JPH09108548A - Immersion type membrane separator - Google Patents

Immersion type membrane separator

Info

Publication number
JPH09108548A
JPH09108548A JP29379295A JP29379295A JPH09108548A JP H09108548 A JPH09108548 A JP H09108548A JP 29379295 A JP29379295 A JP 29379295A JP 29379295 A JP29379295 A JP 29379295A JP H09108548 A JPH09108548 A JP H09108548A
Authority
JP
Japan
Prior art keywords
tank
cleaning
membrane module
sludge
membrane
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP29379295A
Other languages
Japanese (ja)
Inventor
Kunihiro Iwasaki
邦博 岩崎
Kensuke Matsui
謙介 松井
Kazuo Suzuki
和夫 鈴木
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 JP29379295A priority Critical patent/JPH09108548A/en
Publication of JPH09108548A publication Critical patent/JPH09108548A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To perform cleaning of a membrane module immersed in water held in a bioreaction tank in which activated sludge is floated without being inhibited by activated sludge. SOLUTION: The immersion type membrane separator consists of a bioreaction tank 10 in which a membrane module 12 is immersed, a cleaning tank 16 for cleaning the membrane module and a transfer means 17 for transferring the membrane module between the bioreaction tank and the cleaning tank. Fine particles 22 for cleaning and an ultrasonic vibrator are provided in the inside of the cleaning tank or either of both is provided therein.

Description

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

【0001】[0001]

【発明の属する技術分野】この発明は、活性汚泥が浮遊
する生物反応槽の水中に、膜モジュールを浸漬し、生物
反応槽に供給される有機物を含む原水中の有機物を活性
汚泥で分解し、原水中の膜を透過する透過水を膜モジュ
ールの内部から採水する浸漬型膜分離装置に関する。
TECHNICAL FIELD The present invention relates to a method of immersing a membrane module in water of a biological reaction tank in which activated sludge floats, decomposing organic matter in raw water containing organic matter supplied to the biological reaction vessel with the activated sludge, The present invention relates to an immersion type membrane separation device that collects permeated water that permeates a membrane in raw water from the inside of a membrane module.

【0002】[0002]

【従来の技術】膜モジュールを浸漬した生物反応槽の底
部に散気管を敷設し、散気管が噴出する気泡で構内を浮
遊する活性汚泥の活性を高めると共に、気泡のエアリフ
ト作用で膜モジュールの膜に接触して上昇する上昇流を
生じさせ、気泡の剪断力により汚泥や、未分解の有機
物、分解過程で発生した中間代謝物(以下、これ等を総
称して汚泥等とも記す。)が膜の表面に付着するのを抑
制しながら膜濾過を行い、膜を透過した透過水を膜モジ
ュールの内部からポンプで吸引して採水することは従来
から行われている。このようにして汚泥などが膜の表面
に付着するのを抑制しながら膜濾過を行っても、運転の
継続によって膜の表面には次第に汚泥等が付着、蓄積
し、濾過抵抗が増大する。このため、生物反応槽の水中
に微小粒子を懸濁し、散気管が噴出する気泡によってそ
の微小粒子を水中で流動化し、微小粒子が膜に衝突する
衝撃で膜面に付着する汚泥等を剥離したり、膜モジュー
ルに超音波振動板を取付け、振動板により膜面に微振動
を与え、膜面に付着する汚泥等を剥離したりしている。
2. Description of the Related Art An air diffusing pipe is laid at the bottom of a biological reaction tank in which a membrane module is immersed to enhance the activity of activated sludge suspended in the premises by air bubbles ejected from the air diffusing pipe. A sludge, undecomposed organic matter, and intermediate metabolites generated during the decomposition process (hereinafter, also collectively referred to as sludge, etc.) are formed into a film by causing an ascending upward flow by contact with the sludge. It has been conventionally practiced to carry out membrane filtration while suppressing adhesion to the surface of the membrane, and to draw permeated water that has permeated through the membrane by pumping from inside the membrane module. In this way, even if membrane filtration is performed while suppressing sludge and the like from adhering to the surface of the membrane, sludge and the like gradually adhere to and accumulate on the surface of the membrane due to continuous operation, and filtration resistance increases. Therefore, the microparticles are suspended in the water of the biological reaction tank, and the air bubbles ejected from the air diffuser fluidize the microparticles in the water, and the sludge that adheres to the membrane surface is peeled off by the impact of the microparticles colliding with the membrane. Alternatively, an ultrasonic vibrating plate is attached to the membrane module, and the vibrating plate gives a slight vibration to the membrane surface to remove sludge and the like adhering to the membrane surface.

【0003】[0003]

【発明が解決しようとする課題】しかし、生物反応槽内
に微小粒子を懸濁すると、槽内の汚泥濃度が高まったと
き、その濃度を下げて定常にする汚泥の引き抜き時に、
汚泥に混ざって微小粒子も排出され、減少するので、そ
の都度、微小粒子を補給しなければならない。又、汚泥
と一緒に排出された微小粒子を再使用するために回収し
ようとしても、汚泥と分離することが困難である。更
に、生物反応槽内で微小粒子を流動化しても、槽内の水
中には多量の活性汚泥が浮遊しているので微小粒子は活
性汚泥にも衝突するため、膜への衝突力が弱まったり、
衝突回数が減少し、汚泥などの剥離効果を充分に果せな
い。超音波振動板を膜モジュールに取付けた場合は、振
動が水中に浮遊する多量の活性汚泥に吸収される。この
ため、振動が膜面に充分に伝わりにくゝ、矢張り汚泥な
どの剥離効果を充分に果すことができない。又、生物反
応槽内に複数の膜モジュールを浸漬した場合は、各膜モ
ジュールに対応した複数の振動板を必要とし、構造が複
雑になる。
However, when fine particles are suspended in the biological reaction tank, when the sludge concentration in the tank is increased, when the sludge is pulled out to lower the concentration to make it stationary,
The fine particles are mixed with the sludge and are also discharged and reduced. Therefore, the fine particles must be replenished each time. Further, even if the fine particles discharged together with the sludge are to be recovered for reuse, it is difficult to separate them from the sludge. Furthermore, even if the microparticles are fluidized in the biological reaction tank, a large amount of activated sludge floats in the water in the tank, so the microparticles also collide with the activated sludge, weakening the collision force on the membrane. ,
The number of collisions decreases, and the effect of removing sludge cannot be fully achieved. When the ultrasonic diaphragm is attached to the membrane module, the vibration is absorbed by a large amount of activated sludge suspended in water. Therefore, the vibration is not sufficiently transmitted to the film surface, and the effect of peeling off the arrow sludge cannot be sufficiently exerted. Further, when a plurality of membrane modules are immersed in the biological reaction tank, a plurality of diaphragms corresponding to the respective membrane modules are required, and the structure becomes complicated.

【0004】[0004]

【課題を解決するための手段】本発明は、上述した問題
点を解消するために開発されたもので、膜モジュールを
浸漬した生物反応槽と、膜モジュールを洗浄するための
洗浄槽と、生物反応槽と洗浄槽との間で膜モジュールを
移動させる移動手段とからなり、前記洗浄槽の内部に洗
浄用小粒子と、超音波振動子の両方、又はどちらかを設
けたことを特徴とする。
The present invention was developed in order to solve the above-mentioned problems. It is a biological reaction tank in which a membrane module is immersed, a cleaning tank for cleaning the membrane module, and an organism. It comprises a moving means for moving the membrane module between the reaction tank and the cleaning tank, and the cleaning small particles and / or the ultrasonic vibrator are provided inside the cleaning tank. .

【0005】[0005]

【発明の実施の形態】図示の各実施形態において、10
は原水として有機性の廃水がポンプP1 、供給管11に
より供給される生物反応槽で、活性汚泥が多量に浮遊す
る槽内の水中にはMF膜や、UF膜などを有する膜モジ
ュール12が浸漬してあり、槽底には原水中の有機物を
活性汚泥で好気的に生物処理するためと、膜モジュール
12の膜に接触して上昇するエアリフト上向流を槽内の
原水に生じさせ、気泡の剪断力で汚泥等が膜の表面に付
着するのを防止するため、ブロアB1 からの送風を気泡
として噴出する散気管13が敷設してある。又、膜モジ
ュール12には吸引ポンプP2 を接続した採水管14を
連結し、膜モジュールの膜を透過した透過水を吸引ポン
プで吸引して採水する。生物反応槽10は、図面では地
面を掘り下げて構築してある。又、膜モジュールは槽底
に設けた架台(図示せず)の上に設置し、散気管13か
ら上に離す。図では膜モジュールを2台設置し、各膜モ
ジュールは枝管15で採水管14に接続する。
BEST MODE FOR CARRYING OUT THE INVENTION In each of the illustrated embodiments, 10
Is a biological reaction tank in which organic wastewater is supplied as raw water by a pump P1 and a supply pipe 11, and a membrane module 12 having an MF membrane or a UF membrane is immersed in water in the tank in which a large amount of activated sludge floats. In order to aerobically bioprocess organic matter in the raw water with activated sludge at the bottom of the tank, an upward flow of an air lift that rises in contact with the membrane of the membrane module 12 is generated in the raw water in the tank. In order to prevent sludge and the like from adhering to the surface of the membrane due to the shearing force of the bubbles, an air diffuser 13 is installed which blows the air blown from the blower B1 as bubbles. Further, a water sampling pipe 14 connected to a suction pump P2 is connected to the membrane module 12, and the permeated water that has permeated the membrane of the membrane module is sucked by the suction pump to collect water. The biological reaction tank 10 is constructed by digging down the ground in the drawing. Further, the membrane module is installed on a pedestal (not shown) provided on the bottom of the tank and separated from the air diffuser 13 upward. In the figure, two membrane modules are installed, and each membrane module is connected to the water sampling pipe 14 by a branch pipe 15.

【0006】生物反応槽10の傍の地上には膜モジュー
ルを浸漬することができる洗浄槽16を設けると共に、
生物反応槽10と洗浄槽16の上を一連に横切る門形フ
レーム18を地上に立設し、門形フレームの上部横梁1
9に沿って電動ホイスト20を移動可能に設ける。門形
フレーム18、電動ホイスト20は生物反応槽10と洗
浄槽16との間で膜モジュール12を移動させる移動手
段17を構成する。洗浄槽の底部にもブロアB2 からの
送風を気泡として噴出する散気管21が敷設してある。
A cleaning tank 16 capable of immersing the membrane module is provided on the ground near the biological reaction tank 10, and
A gate-shaped frame 18 that crosses the biological reaction tank 10 and the cleaning tank 16 in series is erected on the ground.
An electric hoist 20 is provided so as to be movable along 9. The gate-shaped frame 18 and the electric hoist 20 constitute a moving means 17 for moving the membrane module 12 between the biological reaction tank 10 and the cleaning tank 16. An air diffuser 21 is also installed at the bottom of the cleaning tank to eject the air blown from the blower B2 as bubbles.

【0007】生物反応槽内の膜モジュールを洗浄槽に浸
漬するには、採水管14と接続した枝管15の途中の弁
を閉じ、弁より下のフランジ接合を外して枝管の上下を
切り離し、電動ホイストを生物反応槽中の膜モジュール
の真上に移動し、電動ホイストの吊下げ、吊下げ用のロ
ープ20´を降ろしてその下端のフックを膜モジュール
に連結し、ロープを巻取って膜モジュールを吊上げると
共に、電動ホイストを洗浄槽上に移動し、ロープを降ろ
して膜モジュールを洗浄槽中に浸漬したのちフックを膜
モジュールから外し、ロープを引上げる。洗浄槽内にも
架台(図示せず)を設け、その上に膜モジュールを載せ
て散気管21から上に離す。洗浄槽内の膜モジュールを
生物反応槽内に浸漬するには前述した移動操作を逆に行
い、枝管15の上下を接合すればよい。
To immerse the membrane module in the biological reaction tank in the cleaning tank, the valve in the middle of the branch pipe 15 connected to the water sampling pipe 14 is closed, and the flange joint below the valve is removed to separate the upper and lower parts of the branch pipe. , Move the electric hoist directly above the membrane module in the biological reaction tank, hang the electric hoist, lower the hanging rope 20 ', connect the hook at the lower end to the membrane module, and wind the rope. While lifting the membrane module, the electric hoist is moved onto the washing tank, the rope is lowered to immerse the membrane module in the washing tank, the hook is removed from the membrane module, and the rope is pulled up. A pedestal (not shown) is also provided in the cleaning tank, and the membrane module is placed on the pedestal and separated from the air diffusing pipe 21. In order to immerse the membrane module in the cleaning tank in the biological reaction tank, the above-described moving operation may be performed in reverse, and the upper and lower sides of the branch pipe 15 may be joined.

【0008】図1の第1実施形態では、洗浄槽内に粒径
0.5〜5.0mmの微小粒子22を懸濁させ、散気管
21が噴出する気泡で流動させる。洗浄は薬液による洗
浄と、水によるリンスを行う。洗浄を行うには、例えば
洗浄槽内で次亜塩素酸ソーダ(0.05%)を調整し、
そのpHを苛性ソーダでpH12とし、薬液中に平均直
径3mm、比重1.1の合成樹脂製微小粒子を5kg投
入した。尚、洗浄槽の寸法を長さ1.5m、幅0.5
m、深さ2.0mで、有効水深は1.5mである。そし
て、散気管21が噴出する気泡で上記微小粒子を流動さ
せる。そして、生物反応槽中の汚染された膜モジュール
を洗浄槽に数時間浸漬する。洗浄槽の液中の汚泥は、膜
モジュールの膜面から剥離した微細なものだけで、その
汚泥濃度は、活性汚泥が多量に浮遊する生物反応槽内の
汚泥濃度の1/10〜1/100である。このため、洗
浄槽中で微小粒子は汚泥に阻害されることなく流動し、
強く膜面に衝突して膜面に付着する汚泥などを効果的に
剥離する。
In the first embodiment shown in FIG. 1, fine particles 22 having a particle size of 0.5 to 5.0 mm are suspended in the cleaning tank and are caused to flow by the bubbles ejected from the air diffuser 21. The cleaning is performed by cleaning with a chemical solution and rinsing with water. For cleaning, for example, adjust sodium hypochlorite (0.05%) in a cleaning tank,
The pH was adjusted to 12 with caustic soda, and 5 kg of synthetic resin fine particles having an average diameter of 3 mm and a specific gravity of 1.1 were added to the chemical solution. The size of the cleaning tank is 1.5 m in length and 0.5 in width.
m, depth 2.0 m, effective water depth 1.5 m. Then, the fine particles are caused to flow by the bubbles ejected from the air diffuser 21. Then, the contaminated membrane module in the biological reaction tank is immersed in the cleaning tank for several hours. The sludge in the liquid in the cleaning tank is only the fine ones separated from the membrane surface of the membrane module, and the sludge concentration is 1/10 to 1/100 of the sludge concentration in the biological reaction tank in which a large amount of activated sludge floats. Is. Therefore, the fine particles flow in the washing tank without being obstructed by sludge,
Effectively peels sludge and the like that strongly collides with the membrane surface and adheres to the membrane surface.

【0009】次いで、微小粒子が通過し得ない目開きの
スクリーン23を通じ洗浄槽内の洗浄廃液を槽外に排出
管24で排出する。これにより膜面からの剥離物は水と
一緒にスクリーンを通って排出され、槽内には微小粒子
22が全量保持される。それから洗浄槽に水を張り、散
気管21からの気泡で微小粒子を流動しながら膜モジュ
ールを水洗する。水洗が完了したら洗浄槽の水を排出
し、水洗済みの膜モジュールを生物反応槽に移動して浸
漬する。洗浄槽内に残った微小粒子は、その後の膜モジ
ュールの洗浄に繰返して使用することができる。
Then, the cleaning waste liquid in the cleaning tank is discharged to the outside of the tank through a discharge pipe 24 through an opening screen 23 through which fine particles cannot pass. As a result, the exfoliated substances from the film surface are discharged together with water through the screen, and all the fine particles 22 are retained in the tank. Then, the washing tank is filled with water, and the membrane module is washed while flowing the fine particles by the bubbles from the air diffuser 21. When the washing with water is completed, the water in the washing tank is discharged, and the washed membrane module is moved to and immersed in the biological reaction tank. The fine particles remaining in the cleaning tank can be repeatedly used for subsequent cleaning of the membrane module.

【0010】又、微小粒子22として、平均直径3m
m、比重0.96の合成樹脂製のものを使用すると、浮
上性であるため、洗浄後に散気管21の散気を止めて静
置すると、微小粒子は水面に浮上し、汚泥などの剥離物
は沈降する。従って、スクリーン23を使用することな
く微小粒子を回収して反復使用できる。
The fine particles 22 have an average diameter of 3 m.
When a synthetic resin having a specific gravity of 0.96 and a specific gravity of 0.96 is used, it is buoyant. Therefore, if the diffusing pipe 21 is stopped and left standing after washing, the fine particles float on the surface of the water, and sludge and other debris. Will settle. Therefore, the fine particles can be recovered and repeatedly used without using the screen 23.

【0011】図2の第2実施形態では、洗浄槽内に周波
数コントローラ26により制御できる超音波振動板25
を1基浸漬設置し、散気管21が噴出する気泡によるエ
アリフト循環流と、振動板による振動攪拌流との相乗効
果により洗浄する。洗浄は、薬液による洗浄と、水によ
るリンスを行う。洗浄を行うには、例えば洗浄槽内で次
亜塩素酸ソーダ(0.05%)を調整し、そのpHを苛
性ソーダでpH12にする。そして、生物反応槽中の汚
染された膜モジュールを洗浄槽に数時間浸漬し、その
間、散気管21から気泡を噴出し、振動板25から液に
低周波数(10〜60Hz)の振動を与え、気泡による
エアリフト循環流と、振動板による振動攪拌流との相乗
効果で膜モジュールの膜面に付着する汚泥等の付着物を
剥離する。洗浄槽の液中の汚泥は、膜モジュールの膜面
から剥離した微細なものだけで、その汚泥濃度は、活性
汚泥が多量に浮遊する生物反応槽内の汚泥濃度の1/1
0〜1/100である。従って、振動板からの振動は汚
泥に吸収されず、膜面に付着する汚泥を効果的に剥離す
る。
In the second embodiment of FIG. 2, an ultrasonic vibrating plate 25 that can be controlled by a frequency controller 26 in the cleaning tank.
1 is installed by immersion, and washing is performed by the synergistic effect of the air lift circulation flow due to the bubbles ejected from the air diffusing pipe 21 and the vibration stirring flow due to the vibrating plate. For cleaning, cleaning with a chemical solution and rinsing with water are performed. To perform the cleaning, for example, sodium hypochlorite (0.05%) is adjusted in a cleaning tank, and the pH is adjusted to 12 with caustic soda. Then, the contaminated membrane module in the biological reaction tank is dipped in the cleaning tank for several hours, during which air bubbles are ejected from the air diffuser 21 and vibration of the diaphragm 25 at a low frequency (10 to 60 Hz) is applied to the liquid. The synergistic effect of the air lift circulation flow due to the air bubbles and the vibrating stirring flow due to the vibrating plate separates adhered substances such as sludge adhering to the membrane surface of the membrane module. The sludge in the liquid in the cleaning tank is only the fine ones separated from the membrane surface of the membrane module, and the sludge concentration is 1/1 of the sludge concentration in the biological reaction tank in which a large amount of activated sludge floats.
It is 0 to 1/100. Therefore, the vibration from the diaphragm is not absorbed by the sludge, and the sludge adhering to the film surface is effectively separated.

【0012】次いで、洗浄槽の廃洗浄液を剥離した汚泥
と一緒に排水管24で槽外に排出し、それから洗浄槽に
水を張り、散気と振動で再び膜モジュールを水洗し、水
洗が完了したら洗浄槽の水を排出し、水洗済みの膜モジ
ュールを生物反応槽に移動して浸漬する。
Then, the waste cleaning liquid in the cleaning tank is discharged outside the tank together with the separated sludge through the drainage pipe 24, and then the cleaning tank is filled with water, and the membrane module is again rinsed with aeration and vibration to complete the washing with water. After that, the water in the washing tank is discharged, and the membrane module that has been washed with water is moved to and immersed in the biological reaction tank.

【0013】上述した実施形態では、洗浄槽の内部に、
洗浄用微小粒子と、超音波振動子のどちらか一方を設け
たもので説明した。しかし、洗浄槽の内部に洗浄用微小
粒子と、超音波振動子の両方を設けてもよい。この場合
は、両方の相乗効果により洗浄効果のさらなる向上が図
れる。
In the above-mentioned embodiment, inside the cleaning tank,
The description has been given on the case where either one of the cleaning fine particles and the ultrasonic transducer is provided. However, both the cleaning fine particles and the ultrasonic vibrator may be provided inside the cleaning tank. In this case, the synergistic effect of both can further improve the cleaning effect.

【0014】[0014]

【発明の効果】以上で明らかなように、本発明に依れ
ば、膜面に汚泥などが付着して汚染された膜モジュール
を、汚泥濃度が高い生物反応槽から引上げ、汚泥濃度が
希薄な洗浄槽に浸漬して洗浄するので、水中に浮遊する
汚泥によって薬液洗浄や、水洗が阻害されない。
As is apparent from the above, according to the present invention, a membrane module having a membrane surface contaminated with sludge or the like is pulled up from a biological reaction tank having a high sludge concentration to reduce the sludge concentration. Since it is immersed in a cleaning tank for cleaning, sludge floating in water does not interfere with chemical cleaning and water cleaning.

【0015】つまり、微小粒子を流動して洗浄する場合
は、粒子を流動するエアリフト循環流の流速が大になる
ので比重の大きな粒子を均一に流動することができる。
そして、その粒子は洗浄槽中で汚泥に衝突することが少
ないため膜面への有効衝突回数が増加し、膜面の付着物
を有効に剥離する。又、洗浄で剥離した汚泥から微小粒
子を分離すればよいので、微小粒子の分離、回収が容易
であると共に、微小粒子の消耗が無いので使用量は少な
くて済む。
That is, when the fine particles are washed by flowing, the flow rate of the air lift circulating flow for flowing the particles is high, so that the particles having a large specific gravity can be uniformly flowed.
Since the particles rarely collide with sludge in the cleaning tank, the number of effective collisions with the film surface increases, and the deposits on the film surface are effectively separated. Further, since it is only necessary to separate the fine particles from the sludge separated by washing, the fine particles can be easily separated and collected, and since the fine particles are not consumed, the usage amount can be small.

【0016】超音波振動による洗浄の場合は、振動が汚
泥に吸収されないため、強い振動攪拌流を生起でき、振
動が膜面に伝わるので付着する汚泥等を有効に剥離でき
る。又、洗浄槽に超音波振動板を1基設置するだけでよ
い。
In the case of cleaning by ultrasonic vibration, since vibration is not absorbed by sludge, a strong vibration stirring flow can be generated, and vibration is transmitted to the membrane surface, so that sludge and the like that adhere can be effectively separated. Further, it suffices to install only one ultrasonic vibration plate in the cleaning tank.

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

【図1】第1実施形態の説明図である。FIG. 1 is an explanatory diagram of a first embodiment.

【図2】第2実施形態の説明図である。FIG. 2 is an explanatory diagram of a second embodiment.

【符号の説明】[Explanation of symbols]

10 生物反応槽 11 原水の供給管 12 膜モジュール 13 散気管 14 採水管 15 分岐管 16 洗浄槽 17 膜モジュールの移動手段 18 門形フレーム 19 門形フレームの上部横梁 20 電動ホイスト 21 散気管 22 微小粒子 25 超音波振動板 25 超音波振動板の周波数コントローラ 10 Bioreaction tank 11 Raw water supply pipe 12 Membrane module 13 Diffuser pipe 14 Water sampling pipe 15 Branch pipe 16 Washing tank 17 Means for moving membrane module 18 Gate frame 19 Upper horizontal beam of gate frame 20 Electric hoist 21 Air diffuser 22 Micro particles 25 Ultrasonic Vibration Plate 25 Ultrasonic Vibration Plate Frequency Controller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 膜モジュールを浸漬した生物反応槽と、
膜モジュールを洗浄するための洗浄槽と、生物反応槽と
洗浄槽との間で膜モジュールを移動させる移動手段とか
らなり、前記洗浄槽の内部に洗浄用微小粒子と、超音波
振動子の両方、又はどちらかを設けたことを特徴とする
浸漬型膜分離装置。
1. A biological reaction tank in which a membrane module is immersed,
A cleaning tank for cleaning the membrane module, and a moving means for moving the membrane module between the biological reaction tank and the cleaning tank, both of the cleaning microparticles and the ultrasonic transducer inside the cleaning tank. Or a submerged membrane separation device, characterized in that either one is provided.
JP29379295A 1995-10-18 1995-10-18 Immersion type membrane separator Pending JPH09108548A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29379295A JPH09108548A (en) 1995-10-18 1995-10-18 Immersion type membrane separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29379295A JPH09108548A (en) 1995-10-18 1995-10-18 Immersion type membrane separator

Publications (1)

Publication Number Publication Date
JPH09108548A true JPH09108548A (en) 1997-04-28

Family

ID=17799228

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29379295A Pending JPH09108548A (en) 1995-10-18 1995-10-18 Immersion type membrane separator

Country Status (1)

Country Link
JP (1) JPH09108548A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000024469A (en) * 1998-07-10 2000-01-25 Kubota Corp Device for cleaning membrane cartridge with liquid chemical
JP2002320979A (en) * 2001-04-27 2002-11-05 Sharp Corp Method and system for treating metal-containing drainage
KR100360375B1 (en) * 2000-10-24 2002-11-13 재단법인 포항산업과학연구원 Apparatus and method for sludge separation and membrane cleaning
JP2008161807A (en) * 2006-12-28 2008-07-17 Kuraray Co Ltd Filtering device
WO2009011309A1 (en) * 2007-07-18 2009-01-22 Yuasa Membrane Systems Co., Ltd. Membrane separation apparatus and method of cleaning membrane element
JP2012183470A (en) * 2011-03-04 2012-09-27 Kubota Corp Hanging jig of membrane module, membrane module, and method of using hanging jig of membrane module
JP2021171732A (en) * 2020-04-28 2021-11-01 ダイセン・メンブレン・システムズ株式会社 Waste water treatment system and method for operating the same
WO2022145132A1 (en) * 2020-12-28 2022-07-07 株式会社流機エンジニアリング Filtration system and filtration method
WO2023132146A1 (en) * 2022-01-06 2023-07-13 株式会社デンソー Water treatment device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000024469A (en) * 1998-07-10 2000-01-25 Kubota Corp Device for cleaning membrane cartridge with liquid chemical
KR100360375B1 (en) * 2000-10-24 2002-11-13 재단법인 포항산업과학연구원 Apparatus and method for sludge separation and membrane cleaning
JP2002320979A (en) * 2001-04-27 2002-11-05 Sharp Corp Method and system for treating metal-containing drainage
JP2008161807A (en) * 2006-12-28 2008-07-17 Kuraray Co Ltd Filtering device
WO2009011309A1 (en) * 2007-07-18 2009-01-22 Yuasa Membrane Systems Co., Ltd. Membrane separation apparatus and method of cleaning membrane element
JP2016198770A (en) * 2007-07-18 2016-12-01 株式会社ユアサメンブレンシステム Membrane separator
JP6043465B2 (en) * 2007-07-18 2016-12-14 株式会社ユアサメンブレンシステム Membrane separation apparatus and membrane element cleaning method
JP2012183470A (en) * 2011-03-04 2012-09-27 Kubota Corp Hanging jig of membrane module, membrane module, and method of using hanging jig of membrane module
JP2021171732A (en) * 2020-04-28 2021-11-01 ダイセン・メンブレン・システムズ株式会社 Waste water treatment system and method for operating the same
WO2022145132A1 (en) * 2020-12-28 2022-07-07 株式会社流機エンジニアリング Filtration system and filtration method
JP2022104288A (en) * 2020-12-28 2022-07-08 株式会社流機エンジニアリング Filtration system and filtration method
WO2023132146A1 (en) * 2022-01-06 2023-07-13 株式会社デンソー Water treatment device

Similar Documents

Publication Publication Date Title
JP4421256B2 (en) Filtration unit, method for installing the filtration unit, and filtration device
JP2000189958A (en) Immersion type membrane filter device
JP2008272671A (en) Integrated type solid/liquid separation system and filter apparatus
JPH1128467A (en) Immersion type membrane separation device
JPH09108548A (en) Immersion type membrane separator
JP3123407B2 (en) Immersion type membrane separation device
JP2000167555A (en) Cleaning of immersion membrane
JPH02237693A (en) Sewage treating device
JP2000317482A (en) Fluidization separator for carrier
JP2002263696A (en) Washing apparatus
KR101204395B1 (en) The apparatus to treat municipal and industrial wastewater
JP2000185279A (en) Sewage treatment method and apparatus
JP3480050B2 (en) Immersion type membrane separation device
JP5294555B2 (en) Sewage treatment equipment
JP2001029975A (en) Carrier stirring and separating apparatus
JP3191559B2 (en) Solid-liquid separation device
JP2008142603A (en) Sewage treatment device
KR100761457B1 (en) Sedimentation apparatus
CN217377487U (en) Novel electrode air supporting device
JP2002186838A (en) Immersion type membrane separation device
CN220811942U (en) Novel micro-nano bubble high-efficiency air floatation machine device
JP2005013865A (en) Water purifying apparatus of closed type water circulating system
CN209989095U (en) High-efficient air supporting machine of rapid processing
JP2001310193A (en) Sewage treatment apparatus
CN215962268U (en) Sewage slow-release device