JPH07185271A - Immersion membrane apparatus - Google Patents

Immersion membrane apparatus

Info

Publication number
JPH07185271A
JPH07185271A JP34595793A JP34595793A JPH07185271A JP H07185271 A JPH07185271 A JP H07185271A JP 34595793 A JP34595793 A JP 34595793A JP 34595793 A JP34595793 A JP 34595793A JP H07185271 A JPH07185271 A JP H07185271A
Authority
JP
Japan
Prior art keywords
membrane
liquid
units
membranes
membrane unit
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.)
Granted
Application number
JP34595793A
Other languages
Japanese (ja)
Other versions
JP3341428B2 (en
Inventor
Kazuo Imai
和夫 今井
Shigeki Sawada
繁樹 沢田
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP34595793A priority Critical patent/JP3341428B2/en
Publication of JPH07185271A publication Critical patent/JPH07185271A/en
Application granted granted Critical
Publication of JP3341428B2 publication Critical patent/JP3341428B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To effectively peel the non-filterable substance bonded to a membrane surface. CONSTITUTION:In an immersion membrane apparatus wherein membrane units 11A, 11B are immersed in the liquid of a treatment tank 10 and the filtered treated water transmitted through the membranes of both units is obtained, the membrane units 11A, 11B are arranged in the liquid of the tank so as to be separated by a partition plate 14 and air diffusing devices 15A, 15B are individually installed under the individual membrane units and made alternately operable.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、平膜を複数枚積層し
た積層体や、中空糸膜を平面状、或いはすだれ状にした
膜エレメントを複数枚積層した積層体や、管状膜を複数
本並行に接続したものを膜ユニットとして用いた浸漬膜
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a laminated body in which a plurality of flat membranes are laminated, a laminated body in which a plurality of membrane elements having hollow fiber membranes in a planar shape or a blind shape are laminated, and a plurality of tubular membranes. The present invention relates to a submerged membrane device that uses those connected in parallel as a membrane unit.

【0002】[0002]

【従来の技術】処理槽の液中に上述した膜ユニットを浸
漬し、膜ユニットの内部を吸引して膜を透過した濾過処
理水を得る浸漬膜装置は従来から公知である。又、膜の
下部に散気装置を設け濾過ケークを剥離させることも公
知である。
2. Description of the Related Art Immersion membrane devices for immersing the above-mentioned membrane unit in the liquid of a treatment tank and sucking the inside of the membrane unit to obtain filtered treated water that has permeated the membrane have been conventionally known. It is also known to provide an air diffuser at the bottom of the membrane to separate the filter cake.

【0003】[0003]

【発明が解決しようとする課題】この浸漬膜装置を運転
して膜濾過を行うと、膜面には濃度分極層、ゲール層、
ケーク層などの非濾過物質が付着する。そして、非濾過
物質の厚さが増すと濾過抵抗が増大し、濾過圧力が高ま
って濾過効率は著しく低下する。このため膜ユニットの
下方に散気装置を設け、一定時間膜濾過運転を行った
ら、又は膜濾過運転中に一定濾過圧力になったら、運転
を中止して逆洗を行うが、この逆洗の前後に散気装置を
作動し、膜ユニットの下面全体に下から気泡を浴びせ、
膜の間を上向する気泡と、上向水流の剪断力で膜面に付
着した非濾過物質を剥離する必要がある。この場合、膜
ユニットの回りに槽内の液が下向流して循環する対流ス
ペースを保つことが必要で、処理槽内への膜の充填率が
その対流スペース分だけ減少することになる。
When the immersion membrane device is operated to perform membrane filtration, a concentration polarization layer, a Gael layer,
Non-filtered material, such as cake layers, adheres. When the thickness of the non-filter substance increases, the filtration resistance increases, the filtration pressure increases, and the filtration efficiency significantly decreases. For this reason, an air diffuser is installed below the membrane unit, and when the membrane filtration operation is performed for a certain period of time, or when a certain filtration pressure is reached during the membrane filtration operation, the operation is stopped and backwashing is performed. Operate the air diffuser back and forth to expose the entire bottom surface of the membrane unit to bubbles from below.
It is necessary to separate the bubbles rising between the membranes and the non-filter substance adhering to the membrane surface by the shearing force of the upward water flow. In this case, it is necessary to maintain a convection space in which the liquid in the tank flows downward and circulates around the membrane unit, and the filling rate of the film in the treatment tank is reduced by the amount of the convection space.

【0004】[0004]

【課題を解決するための手段】そこで本発明は、処理槽
の液中に膜ユニットを浸漬し、膜を透過した濾過処理水
を得る浸漬膜装置において、複数の膜ユニットを液中の
仕切板で隔てゝ槽内液中に配置すると共に、その個々の
膜ユニットの下方に個々に散気装置を設け、散気装置を
交互に作動可能にしたことを特徴とする。
Therefore, the present invention is a submerged membrane device in which a membrane unit is immersed in a liquid in a treatment tank to obtain filtered treated water that has permeated the membrane. It is characterized in that it is placed in the liquid in the tank and is separated from each other by an air diffuser provided below each of the membrane units so that the air diffusers can be alternately operated.

【0005】[0005]

【実施例】図示の各実施例において、10は処理槽で、
処理槽の液中には膜ユニット11が浸漬してあり、ポン
プ12を接続した吸引管13が膜ユニットの内部を吸引
し、処理槽内の原液中、膜ユニット11を透過したもの
を濾過処理水として採水する。膜ユニットは、前述した
ように平膜の複数枚の積層体、又は中空糸膜を平面状、
或いはすだれ状にした膜エレメントの複数枚の積層体、
又は管状膜を複数本並行に接続したものである。
EXAMPLES In each of the illustrated examples, 10 is a processing tank,
The membrane unit 11 is immersed in the liquid in the treatment tank, the suction pipe 13 connected to the pump 12 sucks the inside of the membrane unit, and the raw liquid in the treatment tank that has passed through the membrane unit 11 is filtered. Collect as water. The membrane unit is, as described above, a laminate of a plurality of flat membranes, or a hollow fiber membrane in a planar shape,
Or a laminate of a plurality of blind-shaped membrane elements,
Alternatively, a plurality of tubular membranes are connected in parallel.

【0006】図1の実施例では、処理槽10内に2つの
膜ユニット11A,11Bを上端が液面下の仕切板14
で隔てゝ隣接状に配置してあり、各膜ユニット11A,
11Bの下方には個々に散気装置15A,15Bが設け
てある。4つの散気装置15A,15Bは共通のブロワ
ー16に分岐管17で接続し、管に設けた開閉弁18
A,18Bで個々に作動できるようになっている。膜濾
過運転を中止し、逆洗を行う前後に開閉弁18A,18
Bを交互に開閉し、例えば散気装置15Aから15分
間、気泡を膜ユニット11Aに浴びせ、次の15分は散
気装置15Bから気泡を膜ユニット11Bに浴びせ、こ
れを繰返す。これにより散気装置15Aから浮上する気
泡によって膜ユニット11Aの膜の間には上向流が生
じ、気泡と上向水流により膜ユニット11Aの膜面に付
着した非濾過物質は膜面から剥離し、同時に膜ユニット
11Bの膜間には下向流が生じ、この下向水流によって
膜面に付着した非濾過物質が剥離される。散気装置15
Bが作動しているときは上記とは逆で膜ユニット11B
の膜面に付着した非濾過物質は気泡と上向水流により膜
面から剥離し、膜ユニット11Aの膜面に付着した非濾
過物質は膜間に生じた下向水流で膜面から剥離する。
尚、散気は膜の運転を中止して行っても、膜の運転中に
行ってもよい。
In the embodiment shown in FIG. 1, two membrane units 11A and 11B are provided in a processing tank 10 with a partition plate 14 whose upper end is below the liquid surface.
Are separated from each other and are arranged adjacent to each other, and each membrane unit 11A,
Air diffusers 15A and 15B are individually provided below 11B. The four air diffusers 15A and 15B are connected to a common blower 16 by a branch pipe 17, and an on-off valve 18 provided in the pipe.
It can be operated individually by A and 18B. Stop the membrane filtration operation and open / close valves 18A, 18 before and after backwashing.
B is alternately opened and closed, for example, air bubbles are blown on the membrane unit 11A from the air diffuser 15A for 15 minutes, and bubbles are blown on the membrane unit 11B from the air diffuser 15B for the next 15 minutes, and this is repeated. As a result, an upward flow is generated between the membranes of the membrane unit 11A due to the bubbles floating from the air diffuser 15A, and the non-filtration substance attached to the membrane surface of the membrane unit 11A is separated from the membrane surface by the bubbles and the upward water flow. At the same time, a downward flow is generated between the membranes of the membrane unit 11B, and the non-filtration substance attached to the membrane surface is separated by the downward water flow. Air diffuser 15
When B is operating, the reverse of the above, the membrane unit 11B
The non-filtration substance attached to the membrane surface is separated from the membrane surface by the air bubbles and the upward water flow, and the non-filtration substance attached to the membrane surface of the membrane unit 11A is separated from the membrane surface by the downward water flow generated between the membranes.
Aeration may be performed after the operation of the membrane is stopped or during the operation of the membrane.

【0007】図2の実施例では、処理槽10内に4つの
膜ユニット11A,11B,11C,11Dを三枚の仕
切板14A,14B,14Cで隔てゝ隣接状に配置して
あり、各膜ユニットの下方には個々に散気装置15A,
15B,15C,15Dが設けてある。4つの散気装置
は共通のブロワー16に分岐管17で接続し、分岐管に
設けた4つの開閉弁18A,18B,18C,18Dで
4つの散気装置を個々に作動することができる。膜濾過
運転を行っている間、或いは運転を中止し、逆洗の前後
に開閉弁を操作し、例えば散気装置15A,15B,1
5C,15Dの順に15分間宛作動させたり、或いは1
5Aと15C、15Bと15Dを15分間宛交互に作動
させる。作動している散気装置の上の膜ユニットの膜間
には気泡による上向流が生じ、気泡と上向水流が膜面に
付着した非濾過物質を剥離し、作動していない散気装置
の上の膜ユニットの膜間には下向流が生じ、この下向水
流が膜面に付着した非濾過物質を膜面から剥離する。
In the embodiment shown in FIG. 2, four membrane units 11A, 11B, 11C and 11D are arranged in the processing tank 10 by three partition plates 14A, 14B and 14C so as to be adjacent to each other. In the lower part of the unit, individually diffuser 15A,
15B, 15C and 15D are provided. The four air diffusers are connected to a common blower 16 by a branch pipe 17, and the four open / close valves 18A, 18B, 18C, 18D provided in the branch pipe can individually operate the four air diffusers. While performing the membrane filtration operation or stopping the operation, operating the on-off valve before and after backwashing, for example, the air diffusers 15A, 15B, 1
5C, 15D in order for 15 minutes, or 1
5A and 15C and 15B and 15D are alternately operated for 15 minutes. An upward flow due to air bubbles occurs between the membranes of the membrane unit above the operating air diffuser, and the air bubbles and the upward water flow separate the non-filtration material adhering to the membrane surface, and the air diffuser is not operating. A downward flow is generated between the membranes of the membrane unit above the membrane, and this downward water flow separates the non-filtration substance adhering to the membrane surface from the membrane surface.

【0008】[0008]

【発明の効果】以上で明らかなように、散気装置を交互
に作動することで、作動している散気装置の上の膜ユニ
ットの膜間には気泡による上向流が生じ、気泡と上向水
流とにより膜面に付着した非濾過物質を剥離する。そし
て、作動を中止している散気装置の上の膜ユニットの膜
間には下向流が生じ、この下向水流が膜面に付着した非
濾過物質を剥離する。従って、下向流を生じさせる対流
スペースを膜ユニットの間に保つ必要が無くなるので、
処理槽への膜充填率が高まる。又、同じ数の膜ユニット
を充填する場合、使用する処理槽の大きさは大幅に小型
化する。
As is apparent from the above, by alternately operating the air diffusers, an upward flow due to bubbles is generated between the membranes of the membrane unit above the operating air diffusers, and the The non-filter substance adhering to the membrane surface is separated by the upward flow of water. Then, a downward flow is generated between the membranes of the membrane unit above the air diffusing device that has stopped its operation, and this downward water flow separates the non-filter substance adhering to the membrane surface. Therefore, it is not necessary to keep the convection space that causes the downward flow between the membrane units,
The film filling rate in the processing tank is increased. Further, when the same number of membrane units are filled, the size of the processing tank used is greatly reduced.

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

【図1】本発明の浸漬膜装置の第1実施例の断面図であ
る。
FIG. 1 is a sectional view of a first embodiment of an immersion membrane device of the present invention.

【図2】本発明の浸漬膜装置の他の1実施例の断面図で
ある。
FIG. 2 is a sectional view of another embodiment of the immersion membrane device of the present invention.

【符号の説明】[Explanation of symbols]

10 処理槽 11A 膜ユニット 11B 膜ユニット 11C 膜ユニット 11D 膜ユニット 12 ポンプ 13 吸引管 14 仕切板 14A 仕切板 14B 仕切板 14C 仕切板 15A 散気装置 15B 散気装置 15C 散気装置 15D 散気装置 16 ブロワー 17 分岐管 18A 開閉弁 18B 開閉弁 18C 開閉弁 18D 開閉弁 10 Treatment Tank 11A Membrane Unit 11B Membrane Unit 11C Membrane Unit 11D Membrane Unit 12 Pump 13 Suction Pipe 14 Partition Plate 14A Partition Plate 14B Partition Plate 14C Partition Plate 15A Air Diffuser 15B Air Diffuser 15C Air Diffuser 15D Blower 16 17 Branch pipe 18A Open / close valve 18B Open / close valve 18C Open / close valve 18D Open / close valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 処理槽の液中に膜ユニットを浸漬し、膜
を透過した濾過処理水を得る浸漬膜装置において、複数
の膜ユニットを液中の仕切板で隔てゝ槽内液中に配置す
ると共に、その個々の膜ユニットの下方に個々に散気装
置を設け、散気装置を交互に作動可能にしたことを特徴
とする浸漬膜装置。
1. A submerged membrane device in which a membrane unit is immersed in a liquid in a treatment tank to obtain filtered treated water that has permeated the membrane, and a plurality of membrane units are separated by a partition plate in the liquid and arranged in the liquid in the tank. In addition, the submerged membrane device is characterized in that the air diffusers are individually provided below the respective membrane units so that the air diffusers can be alternately operated.
JP34595793A 1993-12-24 1993-12-24 Operating method of immersion membrane device Expired - Fee Related JP3341428B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34595793A JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34595793A JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Publications (2)

Publication Number Publication Date
JPH07185271A true JPH07185271A (en) 1995-07-25
JP3341428B2 JP3341428B2 (en) 2002-11-05

Family

ID=18380157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34595793A Expired - Fee Related JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Country Status (1)

Country Link
JP (1) JP3341428B2 (en)

Cited By (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000021890A1 (en) * 1998-10-09 2000-04-20 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
JP2001276874A (en) * 2000-03-31 2001-10-09 Ebara Corp Solid/liquid separation method and device in organic drain treatment
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6656356B2 (en) 1998-10-09 2003-12-02 Zenon Environmental Inc. Aerated immersed membrane system
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6899811B2 (en) 2000-05-04 2005-05-31 Zenon Environmental Inc. Immersed membrane apparatus
JP2005161178A (en) * 2003-12-02 2005-06-23 Yuasa Corp Membrane filtering apparatus and its operating method
WO2005105275A1 (en) * 2004-04-02 2005-11-10 Koch Membrane Systems Gmbh Method for aerating membrane modules
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
JP2006289370A (en) * 2006-08-07 2006-10-26 Ebara Corp Solid-liquid separation method and apparatus
US7160463B2 (en) 2002-06-18 2007-01-09 U.S. Filter Wastewater Group, Inc. Methods of minimizing the effect of integrity loss in hollow fibre membrane modules
JP2007130579A (en) * 2005-11-10 2007-05-31 Mitsubishi Rayon Eng Co Ltd Filtration membrane cleaning apparatus and method for membrane filtration unit in activated sludge treatment
WO2007097260A1 (en) 2006-02-24 2007-08-30 Toray Industries, Inc. Method of producing chemical product and continuous fermentation apparatus
US7361274B2 (en) 2002-08-21 2008-04-22 Siemens Water Technologies Corp. Aeration method
JP2008246357A (en) * 2007-03-30 2008-10-16 Kubota Corp Membrane separation method and apparatus
WO2009112618A1 (en) * 2008-03-12 2009-09-17 Universisdad De Alicante Compact system for treating household waste water
WO2011152461A1 (en) * 2010-06-01 2011-12-08 三菱レイヨン株式会社 Solid-liquid separator device and operation method thereof
WO2012099140A1 (en) * 2011-01-20 2012-07-26 株式会社クボタ Membrane separation equipment and membrane separation device and operating method for membrane separation equipment
US8357299B2 (en) * 2005-07-12 2013-01-22 Zenon Technology Partnership Process control for an immersed membrane system
JP2013202467A (en) * 2012-03-28 2013-10-07 Kubota Corp Membrane separation facility
WO2013187513A1 (en) * 2012-06-15 2013-12-19 旭化成ケミカルズ株式会社 Immersed membrane unit
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
JP2014184383A (en) * 2013-03-22 2014-10-02 Mitsubishi Rayon Co Ltd Water treatment apparatus
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8876089B2 (en) 2011-09-15 2014-11-04 Zenon Technology Partnership Method and apparatus to keep an aerator full of air
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
JP2016073937A (en) * 2014-10-07 2016-05-12 三菱化学株式会社 Multitubular separation membrane module and liquid treatment method
US9358505B2 (en) 2009-09-03 2016-06-07 General Electric Company Gas sparger for an immersed membrane
US9364805B2 (en) 2010-10-15 2016-06-14 General Electric Company Integrated gas sparger for an immersed membrane
US9463419B2 (en) 2012-01-09 2016-10-11 General Electric Company Pulse aeration for immersed membranes
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 (78)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000021890A1 (en) * 1998-10-09 2000-04-20 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7186343B2 (en) 1998-10-09 2007-03-06 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7625491B2 (en) 1998-10-09 2009-12-01 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6656356B2 (en) 1998-10-09 2003-12-02 Zenon Environmental Inc. Aerated immersed membrane system
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6708957B2 (en) 1998-10-09 2004-03-23 Zenon Environmental Inc. Moving aerator for immersed membranes
KR100439436B1 (en) * 1998-10-09 2004-07-09 제논 인바이런멘탈 인코포레이티드 Cyclic aeration system for submerged membrane modules
EP1445240A1 (en) * 1998-10-09 2004-08-11 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
EP1452493A1 (en) * 1998-10-09 2004-09-01 Zenon Environmental Inc. Aeration system for submerged membrane modules
US6881343B2 (en) 1998-10-09 2005-04-19 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7922910B2 (en) 1998-10-09 2011-04-12 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7347942B2 (en) 1998-10-09 2008-03-25 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
EP2204353A2 (en) 1998-10-09 2010-07-07 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
EP2204353A3 (en) * 1998-10-09 2010-09-15 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7198721B2 (en) 1998-10-09 2007-04-03 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7820050B2 (en) 1998-10-09 2010-10-26 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US6245239B1 (en) 1998-10-09 2001-06-12 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
JP2001276874A (en) * 2000-03-31 2001-10-09 Ebara Corp Solid/liquid separation method and device in organic drain treatment
US7037426B2 (en) 2000-05-04 2006-05-02 Zenon Environmental Inc. Immersed membrane apparatus
US6899811B2 (en) 2000-05-04 2005-05-31 Zenon Environmental Inc. Immersed membrane apparatus
US7300582B2 (en) 2000-11-15 2007-11-27 Zenon Technology Partnership Immersed membrane apparatus
US7160463B2 (en) 2002-06-18 2007-01-09 U.S. Filter Wastewater Group, Inc. Methods of minimizing the effect of integrity loss in hollow fibre membrane modules
US7344645B2 (en) 2002-06-18 2008-03-18 Siemens Water Technologies Corp. Methods of minimising the effect of integrity loss in hollow fibre membrane modules
US7361274B2 (en) 2002-08-21 2008-04-22 Siemens Water Technologies Corp. Aeration method
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
JP2005161178A (en) * 2003-12-02 2005-06-23 Yuasa Corp Membrane filtering apparatus and its operating method
WO2005105275A1 (en) * 2004-04-02 2005-11-10 Koch Membrane Systems Gmbh Method for aerating membrane modules
US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US9783434B2 (en) 2005-07-12 2017-10-10 Zenon Technology Partnership Real-time process control for an immersed membrane filtration system using a control hierarchy of discrete-state parameter changes
US8357299B2 (en) * 2005-07-12 2013-01-22 Zenon Technology Partnership Process control for an immersed membrane system
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
JP2007130579A (en) * 2005-11-10 2007-05-31 Mitsubishi Rayon Eng Co Ltd Filtration membrane cleaning apparatus and method for membrane filtration unit in activated sludge treatment
WO2007097260A1 (en) 2006-02-24 2007-08-30 Toray Industries, Inc. Method of producing chemical product and continuous fermentation apparatus
JP2006289370A (en) * 2006-08-07 2006-10-26 Ebara Corp Solid-liquid separation method and apparatus
JP2008246357A (en) * 2007-03-30 2008-10-16 Kubota Corp Membrane separation method and apparatus
JP4588043B2 (en) * 2007-03-30 2010-11-24 株式会社クボタ Membrane separation method and apparatus
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
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
US10507431B2 (en) 2007-05-29 2019-12-17 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
ES2330824A1 (en) * 2008-03-12 2009-12-15 Universidad De Alicante Compact system for treating household waste water
WO2009112618A1 (en) * 2008-03-12 2009-09-17 Universisdad De Alicante Compact system for treating household waste water
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US10471393B2 (en) 2009-09-03 2019-11-12 Bl Technologies, Inc. Gas sparger for an immersed membrane
US9358505B2 (en) 2009-09-03 2016-06-07 General Electric Company Gas sparger for an immersed membrane
US11219866B2 (en) 2009-09-03 2022-01-11 Bl Technologies, Inc. Gas sparger for an immersed membrane
US9433903B2 (en) 2009-09-03 2016-09-06 Zenon Technology Partnership Gas sparger for a filtering membrane
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
WO2011152461A1 (en) * 2010-06-01 2011-12-08 三菱レイヨン株式会社 Solid-liquid separator device and operation method thereof
US9630147B2 (en) 2010-09-24 2017-04-25 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9364805B2 (en) 2010-10-15 2016-06-14 General Electric Company Integrated gas sparger for an immersed membrane
US10173175B2 (en) 2010-10-15 2019-01-08 Bl Technologies, Inc. Integrated gas sparger for an immersed membrane
WO2012099140A1 (en) * 2011-01-20 2012-07-26 株式会社クボタ Membrane separation equipment and membrane separation device and operating method for membrane separation equipment
US8876089B2 (en) 2011-09-15 2014-11-04 Zenon Technology Partnership Method and apparatus to keep an aerator full of air
US10391432B2 (en) 2011-09-30 2019-08-27 Evoqua Water Technologies Llc Manifold arrangement
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
US9925499B2 (en) 2011-09-30 2018-03-27 Evoqua Water Technologies Llc Isolation valve with seal for end cap of a filtration system
US9463419B2 (en) 2012-01-09 2016-10-11 General Electric Company Pulse aeration for immersed membranes
JP2013202467A (en) * 2012-03-28 2013-10-07 Kubota Corp Membrane separation facility
WO2013187513A1 (en) * 2012-06-15 2013-12-19 旭化成ケミカルズ株式会社 Immersed membrane unit
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
US9764289B2 (en) 2012-09-26 2017-09-19 Evoqua Water Technologies Llc Membrane securement device
US9962865B2 (en) 2012-09-26 2018-05-08 Evoqua Water Technologies Llc Membrane potting methods
US9815027B2 (en) 2012-09-27 2017-11-14 Evoqua Water Technologies Llc Gas scouring apparatus for immersed membranes
JP2014184383A (en) * 2013-03-22 2014-10-02 Mitsubishi Rayon Co Ltd Water treatment apparatus
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
JP2016073937A (en) * 2014-10-07 2016-05-12 三菱化学株式会社 Multitubular separation membrane module and liquid treatment method
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system

Also Published As

Publication number Publication date
JP3341428B2 (en) 2002-11-05

Similar Documents

Publication Publication Date Title
JPH07185271A (en) Immersion membrane apparatus
JP3446399B2 (en) Immersion type membrane separation device and membrane separation method using the same
JP3341427B2 (en) Immersion membrane equipment
SE503277C2 (en) Filters intended for cross-flow filtration
TW200400082A (en) Membrane separation device and membrane separation method
JP3401874B2 (en) Immersion type membrane separation device
JP2000343095A (en) Activated sludge treating device
JPH0999222A (en) Hollow fiber membrane module unit and filtering device
JP3554296B2 (en) Filtration device using filtration separation membrane cartridge
JPH01168304A (en) Solid/liquid separation and condensation apparatus
JP3333086B2 (en) Water treatment equipment
JPH10263371A (en) Immersion type filter membrane element
JP3557655B2 (en) Membrane separation device using internal pressure type tubular membrane module
JP3124174B2 (en) Water treatment equipment
JPS61200808A (en) Apparatus for filtering solution
JPH0474584A (en) Treatment of waste water
JPH07194945A (en) Flat membrane element for immersion-type mambrane separation apparatus
JPH07132214A (en) Membrane element
JP2500181B2 (en) Backwashing method for ceramic membrane
JP2002248323A (en) Filtering device
JPH04323470A (en) Purifying device for pool water
JPH10258220A (en) Waste water treatment facility
JPH06342A (en) Hollow-fiber membrane module and its assembly
JP3461657B2 (en) Water treatment equipment
JPH09299951A (en) Dipping type plane membrane separation device

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080823

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090823

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090823

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 8

Free format text: PAYMENT UNTIL: 20100823

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 9

Free format text: PAYMENT UNTIL: 20110823

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120823

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees