JPS61263605A - Hollow yarn membrane device - Google Patents

Hollow yarn membrane device

Info

Publication number
JPS61263605A
JPS61263605A JP10391185A JP10391185A JPS61263605A JP S61263605 A JPS61263605 A JP S61263605A JP 10391185 A JP10391185 A JP 10391185A JP 10391185 A JP10391185 A JP 10391185A JP S61263605 A JPS61263605 A JP S61263605A
Authority
JP
Japan
Prior art keywords
support
hollow fiber
fiber membrane
hollow yarn
yarn membrane
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
Application number
JP10391185A
Other languages
Japanese (ja)
Inventor
Shinichi Ishisato
新一 石里
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP10391185A priority Critical patent/JPS61263605A/en
Publication of JPS61263605A publication Critical patent/JPS61263605A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To prevent the bending fatigue and entanglement of a hollow yarn membrane and to prolong the life of a hollow yarn membrane module by providing a support for supporting the hollow yarn membrane module consisting of a combustible material. CONSTITUTION:Plural hollow yarn membrane modules 8 are hung in a vessel 1 and a support 9 is attached on the outside of the module. A semicircular supporting part 10 is provided at the lower part of the support 9. The entanglement of the modules with each other is prevented by the support 9 and the whirling up of the module during backwashing is controlled by the semicircular supporting part 10. The support 9 can be burned along with the hollow yarn membrane by forming the support with the same material as that of the hollow yarn membrane and the output of wastes can be reduced.

Description

【発明の詳細な説明】 [発明の技術分野] 本発明はろ過装置It(ユ使用される中空糸膜装置C;
関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to a filtration device It (a hollow fiber membrane device C used in the filtration device It);
related.

[発明の技術的背景とその問題点] たとえば原子力発電プラントで発生する放射性廃液のろ
過装置としては、現在限界ろ過や1μm孔径の平膜によ
るろ過方式が採用されている。
[Technical background of the invention and its problems] For example, as a filtering device for radioactive waste liquid generated in a nuclear power plant, ultrafiltration or a filtration method using a flat membrane with a pore diameter of 1 μm is currently employed.

一方、限界ろ過は不溶解性不純物(クラッド)と比較し
て、孔径が小さい九め透過水量が少なく、したがって所
要ろ過面積が大きくなり、かつ高流量の循環流量及び高
ろ過圧力が必要となる。このため、装置が複雑となり、
設備費・所要スペースが大きくなる。
On the other hand, in ultrafiltration, compared to insoluble impurities (crud), the amount of permeated water is small due to the small pore size, so the required filtration area is large, and a high circulating flow rate and high filtration pressure are required. This makes the device complex and
Equipment costs and space requirements increase.

又、1μm前後の孔径の平膜I:よるろ過装置C二おい
ては廃液中ε:l−1.am以下の固形分が多いため、
目詰りが多くなり膜の交換頻度が増大する。
In addition, in the filtration device C2 using a flat membrane I with a pore size of around 1 μm, ε: l-1. Because it has a high solid content below am,
Clogging increases and the frequency of membrane replacement increases.

このため、少ないスペースでろ過面積を大きくとること
ができ、放射性廃液のろ過処理を効果的61行なえる中
空糸膜ろ過装置が用いられる。
For this reason, a hollow fiber membrane filtration device is used, which can provide a large filtration area in a small space and can effectively filter radioactive waste liquid.

しかし、中9糸展ろ過装置は中空糸膜な数万本まとめた
モジュールを配置する構造であるため、剛性を有する膜
はハンドリング等で破損する恐れがあり、又弾性を有す
る膜は逆洗等−二より膜がからみつき、運転C:支障を
きたす恐れがある。
However, since the medium 9-thread filtration device has a structure in which tens of thousands of hollow fiber membrane modules are arranged, the rigid membranes may be damaged during handling, and the elastic membranes may be damaged due to backwashing. - The two membranes may become entangled, causing problems in operation C.

さらg:、これらの中空糸膜モジュールを多数設置する
場合シーは、モジュール相互間のからみ防止l:ついて
考慮しなければならず、モジュール間の距離を大きくと
る等の対策が必要となり装置が大塁化する。
Furthermore, when installing a large number of these hollow fiber membrane modules, consideration must be given to preventing entanglement between the modules, and measures such as increasing the distance between modules are required, resulting in a large equipment size. Become a base.

[発明の目的コ 本発明の目的は、上記事情C:鑑みてなされたもので、
その目的は、中空糸膜モジュールの寿命な延長させる中
空糸膜装置を提供することζ:ある。
[Object of the invention] The object of the present invention was made in view of the above-mentioned situation C.
The purpose is to provide a hollow fiber membrane device that extends the life of the hollow fiber membrane module.

[発明の概要] 本発明は、廃液の処理に用いらねる中空糸膜ろ過装量内
の中空糸膜装置C−関するもので、中空糸膜モジュール
と一体化した構造をもち、焼却可能な材料で製作するこ
とを特徴とする本のである。
[Summary of the Invention] The present invention relates to a hollow fiber membrane device C in a hollow fiber membrane filtration unit used for processing waste liquid, which has a structure integrated with a hollow fiber membrane module and is made of incinerated material. This book is characterized by the fact that it is produced by

[発明の実施例] 本発明の実施例を図面を参照して説明する。[Embodiments of the invention] Embodiments of the present invention will be described with reference to the drawings.

第1図は、本発明の一実施例を示す放射性廃液用中空糸
膜ろ過装置の概略図である。
FIG. 1 is a schematic diagram of a hollow fiber membrane filtration device for radioactive waste liquid showing one embodiment of the present invention.

第1図ζ二示すよう(二、容器1(ユは処理丁べき放射
性廃液が流入するノズル2.ろ液の出口であるノズル3
.逆洗水の出口であるノズル4.バブリング用空気の入
口であるノズル5.ベント用のノズル6、ドレン用のノ
ズル7が取付けられており、中空糸膜モジュール8が複
数個吊り下げられ、その外側Cユ支持具9が取付けられ
ている。
As shown in FIG.
.. Nozzle 4, which is the outlet of backwash water. Nozzle which is the inlet of air for bubbling 5. A vent nozzle 6 and a drain nozzle 7 are attached, a plurality of hollow fiber membrane modules 8 are suspended, and an outer C unit support 9 is attached.

第2図は、第1図C二おけるA部を拡大したもので、支
持具9は中空糸膜モジュールを囲むように取付けられて
いる。
FIG. 2 is an enlarged view of section A in FIG. 1 C2, in which the support 9 is attached so as to surround the hollow fiber membrane module.

又、支持具9の下部には半円状支持部IOが取り付けら
れている。
Further, a semicircular support portion IO is attached to the lower part of the support tool 9.

本実施例では、中空糸膜モジュール8の周囲の支持具9
にて他モジュールとのからみを防止し、下部の半円状支
持部10(ユより逆洗時等の中空糸膜の舞い上りを防止
している。
In this embodiment, a support 9 around the hollow fiber membrane module 8 is used.
This prevents entanglement with other modules, and prevents the hollow fiber membrane from flying up from the lower semicircular support part 10 (Y) during backwashing.

次Cユ本発明の他の実施例を第3図ないし第6図にて説
明する。
Next, another embodiment of the present invention will be described with reference to FIGS. 3 to 6.

第3図は、中空糸膜モジュール8の中央5−支持具9a
が取付けられた場合の側面図を示している。
FIG. 3 shows the center 5-support 9a of the hollow fiber membrane module 8.
A side view is shown when the is installed.

又、第4図は、第3図のAA断面図である。Further, FIG. 4 is a sectional view taken along line AA in FIG. 3.

本実施例では、中空糸膜モジユール中央に丸棒11を取
付は丸棒の先端のU字型11aにて中空糸膜の舞い上が
りを防止する構造となっている。
In this embodiment, a round rod 11 is attached to the center of the hollow fiber membrane module, and the structure is such that the U-shaped tip 11a of the round rod prevents the hollow fiber membrane from flying up.

第5図は、支持具12が中空糸膜13と同じ糸状の支持
体である場合の実施例を示している。
FIG. 5 shows an embodiment in which the support 12 is the same filamentous support as the hollow fiber membrane 13.

第6図は、第5図の中空糸膜モジュールの断面Bを拡大
した図である。
FIG. 6 is an enlarged view of cross section B of the hollow fiber membrane module in FIG. 5.

本実施例では、中空糸膜13数の数チ程度の糸状の支持
体を支持具12としてモジュール内に配置しており、こ
れCユより中空糸膜13の脚上がりゃ曲げ疲労等を減少
させることができる。
In this embodiment, a filament-like support of about several inches, the number of which is equal to the number of the hollow fiber membranes 13, is arranged in the module as a support 12, and this reduces bending fatigue, etc. when the legs of the hollow fiber membrane 13 rise from the C unit. be able to.

又、この支持具12をモジュールの外周部分(:集中的
C二装置すれば、他モジュールとのからみ防止をもかね
ることが可能となる。
Furthermore, if this support 12 is placed on the outer peripheral portion of the module (i.e., a concentrated C2 device), it is possible to prevent entanglement with other modules.

なお支持具を中空糸膜と同材料で製作すること(二より
モジュールと一体で焼却でき、廃棄物発生量を低減させ
ることができる。
Note that the support tool can be made of the same material as the hollow fiber membrane (it can be incinerated together with the second-strand module, reducing the amount of waste generated.

[発明の効果コ 以上述べたように、本発明C二よれば中空糸膜ろ過装置
を使用する場合C;発生する中空糸膜の曲は疲労、から
み等を防止でき、中空糸膜モジュールの寿命を延ばすこ
とが可能となる。
[Effects of the Invention] As described above, according to the present invention C2, when a hollow fiber membrane filtration device is used, bending of the hollow fiber membrane that occurs can prevent fatigue, entanglement, etc., and extend the life of the hollow fiber membrane module. It becomes possible to extend the

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の一実施例を示す放射性廃液用中空糸
膜ろ過装置の概略図、第2図は第1図のA部を拡大した
中空糸膜装置の概略図、纂3図は本発明の他の実施例の
側面図、第4図は第3図のA入断面図、第5図は本発明
の他の実施例を一部切欠いて示す斜視図、第6図は第5
図のB部の拡大図である。 1・・・容器     8・・・中空糸膜モジュール9
、10.11.12・・・支持具  13・・・中空糸
膜代理人 弁理士 則 近 憲 佑(ほか1名)第1図 第21!I A 第3図   第4図
Fig. 1 is a schematic diagram of a hollow fiber membrane filtration device for radioactive waste liquid showing an embodiment of the present invention, Fig. 2 is a schematic diagram of the hollow fiber membrane filtration device with section A in Fig. FIG. 4 is a side view of another embodiment of the present invention, FIG. 4 is a sectional view taken along A in FIG. 3, FIG.
It is an enlarged view of part B of the figure. 1... Container 8... Hollow fiber membrane module 9
, 10.11.12...Support 13...Hollow fiber membrane agent Patent attorney Noriyuki Chika (and 1 other person) Figure 1 Figure 21! I A Figure 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] (1)中空糸膜モジュールと、この中空糸膜モジュール
を支持し焼却可能な材質よりなる支持具とを具備した中
空糸膜装置。
(1) A hollow fiber membrane device comprising a hollow fiber membrane module and a supporting tool made of a material that supports the hollow fiber membrane module and can be incinerated.
JP10391185A 1985-05-17 1985-05-17 Hollow yarn membrane device Pending JPS61263605A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10391185A JPS61263605A (en) 1985-05-17 1985-05-17 Hollow yarn membrane device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10391185A JPS61263605A (en) 1985-05-17 1985-05-17 Hollow yarn membrane device

Publications (1)

Publication Number Publication Date
JPS61263605A true JPS61263605A (en) 1986-11-21

Family

ID=14366608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10391185A Pending JPS61263605A (en) 1985-05-17 1985-05-17 Hollow yarn membrane device

Country Status (1)

Country Link
JP (1) JPS61263605A (en)

Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1272262A1 (en) * 2000-04-10 2003-01-08 U.S. Filter Wastewater Group, Inc. Hollow fibre restraining system
WO2005105273A1 (en) * 2004-04-02 2005-11-10 Koch Membrane Systems Gmbh Hollow fiber membrane filter with a supporting structure
US7025885B2 (en) 1998-11-23 2006-04-11 Zenon Environmental Inc. Water filtration using immersed membranes
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. 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
USRE39294E1 (en) 1995-08-11 2006-09-19 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
JP2007021498A (en) * 2000-10-09 2007-02-01 Us Filter Wastewater Group Inc Improved membrane filtration system
US8057574B2 (en) 2003-07-08 2011-11-15 Siemens Industry, Inc. Membrane post treatment
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
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
CN104332209A (en) * 2014-09-05 2015-02-04 上海华畅环保设备发展有限公司 Waste liquid processing system radiating waste liquid whirl separating purifying method and device
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
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
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
US9962865B2 (en) 2012-09-26 2018-05-08 Evoqua Water Technologies Llc Membrane potting methods
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system
US10427102B2 (en) 2013-10-02 2019-10-01 Evoqua Water Technologies Llc Method and device for repairing a membrane filtration module

Cited By (54)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7615157B2 (en) 1995-08-11 2009-11-10 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
USRE42669E1 (en) 1995-08-11 2011-09-06 Zenon Technology Partnership Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
US8075776B2 (en) 1995-08-11 2011-12-13 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre 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
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. 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
USRE39294E1 (en) 1995-08-11 2006-09-19 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US7025885B2 (en) 1998-11-23 2006-04-11 Zenon Environmental Inc. Water filtration using immersed membranes
EP1272262A1 (en) * 2000-04-10 2003-01-08 U.S. Filter Wastewater Group, Inc. Hollow fibre restraining system
JP2003530206A (en) * 2000-04-10 2003-10-14 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 Hollow fiber holding device
EP1272262A4 (en) * 2000-04-10 2003-05-28 Us Filter Wastewater Group Inc Hollow fibre restraining system
JP4808897B2 (en) * 2000-04-10 2011-11-02 シーメンス・ウォーター・テクノロジーズ・コーポレイション Hollow fiber holding device
US6783008B2 (en) 2000-04-10 2004-08-31 U.S. Filter Wastewater Group, Inc. Hollow fibre restraining system
JP2007021498A (en) * 2000-10-09 2007-02-01 Us Filter Wastewater Group Inc Improved membrane filtration system
JP4617285B2 (en) * 2000-10-09 2011-01-19 シーメンス・ウォーター・テクノロジーズ・コーポレイション Improved membrane filtration system
US8262778B2 (en) 2003-07-08 2012-09-11 Siemens Industry, Inc. Membrane post treatment
US8057574B2 (en) 2003-07-08 2011-11-15 Siemens Industry, Inc. Membrane post treatment
US8268176B2 (en) 2003-08-29 2012-09-18 Siemens Industry, Inc. Backwash
US7531091B2 (en) 2004-04-02 2009-05-12 Koch Membrane Systems Gmbh Hollow fiber membrane filter with a supporting structure
WO2005105273A1 (en) * 2004-04-02 2005-11-10 Koch Membrane Systems Gmbh Hollow fiber membrane filter with a supporting structure
US8377305B2 (en) 2004-09-15 2013-02-19 Siemens Industry, Inc. Continuously variable aeration
US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
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
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
US8287743B2 (en) 2007-05-29 2012-10-16 Siemens Industry, Inc. Membrane cleaning with pulsed airlift pump
US10507431B2 (en) 2007-05-29 2019-12-17 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
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
US9206057B2 (en) 2007-05-29 2015-12-08 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9573824B2 (en) 2007-05-29 2017-02-21 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US8382981B2 (en) 2008-07-24 2013-02-26 Siemens Industry, Inc. Frame system for membrane filtration modules
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US9914097B2 (en) 2010-04-30 2018-03-13 Evoqua Water Technologies Llc Fluid flow distribution device
US10441920B2 (en) 2010-04-30 2019-10-15 Evoqua Water Technologies Llc Fluid flow distribution device
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
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
US10391432B2 (en) 2011-09-30 2019-08-27 Evoqua Water Technologies Llc Manifold arrangement
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
US11173453B2 (en) 2013-10-02 2021-11-16 Rohm And Haas Electronic Materials Singapores Method and device for repairing a membrane filtration module
US10427102B2 (en) 2013-10-02 2019-10-01 Evoqua Water Technologies Llc Method and device for repairing a membrane filtration module
CN104332209A (en) * 2014-09-05 2015-02-04 上海华畅环保设备发展有限公司 Waste liquid processing system radiating waste liquid whirl separating purifying method and device
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system

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