JPH08332357A - Method and apparatus for regenerating filter module - Google Patents

Method and apparatus for regenerating filter module

Info

Publication number
JPH08332357A
JPH08332357A JP7139448A JP13944895A JPH08332357A JP H08332357 A JPH08332357 A JP H08332357A JP 7139448 A JP7139448 A JP 7139448A JP 13944895 A JP13944895 A JP 13944895A JP H08332357 A JPH08332357 A JP H08332357A
Authority
JP
Japan
Prior art keywords
water
filter module
filter
module
backwash water
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
JP7139448A
Other languages
Japanese (ja)
Inventor
Tetsuya Miyamoto
鐡也 宮本
Yukio Hatano
征雄 畑野
Seiji Kawai
精二 川井
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP7139448A priority Critical patent/JPH08332357A/en
Publication of JPH08332357A publication Critical patent/JPH08332357A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To efficiently remove the deposit bonded to the filtering surfaces of hollow yarn membranes by appropriately changing over the supply and discharge of backwashing water to change the water level in a module along hollow yarn bundles. CONSTITUTION: The filtering operation of a filter module 1 is performed by supplying raw water to the partitioned space 5 of a cylindrical case 2 as shown by an arrow A to filter the same by semipermeable hollow yarn bundles 3 and allowing the filtered water to flow out toward the upper surface of a partition wall as shown by an arrow B. A vibrator 8 is horizontally moved, for example, in amplitude of 5cm at 150 cycles/min and a filter to be regenerated is fixed to this vibration part so that a raw water supply port at a time of filtering becomes an upper side and a washing water discharge pipe 9 is connected to the filter and a backwashing water supply pipe 10 is connected to the transmitted water outlet at the time of filtering. An opening and closing valve 12 is provided to the backwashing water supply pipe 10. A backwashing water drain pipe 11 is provided between a filter connection port and the opening and closing valve 12 as a branch pipe and an opening and closing valve 13 is provided to the backwashing water drain pipe 11.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は透水性の中空糸膜を利用
した濾過器モジュールの中空糸膜濾過面に付着した堆積
物を除去する濾過器モジュールの再生方法及び装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for regenerating a filter module for removing deposits adhering to the filtration surface of a hollow fiber membrane of a filter module using a water permeable hollow fiber membrane.

【0002】[0002]

【従来の技術】中空糸膜を用いて濾過する場合に、中空
糸膜によって阻止された微粒子が濾過面に付着し目詰ま
りを起こし透過流束が低下してくる問題がある。このた
め、濾過面に付着した堆積物を除去する方法として定期
的に濾膜の二次側から水や空気または炭酸ガス飽和水を
圧送する逆洗や、超音波や空気泡により濾過面を振動さ
せて付着した堆積物を剥離する方法が行われているが、
一様に付着物を除去できないという問題があった。この
ため、洗浄しても濾過能力の回復率が低く、使用時間が
短かくなるという欠点があった。
2. Description of the Related Art When a hollow fiber membrane is used for filtration, there is a problem that fine particles blocked by the hollow fiber membrane adhere to the filtration surface to cause clogging and reduce the permeation flux. Therefore, as a method of removing deposits adhering to the filtration surface, backwashing is performed by periodically pumping water, air or carbon dioxide saturated water from the secondary side of the filtration membrane, or the filtration surface is vibrated by ultrasonic waves or air bubbles. There is a method to remove the deposited deposits by
There is a problem in that the deposits cannot be removed uniformly. For this reason, there is a drawback that the recovery rate of the filtering ability is low even after washing and the use time is short.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は中空糸
膜の濾過面に付着した堆積物を効率よく除去する濾過器
モジュールの再生方法および装置を提供することにあ
る。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method and an apparatus for regenerating a filter module for efficiently removing deposits adhering to the filtration surface of a hollow fiber membrane.

【0004】[0004]

【課題を解決するための手段】上記目的を達成する本発
明は、中空糸膜利用の濾過器モジュールに機械的な振動
を与えつつ、該濾過器モジュールに逆洗水を流してモジ
ュール内の水を揺動し、濾過面に付着した堆積物を剥離
させ、系外に流出させるに際し、逆洗水の給排水を適宜
切り換えて、モジュール内の水位を中空糸束に沿って変
化させることを特徴とする濾過器モジュールの再生方法
である。
Means for Solving the Problems The present invention which achieves the above object is to provide a backwash water to the filter module using hollow fiber membranes while mechanically vibrating the filter module so that the water in the module is filtered. When the water is shaken to separate the deposits adhering to the filtration surface and flow out to the outside of the system, the water level in the module is changed along the hollow fiber bundle by appropriately switching the water supply and drainage of the backwash water. It is a method of regenerating the filter module.

【0005】なお、付着した堆積物が容易に剥離し難い
ときには、洗浄効果を高めるために、逆洗水に塩酸、ク
エン酸、蓚酸、次亜塩素酸、合成洗剤の水溶液を単独ま
たは混合して使用してもよく、また前処理としてそれら
の単独または混合した水溶液に浸漬した後上記方法を行
ってもよい。
When it is difficult to easily remove the deposited deposits, in order to enhance the cleaning effect, an aqueous solution of hydrochloric acid, citric acid, oxalic acid, hypochlorous acid, or synthetic detergent may be used alone or mixed in backwash water. They may be used, or as a pretreatment, the above method may be carried out after immersing them in an aqueous solution of them or a mixture thereof.

【0006】次に本発明の濾過器モジュールの再生装置
は、機械的な振動を与える振動装置に中空糸膜利用の濾
過器モジュールを係合せしめるとともに、該モジュール
に逆洗水を供給する逆洗水供給管と、モジュールを通過
した洗浄水を系外に排出させるための洗浄水排出管と、
前記逆洗水供給管から濾過器モジュールに至る逆洗水を
系外に排出する逆洗水排出管とを設け、さらに、これら
逆洗水供給管と逆洗水排出管との間で逆洗水の給排水を
任意に切り換えできる開閉弁を設けたことを特徴とする
ものである。
Next, in the regenerating apparatus for a filter module of the present invention, a filter module using a hollow fiber membrane is engaged with an oscillating device for giving mechanical vibration, and backwashing water for supplying backwashing water to the module is engaged. A water supply pipe and a wash water discharge pipe for discharging wash water that has passed through the module to the outside of the system,
A backwash water discharge pipe for discharging the backwash water from the backwash water supply pipe to the filter module to the outside of the system is provided, and further backwash water is provided between the backwash water supply pipe and the backwash water discharge pipe. It is characterized by being provided with an on-off valve capable of arbitrarily switching water supply / drainage.

【0007】すなわち、本発明は、上記の如く目詰まり
したモジュールに逆洗水を流し、外部より機械的振動を
与えてモジュール内の水を揺動し濾過面に付着した堆積
物を剥離させ、または、外部より機械的水平振動を与え
ながら逆洗水の給排水を適宜切り換えて、モジュール内
の水位を中空糸束に沿って上下に変化させることで濾過
面に付着した堆積物を剥離させることを特徴とするもの
である。
That is, according to the present invention, the backwashing water is flown through the clogged module as described above, and mechanical vibration is externally applied to rock the water in the module to remove the deposits adhering to the filtration surface. Alternatively, it is possible to separate the deposits adhering to the filtration surface by changing the water level in the module up and down along the hollow fiber bundle by appropriately switching the water supply and drainage of the backwash water while applying mechanical horizontal vibration from the outside. It is a feature.

【0008】[0008]

【実施例】以下に具体例をあげて本発明を説明するが、
発明の趣旨を越えない限り本発明は実施例に限定される
ものではない。
The present invention will be described below with reference to specific examples.
The present invention is not limited to the examples as long as the gist of the invention is not exceeded.

【0009】図1は、本発明の中空糸膜利用の濾過器モ
ジュール再生装置の一実施例を示す斜視図である。
FIG. 1 is a perspective view showing an embodiment of a filter module regenerating apparatus using a hollow fiber membrane of the present invention.

【0010】図2は、本発明の実施例に適用した濾過器
モジュールの一例を示す縦断面図である。
FIG. 2 is a vertical sectional view showing an example of a filter module applied to the embodiment of the present invention.

【0011】図3は、本発明の実施例に適用した濾過器
の一例を示す縦断面図である。
FIG. 3 is a vertical sectional view showing an example of a filter applied to the embodiment of the present invention.

【0012】図2における濾過器モジュール1は、円筒
状のケース2、半透膜からなる中空糸束3、熱硬化性樹
脂から成型された仕切り壁4からなる。
The filter module 1 in FIG. 2 comprises a cylindrical case 2, a hollow fiber bundle 3 made of a semipermeable membrane, and a partition wall 4 molded from a thermosetting resin.

【0013】筒状のケース1は内部が仕切り壁4で仕切
られ、片側に原水供給用の仕切り空間5を形成してい
る。この仕切り空間5に中空糸束3がU字状に折り曲げ
て収納され、かつその両端部を仕切り壁4に対して中空
部が反対側壁面に開口するように設けられ、仕切り空間
5内部と仕切り壁4の上面側とを連通している。
The inside of the cylindrical case 1 is partitioned by a partition wall 4, and a partition space 5 for supplying raw water is formed on one side. The hollow fiber bundle 3 is folded in a U shape and stored in the partition space 5, and both ends of the hollow fiber bundle 3 are provided so that the hollow portion opens to the opposite side wall surface with respect to the partition wall 4. It communicates with the upper surface side of the wall 4.

【0014】なお、上記モジュールにおいて中空糸束の
一方の端部を閉塞するようにした濾過器モジュールであ
ってもよい。
The above module may be a filter module in which one end of the hollow fiber bundle is closed.

【0015】上記構成からなる濾過器モジュール1にお
ける濾過操作は、原水が矢印Aのように筒状のケース2
の仕切り空間5に供給され、それが半透膜の中空糸束3
で濾過されて仕切り壁4の上面側に矢印Bのように流出
するように行われる。
In the filtering operation in the filter module 1 having the above structure, the raw water is in the cylindrical case 2 as shown by the arrow A.
Is supplied to the partition space 5 of the hollow fiber bundle 3 of the semipermeable membrane.
It is filtered so as to flow out to the upper surface side of the partition wall 4 as indicated by arrow B.

【0016】図3は複数本の濾過器モジュール1を一対
のコネクタ6,7によって並列的に接続された濾過器で
ある。原水が矢印Aより供給され、透過水が矢印Bから
流出するようになっている。
FIG. 3 shows a filter in which a plurality of filter modules 1 are connected in parallel by a pair of connectors 6 and 7. Raw water is supplied from the arrow A, and permeated water flows out from the arrow B.

【0017】次に本発明の再生方法および再生装置を図
1に基づいて説明すると、図1において、8は振動装置
であって、この振動装置は、例えば振幅5cm、1分間1
50サイクルの水平動をする振動器であって、この振動
部分に、再生しようとする例えば図3に示す濾過器を、
濾過時の原水供給口が上側になるように固定し、これに
洗浄水排出管9を接続するとともに濾過時の透過水出口
に逆洗水供給管10を接続する。この逆洗水供給管10
には開閉弁12が設けられている。一方、濾過器接続口
と開閉弁12の間に枝管として逆洗水排出管11が設け
られており、逆洗水排出管11には開閉弁13が設けら
れている。
Next, a reproducing method and a reproducing apparatus of the present invention will be described with reference to FIG. 1. In FIG. 1, reference numeral 8 is a vibrating device, and the vibrating device has, for example, an amplitude of 5 cm and a period of 1 minute.
A vibrating device that horizontally moves for 50 cycles, and a filter to be regenerated, for example, a filter shown in FIG.
The raw water supply port at the time of filtration is fixed so that the washing water discharge pipe 9 is connected to this, and the backwash water supply pipe 10 is connected to the permeate outlet at the time of filtration. This backwash water supply pipe 10
An on-off valve 12 is provided in the. On the other hand, a backwash water discharge pipe 11 is provided as a branch pipe between the filter connection port and the open / close valve 12, and the backwash water discharge pipe 11 is provided with an open / close valve 13.

【0018】逆洗水は、逆洗水供給管10から開閉弁1
2を通って濾過器に送られ、中空糸の内側から外側へ通
過して洗浄水排出管9から排水される。このとき開閉弁
12は開、開閉弁13は閉である。開閉弁12が閉にな
り、逆洗水の供給が止まると開閉弁13は開となり、水
頭差により洗浄水排出管9から空気が導入されて濾過器
モジュールの仕切空間5の逆洗水は中空糸の外側から内
側へ通過して逆洗水排出管11から排出される。開閉弁
12,13は連動し、この操作が繰返される。逆洗水の
給排水時間は付着物の状態に応じて適宜設定し、洗浄排
水が濁らなくなるまで洗浄を続ける。
The backwash water is supplied from the backwash water supply pipe 10 to the opening / closing valve 1.
It is sent to the filter through 2 and is passed from the inside to the outside of the hollow fiber to be discharged from the wash water discharge pipe 9. At this time, the open / close valve 12 is open and the open / close valve 13 is closed. When the on-off valve 12 is closed and the supply of backwash water is stopped, the on-off valve 13 is opened, air is introduced from the wash water discharge pipe 9 due to the head difference, and the backwash water in the partition space 5 of the filter module is hollow. The yarn passes from the outside to the inside and is discharged from the backwash water discharge pipe 11. The on-off valves 12 and 13 are interlocked, and this operation is repeated. The time for supplying and draining the backwash water is appropriately set according to the state of the adhered substances, and the washing is continued until the wash drainage does not become turbid.

【0019】具体的にプール水浄化に用いたモジュール
の付着物は、エステル化合物、アミド化合物などの有機
物質とケイ酸塩、鉄分などの無機物質の混合物であり、
堅固に付着しているため通常の逆洗では除去され難い
が、本発明の再生方法によると、濾過能力の回復は一段
と効果的である。
Specifically, the deposits of the module used for purifying the pool water are a mixture of organic substances such as ester compounds and amide compounds and inorganic substances such as silicates and iron,
Since it adheres firmly, it is difficult to remove it by normal backwashing, but according to the regeneration method of the present invention, the recovery of the filtering ability is more effective.

【0020】以下、具体例に基づいて本発明を説明す
る。
The present invention will be described below based on specific examples.

【0021】目詰まりしたモジュールをクエン酸溶液に
浸漬し、鉄分を十分溶解した後、クエン酸溶液を排除し
て、次に合成洗剤の水溶液に浸漬した後、本発明の濾過
器モジュールに適用した。モジュール8本からなる濾過
器を振動機にセットし、逆洗水圧50KPa(0.5k
gf/cm2 )、逆洗水の給水時間90秒、給水停止時
間(排出時間)30秒、振幅5cm、1分間150サイ
クルの水平振動で1時間洗浄した。
The clogged module was immersed in a citric acid solution to sufficiently dissolve iron, the citric acid solution was removed, and then the module was immersed in an aqueous solution of a synthetic detergent and then applied to the filter module of the present invention. . A filter consisting of eight modules was set on a vibrator, and the backwash water pressure was 50 KPa (0.5 k
gf / cm 2 ), water supply time of backwash water 90 seconds, water supply stop time (drainage time) 30 seconds, amplitude 5 cm, 1 minute by horizontal vibration of 150 cycles for 1 hour.

【0022】再生による濾過能力の回復率は、水頭圧5
0cmにおける膜濾過水量を測定し、新膜の濾過水量に
対する比で表した。上述の条件で洗浄したときと、同時
間逆洗水の給水のみで洗浄したときと、同時間洗浄しな
いで逆洗水の給排水のみで洗浄したときの濾過能力の回
復率を比較した。モジュール間の差はあるが、逆洗の方
法によって、およそ次のような回復率の差が確認され
た。
The recovery rate of the filtration capacity due to regeneration is the head pressure of 5
The membrane filtered water amount at 0 cm was measured and expressed as a ratio to the filtered water amount of the new membrane. The recovery rate of the filtration performance was compared between the case of washing under the above-mentioned conditions, the case of washing only with backwash water for the same time, and the case of washing with only water supply / drainage of backwash without washing for the same time. Although there are differences between the modules, the following differences in recovery rates were confirmed by the backwash method.

【0023】 振動と逆洗水の給排水を行なった場合 回復率 85〜95% 振動と逆洗水の給水のみ行なった場合 回復率 45〜55% 逆洗水の給排水のみ行なった場合 回復率 40〜50% また、水道水を濾過した目詰まりモジュールの例では、
50℃、4%塩酸溶液に20分間浸漬した後、振動と逆
洗水の給排水を行なった場合と、振動と逆洗水の給水の
み行なった場合を比較したが、20分間洗浄で共に回復
率は95〜100%であった。
When vibration and water supply / drainage of backwash water are performed Recovery rate 85-95% When only water supply of vibration and backwash water is performed Recovery rate 45-55% When water supply / drainage of backwash water is performed Recovery rate 40- 50% Moreover, in the example of the clogging module which filtered tap water,
After immersing in 50% 4% hydrochloric acid solution for 20 minutes, vibration and backwash water supply and drainage were compared with vibration and backwash water supply only. Was 95-100%.

【0024】[0024]

【発明の効果】以上のように、この発明の濾過器モジュ
ールの再生方法および装置は、目詰り状態や付着した堆
積物の性質により適切な逆洗条件を選択することで通常
の逆洗では除去され難い付着物も除去することができ、
再使用にほとんど支承のないところまで濾過能力を回復
させることができた。また、濾過器モジュールの再使用
で濾過コストを低減することができた。
As described above, in the method and apparatus for regenerating the filter module of the present invention, the appropriate backwashing conditions are selected depending on the clogging condition and the nature of the deposited deposits, so that the normal backwashing can remove them. It is possible to remove deposits that are difficult to remove,
It was possible to restore the filtration capacity to the point where it had almost no bearing for reuse. In addition, the filtration cost could be reduced by reusing the filter module.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の中空糸膜利用の濾過器モジュール再生
装置の一実施例を示す斜視図である。
FIG. 1 is a perspective view showing an embodiment of a filter module regenerating apparatus using a hollow fiber membrane of the present invention.

【図2】本発明の実施例に適用した濾過器モジュールの
一例を示す縦断面図である。
FIG. 2 is a vertical sectional view showing an example of a filter module applied to an embodiment of the present invention.

【図3】本発明の実施例に適用した濾過器の一例を示す
縦断面図である。
FIG. 3 is a vertical sectional view showing an example of a filter applied to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 濾過器モジュール 2 筒状ケース 3 中空糸束 4 仕切壁 5 仕切空間 6,7 コネクター 8 振動機 9 洗浄水排出管 10 逆洗水供給管 11 逆洗水排出管 12,13 開閉弁 1 Filter Module 2 Cylindrical Case 3 Hollow Fiber Bundle 4 Partition Wall 5 Partition Space 6, 7 Connector 8 Vibration Machine 9 Wash Water Discharge Pipe 10 Backwash Water Supply Pipe 11 Backwash Water Discharge Pipe 12, 13 Open / close Valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】中空糸膜利用の濾過器モジュールに機械的
な振動を与えつつ、該濾過器モジュールに逆洗水を流し
てモジュール内の水を揺動し、濾過面に付着した堆積物
を剥離させ、系外に流出させるに際し、逆洗水の給排水
を適宜切り換えて、モジュール内の水位を中空糸束に沿
って変化させることを特徴とする濾過器モジュールの再
生方法。
Claim: What is claimed is: 1. While mechanically vibrating a filter module using a hollow fiber membrane, backwash water is flown through the filter module to rock the water in the module to remove deposits adhering to the filtration surface. A method of regenerating a filter module, wherein the water level in the module is changed along the hollow fiber bundle by appropriately switching the water supply and drainage of the backwash water when peeling and flowing out of the system.
【請求項2】前記逆洗水に塩酸、クエン酸、蓚酸、次亜
塩素酸、合成洗剤の少なくとも1種を含ませたことを特
徴とする請求項1に記載の濾過器モジュールの再生方
法。
2. The method for regenerating a filter module according to claim 1, wherein the backwash water contains at least one of hydrochloric acid, citric acid, oxalic acid, hypochlorous acid, and a synthetic detergent.
【請求項3】機械的な振動を与える振動装置に中空糸膜
利用の濾過器モジュールを係合せしめるとともに、該モ
ジュールに、逆洗水を供給する逆洗水供給管と、モジュ
ールを通過した洗浄水を系外に排出させるための洗浄水
排出管と、前記逆洗水供給管から濾過器モジュールに至
る逆洗水を系外に排出する逆洗水排出管とを設け、さら
に、これら逆洗水供給管と逆洗水排出管との間で逆洗水
の給排水を任意に切り換えできる開閉弁を設けたことを
特徴とする濾過器モジュールの再生装置。
3. A backwash water supply pipe for supplying backwash water to the module while engaging a filter module using a hollow fiber membrane with a vibrating device for giving a mechanical vibration, and a washing which has passed through the module. A wash water discharge pipe for discharging water to the outside of the system and a backwash water discharge pipe for discharging the backwash water from the backwash water supply pipe to the filter module to the outside of the system are provided, and further, these backwash waters are provided. A regeneration device for a filter module, which is provided with an opening / closing valve capable of arbitrarily switching the supply and drainage of the backwash water between the water supply pipe and the backwash water discharge pipe.
JP7139448A 1995-06-06 1995-06-06 Method and apparatus for regenerating filter module Pending JPH08332357A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7139448A JPH08332357A (en) 1995-06-06 1995-06-06 Method and apparatus for regenerating filter module

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Application Number Priority Date Filing Date Title
JP7139448A JPH08332357A (en) 1995-06-06 1995-06-06 Method and apparatus for regenerating filter module

Publications (1)

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JPH08332357A true JPH08332357A (en) 1996-12-17

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JP7139448A Pending JPH08332357A (en) 1995-06-06 1995-06-06 Method and apparatus for regenerating filter module

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JP (1) JPH08332357A (en)

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JP2000005780A (en) * 1998-06-24 2000-01-11 Kantou Regional Constr Bureau Ministry Of Constr River purifying method using membrane
US6319411B1 (en) 1998-10-09 2001-11-20 Zenon Environmental Inc. Method of maintaining clean vertical skeins of hollow fiber membranes and system therefor
WO2006074519A1 (en) 2005-01-14 2006-07-20 Siemens Water Technologies Corp. Filtration system
US20130092618A1 (en) * 2011-10-13 2013-04-18 Sumitomo Electric Industries, Ltd. Separation membrane, water treatment unit and water treatment apparatus
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
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
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US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US9764289B2 (en) 2012-09-26 2017-09-19 Evoqua Water Technologies Llc Membrane securement device
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
US9815027B2 (en) 2012-09-27 2017-11-14 Evoqua Water Technologies Llc Gas scouring apparatus for immersed membranes
US9914097B2 (en) 2010-04-30 2018-03-13 Evoqua Water Technologies Llc Fluid flow distribution device
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JPH038419A (en) * 1989-03-02 1991-01-16 Yamada Mekki Kogyosho:Kk Method for preventing clogging of filter membrane of liquid filter device and liquid filter device
JPH05184884A (en) * 1992-01-08 1993-07-27 Mitsubishi Rayon Co Ltd Method for backwashing hollow fiber membrane module
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JPS62262710A (en) * 1986-05-09 1987-11-14 Toshiba Corp Hollow yarn membrane filter
JPH02164423A (en) * 1988-12-20 1990-06-25 Toshiba Corp Method for washing hollow fiber membrane filter
JPH038419A (en) * 1989-03-02 1991-01-16 Yamada Mekki Kogyosho:Kk Method for preventing clogging of filter membrane of liquid filter device and liquid filter device
JPH05184884A (en) * 1992-01-08 1993-07-27 Mitsubishi Rayon Co Ltd Method for backwashing hollow fiber membrane module
JPH06277664A (en) * 1993-01-29 1994-10-04 Daicel Chem Ind Ltd Method and apparatus for clarifying surface flowing water with membrane

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JP2000005780A (en) * 1998-06-24 2000-01-11 Kantou Regional Constr Bureau Ministry Of Constr River purifying method using membrane
US6319411B1 (en) 1998-10-09 2001-11-20 Zenon Environmental Inc. Method of maintaining clean vertical skeins of hollow fiber membranes and system therefor
WO2006074519A1 (en) 2005-01-14 2006-07-20 Siemens Water Technologies Corp. Filtration system
JP2008526497A (en) * 2005-01-14 2008-07-24 シーメンス・ウォーター・テクノロジーズ・コーポレーション Filtration system
AU2006206046B2 (en) * 2005-01-14 2010-10-28 Evoqua Water Technologies Llc Filtration system
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
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
US9573824B2 (en) 2007-05-29 2017-02-21 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9206057B2 (en) 2007-05-29 2015-12-08 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US10507431B2 (en) 2007-05-29 2019-12-17 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
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
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US9630147B2 (en) 2010-09-24 2017-04-25 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
US11065569B2 (en) 2011-09-30 2021-07-20 Rohm And Haas Electronic Materials Singapore Pte. Ltd. Manifold arrangement
US20130092618A1 (en) * 2011-10-13 2013-04-18 Sumitomo Electric Industries, Ltd. Separation membrane, water treatment unit and water treatment apparatus
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
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