JPS61293504A - Separation device utilizing hollow yarn membrane - Google Patents

Separation device utilizing hollow yarn membrane

Info

Publication number
JPS61293504A
JPS61293504A JP13591485A JP13591485A JPS61293504A JP S61293504 A JPS61293504 A JP S61293504A JP 13591485 A JP13591485 A JP 13591485A JP 13591485 A JP13591485 A JP 13591485A JP S61293504 A JPS61293504 A JP S61293504A
Authority
JP
Japan
Prior art keywords
holding plate
air
module
filtration module
plate
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
JP13591485A
Other languages
Japanese (ja)
Other versions
JPH0234648B2 (en
Inventor
Hiroshi Fukuhara
福原 博
Hiroshi Saito
浩 斉藤
Masahiro Furukawa
征弘 古川
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 JP13591485A priority Critical patent/JPS61293504A/en
Publication of JPS61293504A publication Critical patent/JPS61293504A/en
Publication of JPH0234648B2 publication Critical patent/JPH0234648B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/20Accessories; Auxiliary operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/18Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/04Hollow fibre modules comprising multiple hollow fibre assemblies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/18Use of gases
    • B01D2321/185Aeration

Landscapes

  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To remove contaminants sticking to the external surface of hollow yarn effectively, by fixing a holding plate provided with a fitting port surrounding a foot end of each filter module, and providing also a downwardly directed cylinder to an external edge of a bottom surface of the holding plate. CONSTITUTION:Many holes arranged coincidently to filter modules 5 are bored to a separating plate 2 and a holding plate 6, and a short cylindrical piece is fitted as fitting piece 15 to each hole of the holding plate 6. A foot end board 14 of the module 5 is fitted to the fitting piece 15 and the top end is fixed to the hole in the separating plate 2. In the stage of washing of the module 5, air is fed to the inside part surrounded by lower cylinders 8 of the holding plate 6 through an air feeding pipe 9. Almost whole amt. of the air is introduced evenly into the inside of the module 5 from through holes 14' on the foot end board 14, then, raised upward among the hollow yarns 12 removing thereby contaminants sticking to the external surface of the hollow yarn. By this method, flushing is performed efficiently in a short time with small amt. of air.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は中空糸を利用し友中空糸型膜分離装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a hollow fiber type membrane separation device using hollow fibers.

(従来の技術) 処理塔の上部に仕切板を設けて仕切板の止金集水室、下
を処理室とし、多数本の中空糸を多孔の保護筒内で集束
して構成しa濾過モジュールの上端を前記仕切板に固定
して処理室内に多数のろ過モジュールを吊設し、上記処
理室内に供給した原水を各濾過モジュールを構成する中
空糸の外面でろ過し、処理水を中空糸の中空内部を経て
前記集水室に得る外圧濾過式の中空糸型膜分離装置に従
来から公知である。
(Prior art) A filtration module is constructed by providing a partition plate at the top of the treatment tower, using a stopper on the partition plate as a water collection chamber, and a treatment chamber at the bottom, and converging a large number of hollow fibers in a porous protective cylinder. A large number of filtration modules are suspended in the processing chamber with their upper ends fixed to the partition plate, and the raw water supplied into the processing chamber is filtered by the outer surface of the hollow fibers constituting each filtration module, and the treated water is filtered through the hollow fibers. An external pressure filtration type hollow fiber type membrane separation device that obtains water into the water collection chamber through a hollow interior is conventionally known.

上記装置でろ過を行うと時間の経過にっn原水中の濁質
が中空糸の外面に捕捉さnて付着し、次第に濾過差圧が
高くなって濾過効率が低下するので定期的に、或は随時
に濾過全中断し、処理室内に下から空気を吹込み、この
空気と、処理室中の水とにより各濾過モジュールを構成
する夫々の中空糸の外面に付着した濁質を剥離(フラッ
シング〕し、次に処理室内から水を塔外に抜出して剥離
した濁質を処理室から除去する洗浄を行うことが必要で
ある。
When filtration is performed using the above device, as time passes, suspended matter in the raw water is captured and attached to the outer surface of the hollow fibers, and the filtration differential pressure gradually increases, reducing the filtration efficiency. At any time, the entire filtration is interrupted, air is blown into the processing chamber from below, and this air and water in the processing chamber are used to remove suspended matter adhering to the outer surface of each hollow fiber that makes up each filtration module (flushing). ] Then, it is necessary to carry out cleaning to remove the separated suspended solids from the processing chamber by extracting water from the processing chamber to the outside of the tower.

(発明が解決しようとする問題点〕 しかしながら従来装置では洗浄の之めに処理室内に下か
ら空気を吹込んでも、気泡は仕切板から吊下がった各濾
過モジュールの隣接間隔中を浮上し、多孔の保護筒で囲
in次モジュール内部に入って濾過モジュールを構成す
る個々の中空糸の外面に作用することが少ない友め、中
空糸外面に付着した濁質を剥離する7ラツンングに時間
を要し、且っ送気のための動力費も嵩む。
(Problem to be solved by the invention) However, in the conventional device, even if air is blown into the processing chamber from below for cleaning, air bubbles float up in the adjacent spaces between the filtration modules suspended from the partition plate, causing the porous Surrounded by a protective tube, the filter enters the inside of the module and rarely acts on the outer surface of the individual hollow fibers that make up the filtration module. , and the power cost for supplying air also increases.

(問題点を解決するための手段) そこで本発明は各濾過モジュールの下端を包囲する嵌合
口を備えた保持板を前記仕切板に対し下方に離して固定
することにより上記嵌合口を各濾過モジュールの下端に
嵌合し、上記保持板の下面外縁沿いに下向きの筒部を設
けると共に、前記処理室内下部には上記筒部で囲まれた
内部に洗浄用空気を供給する送気管を配設したことを特
徴とする。
(Means for Solving the Problems) Therefore, the present invention fixes a holding plate provided with a fitting opening that surrounds the lower end of each filtration module at a distance downward from the partition plate, so that the fitting opening can be connected to each filtration module. A cylindrical portion that fits into the lower end of the holding plate and faces downward along the outer edge of the lower surface of the holding plate is provided, and an air supply pipe that supplies cleaning air to the interior surrounded by the cylindrical portion is provided at the lower part of the processing chamber. It is characterized by

(作 用) 濾過は従来装置と同様に行うことができる。(for production) Filtration can be performed similarly to conventional devices.

そして、洗浄に際し、送気管から処理室内に空気を供給
すると気泡は保持板の下の筒部で囲まn友内部に集まり
、保持板の各嵌合口に嵌合し7j濾過モジユールの下端
から内部を浮上し、濾過モジュールを構成する中空糸の
外面に付着しfcgA’Xを効果的に剥離する。
During cleaning, when air is supplied into the processing chamber from the air supply pipe, air bubbles are surrounded by the cylindrical part under the holding plate and gather inside the chamber, and are fitted into the respective fitting holes of the holding plate to open the inside of the filtration module from the lower end of the filtration module. It floats up, adheres to the outer surface of the hollow fibers constituting the filtration module, and effectively peels off fcgA'X.

(実施例〕 図示の実施例において、/は処理塔、コは処理塔内上部
に設けらnてその上を集水室3、下を処理室グに区劃す
る仕切板、S・・・は上端を仕切板−に固定さnる処理
室内に吊設さfL2多数のろ過モジュール、6は保持板
、りは上記保持板を仕切板コの下方に離して固定するた
めのステー、gは上記保持板゛の下面外縁清いに下向き
に設けた筒部、デは上記筒部で囲まf′Lfc内部に洗
浄用空気全供給する送気管、10は保持板乙の下面に少
くとも上記筒部とと同等か、そILよりも長く下向きに
設けに通水管?示す。
(Embodiment) In the illustrated embodiment, / is a treatment tower, K is a partition plate provided at the upper part of the treatment tower, dividing the upper part into a water collection chamber 3, and the lower part into a treatment chamber group, S... is a large number of filtration modules suspended in the processing chamber, 6 is a holding plate, li is a stay for fixing the above-mentioned holding plate away from the bottom of the partition plate, g is A cylindrical portion is provided on the outer edge of the lower surface of the holding plate ``d'', D is surrounded by the cylindrical portion f'Lfc, and an air pipe for supplying all of the cleaning air into the inside, 10 is at least the cylindrical portion provided on the lower surface of the holding plate B. Is it the same as or is the water pipe installed downward and longer than the IL?

各濾過モジュールよは多孔の保護筒/lと、上記保護筒
の内部で集束さ几た多数本の中空糸/コ・・・と、保護
筒と中空糸の上下各端部を接着結合した保護筒よりも外
径が−回り大きな上端盤/J及び下端盤IQからなる。
Each filtration module has a porous protection tube/l, a large number of hollow fibers/coats converged inside the protection tube, and protection in which the protection tube and the upper and lower ends of the hollow fibers are adhesively bonded. It consists of an upper end plate /J and a lower end plate IQ whose outer diameter is larger than that of the cylinder.

上記両盤/3.1tii1:筒形のプラスチック製外枠
と、この外枠中に充填さnて硬化し、保護筒と中空糸の
各端部を結合するエポキシ樹脂などの接着層で形成さn
、保護筒の内部に集束さnfc各中空糸/コ・・・の上
部は上端盤/、3f貫通して上端盤の上面に開口し、下
端は保¥Ij筒の各端と同様に下端盤ll中で接着層に
ょシ塞がれる。尚、下端盤/ダは中空糸/2 =0.の
隣接間隔に上下方向の貫通孔/q′・・・を有する。
Both panels above / 3.1tii1: Made of a cylindrical plastic outer frame and an adhesive layer such as epoxy resin that is filled into this outer frame and hardened to bond the protective tube and each end of the hollow fiber. n
, the upper part of each NFC hollow fiber condensed inside the protection tube passes through the upper end plate/, 3F and opens on the upper surface of the upper end plate, and the lower end is connected to the lower end plate in the same way as each end of the protection tube. It is filled with adhesive layer in ll. In addition, the lower end board/da is hollow fiber/2 = 0. There are vertical through holes /q' at adjacent intervals.

各濾過モジュール3を取付ける九め、仕切板−と保持板
乙には濾過モジュールと同配置の孔を開設し、この実施
例では保持板の上記多孔には嵌合口/!として上手部の
内径が上向きに拡大する短か5筒を固着し、仕切板コの
孔から処理室ダ内に各濾過モジュールSを降し、その下
端盤   ″/4tf上記嵌合口15にピッタリと嵌合
し、その状態に各濾過モジュールの上端を仕切板コの前
記孔内に適宜固定する。固定は、例えば図示の如く各濾
過モジュールの上端盤の外周に環状溝λ/を形成し、二
つの半円形リング、2.2、−の半径方向内向きの爪2
2′ヲ上記環状溝コ/に入nて両リングで環状溝から上
の上端盤の上部klBみ、仕切板−の孔の大径な上半部
下面の段コ′止に両リングを受止め(上端盤i4Iの環
状溝がち下の部分は仕切板の孔の小径々下半部にoリン
グで気密に嵌合する。]、両リすグの上端盤/3がら上
に突出し次上端を仕切板の上面と一致させ、仕切板の上
から板コ3を当接し、この板コ3を仕切板にネジ止めな
どして取外し可能にすnばよい。尚、板コ3には濾過モ
ジュールと同配置ではあるが、半円形リングよりも小さ
な通水ロー3′が開設しである。又、板2Jヲ外し、濾
過モジュールを上に引出したり、或は逆に処理室内に降
す作業を容易にするため各半円形リングnには直径方向
に棒材の両端を溶接して取手:t41を設け、両リング
の取手、2り、評を一緒に掴むことができる様にすると
よい。
Holes arranged in the same manner as the filtration modules are provided in the partition plate 3 and the holding plate 3 at the 9th point where each filtration module 3 is attached, and in this embodiment, the holes in the holding plate are provided with fitting holes/! Attach five short cylinders with the inner diameter of the upper part expanding upward, lower each filtration module S into the processing chamber through the hole in the partition plate, and fit the lower end plate ″/4tf perfectly into the fitting opening 15 above. In this state, the upper end of each filtration module is appropriately fixed in the hole of the partition plate.For example, as shown in the figure, an annular groove λ/ is formed on the outer periphery of the upper end plate of each filtration module. two semicircular rings, 2.2, - radially inward pawls 2;
2' Insert the annular groove into the upper part of the upper end plate above the annular groove with both rings, and insert both rings into the step stop on the lower surface of the large diameter upper half of the hole in the partition plate. Stopper (the lower part of the annular groove of the upper end plate i4I fits airtightly into the lower half of the small diameter hole of the partition plate with an O-ring.), the upper end plate of both rigs protrudes upward from the upper end plate/3, and then the upper end It is sufficient to match the top surface of the partition plate with the top surface of the partition plate, abut the plate 3 from above the partition plate, and screw the plate 3 to the partition plate to make it removable. Although the arrangement is the same as that of the module, there is a water flow row 3' that is smaller than the semicircular ring.Also, it is necessary to remove the plate 2J and pull out the filtration module upward, or conversely, lower it into the processing chamber. In order to facilitate this, it is preferable that each semicircular ring n is provided with a handle t41 by welding both ends of the rod in the diametrical direction so that the handles, 2 and 41 of both rings can be grasped together.

尚、必要に応じ仕切板の上記孔の回りの下面に上端が当
接し、下端は嵌合口/jを構成する筒の上半部外周に嵌
合する多孔のガイド筒/6を設けてもよい。又、上記筒
の下半部の回りには孔/りを1つ或は数個開設して置く
ことがのぞましい。
If necessary, a multi-hole guide cylinder /6 may be provided whose upper end abuts the lower surface around the hole of the partition plate and whose lower end fits into the outer periphery of the upper half of the cylinder constituting the fitting opening /j. . Further, it is preferable that one or more holes be provided around the lower half of the tube.

濾過を行うには処理室q内に底部の口/lから原水を供
給する。こnにより原水は各濾過モジュール5の内部に
下端盤/qの貫通孔IQ’や、ガイド筒/6、保護筒7
ノの孔を通って入り、中空糸/コの管壁を透過し、各中
空糸の中空部を経て集水室3に集まシ、処理筒/の頂部
の口/9から出、中空糸の外面には原水中の濁質が捕捉
さnて次第に付着する。
To perform filtration, raw water is supplied into the processing chamber q from the bottom port/l. As a result, raw water flows through the through hole IQ' of the lower end plate /q, the guide tube /6, and the protection tube 7 inside each filtration module 5.
The water enters through the hole in the hollow fiber, passes through the tube wall of the hollow fiber, collects in the water collection chamber 3 through the hollow part of each hollow fiber, exits from the opening 9 at the top of the processing tube, and the hollow fiber passes through the tube wall of the hollow fiber. Suspended matter in the raw water is captured and gradually adheres to the outer surface of the tank.

中空糸の外面に付着し几濁質によって濾過差圧が上昇し
て来几ら、濾過を中断して洗浄を行う。
When the filtration differential pressure rises due to suspended matter adhering to the outer surface of the hollow fiber, filtration is interrupted and cleaning is performed.

そRVcは種々の方法があるが、いずnにしても空気排
出口Jに接続した排気管の弁を開き、保持板乙の下の筒
部tで囲まれた内部に送気管テで空気を供給する。
There are various ways to create the RVc, but in any case, open the valve of the exhaust pipe connected to the air outlet J, and supply air with the air supply pipe to the inside surrounded by the cylindrical part t below the retaining plate O. supply.

こnにより空気は各濾過モジュールjの下端盤/lの貫
通孔/4I′からモジュールよの各々の内部に均等に入
シ、中空糸lコの間隔中を気泡となって浮上する際に水
と協同して中空糸の、外面に付着し建濁質を剥離する。
As a result, air enters the inside of each module equally from the through hole/4I' of the lower end plate/l of each filtration module j, and when it floats in the form of air bubbles between the hollow fibers l, the water It works together with the hollow fibers to peel off the suspended solids that adhere to the outer surface of the hollow fibers.

つtシ、送気管9が供給し次空気はその殆んどが筒部t
で囲まn次保持板乙の下に浮集し、各濾過モジュールの
下端盤の貫通孔/り′ヲ通ってモジュールの内部を上昇
する。従って、少ない空気で極めて効率よく短時間で7
ラツシングを行うことができる。そして、処理室の水面
上に出た空気は空気排出口Jから塔外に排気される。
Most of the air supplied by the air pipe 9 is in the cylindrical part t.
It floats under the n-th holding plate surrounded by the filtration module, passes through the through hole in the lower end plate of each filtration module, and rises inside the module. Therefore, it can be used extremely efficiently and in a short period of time with a small amount of air.
Lashing can be performed. The air that has risen above the water surface in the processing chamber is then exhausted from the air outlet J to the outside of the tower.

こうしてフラッシングを行ったら空気の供気を停止し、
処理室内の水を剥離した濁質とともに洗浄廃水として口
/ざから処理塔の外に排出する。
After flushing in this way, stop the air supply,
The water in the treatment chamber and the separated suspended solids are discharged to the outside of the treatment tower through the mouth as cleaning wastewater.

この場合、外径が仕切板コよりも−回り小さい保持板A
は濾過時、逆洗時とも水の流nk阻害するが、濾過モジ
ュール5の堰付間隔に位置させて数本の通水管70を設
けて置くことにより、この通水管10f通じ保持板6上
の水を下に抜くことができ、且つ濾過時は通水できるの
で何等支障はない。そして、フラッシングの際に空気が
この通水管10中を通ってp過モジュールSの間隔を浮
上するのを防止するtめに通水管IOの下向き長さを前
述の様に筒部Sと同等か、そnよりも長くして置く。
In this case, retaining plate A has an outer diameter smaller than that of partition plate A.
This impedes the flow of water during both filtration and backwashing, but by providing several water pipes 70 at intervals between the weirs of the filtration module 5, the water pipes 10f can be connected to the water on the retaining plate 6. Since water can be drained downward and water can be passed through during filtration, there is no problem. In order to prevent air from passing through the water pipe 10 and rising above the gap between the p-passage modules S during flushing, the downward length of the water pipe IO is set to be equal to the length of the cylindrical portion S as described above. , leave it longer than son.

又、各濾過モジュールの中空糸外面から剥離した濁質が
モジュールの下端’41合した筒の内周の嵌合口15内
に水とともに溜ることは、前述の様に筒の回シに孔/7
を開設して置くことで防止できる。即ち、この孔/7は
筒の内周VC嵌合し次各濾過モジュール3の下端盤/4
1の上に連通し、下端盤IQで塞がn*嵌合口の内部に
残溜しようとする水金濁質とともに保持板6上に排出す
るからである。
In addition, the suspended solids separated from the outer surface of the hollow fibers of each filtration module may accumulate together with water in the fitting opening 15 on the inner circumference of the cylinder that meets the lower end of the module.
This can be prevented by opening a . That is, this hole /7 is fitted with the inner circumference VC of the cylinder, and then the lower end plate /4 of each filtration module 3 is fitted.
This is because it is connected to the top of the n* fitting opening and is blocked by the lower end plate IQ, and is discharged onto the holding plate 6 together with the water and gold suspended solids that would remain inside the n* fitting opening.

こうして、処理室ダ中の水をロアgから全部排水し終っ
たら、再び濾過を再開する。尚、濾過モジュールの寿命
が尽きて交換する等の際は集水室Jを覆り頂壁3′を外
し、仕切板コごと濾過モジュールよ、保持板10′t−
処理塔/から抜出して取扱うことができる。
In this way, once all the water in the processing chamber DA has been drained from the lower g, filtration is restarted. When the filtration module reaches the end of its lifespan and needs to be replaced, cover the water collection chamber J, remove the top wall 3', remove the filtration module together with the partition plate, and replace the retaining plate 10't-
It can be extracted from the treatment tower and handled.

(発明の効果〕 この様に本発明によnば送気管りで処理室l内に供給し
た空気のは輩全量を濾過モジュール!の全部の内部に浮
上させ、中空糸の外面に付着した濁質を剥離するのに使
用できる。このため、従来に較べ空気の供給量を節減し
、且つ短時間で効率的にフラッシングを行うことができ
る。又、仕切板にすべての部品が固定さnているので筒
内よりの着脱が容易で、保守の際の効率がよい。
(Effects of the Invention) As described above, according to the present invention, the entire amount of air supplied into the processing chamber l by the air supply pipe is floated inside the entire filtration module! It can be used to peel off the material. Therefore, compared to conventional methods, the amount of air supplied can be reduced and flushing can be performed efficiently in a short time. In addition, all parts are fixed to the partition plate. This makes it easy to attach and detach from the cylinder, making maintenance more efficient.

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

図面は本発明の一実施例を示すもので、第1図は全体の
概略断面図、@2図は同上の要部の拡大断面図であって
、図中、/は処理塔、コは仕切板、3は集水室、ダは処
理室、Sは濾過モジュール、6は保持板、gは筒部、9
は送気管、15は嵌合口を示す。 同 代理人 弁理士  福  1) 弐  通 、、、
5.、二1.。
The drawings show one embodiment of the present invention, and Fig. 1 is a schematic sectional view of the whole, and Fig. 2 is an enlarged sectional view of the main parts of the same. board, 3 is a water collection chamber, da is a processing chamber, S is a filtration module, 6 is a holding plate, g is a cylinder part, 9
15 indicates an air supply pipe, and 15 indicates a fitting port. Patent attorney Fuku 1) Nitoshi...
5. , 21. .

Claims (2)

【特許請求の範囲】[Claims] (1)処理塔の上部に仕切板を設けて仕切板の上を集水
室、下を処理室とし、多数本の中空糸を多孔の保護筒内
で集束して構成したろ過モジュールの上端を前記仕切板
に固定して処理室内に多数のろ過モジュールを吊設し、
上記処理室内に供給した原水を各ろ過モジュールを構成
する中空糸の外面でろ過し、処理水を中空糸の中空内部
を経て前記集水室に得る中空糸型膜分離装置において、 前記各ろ過モジュールの下端を嵌合する嵌合口を備えた
保持板を前記仕切板に対し下方に離して固定することに
より上記嵌合口に各ろ過モジュールの下端を嵌合し、上
記保持板の下面外縁沿いに下向きの筒部を設けると共に
、前記処理室内下部には上記筒部で囲まれた内部に洗浄
用空気を供給する送気管を配設したことを特徴とする中
空糸型膜分離装置。
(1) A partition plate is installed at the top of the treatment tower, the top of the partition plate is used as a water collection chamber, and the bottom part is used as a treatment chamber. A large number of filtration modules are fixed to the partition plate and suspended within the processing chamber,
In the hollow fiber membrane separation device, the raw water supplied into the treatment chamber is filtered by the outer surface of the hollow fibers constituting each filtration module, and the treated water is obtained into the water collection chamber through the hollow interior of the hollow fiber. By fixing a holding plate having a fitting opening into which the lower end of the filtration module is fitted downwardly to the partition plate, the lower end of each filtration module is fitted into the fitting opening, and the lower end of each filtration module is fitted downward along the outer edge of the lower surface of the holding plate. A hollow fiber type membrane separation apparatus characterized in that a cylindrical part is provided, and an air supply pipe for supplying cleaning air to the inside surrounded by the cylindrical part is arranged in the lower part of the processing chamber.
(2)特許請求の範囲(1)の装置において、保持板に
は下向き長さが前記筒部と同等又はそれよりも長い通水
管を取付けた中空糸型膜分離装置。
(2) A hollow fiber membrane separation device according to claim (1), in which a water pipe having a downward length equal to or longer than the cylindrical portion is attached to the holding plate.
JP13591485A 1985-06-24 1985-06-24 Separation device utilizing hollow yarn membrane Granted JPS61293504A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13591485A JPS61293504A (en) 1985-06-24 1985-06-24 Separation device utilizing hollow yarn membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13591485A JPS61293504A (en) 1985-06-24 1985-06-24 Separation device utilizing hollow yarn membrane

Publications (2)

Publication Number Publication Date
JPS61293504A true JPS61293504A (en) 1986-12-24
JPH0234648B2 JPH0234648B2 (en) 1990-08-06

Family

ID=15162787

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13591485A Granted JPS61293504A (en) 1985-06-24 1985-06-24 Separation device utilizing hollow yarn membrane

Country Status (1)

Country Link
JP (1) JPS61293504A (en)

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62171711A (en) * 1986-01-22 1987-07-28 Toshiba Corp Filter
JPS62130710U (en) * 1986-02-05 1987-08-18
FR2639248A1 (en) * 1988-11-21 1990-05-25 Lyonnaise Eaux HOUSING FOR FILTER MODULES WITH FIBER BEAMS
EP0659694A1 (en) * 1993-12-24 1995-06-28 Stork Friesland B.V. Membrane bioreactor with gas lift system
EP0952885A4 (en) * 1996-12-20 2001-04-04 Usf Filtration & Separations Scouring method
EP1115474A4 (en) * 1998-09-25 2005-03-30 Us Filter Wastewater Group Inc Apparatus and method for cleaning membrane filtration modules
US6964741B2 (en) 1995-08-11 2005-11-15 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes
US7022231B2 (en) 1995-08-11 2006-04-04 Zenon Environmental Inc. Apparatus incorporating potted hollow fiber membranes
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
USRE39294E1 (en) 1995-08-11 2006-09-19 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
WO2007135087A1 (en) * 2006-05-23 2007-11-29 Otv Sa Aerating device for a water filtering system with immersed membranes, including a floor provided with means for injecting a gas and at least one pressure balancing system
US7361274B2 (en) 2002-08-21 2008-04-22 Siemens Water Technologies Corp. Aeration method
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
US8377305B2 (en) 2004-09-15 2013-02-19 Siemens Industry, Inc. Continuously variable aeration
US8382981B2 (en) 2008-07-24 2013-02-26 Siemens Industry, Inc. Frame system for membrane filtration modules
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
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
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

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61254207A (en) * 1985-05-07 1986-11-12 Japan Organo Co Ltd Filtering tower using hollow yarn module

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61254207A (en) * 1985-05-07 1986-11-12 Japan Organo Co Ltd Filtering tower using hollow yarn module

Cited By (58)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62171711A (en) * 1986-01-22 1987-07-28 Toshiba Corp Filter
JPS62130710U (en) * 1986-02-05 1987-08-18
JPH046820Y2 (en) * 1986-02-05 1992-02-25
FR2639248A1 (en) * 1988-11-21 1990-05-25 Lyonnaise Eaux HOUSING FOR FILTER MODULES WITH FIBER BEAMS
EP0659694A1 (en) * 1993-12-24 1995-06-28 Stork Friesland B.V. Membrane bioreactor with gas lift system
NL9302260A (en) * 1993-12-24 1995-07-17 Stork Friesland Bv Membrane bioreactor with gas-lift system.
US5494577A (en) * 1993-12-24 1996-02-27 Stork Friesland B.V. Membrane bioreactor with gas lift system
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
US7534353B2 (en) 1995-08-11 2009-05-19 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US8075776B2 (en) 1995-08-11 2011-12-13 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
USRE42669E1 (en) 1995-08-11 2011-09-06 Zenon Technology Partnership Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
US6964741B2 (en) 1995-08-11 2005-11-15 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes
US7022231B2 (en) 1995-08-11 2006-04-04 Zenon Environmental Inc. Apparatus incorporating potted hollow fiber membranes
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
USRE39294E1 (en) 1995-08-11 2006-09-19 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US7708888B2 (en) 1995-08-11 2010-05-04 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US7615157B2 (en) 1995-08-11 2009-11-10 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
JP2001510396A (en) * 1996-12-20 2001-07-31 ユーエスエフ・フィルトレイション・アンド・セパレイションズ・グループ・インコーポレイテッド Cleaning method
EP0952885A4 (en) * 1996-12-20 2001-04-04 Usf Filtration & Separations Scouring method
US6555005B1 (en) 1996-12-20 2003-04-29 Usf Filtration & Separations Group Inc. Scouring method
EP1736234A3 (en) * 1996-12-20 2007-06-13 Siemens Water Technologies Corp. Method for scouring fouled membranes
EP1115474A4 (en) * 1998-09-25 2005-03-30 Us Filter Wastewater Group Inc Apparatus and method for cleaning membrane filtration modules
US7361274B2 (en) 2002-08-21 2008-04-22 Siemens Water Technologies Corp. Aeration method
US8268176B2 (en) 2003-08-29 2012-09-18 Siemens Industry, Inc. Backwash
US8377305B2 (en) 2004-09-15 2013-02-19 Siemens Industry, Inc. Continuously variable aeration
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
WO2007135087A1 (en) * 2006-05-23 2007-11-29 Otv Sa Aerating device for a water filtering system with immersed membranes, including a floor provided with means for injecting a gas and at least one pressure balancing system
FR2901488A1 (en) * 2006-05-23 2007-11-30 Otv Sa AERATION DEVICE FOR IMMERSION MEMBRANE-BASED WATER FILTRATION SYSTEM INCLUDING FLOOR WITH GAS INJECTION MEANS AND AT LEAST ONE PRESSURE BALANCING SYSTEM
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
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
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US8372276B2 (en) 2007-05-29 2013-02-12 Siemens Industry, Inc. Membrane cleaning with pulsed airlift pump
US9573824B2 (en) 2007-05-29 2017-02-21 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US8287743B2 (en) 2007-05-29 2012-10-16 Siemens Industry, Inc. Membrane cleaning with pulsed airlift pump
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US8382981B2 (en) 2008-07-24 2013-02-26 Siemens Industry, Inc. 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
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
US10391432B2 (en) 2011-09-30 2019-08-27 Evoqua Water Technologies Llc Manifold arrangement
US11065569B2 (en) 2011-09-30 2021-07-20 Rohm And Haas Electronic Materials Singapore Pte. Ltd. Manifold arrangement
US9604166B2 (en) 2011-09-30 2017-03-28 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
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
US9962865B2 (en) 2012-09-26 2018-05-08 Evoqua Water Technologies Llc Membrane potting methods
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
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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