JPH1190189A - Method for cleaning membrane with liquid chemical - Google Patents
Method for cleaning membrane with liquid chemicalInfo
- Publication number
- JPH1190189A JPH1190189A JP27388197A JP27388197A JPH1190189A JP H1190189 A JPH1190189 A JP H1190189A JP 27388197 A JP27388197 A JP 27388197A JP 27388197 A JP27388197 A JP 27388197A JP H1190189 A JPH1190189 A JP H1190189A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- tank
- chemical
- chemical solution
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、膜を薬液により洗浄
する洗浄方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning method for cleaning a film with a chemical.
【0002】[0002]
【従来の技術及びその課題】従来、図2〜図5に示すよ
うに、処理槽51内には中空糸膜とか平膜で構成された
膜52が配設されており、処理槽51内には汚泥54が
満たされて、膜52にはポンプ53が接続されており、
処理槽51内で活性汚泥により生活排水等を浄化処理で
きるように構成されており、この膜52は、例えば年に
2回程度は膜52の詰まりをなくするために洗浄する必
要があり、従来では前記処理槽51内の汚泥54を排出
させて図3のように処理槽51内に薬液55を満たし、
薬液55内に膜52を浸漬させた状態で放置して、薬液
55により膜52を洗浄し、図4のように薬液55を中
和させた後に排出させて、再び図5に示すように処理槽
51内に汚泥54を入れて、膜52を通し活性汚泥によ
る浄化処理を続けることが行われており、また、別の膜
の洗浄方法として、図6〜図9に示すように、前記処理
槽51とは別に薬液55を満たした薬液槽56を用意し
ておき、図7に示すように前記処理槽51内の膜52を
吊り上げ等して、図8に示すように別体の薬液槽56内
に入れて薬液55内に膜52を浸漬させて、この状態で
放置し、その後に図9に示すように薬液槽56から膜5
2を引き上げて、再び汚泥54の満たされた処理槽51
内に戻すことが行われており、このような従来の何れの
洗浄方法においても、薬液55内に膜52を浸漬させて
放置して膜を洗浄するものであるため、膜52の内部を
完全に薬液により洗浄することが困難な場合があり、膜
の内部に洗浄されない部分が残ってしまうという問題点
があった。2. Description of the Related Art Conventionally, as shown in FIGS. 2 to 5, a membrane 52 composed of a hollow fiber membrane or a flat membrane is disposed in a treatment tank 51, and is disposed in the treatment tank 51. Is filled with sludge 54, a pump 53 is connected to the membrane 52,
It is configured so that domestic sludge can be purified by activated sludge in the treatment tank 51. The membrane 52 needs to be washed, for example, about twice a year to eliminate clogging of the membrane 52. Then, the sludge 54 in the processing tank 51 is discharged to fill the processing tank 51 with a chemical solution 55 as shown in FIG.
The film 52 is washed with the chemical solution 55 by leaving the film 52 immersed in the chemical solution 55, neutralized as shown in FIG. 4 and then discharged, and treated again as shown in FIG. The sludge 54 is put into the tank 51, and the purification treatment by the activated sludge is continued through the membrane 52. As another method for cleaning the membrane, as shown in FIGS. A chemical liquid tank 56 filled with a chemical liquid 55 is prepared separately from the tank 51, and the film 52 in the processing tank 51 is lifted as shown in FIG. 7, and a separate chemical liquid tank as shown in FIG. The membrane 52 is immersed in the chemical solution 55 by being put in the chemical solution 55, and is left in this state. Thereafter, as shown in FIG.
2 and the processing tank 51 filled with the sludge 54 again.
In any of such conventional cleaning methods, since the film 52 is immersed in the chemical solution 55 and left to clean the film, the inside of the film 52 is completely cleaned. In some cases, it is difficult to perform cleaning with a chemical solution, and there is a problem that a portion that is not cleaned remains inside the film.
【0003】[0003]
【課題を解決するための手段】本発明は上記従来の問題
点に鑑み案出したものであって、膜内を完全に洗浄する
ことのできる膜の薬液洗浄方法を提供せんことを目的と
し、その第1の要旨は、槽内に薬液を満たし、槽の底側
には散気管を配設し、該散気管の上方に薬液中に浸漬さ
せた状態で膜を配設し、該膜にポンプを有する配管を接
続し、前記散気管から噴出させた泡を前記膜に当てなが
ら前記ポンプにより膜内を通し薬液を吸引し、吸引した
薬液を前記槽内に循環させることである。また、第2の
要旨は、前記配管内に差圧計を設け、該差圧計により前
記膜の洗浄度合いをチェックすることである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems, and an object of the present invention is to provide a method for cleaning a chemical solution of a film which can completely clean the inside of the film. The first gist is that a tank is filled with a chemical solution, an air diffuser is provided on the bottom side of the tank, and a film is disposed above the air diffuser in a state of being immersed in the chemical solution. A pipe having a pump is connected, and a chemical solution is sucked through the membrane by the pump while the foam ejected from the air diffuser is applied to the membrane, and the sucked chemical solution is circulated in the tank. The second gist is to provide a differential pressure gauge in the pipe and check the degree of cleaning of the membrane by the differential pressure gauge.
【0004】[0004]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1は、槽1内に薬液8を満たして、その内部に
薬液8に浸漬させて膜2を配置したものであり、槽1の
底側には散気管3が配設されて、この散気管3は外部の
ブロア4と接続されたものとなっており、散気管3から
泡を上方へ噴出させて膜2に泡を当てることができるよ
うに構成されており、また、膜2の上端には配管5が接
続されており、配管5内には差圧計6と、その下流側に
ポンプ7が設けられて、ポンプ7の下流側の配管は前記
槽1内へ向かって配管されたものとなっている。なお、
前記膜2は中空糸膜とか平膜でモジュール化されて形成
されたものであり、また、前記薬液8は次亜塩素酸ナト
リウム等が用いられるものである。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a case in which a tank 1 is filled with a chemical solution 8 and the membrane 2 is disposed by being immersed in the chemical solution 8, and a diffuser 3 is provided at the bottom side of the tank 1. The trachea 3 is connected to an external blower 4, and is configured so that bubbles can be ejected upward from the diffuser 3 to apply bubbles to the membrane 2. Is connected to a pipe 5, a differential pressure gauge 6 is provided in the pipe 5, and a pump 7 is provided downstream thereof, and a pipe downstream of the pump 7 is piped into the tank 1. It has become. In addition,
The membrane 2 is formed as a module by a hollow fiber membrane or a flat membrane, and the chemical solution 8 is made of sodium hypochlorite or the like.
【0005】このような構成において、ブロア4を作動
させて散気管3から前記膜2に向かって泡を噴出させな
がら、前記ポンプ7を作動させて、膜2を通し薬液8を
配管5内に吸引し、吸引した薬液8は再び槽1内に戻し
て循環させ、薬液8を膜2内を通し連続的に循環させ
て、かつ散気管3からの泡を膜2に当てて、膜2内を通
過する薬液8により完全に膜2を洗浄できるように構成
したものであり、この場合に、最初は膜2内に詰まりが
生じているため前記差圧計6の目盛表示は大となってい
るが、次第に洗浄が進むにつれて膜2内の詰まりが除去
されて膜2内の通過抵抗が減少するために差圧計6の目
盛表示は小となり、従って、この差圧計6をチェックし
ていれば膜2の洗浄度合いを良好に認識することができ
るものとなり、差圧計6の目盛が所定値に達した状態で
完全に膜2内が洗浄された状態となり、その状態でポン
プ7及びブロア4の作動を停止させて洗浄を完了するこ
とができるものである。In such a configuration, while operating the blower 4 to eject bubbles from the air diffuser 3 toward the membrane 2, the pump 7 is operated to pass the chemical solution 8 through the membrane 2 into the pipe 5. The suctioned chemical solution 8 is returned to the tank 1 and circulated again. The chemical solution 8 is continuously circulated through the inside of the membrane 2, and bubbles from the air diffuser 3 are applied to the membrane 2. The membrane 2 can be completely washed with the chemical solution 8 passing through. In this case, since the clogging occurs in the membrane 2 at first, the scale display of the differential pressure gauge 6 is large. However, as the cleaning progresses, the clogging in the membrane 2 is removed, and the passage resistance in the membrane 2 is reduced, so that the scale display of the differential pressure gauge 6 becomes small. 2, the degree of cleaning can be recognized well, and the differential pressure Become completely state intima 2 is washed in a state where the scale of 6 reaches a predetermined value, is capable to complete the cleaning by stopping the operation of the pump 7 and the blower 4 in this state.
【0006】このように膜2内に強制的に薬剤を通して
吸引しながら確実に膜2を洗浄することができるもので
ある。なお、洗浄が終了した後には前記薬液8を中和さ
せて、その後に中和させた薬液を放流させることがで
き、放流後に槽1内に汚泥54を入れて活性汚泥による
浄化処理を行うことができるものである。なお、槽1は
予め薬液8を満たした別体の槽であっても、同様に膜2
内を完全に洗浄することができるものであり、膜2は洗
浄後に槽1から引き上げて所定の処理槽へ戻すことがで
きるものである。As described above, the membrane 2 can be surely washed while forcibly sucking the medicine into the membrane 2. After the washing is completed, the chemical solution 8 can be neutralized, and then the neutralized chemical solution can be discharged. After the discharge, the sludge 54 is put into the tank 1 and the purification treatment with activated sludge is performed. Can be done. Even if the tank 1 is a separate tank previously filled with the chemical solution 8, the tank 2
The inside can be completely washed, and the membrane 2 can be pulled out of the tank 1 after washing and returned to a predetermined processing tank.
【0007】[0007]
【発明の効果】本発明は、槽内に薬液を満たし、槽の底
側には散気管を配設し、該散気管の上方に薬液中に浸漬
させた状態で膜を配設し、該膜にポンプを有する配管を
接続し、前記散気管から噴出させた泡を前記膜に当てな
がら前記ポンプにより膜内を通し薬液を吸引し、吸引し
た薬液を前記槽内に循環させることとしたため、膜に対
し散気管から泡を噴出させて、またポンプにより膜内に
強制的に薬液が循環されて、泡と薬液により確実に膜内
を洗浄することができ、洗浄力が強力で、膜の洗浄を完
全に行うことができる効果を有する。According to the present invention, a tank is filled with a chemical solution, an air diffuser is disposed at the bottom of the tank, and a film is disposed above the air diffuser in a state of being immersed in the chemical liquid. A pipe having a pump is connected to the membrane, and a chemical solution is sucked through the membrane by the pump while the foam ejected from the air diffuser is applied to the membrane, and the sucked chemical solution is circulated in the tank. Bubbles are blown out from the air diffuser to the membrane, and a chemical solution is forcibly circulated in the membrane by the pump, so that the inside of the membrane can be reliably washed with the bubbles and the chemical solution, and the cleaning power is strong. This has the effect that cleaning can be performed completely.
【0008】また、前記配管内に差圧計を設け、該差圧
計により前記膜の洗浄度合いをチェックすることとした
ため、膜の洗浄度合いを差圧計を見ながら良好にチェッ
クすることができ、洗浄の完了時を正確に把握して洗浄
作業を良好に行うことができる効果を有する。Further, since a differential pressure gauge is provided in the pipe and the degree of cleaning of the membrane is checked by the differential pressure gauge, the degree of cleaning of the membrane can be checked satisfactorily while looking at the differential pressure gauge. This has the effect that the completion time can be accurately grasped and the cleaning operation can be performed satisfactorily.
【図1】膜の洗浄装置の概略構成図である。FIG. 1 is a schematic configuration diagram of an apparatus for cleaning a film.
【図2】従来の処理槽内に配設された膜の概略構成図で
ある。FIG. 2 is a schematic configuration diagram of a film provided in a conventional processing tank.
【図3】処理槽内から汚泥を抜いて処理槽内に薬液を満
たした状態の概略構成図である。FIG. 3 is a schematic configuration diagram of a state in which sludge is extracted from the inside of a processing tank and the inside of the processing tank is filled with a chemical solution.
【図4】その後に薬液を中和して排出する状態の概略構
成図である。FIG. 4 is a schematic configuration diagram of a state in which a chemical solution is neutralized and discharged thereafter.
【図5】再び処理槽内に汚泥を入れた状態の概略構成図
である。FIG. 5 is a schematic configuration diagram of a state in which sludge is again put into the processing tank.
【図6】別の薬液槽を設けた概略構成図である。FIG. 6 is a schematic configuration diagram in which another chemical solution tank is provided.
【図7】処理槽内の膜を別体の薬液槽内に移す状態の概
略構成図である。FIG. 7 is a schematic configuration diagram of a state in which a film in a processing tank is transferred into a separate chemical liquid tank.
【図8】別体の薬液槽内で膜を放置させる状態の概略構
成図である。FIG. 8 is a schematic configuration diagram of a state in which a film is left in a separate chemical solution tank.
【図9】洗浄後に薬液槽から再び処理槽内へ膜を移し変
える状態の概略構成図である。FIG. 9 is a schematic configuration diagram of a state in which a film is transferred from a chemical solution tank to a processing tank again after cleaning.
1 槽 2 膜 3 散気管 4 ブロア 5 配管 6 差圧計 7 ポンプ 8 薬液 1 tank 2 membrane 3 air diffuser 4 blower 5 pipe 6 differential pressure gauge 7 pump 8 chemical
Claims (2)
管を配設し、該散気管の上方に薬液中に浸漬させた状態
で膜を配設し、該膜にポンプを有する配管を接続し、前
記散気管から噴出させた泡を前記膜に当てながら前記ポ
ンプにより膜内を通し薬液を吸引し、吸引した薬液を前
記槽内に循環させることを特徴とする膜の薬液洗浄方
法。A tank is filled with a chemical solution, an air diffuser is provided at the bottom side of the tank, a membrane is provided above the air diffuser in a state of being immersed in the chemical, and a pump is provided to the membrane. Connecting a pipe having a chemical solution to the membrane by sucking a chemical solution through the membrane by the pump while applying bubbles ejected from the air diffuser to the membrane, and circulating the sucked chemical solution into the tank. Cleaning method.
より前記膜の洗浄度合いをチェックすることを特徴とす
る請求項1に記載の膜の薬液洗浄方法。2. The method according to claim 1, wherein a differential pressure gauge is provided in the pipe, and the degree of cleaning of the film is checked by the differential pressure gauge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27388197A JPH1190189A (en) | 1997-09-19 | 1997-09-19 | Method for cleaning membrane with liquid chemical |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27388197A JPH1190189A (en) | 1997-09-19 | 1997-09-19 | Method for cleaning membrane with liquid chemical |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1190189A true JPH1190189A (en) | 1999-04-06 |
Family
ID=17533882
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27388197A Pending JPH1190189A (en) | 1997-09-19 | 1997-09-19 | Method for cleaning membrane with liquid chemical |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH1190189A (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010058120A (en) * | 2004-12-24 | 2010-03-18 | Siemens Water Technologies Corp | Cleaning in membrane filtration system |
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 |
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 |
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 |
-
1997
- 1997-09-19 JP JP27388197A patent/JPH1190189A/en active Pending
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010058120A (en) * | 2004-12-24 | 2010-03-18 | Siemens Water Technologies Corp | Cleaning in membrane filtration system |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US8894858B1 (en) | 2005-08-22 | 2014-11-25 | Evoqua Water Technologies Llc | Method and assembly for water filtration using a tube manifold to minimize backwash |
US8858796B2 (en) | 2005-08-22 | 2014-10-14 | Evoqua Water Technologies Llc | Assembly for water filtration using a tube manifold to minimise backwash |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
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 |
US8840783B2 (en) | 2007-05-29 | 2014-09-23 | Evoqua Water Technologies Llc | Water treatment membrane cleaning with pulsed airlift pump |
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 |
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 |
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 |
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 |
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 |
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 |
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