en) * | 1998-09-25 | 2002-08-13 | ユー・エス・フィルター・ウェイストウォーター・グループ・インコーポレイテッド | Cleaning device and cleaning method for filtration membrane module |
US6620319B2 (en) | 1995-08-11 | 2003-09-16 | Zenon Enviromental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US6969465B2 (en) | 1996-12-20 | 2005-11-29 | U. S. Filter Wastewater Group, Inc. | Scouring method |
US7025885B2 (en) | 1998-11-23 | 2006-04-11 | Zenon Environmental Inc. | Water filtration using immersed membranes |
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
JP2007090309A (en) * | 2005-09-30 | 2007-04-12 | Kureha Corp | Hollow fiber bundle, method for producing the same, tubular hollow fiber membrane module, and immersion type hollow fiber membrane module |
WO2007040036A1 (en) * | 2005-09-30 | 2007-04-12 | Kureha Corporation | Hollow fiber bamboo-blind-like article, process for producing hollow fiber bundle, tubular hollow fiber membrane module and immersion type hollow fiber membrane module |
WO2007040035A1 (en) * | 2005-09-30 | 2007-04-12 | Kureha Corporation | Hollow fiber bundle, process for producing hollow fiber bundle, tubular hollow fiber membrane module and immersion type hollow fiber membrane module |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
JP2007144349A (en) * | 2005-11-29 | 2007-06-14 | Ebara Corp | Hollow fiber membrane module |
US7247210B2 (en) | 2004-02-23 | 2007-07-24 | Ecolab Inc. | Methods for treating CIP equipment and equipment for treating CIP equipment |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
US7850853B2 (en) | 2005-03-09 | 2010-12-14 | Zhejiang Environmental Engineering Company Limited | Floating porous hollow fiber membrane bundle |
US8057574B2 (en) | 2003-07-08 | 2011-11-15 | Siemens Industry, Inc. | Membrane post treatment |
US8173018B2 (en) | 2010-08-25 | 2012-05-08 | Dow Global Technologies Llc | Fluid filter module including sealed boss |
US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
US8287743B2 (en) | 2007-05-29 | 2012-10-16 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
US8293098B2 (en) | 2006-10-24 | 2012-10-23 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8318028B2 (en) | 2007-04-02 | 2012-11-27 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
US8382981B2 (en) | 2008-07-24 | 2013-02-26 | Siemens Industry, Inc. | Frame system for membrane filtration modules |
US8894858B1 (en) | 2005-08-22 | 2014-11-25 | Evoqua Water Technologies Llc | Method and assembly for water filtration using a tube manifold to minimize backwash |
US8956464B2 (en) | 2009-06-11 | 2015-02-17 | Evoqua Water Technologies Llc | Method of cleaning membranes |
US9022224B2 (en) | 2010-09-24 | 2015-05-05 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
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US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
US9764289B2 (en) | 2012-09-26 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane securement device |
US9815027B2 (en) | 2012-09-27 | 2017-11-14 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
US9868834B2 (en) | 2012-09-14 | 2018-01-16 | Evoqua Water Technologies Llc | Polymer blend for membranes |
US9914097B2 (en) | 2010-04-30 | 2018-03-13 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US9925499B2 (en) | 2011-09-30 | 2018-03-27 | Evoqua Water Technologies Llc | Isolation valve with seal for end cap of a filtration system |
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-
1985
- 1985-02-21 JP JP3154285A patent/JPS61192309A/en active Pending
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US7063788B2 (en) | 1995-08-11 | 2006-06-20 | Zenon Environmental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US6620319B2 (en) | 1995-08-11 | 2003-09-16 | Zenon Enviromental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US6682652B2 (en) | 1995-08-11 | 2004-01-27 | Zenon Environmental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes |
US6964741B2 (en) | 1995-08-11 | 2005-11-15 | Zenon Environmental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes |
US7534353B2 (en) | 1995-08-11 | 2009-05-19 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
US8075776B2 (en) | 1995-08-11 | 2011-12-13 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7708888B2 (en) | 1995-08-11 | 2010-05-04 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7615157B2 (en) | 1995-08-11 | 2009-11-10 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US6969465B2 (en) | 1996-12-20 | 2005-11-29 | U. S. Filter Wastewater Group, Inc. | Scouring method |
US8048306B2 (en) * | 1996-12-20 | 2011-11-01 | Siemens Industry, Inc. | Scouring method |
JP2002525197A (en) * | 1998-09-25 | 2002-08-13 | ユー・エス・フィルター・ウェイストウォーター・グループ・インコーポレイテッド | Cleaning device and cleaning method for filtration membrane module |
US7025885B2 (en) | 1998-11-23 | 2006-04-11 | Zenon Environmental Inc. | Water filtration using immersed membranes |
US8057574B2 (en) | 2003-07-08 | 2011-11-15 | Siemens Industry, Inc. | Membrane post treatment |
US8262778B2 (en) | 2003-07-08 | 2012-09-11 | Siemens Industry, Inc. | Membrane post treatment |
US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
US7247210B2 (en) | 2004-02-23 | 2007-07-24 | Ecolab Inc. | Methods for treating CIP equipment and equipment for treating CIP equipment |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
US7850853B2 (en) | 2005-03-09 | 2010-12-14 | Zhejiang Environmental Engineering Company Limited | Floating porous hollow fiber membrane bundle |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US8894858B1 (en) | 2005-08-22 | 2014-11-25 | Evoqua Water Technologies Llc | Method and assembly for water filtration using a tube manifold to minimize backwash |
WO2007040035A1 (en) * | 2005-09-30 | 2007-04-12 | Kureha Corporation | Hollow fiber bundle, process for producing hollow fiber bundle, tubular hollow fiber membrane module and immersion type hollow fiber membrane module |
WO2007040036A1 (en) * | 2005-09-30 | 2007-04-12 | Kureha Corporation | Hollow fiber bamboo-blind-like article, process for producing hollow fiber bundle, tubular hollow fiber membrane module and immersion type hollow fiber membrane module |
JPWO2007040035A1 (en) * | 2005-09-30 | 2009-04-16 | 株式会社クレハ | Hollow fiber bundle, method for producing hollow fiber bundle, cylindrical hollow fiber membrane module, and immersion hollow fiber membrane module |
JP2007090309A (en) * | 2005-09-30 | 2007-04-12 | Kureha Corp | Hollow fiber bundle, method for producing the same, tubular hollow fiber membrane module, and immersion type hollow fiber membrane module |
JP2007144349A (en) * | 2005-11-29 | 2007-06-14 | Ebara Corp | Hollow fiber membrane module |
US8293098B2 (en) | 2006-10-24 | 2012-10-23 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8318028B2 (en) | 2007-04-02 | 2012-11-27 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
US8372276B2 (en) | 2007-05-29 | 2013-02-12 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
US8840783B2 (en) | 2007-05-29 | 2014-09-23 | Evoqua Water Technologies Llc | Water treatment membrane cleaning with pulsed airlift pump |
US8287743B2 (en) | 2007-05-29 | 2012-10-16 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
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US9573824B2 (en) | 2007-05-29 | 2017-02-21 | Evoqua Water Technologies Llc | Membrane cleaning with pulsed airlift pump |
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US8956464B2 (en) | 2009-06-11 | 2015-02-17 | Evoqua Water Technologies Llc | Method of cleaning membranes |
US10441920B2 (en) | 2010-04-30 | 2019-10-15 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US9914097B2 (en) | 2010-04-30 | 2018-03-13 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US8173018B2 (en) | 2010-08-25 | 2012-05-08 | Dow Global Technologies Llc | Fluid filter module including sealed boss |
US9022224B2 (en) | 2010-09-24 | 2015-05-05 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
US9630147B2 (en) | 2010-09-24 | 2017-04-25 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
US10391432B2 (en) | 2011-09-30 | 2019-08-27 | Evoqua Water Technologies Llc | Manifold arrangement |
US11065569B2 (en) | 2011-09-30 | 2021-07-20 | Rohm And Haas Electronic Materials Singapore Pte. Ltd. | Manifold arrangement |
US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US9925499B2 (en) | 2011-09-30 | 2018-03-27 | Evoqua Water Technologies Llc | Isolation valve with seal for end cap of a filtration system |
US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
US9868834B2 (en) | 2012-09-14 | 2018-01-16 | Evoqua Water Technologies Llc | Polymer blend for membranes |
US9962865B2 (en) | 2012-09-26 | 2018-05-08 | Evoqua Water Technologies Llc | Membrane potting methods |
US9764289B2 (en) | 2012-09-26 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane securement device |
US9815027B2 (en) | 2012-09-27 | 2017-11-14 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
US10427102B2 (en) | 2013-10-02 | 2019-10-01 | Evoqua Water Technologies Llc | Method and device for repairing a membrane filtration module |
US11173453B2 (en) | 2013-10-02 | 2021-11-16 | Rohm And Haas Electronic Materials Singapores | Method and device for repairing a membrane filtration module |
US10322375B2 (en) | 2015-07-14 | 2019-06-18 | Evoqua Water Technologies Llc | Aeration device for filtration system |
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