JPH09103661A - Immersion type membrane separation apparatus - Google Patents
Immersion type membrane separation apparatusInfo
- Publication number
- JPH09103661A JPH09103661A JP28915095A JP28915095A JPH09103661A JP H09103661 A JPH09103661 A JP H09103661A JP 28915095 A JP28915095 A JP 28915095A JP 28915095 A JP28915095 A JP 28915095A JP H09103661 A JPH09103661 A JP H09103661A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- water
- bubbles
- membrane element
- air
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、平膜、中空糸
膜、管状膜などの膜を本体に取付け、膜を透過する透過
水を本体の内部に得る膜エレメントを使用した浸漬型膜
分離装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a submerged membrane separation device using a membrane element in which a membrane such as a flat membrane, a hollow fiber membrane or a tubular membrane is attached to a main body, and permeated water that permeates the membrane is obtained inside the main body. Regarding
【0002】[0002]
【従来の技術】このような浸漬型膜分離装置として、処
理槽内の原水中に、所定の間隔を保って複数の膜エレメ
ントを立て並べ、各膜エレメントの採水口にヘッダー管
を介して吸引ポンプを接続し、槽底に微細気泡を噴出す
る散気管を敷設し、散気管が噴出する微細気泡のエアリ
フト作用により膜エレメントの間隔に膜に接触して流れ
る上昇流を生じさせ、前記吸引ポンプの吸引作用で原水
中の透過水を各膜エレメントの内部に吸引し、採水口、
及びヘッダー管を介して採水するようにしたものは従来
から公知である。2. Description of the Related Art As such an immersion type membrane separation device, a plurality of membrane elements are vertically arranged in a raw water in a treatment tank at a predetermined interval and sucked through a header pipe at a water collecting port of each membrane element. A suction pipe is connected to the pump, and an air diffusing pipe for jetting fine bubbles is laid at the bottom of the tank, and an upward flow that flows in contact with the membrane is generated in the space between the membrane elements by the air lift action of the fine bubbles jetting by the diffusing pipe. The permeated water in the raw water is sucked into each membrane element by the suction action of
Also, a device adapted to collect water via a header pipe is conventionally known.
【0003】[0003]
【発明が解決しようとする課題】上記従来装置におい
て、散気管から微細気泡を噴出させる目的の1つは、微
細気泡の剪断力によって膜の表面に汚染物質が付着する
のを防止するためであるが、原水が多量のMLSSを含
んでいる場合は、運転の継続により膜の表面に次第に汚
染物質が付着し、膜の濾過性能は低下する。そして、濾
過性能が或る程度低下したら、膜エレメントを処理槽の
外に引出し、薬液で膜の表面を洗浄し、付着している汚
染物質を剥離除去する必要があるが、それには非常に手
数がかゝる。In the above conventional apparatus, one of the purposes of ejecting fine bubbles from the air diffusing tube is to prevent contaminants from adhering to the surface of the membrane due to the shearing force of the fine bubbles. However, when the raw water contains a large amount of MLSS, the pollutants gradually adhere to the surface of the membrane due to the continuous operation, and the filtration performance of the membrane deteriorates. Then, when the filtration performance deteriorates to some extent, it is necessary to draw the membrane element out of the treatment tank, wash the surface of the membrane with a chemical solution, and peel off the attached contaminants. I'm sorry.
【0004】[0004]
【課題を解決するための手段】この発明は、上述した問
題点を解消するためのもので、処理槽内の原水中に、所
定の間隔を保って複数の膜エレメントを立て並べ、各膜
エレメントの採水口と吸引ポンプを接続し、槽底に気泡
を噴出する散気管を敷設し、散気管が噴出する気泡のエ
アリフト作用により膜エレメントの間隔に膜に接触して
流れる上昇流を生じさせ、前記吸引ポンプの吸引作用で
原水中の透過水を各膜エレメントの内部に吸引し、採水
口を介して採水する浸漬型膜分離装置において、各膜エ
レメントの内部に洗浄薬液を注入し、膜の外に浸出させ
る洗浄薬液の加圧注入手段と、槽底に粗大気泡を噴出す
る散気管を設けたことを特徴とする。The present invention is intended to solve the above-mentioned problems, and a plurality of membrane elements are arranged side by side in raw water in a treatment tank at a predetermined interval. The water sampling port and suction pump are connected, and a diffusing pipe for ejecting bubbles is laid on the bottom of the tank, and an air-lifting action of the bubbles ejected by the diffusing pipe causes an upward flow that flows in contact with the membrane at the interval between the membrane elements, In the immersion type membrane separation device that sucks the permeated water in the raw water into the inside of each membrane element by the suction action of the suction pump and collects the water through the water sampling port, the cleaning chemical solution is injected into the inside of each membrane element, It is characterized in that a means for pressurizing and injecting a cleaning chemical liquid to be leached to the outside of the tank and an air diffuser for jetting coarse bubbles are provided at the bottom of the tank.
【0005】図示の実施形態において、1は有機物を含
む原水が供給される活性汚泥処理装置の処理槽で、活性
汚泥は浮遊する槽内の水中にエアリフト筒2を立設し、
このエアリフト筒上に透過水の採水口4を有する複数枚
の平膜エレメント3を前後方向に間隔を保って一列に立
て並べてある。エアリフト筒の内部下方にはブロアBか
ら供給される空気を微細気泡にして噴出する微細気泡用
散気管5と、粗大気泡にして噴出する粗大気泡用散気管
6とが弁で切換えて散気するように敷設してある。In the illustrated embodiment, reference numeral 1 denotes a treatment tank of an activated sludge treatment apparatus to which raw water containing organic matter is supplied. The activated sludge has an air lift tube 2 set up in the water in a floating tank.
On the air lift cylinder, a plurality of flat sheet membrane elements 3 having permeated water sampling ports 4 are arranged in a row in the front-rear direction at intervals. Below the inside of the air lift cylinder, a diffuser 5 for fine bubbles that ejects air supplied from the blower B in the form of fine bubbles and a diffuser 6 for coarse bubbles that ejects in the form of coarse bubbles are switched by a valve to diffuse air. Has been laid.
【0006】膜濾過運転を行う際は、微細気泡用散気管
5から微細気泡を散気する。これによって原水の有機物
を分解する活性汚泥の活性を高め、同時に平膜エレメン
ト3の相対向した膜の間隔に微細気泡のエアリフト作用
で膜に接触して流れる上昇流を生じさせ、気泡の剪断作
用によって膜の表面にゲル状の汚染物質が付着するのを
防止しながら膜を透過する透過水を平膜エレメントの本
体の内部に得、この透過水を各平膜エレメントの採水口
4に接続したヘッダー管7を介しポンプP1 で吸引して
採水する。When performing the membrane filtration operation, fine bubbles are diffused from the fine bubble diffuser 5. As a result, the activity of the activated sludge that decomposes the organic matter of the raw water is increased, and at the same time, the air-lifting action of the fine bubbles causes an upward flow that flows in contact with the membranes in the space between the facing membrane elements of the flat sheet membrane element 3, thereby shearing the bubbles. The permeated water that permeates the membrane while preventing the gel-like contaminants from adhering to the surface of the membrane was obtained inside the main body of the flat membrane element, and this permeated water was connected to the water intake port 4 of each flat membrane element. Water is drawn by sucking with the pump P1 through the header pipe 7.
【0007】ヘッダー管7にはタンク8中の洗浄薬液を
ポンプP2 で加圧して供給する薬注管9が接続してあ
り、このタンク8、薬注管9、ポンプP2 は洗浄薬液の
加圧注入手段10を構成する。薬注管9と、採水用ポン
プP1 の上流には弁を設け、膜濾過運転中は注入管の弁
を閉にしておく。The header pipe 7 is connected to a chemical injection pipe 9 for supplying the cleaning chemical in the tank 8 by pressurizing it with a pump P2. The tank 8, chemical injection pipe 9 and pump P2 pressurize the cleaning chemical. The injection means 10 is configured. A valve is provided upstream of the chemical injection pipe 9 and the water sampling pump P1, and the valve of the injection pipe is closed during the membrane filtration operation.
【0008】膜の表面に汚染物質が付着し、膜の濾過性
能が低下して来たら、ポンプP1 を停めると共に、ポン
プ側の弁を閉じ、薬注管9の弁を開き、ポンプP2 を運
転してタンク8内の洗浄薬液を薬注管9、ヘッダー管7
を介して各平膜エレメントの本体の内部に加圧して注入
する。勿論、水頭差で注入しても良い。使用する洗浄薬
液は、次亜塩素酸ナトリウム、水酸化ナトリウム、硫
酸、過酸化水素などである。同時に粗大気泡用散気管6
から粗大気泡を散気する。When contaminants adhere to the surface of the membrane and the filtration performance of the membrane deteriorates, the pump P1 is stopped, the valve on the pump side is closed, the valve of the chemical injection pipe 9 is opened, and the pump P2 is operated. Then, the cleaning chemical in the tank 8 is filled with the chemical injection pipe 9 and the header pipe 7.
It is pressurized and injected into the main body of each flat sheet membrane element via Of course, you may inject by a water head difference. The cleaning chemicals used are sodium hypochlorite, sodium hydroxide, sulfuric acid, hydrogen peroxide and the like. At the same time, air diffuser 6 for large bubbles
Diffuse coarse bubbles from.
【0009】これにより、膜エレメントの内部に加圧し
て注入された洗浄薬液は膜を透過して膜の表面に浸出
し、膜の表面に付着した汚染物質と接触して化学変化
し、汚染物質の膜に対する付着力を低下させる。そし
て、膜に接触して上昇する粗大気泡が、その大きな剪断
力で、付着力を低下した汚染物質を膜から剥離し、除去
する。洗浄薬液による洗浄を所定時間行ったら、ポンプ
P2 を停め、薬注管の弁を閉じ、ポンプP1 を運転し、
微細気泡を散気管5から散気して膜濾過運転を再開す
る。As a result, the cleaning chemical injected under pressure into the membrane element permeates the membrane, leaches out to the surface of the membrane, contacts the pollutants adhering to the surface of the membrane, and undergoes a chemical change, resulting in pollutants. Reduces the adhesion to the film. Then, the large bubbles rising in contact with the film peel off and remove the pollutant whose adhesive force has been reduced from the film due to the large shearing force. After cleaning with the cleaning chemical for a predetermined time, stop the pump P2, close the valve of the chemical injection pipe, and operate the pump P1.
Fine bubbles are diffused from the diffuser 5 and the membrane filtration operation is restarted.
【0010】本発明の実施形態は、平膜エレメントで説
明したが、四角形の枠組みに中空糸膜をのれん状に取付
けた膜エレメントを立て並べたものでも良く、管状膜を
同様に取付けた膜エレメントを立て並べたものでも良
い。又、微細気泡と粗大気泡の散気管を別々としたが両
方の機能を兼ね備えた散気管の一種類でも良い。この場
合、散気管に供給する空気量を増減することにより対処
する。Although the embodiment of the present invention has been described with respect to the flat membrane element, a membrane element having hollow fiber membranes mounted in a goodwill shape may be vertically arranged in a square frame, and a membrane element similarly mounted with a tubular membrane. It may be a set of. Further, although the diffuser tubes for the fine bubbles and the coarse bubbles are separate, one type of diffuser tube having both functions may be used. In this case, this is dealt with by increasing or decreasing the amount of air supplied to the air diffuser.
【0011】[0011]
【発明の効果】以上で明らかなように、本発明によれば
膜エレメントの内部に洗浄薬液を加圧注入して膜の表面
に付着する汚染物質の付着力を弱め、粗大気泡の大きな
剪断力で汚染物質を膜の表面から剥離して除去するの
で、洗浄が容易に行え、且つ洗浄効果が大である。As is apparent from the above, according to the present invention, a cleaning chemical liquid is pressure-injected into the inside of the membrane element to weaken the adhesion force of the contaminants adhering to the surface of the membrane, and the large shearing force of the coarse bubbles. Since the contaminants are peeled off from the surface of the film and removed, the cleaning can be easily performed and the cleaning effect is great.
【図1】Aは本発明の一実施形態の断面図、Bはその洗
浄中の状態の断面図である。FIG. 1A is a cross-sectional view of an embodiment of the present invention, and B is a cross-sectional view of a state during cleaning.
1 処理槽 2 エアリフト筒 3 膜エレメント 4 膜エレメントの採水口 5 微細気泡用散気管 6 粗大気泡用散気管 7 ヘッダー管 8 タンク 9 薬注管 10 洗浄薬液の加圧注入手段 1 Treatment Tank 2 Air Lift Cylinder 3 Membrane Element 4 Membrane Element Water Collection Port 5 Fine Air Bubble Diffuser 6 Large Coarse Bubble Diffuser 7 Header Pipe 8 Tank 9 Chemical Injection Pipe 10 Pressurizing and Injecting Medication Solution
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 65/08 B01D 65/08 C02F 1/44 C02F 1/44 K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01D 65/08 B01D 65/08 C02F 1/44 C02F 1/44 K
Claims (1)
て複数の膜エレメントを立て並べ、各膜エレメントの採
水口と吸引ポンプを接続し、槽底に気泡を噴出する散気
管を敷設し、散気管が噴出する気泡のエアリフト作用に
より膜エレメントの間隔に膜に接触して流れる上昇流を
生じさせ、前記吸引ポンプの吸引作用で原水中の透過水
を各膜エレメントの内部に吸引し、採水口を介して採水
する浸漬型膜分離装置において、各膜エレメントの内部
に洗浄薬液を注入し、膜の外に浸出させる洗浄薬液の加
圧注入手段と、槽底に粗大気泡を噴出する散気管を設け
たことを特徴とする浸漬型膜分離装置。1. A plurality of membrane elements are vertically arranged in a raw water in a treatment tank at a predetermined interval, a sampling port of each membrane element and a suction pump are connected, and an air diffuser for ejecting bubbles to the bottom of the tank is provided. By laying the air diffuser, the air lift action of the air bubbles ejected from the diffuser creates an upward flow that flows in contact with the membrane in the space between the membrane elements, and the suction action of the suction pump sucks the permeate in the raw water into each membrane element. Then, in the immersion type membrane separation device that collects water through the water sampling port, the cleaning chemical solution is injected into each membrane element, and the cleaning chemical solution is pressurized and injected to the outside of the membrane. An immersion-type membrane separation device, which is provided with an air diffuser for jetting.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28915095A JP3671477B2 (en) | 1995-10-12 | 1995-10-12 | Cleaning method for submerged membrane separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28915095A JP3671477B2 (en) | 1995-10-12 | 1995-10-12 | Cleaning method for submerged membrane separator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09103661A true JPH09103661A (en) | 1997-04-22 |
JP3671477B2 JP3671477B2 (en) | 2005-07-13 |
Family
ID=17739416
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28915095A Expired - Fee Related JP3671477B2 (en) | 1995-10-12 | 1995-10-12 | Cleaning method for submerged membrane separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3671477B2 (en) |
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007152227A (en) * | 2005-12-05 | 2007-06-21 | Hiroyoshi Hamanaka | Release cleaning method using kinetically functional aerosol |
WO2009000035A1 (en) * | 2007-06-28 | 2008-12-31 | Siemens Water Technologies Corp. | Cleaning method for simple filtration systems |
US7958652B2 (en) * | 2005-01-07 | 2011-06-14 | Bissell Homecare Inc. | Extraction cleaning with plenum and air outlets facilitating air flow drying |
CN102371123A (en) * | 2010-08-24 | 2012-03-14 | 苏州立升净水科技有限公司 | On-line cleaning method of immersed hollow fiber membrane module |
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 |
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 |
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 |
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 |
US9873088B2 (en) | 2011-05-17 | 2018-01-23 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
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 |
US10800808B2 (en) | 2008-09-02 | 2020-10-13 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
-
1995
- 1995-10-12 JP JP28915095A patent/JP3671477B2/en not_active Expired - Fee Related
Cited By (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
US7958652B2 (en) * | 2005-01-07 | 2011-06-14 | Bissell Homecare Inc. | Extraction cleaning with plenum and air outlets facilitating air flow drying |
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 |
JP2007152227A (en) * | 2005-12-05 | 2007-06-21 | Hiroyoshi Hamanaka | Release cleaning method using kinetically functional aerosol |
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 |
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 |
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 |
US9206057B2 (en) | 2007-05-29 | 2015-12-08 | Evoqua Water Technologies Llc | Membrane cleaning with pulsed airlift pump |
WO2009000035A1 (en) * | 2007-06-28 | 2008-12-31 | Siemens Water Technologies Corp. | Cleaning method for simple filtration systems |
US8382981B2 (en) | 2008-07-24 | 2013-02-26 | Siemens Industry, Inc. | Frame system for membrane filtration modules |
US9023206B2 (en) | 2008-07-24 | 2015-05-05 | Evoqua Water Technologies Llc | Frame system for membrane filtration modules |
US10981949B2 (en) | 2008-09-02 | 2021-04-20 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
US11884701B2 (en) | 2008-09-02 | 2024-01-30 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
US10800808B2 (en) | 2008-09-02 | 2020-10-13 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
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 |
CN102371123A (en) * | 2010-08-24 | 2012-03-14 | 苏州立升净水科技有限公司 | On-line cleaning method of immersed hollow fiber membrane module |
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 |
US10195567B2 (en) | 2011-05-17 | 2019-02-05 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
US9873088B2 (en) | 2011-05-17 | 2018-01-23 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
US10874990B2 (en) | 2011-05-17 | 2020-12-29 | Merck Millipore Ltd. | Layered tubular membranes for chromatography, and methods of use thereof |
US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US10391432B2 (en) | 2011-09-30 | 2019-08-27 | 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 |
US11065569B2 (en) | 2011-09-30 | 2021-07-20 | Rohm And Haas Electronic Materials Singapore Pte. Ltd. | Manifold arrangement |
US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
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 |
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 |
Also Published As
Publication number | Publication date |
---|---|
JP3671477B2 (en) | 2005-07-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH09103661A (en) | Immersion type membrane separation apparatus | |
JPH07185270A (en) | Immersion membrane apparatus | |
KR20100028116A (en) | Cleaning method for simple filtration systems | |
JP2002307091A (en) | Cleaning method of diffuser | |
JP3290556B2 (en) | Cleaning method for immersion type membrane cartridge | |
JP5238128B2 (en) | Solid-liquid separation device for solid-liquid mixed processing liquid | |
JP3257933B2 (en) | Chemical cleaning method for membrane cartridge | |
JP4530621B2 (en) | Cleaning method for air diffuser | |
KR100999945B1 (en) | Air relif device for membrane filter pipe | |
JP3554296B2 (en) | Filtration device using filtration separation membrane cartridge | |
JP3959758B2 (en) | Immersion membrane separator | |
JP2001170677A (en) | Air diffuser for high-concentration sewage | |
JP3178977B2 (en) | Cleaning method of membrane element | |
JP6411051B2 (en) | Immersion membrane separator and method for operating the same | |
JPH08206472A (en) | Washing of filter membrane | |
JPH11267474A (en) | Separation membrane cleaner | |
JP2002096062A (en) | Membrane cartridge with safety valve and throw-in type immersion membrane separator | |
JP3105140B2 (en) | Sewage treatment equipment | |
JP2000210660A (en) | Immersion type membrane filter, and production of clarified water | |
JP3880251B2 (en) | Backwash method for submerged membrane separator | |
JP4023959B2 (en) | High-concentration wastewater treatment method | |
JP2004066025A (en) | Difer | |
JPH11267473A (en) | Operation of membrane separator | |
JPH10258220A (en) | Waste water treatment facility | |
JP2556521Y2 (en) | Water treatment equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20040416 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20040511 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20040708 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20050329 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20050411 |
|
R150 | Certificate of patent (=grant) or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080428 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090428 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090428 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100428 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100428 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110428 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120428 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120428 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130428 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140428 Year of fee payment: 9 |
|
LAPS | Cancellation because of no payment of annual fees |