JPH04180821A - Hollow yarn film filtration device - Google Patents

Hollow yarn film filtration device

Info

Publication number
JPH04180821A
JPH04180821A JP30848890A JP30848890A JPH04180821A JP H04180821 A JPH04180821 A JP H04180821A JP 30848890 A JP30848890 A JP 30848890A JP 30848890 A JP30848890 A JP 30848890A JP H04180821 A JPH04180821 A JP H04180821A
Authority
JP
Japan
Prior art keywords
hollow fiber
hollow
fiber membrane
cleaning
water
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
JP30848890A
Other languages
Japanese (ja)
Other versions
JPH0716589B2 (en
Inventor
Giichi Ito
義一 伊藤
Taku Kono
鴻野 卓
Kanroku Naganami
長南 勘六
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.)
Ebara Corp
Original Assignee
Ebara Infilco Co 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 Ebara Infilco Co Ltd filed Critical Ebara Infilco Co Ltd
Priority to JP2308488A priority Critical patent/JPH0716589B2/en
Publication of JPH04180821A publication Critical patent/JPH04180821A/en
Publication of JPH0716589B2 publication Critical patent/JPH0716589B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To obtain an energy-saving hollow yarn film filtration device with the high cleaning effects on an external pressure-type hollow yarn by supporting the hollow yarn of a hollow yarn film module in a horizontal direction, and at the same time, providing an air diffusion device and/or a water spray device which clean hollow yarn. CONSTITUTION:At least, one or more hollow yarn modules consisting of hollow yarns 18 and a water collection part 17 connected to the hollow yarns 18 are arranged in a tank 15. The hollow yarns 18 of the hollow yarn module 2 are supported horizontally, and at the same time, an air diffusion device and/or a water spray device for cleaning the hollow yarns 18 are arranged. As a result, it is possible to obtain a hollow yarn film filtration device capable of cleaning an external pressure-type hollow yarn efficiently and securing an adequate quantity of processing water in saved space with energy-saving function.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は河川水、湖沼水、井水、し尿、下水、用水、廃
水等の液中に含まれる懸濁物を濾過するための中空糸膜
濾過装置、特に効果的に中空糸の洗浄ができる構造の中
空糸膜濾過装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a hollow fiber for filtering suspended matter contained in liquids such as river water, lake water, well water, human waste, sewage, industrial water, and wastewater. The present invention relates to a membrane filtration device, particularly a hollow fiber membrane filtration device having a structure that allows effective cleaning of hollow fibers.

〔従来の技術〕[Conventional technology]

一般に精密濾過膜と称される膜の有する孔径は0.01
J−〜数−である。これらの孔径を有する中空糸膜濾過
には膜の外側から内側に液体を濾過する外圧型とその反
対の内圧型がある。外圧型は0,5〜2時間濾過の後、
数分間の空気を用いた洗浄または膜の内側から外側に処
理水を通水する処理水洗浄が行われている。
The pore diameter of a membrane generally called a precision filtration membrane is 0.01
J-~number-. Hollow fiber membrane filtration having these pore sizes includes an external pressure type that filters liquid from the outside to the inside of the membrane, and an internal pressure type that is the opposite. For the external pressure type, after filtration for 0.5 to 2 hours,
Cleaning using air for several minutes or treated water cleaning is performed by passing treated water from the inside of the membrane to the outside.

また、従来の中空糸膜モジュールはスペースを小さくす
るため中空糸を密に配置し、中空糸本数を増やし、膜面
積を大きくしてモジュール当たりの処理水量を確保して
いる。
In addition, in conventional hollow fiber membrane modules, in order to reduce space, the hollow fibers are arranged closely, the number of hollow fibers is increased, and the membrane area is increased to ensure the amount of water treated per module.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の外圧式中空糸膜モジニールは中空糸が密に配置さ
れているためにSS等がモジュール内部に入り込むと通
常の空気を用いた洗浄方式ではモジュールからの剥離、
除去が困難であり、数週間でフラックスが低下してしま
う。洗浄性を良くするためにモジュール当たりの中空糸
の本数を減らし、粗に配置すると必要な処理水量を確保
するのにモジュールの本数が大幅に増加する。
In the conventional external pressure type hollow fiber membrane Modineal, the hollow fibers are densely arranged, so if SS etc. gets inside the module, it will peel off from the module with the normal cleaning method using air.
It is difficult to remove and the flux degrades within a few weeks. If the number of hollow fibers per module is reduced and arranged sparsely in order to improve cleaning performance, the number of modules will increase significantly to secure the required amount of treated water.

従って、通常のモジュールの配置方法では、モジュール
の増加に伴い設置面積が増加すると共に洗浄用の空気量
が増大する。モジュールの本数を増さず膜面積を確保す
る方法として中空糸の長さを長くすることが考えられる
が、中空糸内部の圧力損失により集水部近くの中空糸部
分しか機能しないためあまり長くすることは意味がない
Therefore, in the usual method of arranging modules, as the number of modules increases, the installation area increases and the amount of air for cleaning increases. One possible way to secure membrane area without increasing the number of modules is to increase the length of the hollow fibers, but due to the pressure loss inside the hollow fibers, only the hollow fibers near the water collection area function, so do not make them too long. That makes no sense.

従って、本発明は省エネルギーでしかも外圧式中空糸の
洗浄効果が高く、かつ省スペースで処理水量を確保でき
る中空糸膜濾過装置を提供することを解決課題とするも
のであり、従来適用分野が限定されていた外圧型中空糸
膜の用途を拡げようとするものである。
Therefore, an object of the present invention is to provide a hollow fiber membrane filtration device that saves energy, has a high external pressure type hollow fiber cleaning effect, and can secure the amount of water to be treated in a small space. This is an attempt to expand the uses of external pressure type hollow fiber membranes, which had previously been used.

〔課題を解決するだめの手段〕[Failure to solve the problem]

本発明は以下の(1)〜(2)記載のものであり、これ
により上記課題を解決できる。
The present invention is described in (1) to (2) below, and can thereby solve the above problems.

(1)複数の中空糸と、中空糸と連通した集水部とを有
する中空糸膜モジュールの1以上を槽内に少なくとも備
えた中空糸膜濾過装置において、該中空糸膜モジュール
の中空糸を水平方向に支持すると共に中空糸を洗浄する
ための散気装置および/または散水装置を配備したこと
を特徴とする中空糸膜濾過装置。
(1) In a hollow fiber membrane filtration device including at least one or more hollow fiber membrane modules each having a plurality of hollow fibers and a water collection portion communicating with the hollow fibers in a tank, the hollow fibers of the hollow fiber membrane module are A hollow fiber membrane filtration device characterized in that it supports the hollow fibers in a horizontal direction and is equipped with an aeration device and/or a water sprinkler device for cleaning the hollow fibers.

(2)複数の中空糸と、中空糸と連通した集水部とを有
する中空糸膜モジュールの1以上を槽内に少なくとも備
えた中空糸膜濾過装置において、中空糸膜モジュールの
中空糸を水平方向又は垂直方向に支持すると共に該装置
の外から部材を運動させることにより各モジュールの一
部又は全ての中空糸を運動させ、洗浄せしめるように該
部材を配備したことを特徴とする中空糸膜濾過装置。
(2) In a hollow fiber membrane filtration device including at least one or more hollow fiber membrane modules each having a plurality of hollow fibers and a water collection portion communicating with the hollow fibers in a tank, the hollow fibers of the hollow fiber membrane modules are horizontally disposed. A hollow fiber membrane characterized in that the member is arranged so as to support in the direction or perpendicular direction and to move a part or all of the hollow fibers of each module by moving the member from outside the device and cleaning it. Filtration device.

本発明は、上記のように中空糸膜モジュールを配備する
ことにより、中空糸の洗浄および/または汚染防止を効
率的に行うことができる。
By arranging the hollow fiber membrane module as described above, the present invention can efficiently clean the hollow fibers and/or prevent contamination.

ここで、中空糸とは、少なくとも一つの集水部に連通し
た端部を有する一本の中空糸膜を意味し、他端がフリー
であっても他端が折り返し部から同一の集水部に至るも
のでも、あるいは他の集水部に連通したものであっても
よい。
Here, the term "hollow fiber" refers to a single hollow fiber membrane having an end communicating with at least one water collection part, and even if the other end is free, the other end is connected to the same water collection part from the folded part. It may also be connected to another water collection area.

上記(1)記載の発明(以下、本発明(1)と言う)に
ついて以下説明する。
The invention described in (1) above (hereinafter referred to as invention (1)) will be explained below.

この本発明(1)は、中空糸を水平方向に支持したもの
である。ここで、水平方向に支持するとは、集水部端部
に保持されていない一端あるいは折り返し部が重力方向
に垂れ下がり、中空糸全体が垂直になることがなければ
、文字通り中空糸が水平にならなくともよく、水平に近
い傾斜、中空糸中央部がやや下方に落ちた状態等を包含
するものである。
In the present invention (1), hollow fibers are supported in the horizontal direction. Here, supporting in the horizontal direction literally means that the hollow fiber will not become horizontal unless one end that is not held at the end of the water collection part or the folded part hangs in the direction of gravity and the entire hollow fiber does not become vertical. This may include a state where the hollow fiber is tilted close to horizontal, or where the central portion of the hollow fiber is slightly downwardly tilted.

具体的には、中空糸折り返し部の間に棒材等の支持体を
挿入して中空糸を保持する方法、中空糸両端を異なる集
水部に連通して、該集水部を中空糸が水平方向に支持さ
れるように配備すること等が例示される。
Specifically, the hollow fibers are held by inserting a support such as a rod between the folded portions of the hollow fibers, and the hollow fibers are connected to different water collecting portions by connecting both ends of the hollow fibers to different water collecting portions. For example, it may be arranged so as to be supported in the horizontal direction.

また、本発明(1)は中空糸膜モジュールを単独に使用
してもよいが、特に2以上の中空糸膜モジュールを中空
糸を水平方向に維持しつつ垂直方向に多段に配備するこ
とにより中空糸膜濾過装置を構成することが好ましく、
より省スペースで洗浄用気体の有効利用を図ることがで
きる。
In addition, in the present invention (1), a hollow fiber membrane module may be used alone, but in particular, two or more hollow fiber membrane modules can be arranged vertically in multiple stages while maintaining the hollow fibers in the horizontal direction. It is preferable to configure a thread membrane filtration device,
The cleaning gas can be used more effectively in a more space-saving manner.

該中空糸膜モジュールは従来公知のものが使用でき、集
水部の形状等は特に制限はないが、好ましくは、中空糸
の存在密度を低減させ、中空糸間に間隙を持たせたもの
が好ましく、また集水部端部形状が矩形の中空糸折り返
し部を有する中空糸膜モジュールで、中空糸全体の形状
が板状であるものが好ましい。この中空糸膜モジュール
はその板状の低面を構成する中空糸が水平方向になるよ
うに中空糸膜濾過装置に配備されることが好ましい。
Conventionally known hollow fiber membrane modules can be used, and there are no particular restrictions on the shape of the water collection part, but preferably one with a reduced density of hollow fibers and gaps between the hollow fibers. Preferably, the hollow fiber membrane module has a hollow fiber folded portion with a rectangular end shape of the water collecting portion, and the hollow fiber has a plate-like shape as a whole. It is preferable that this hollow fiber membrane module is installed in a hollow fiber membrane filtration device so that the hollow fibers constituting the plate-like lower surface thereof are oriented horizontally.

これら中空糸膜モジュールは上記条件を満足するならば
、どのように中空糸膜濾過装置に配備されてもよいが、
好ましくは、中空糸膜濾過装置の処理水集水部と中空糸
膜モジュールの集水部が中空糸膜濾過装置の側部に設け
られる構成とすることが好ましい。この場合、中空糸膜
モジユール集水部の配備方法は特に制限なく中空糸膜濾
過装置の同一側に設けても交互に対向するように設けて
もランダムに設けてもよい。ただし、中空糸膜濾過装置
を垂直面で切ったとき異なる中空糸膜モジュールの中空
糸の切断部が該垂直面の垂直方向に所定間隔をとって並
ぶような位置にとることが好ましい。
These hollow fiber membrane modules may be installed in the hollow fiber membrane filtration device in any way as long as they satisfy the above conditions.
Preferably, the treated water collection section of the hollow fiber membrane filtration device and the water collection section of the hollow fiber membrane module are preferably provided on the side of the hollow fiber membrane filtration device. In this case, the method of disposing the hollow fiber membrane module water collection parts is not particularly limited and may be disposed on the same side of the hollow fiber membrane filtration device, alternately facing each other, or disposed randomly. However, it is preferable to position the hollow fiber membrane filtration device at a position such that when the hollow fiber membrane filtration device is cut along a vertical plane, the cut portions of the hollow fibers of different hollow fiber membrane modules are lined up at a predetermined interval in the direction perpendicular to the vertical plane.

次に本発明である上記(2)に記載した中空糸膜濾過装
置(以下本発明(2)と言う)について説明する。
Next, the hollow fiber membrane filtration device described in the above (2), which is the present invention (hereinafter referred to as the present invention (2)), will be explained.

この装置は、該装置の外から部材を運動させることによ
り配備されている中空糸膜モジュールの各モジニールの
一部又は全ての中空糸を一律に運動させ、洗浄せしめる
ように該部材(以下、洗浄用部材と言う)を配備したこ
とを特徴とするものである。
This device uniformly moves some or all of the hollow fibers of each module of the hollow fiber membrane module installed by moving a member from outside the device (hereinafter referred to as cleaning). This feature is characterized by the fact that it is equipped with a

ここで該中空糸を一律に運動させるとは、洗浄用部材の
運動に対応して一部又は全ての中空糸膜モジュールの中
空糸が運動せしめられることを意味する。即ち、本発明
は、これにより中空糸自体の振動と水流との相互作用に
より中空糸を洗浄するものである。
Here, uniformly moving the hollow fibers means that some or all of the hollow fibers of the hollow fiber membrane module are moved in response to the movement of the cleaning member. That is, the present invention cleans the hollow fibers by the interaction between the vibration of the hollow fibers themselves and the water flow.

そして、上記洗浄を達成するための手段は特に制限され
ず公知の手段を適用でき、中空糸と洗浄用部材が洗浄用
部材の運動に対応して衝突するように配置しても、予め
中空糸と洗浄用部材とを結合させておいてもかまわない
The means for achieving the above-mentioned cleaning is not particularly limited and any known means can be applied. The cleaning member may be combined with the cleaning member.

また、使用しえる中空糸膜モジュールの種類も制限され
ることはなく、中空糸膜濾過装置における配置も任意で
あるが、洗浄用部材と中空糸膜モジュールとの構成は、
中空糸が洗浄用部材により損傷されないように洗浄用部
材の素材を選定すると共にこれらを配備することが望ま
しい。
In addition, the types of hollow fiber membrane modules that can be used are not limited, and the arrangement in the hollow fiber membrane filtration device is arbitrary, but the configuration of the cleaning member and the hollow fiber membrane module is as follows:
It is desirable to select a material for the cleaning member and to provide it so that the hollow fibers are not damaged by the cleaning member.

洗浄用部材の構成の好ましい例としては、中空糸膜モジ
ニールの中空糸折り返し部に使用される中空糸支持部材
を例えば連結棒で各モジュールにおいて固定する構成が
挙げられる。
A preferred example of the configuration of the cleaning member is a configuration in which a hollow fiber support member used in the hollow fiber folded portion of the hollow fiber membrane Modineal is fixed in each module using, for example, a connecting rod.

洗浄用部材を運動させる力の印加方法は特に制限なく、
機械的に制御しても、人により操作してもかまわない。
There are no particular restrictions on the method of applying force to move the cleaning member.
It may be controlled mechanically or operated by a person.

この場合の洗浄用部材の印加部は一箇所で十分であるが
、複数箇所でもかまわない。
In this case, it is sufficient for the cleaning member to have one application section, but it is also possible to use a plurality of application sections.

また、洗浄用部材の運動方向も一次元の往復運動(上下
、左右、等)で十分であるが、特に制限はない。
Further, the direction of movement of the cleaning member is not particularly limited, although one-dimensional reciprocating movement (up and down, left and right, etc.) is sufficient.

また、中空糸膜モジュールの中空糸を水平方向又は垂直
方向に支持することにより、例えば、中空糸支持部材を
連結した洗浄用部材を適宜方向に運動して中空糸の洗浄
を行うと、省スペースで効率的な洗浄ができる。また、
上記(1)で記載したバブリング洗浄方式中空糸膜濾過
装置と併用することできる。
In addition, by supporting the hollow fibers of the hollow fiber membrane module horizontally or vertically, for example, cleaning the hollow fibers by moving the cleaning member connected to the hollow fiber supporting member in an appropriate direction can save space. for efficient cleaning. Also,
It can be used in combination with the bubbling cleaning type hollow fiber membrane filtration device described in (1) above.

以下、本発明(1)および(2)の両発明に共通してい
える一般的事項につき記載する。
General matters common to both inventions (1) and (2) will be described below.

本発明に於ける中空糸膜モジュールの濾過方式は外圧型
が好ましく、外圧型とは中空糸外部の被処理水が中空糸
膜を経て中空糸内部に濾過水が至るように鉄膜と被処理
水との界面に圧力差が印加される型を意味し、その圧力
差を生じさせる手段は特に制限なく、従来公知の手段を
使用できる。
The filtration method of the hollow fiber membrane module in the present invention is preferably an external pressure type, and the external pressure type means that the water to be treated outside the hollow fibers is connected to an iron membrane so that the filtrate reaches the inside of the hollow fibers through the hollow fiber membrane. It refers to a type in which a pressure difference is applied at the interface with water, and the means for creating the pressure difference is not particularly limited, and conventionally known means can be used.

また、中空糸の素材、孔サイズ等は任意であり、従来公
知のものが使用できる。
Further, the material, hole size, etc. of the hollow fibers are arbitrary, and conventionally known ones can be used.

また、中空糸の長さは圧力損失を考慮すると、−船釣に
は集水部端面から折り返し部までの長さとして300〜
600.mmが好ましい。
In addition, considering the pressure loss, the length of the hollow fiber is - For boat fishing, the length from the end of the water collection part to the folded part is 300~
600. mm is preferred.

また、本発明の中空糸膜濾過装置は固液分離手段として
用いられるものなら全ての装置に適用できる。例えば、
曝気槽等の生物処理槽内に中空糸膜モジュールからなる
濾過部を設け、濾過機能と生物学的処理機能を兼備させ
ることもでき、好気性生物処理を兼ねる場合は、好気性
を維持するための空気供給管を本発明(1)の場合は中
空系洗浄用として兼用することができる。本発明(2)
の場合も該空気供給管を洗浄手段としても利用してよい
Further, the hollow fiber membrane filtration device of the present invention can be applied to any device used as a solid-liquid separation means. for example,
A filtration section consisting of a hollow fiber membrane module can be installed in a biological treatment tank such as an aeration tank to have both filtration function and biological treatment function.If it also serves as aerobic biological treatment, it can be used to maintain aerobic conditions. In the case of the present invention (1), the air supply pipe can also be used for cleaning the hollow system. Present invention (2)
In this case, the air supply pipe may also be used as a cleaning means.

また、生物学処理が嫌気性処理の場合は窒素成分ガス等
を使用することができる。
Further, when the biological treatment is anaerobic treatment, nitrogen component gas or the like can be used.

また、中空糸洗浄は原水導入時の水流によっても行える
が、別途水放出手段から水を供給するようにしてもよい
Further, hollow fiber cleaning can be performed by using a water stream when raw water is introduced, but water may also be supplied from a separate water discharge means.

このような気体、水供給手段は両者を兼用した手段であ
ってもよく、従来公知の装置を使用できる。
Such gas and water supply means may be a means that serves both, and conventionally known devices can be used.

また、洗浄効果をより一層向上させるために粒状物を装
置内部に存在させ、バブリングおよび/または水噴流に
より粒状物を中空糸と接触させて中空糸を洗浄する手段
を更に加えた構成としてもよい。この場合の粒状物とし
て透過性有機物等を吸着する吸着剤を使用してもよい。
Furthermore, in order to further improve the cleaning effect, a configuration may be adopted in which particulate matter is present inside the device, and a means for cleaning the hollow fibers by bringing the particulate matter into contact with the hollow fibers by bubbling and/or water jets may be added. . In this case, an adsorbent that adsorbs permeable organic substances may be used as the particulate material.

本発明の中空糸膜濾過装置は中空糸の洗浄を処理を継続
しながら行なっても、処理を停止しておこなってもよい
。特に中空糸内部の洗浄はこの停止時に行うとよい。
In the hollow fiber membrane filtration apparatus of the present invention, the hollow fibers may be washed while the treatment continues or after the treatment is stopped. In particular, cleaning the inside of the hollow fibers is preferably carried out during this stop.

〔実施例〕〔Example〕

以下、本発明の具体的実施例について説明するが、本発
明はこれに限定されるものではない。
Hereinafter, specific examples of the present invention will be described, but the present invention is not limited thereto.

実施例1 第1図は、中空糸膜濾過装置の空気洗浄方式の一例であ
る。
Example 1 FIG. 1 is an example of an air cleaning system for a hollow fiber membrane filtration device.

中空糸膜濾過装置1は、原水水槽15と処理水水槽16
からなり原水槽下部に散気装置3を設置している。
The hollow fiber membrane filtration device 1 includes a raw water tank 15 and a treated water tank 16.
An air diffuser 3 is installed at the bottom of the raw water tank.

中空糸膜モジュール2を集水部17を処理水槽側16、
中空糸を原水槽側にし散気装置の上部に多段に設置しで
ある。
The hollow fiber membrane module 2 is connected to the water collecting section 17 to the treatment water tank side 16,
The hollow fibers are installed in multiple stages above the air diffuser, with the hollow fibers facing the raw water tank.

該中空糸膜モジュールの構造を第2図に示す。The structure of the hollow fiber membrane module is shown in FIG. 2.

中空糸膜モジュール2は、片端集水タイプの膜モジュー
ルであり、集水部17と、集水部に両端部を連結すると
ともに中空糸折り返し部19を有する中空糸18からな
り、中空糸は中空糸折り返し部に挿入された支持棒20
で水平方向に支持されている。
The hollow fiber membrane module 2 is a one-end water collection type membrane module, and consists of a water collection part 17 and a hollow fiber 18 that connects both ends to the water collection part and has a hollow fiber folded part 19. Support rod 20 inserted into the yarn folded part
is supported horizontally.

原水は原水ポンプ6 (圧力が確保される場合、自然流
下でかまわない)で原水水槽15へ通水され、中空糸膜
モジュール2にて濾過され処理水水槽16を経て処理水
管10より流出する。
Raw water is passed through a raw water tank 15 by a raw water pump 6 (gravity flow is acceptable if pressure is secured), filtered by a hollow fiber membrane module 2, passed through a treated water tank 16, and then flows out from a treated water pipe 10.

洗浄は原水ポンプ6を停止し、排気弁12を開とする。For cleaning, the raw water pump 6 is stopped and the exhaust valve 12 is opened.

ブロワ5を起動し、空気洗浄を開始する。Start the blower 5 and start air cleaning.

洗浄空気は散気装置3より均一に流出し、気泡の上昇に
従って下部のモジュールより順次、洗浄を行う。一定時
間空気で洗浄した後、膜面の汚染状況等により必要に応
じて処理水洗浄を行う。処理水洗浄は排水弁13を開と
して洗浄ポンプ8を起動して処理水を中空糸内部から外
部へ通水する。
The cleaning air flows out uniformly from the air diffuser 3, and cleaning is performed sequentially from the lower module as the air bubbles rise. After cleaning with air for a certain period of time, the treated water is cleaned as necessary depending on the contamination status of the membrane surface. For cleaning the treated water, the drain valve 13 is opened and the cleaning pump 8 is started to flow the treated water from inside the hollow fibers to the outside.

空気洗浄および処理水洗浄により剥離した88分は排水
管14により排出される。
The 88 minutes removed by air cleaning and treated water cleaning are discharged through the drain pipe 14.

第1図に示した中空糸膜濾過装置の構造は、中空糸膜モ
ジュールが多段垂直に配置さnた本発明(1)の単なる
一例であり、原水の流入方向、処理水の流出方向、膜の
挿入方向などには制限がない。
The structure of the hollow fiber membrane filtration device shown in FIG. There are no restrictions on the direction of insertion.

その例を以下に示すが、変更部以外は図示を略すが、不
図示の箇所は第1図が適用できる。
An example of this is shown below, and although the illustrations are omitted except for the changed parts, FIG. 1 can be applied to the unillustrated parts.

例えば、第3図に示した中空糸膜濾過装置21は、該装
置両側面に処理水水槽16を設け、第2図に示した水平
方向に支持された中空糸膜モジュールを両側から交互に
処理水水槽に挿入した場合を示す。
For example, the hollow fiber membrane filtration device 21 shown in FIG. 3 is provided with treated water tanks 16 on both sides of the device, and the hollow fiber membrane modules supported in the horizontal direction shown in FIG. 2 are alternately treated from both sides. Shown when inserted into a water tank.

また、第4図に示した中空糸膜濾過装置22は、該装置
両側面に処理水水槽16を設け、第5図に示した両端集
水タイプの中空糸膜モジュール23を処理水水槽16に
挿入した場合を示す。
In addition, the hollow fiber membrane filtration device 22 shown in FIG. 4 is provided with treated water tanks 16 on both sides of the device, and a hollow fiber membrane module 23 of a water collecting type at both ends shown in FIG. 5 is installed in the treated water tank 16. Indicates when inserted.

該モジュール23は、中空糸24両端が集水部25およ
び26に連通したタイプであり、第2図に示した様に中
空糸を水平方向に支持するための支持棒20が無くとも
処理水槽16に配備する時に中空糸を水平方向に配備す
れば十分である。
The module 23 is of a type in which both ends of the hollow fibers 24 are connected to water collection parts 25 and 26, and as shown in FIG. It is sufficient to deploy the hollow fibers horizontally when deploying them.

実施例2 次に本発明(2)の洗浄用部材を使用した具体的実施例
について説明する。
Example 2 Next, a specific example using the cleaning member of the present invention (2) will be described.

第6図に示す中空糸膜濾過装置101は、原水水槽11
3と処理水槽114から成り、中空糸膜モジニール10
2を集水部116を処理水水槽114側に中空糸117
を原水水槽側にして垂直に多段に設置する。
The hollow fiber membrane filtration device 101 shown in FIG.
3 and a treated water tank 114, the hollow fiber membrane Modinyl 10
2, connect the water collecting part 116 to the treated water tank 114 side with the hollow fiber 117
Install vertically in multiple tiers with the raw water tank side facing the tank.

全ての中空糸膜モジニール102は第7図に示す通り洗
浄用部材103が挿入され、該部材103は中空糸折り
返し部118を支持する支持棒119とこれを連結した
連結棒120からなり、該連結棒120は軸封水部11
5から槽外にでている。
A cleaning member 103 is inserted into each of the hollow fiber membranes Modineal 102 as shown in FIG. The rod 120 is the shaft water sealing part 11
It is out of the tank from 5 onwards.

処理時の水の流れは実施例1の場合と同様で原水ポンプ
104から導入された原水を中空糸膜モジュール102
により処理し、処理水槽114から処理水管108より
処理水を得る。
The flow of water during treatment is the same as in Example 1, and the raw water introduced from the raw water pump 104 is passed through the hollow fiber membrane module 102.
The treated water is obtained from the treated water tank 114 through the treated water pipe 108.

洗浄は連結棒を上下させ膜の上下振動、水流により濁質
を剥離させる。定期的に排水弁111を開として剥離し
たSSを排水管112にて排出する。
For cleaning, the connecting rod is moved up and down, the membrane is vibrated up and down, and suspended matter is removed by water flow. The drain valve 111 is periodically opened to drain the separated SS through the drain pipe 112.

必要に応じて処理水洗浄を行う。処理水洗浄方式は前述
と同じで洗浄ポンプ106で処理水を中空糸内部に圧入
して行う。
Clean treated water as necessary. The treated water cleaning method is the same as described above, and is performed by pressurizing treated water into the hollow fibers using the cleaning pump 106.

連結棒の上下は人力によっても動力によってもかまわな
い。膜の汚染状況によって上下運動の強度を調節するこ
とができる。
The connecting rod may be moved up and down by human power or power. The intensity of the vertical movement can be adjusted depending on the degree of contamination of the membrane.

上記中空糸膜濾過装置101において、中空糸膜モジニ
ールは中空糸を水平方向に集水部を垂直方向に配備した
タイプであるが、本発明はこれに限定されず、第8図に
示した様に中空糸膜モジュール102を集水部116を
水平方向に中空糸117を垂直方向に配備して構成した
中空糸膜濾通装置121でもよい。なお、実施例1では
散水装置を設けて水流による洗浄を併用してもよく、実
施例2では散気装置および/または散水装置を設けて散
気と水流による洗浄を併用してもよい。
In the hollow fiber membrane filtration device 101, the hollow fiber membrane Modineal is of a type in which the hollow fibers are arranged horizontally and the water collection part is arranged vertically, but the present invention is not limited to this, and as shown in FIG. Alternatively, a hollow fiber membrane filtration device 121 may be used in which the hollow fiber membrane module 102 is arranged with the water collecting section 116 arranged in the horizontal direction and the hollow fibers 117 arranged in the vertical direction. Note that in Example 1, a water sprinkler may be provided and cleaning using a water stream may be used in combination, and in Example 2, an aeration device and/or a water sprinkler may be provided to use a combination of aeration and washing using a water stream.

〔発明の効果〕〔Effect of the invention〕

本発明による空気洗浄方式の中空糸膜濾過装置は設置面
積が小さく下部から上昇する空気が下部のモジュールか
ら上部のモジュールへと順次洗浄していくため洗浄空気
量が小さくて済む。
The air cleaning type hollow fiber membrane filtration device according to the present invention has a small installation area and the air rising from the lower part cleans the module sequentially from the lower module to the upper module, so the amount of cleaning air can be small.

洗浄用部材可動式中空糸膜濾過装置では単一の動力源(
人力でもかまわない)によりすべてのモジュールを上下
または左右に可動させ振動、水流による洗浄ができるた
め空気源を必要としない。
A hollow fiber membrane filtration device with movable cleaning members uses a single power source (
All modules can be moved up and down or left and right and cleaned by vibration and water flow, so no air source is required.

更に可動させるのは処理中でよく洗浄のために処理を停
止する必要がない。
Moreover, it is movable during processing and there is no need to stop processing for cleaning.

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

第1図は空気洗浄方式の中空糸膜濾過装置の一例を説明
するための断面概略図、第2図は第1図に適用される片
端集水タイプの中空糸膜モジュールを説明するための斜
視図、第3図及び第4図は、第1図の空気洗浄方式の中
空糸膜濾過装置の変形例を説明するための断面概略図、
第5図は第4図に示す装置に配備される両端集水タイプ
の中空系膜モジュールを説明するための斜視図、第6図
は洗浄用部材可動式中空糸膜濾過装置の一例を示す断面
概略図、第7図は洗浄用部材と中空糸膜モジュールとの
構成を示す斜視図、第8図は第6図に示す洗浄用部材可
動式中空糸膜濾過装置の変形例を説明するための断面概
略図である。 1:中空糸膜濾過装置 2:中空糸膜モジュール3:散
気装置     4:空気管 5ニブロワ      6:原水ポンプ7:原水流入管
    8:洗浄ポンプ9:洗浄管      10:
処理水管11:排水弁      12:排気管13:
排水弁      14:排水管15:原水水管   
  16:処理水水槽−17:集水部      18
:中空糸19:中空糸折り返し部 20:支持棒21.
22:中空糸膜濾過装置 23:両端集水タイプの中空糸膜モジニール24:中空
糸      25.26:集水部101:中空糸膜濾
過装置 102:中空糸膜モジュール 103:洗浄用部材   104:原水ポンプ105:
原水流入管   106:洗浄ポンプ107:洗浄管 
    108:処理水管109:処理水弁    1
10:洗浄弁111:排水弁     112:排水管
113:原水水槽    114:処理水水槽115:
軸封水部    116:集水部117  :中空糸 
    118;中空糸折り返し部119:支持棒  
   120:連結棒121:中空糸膜濾過装置
Fig. 1 is a schematic cross-sectional view for explaining an example of an air cleaning type hollow fiber membrane filtration device, and Fig. 2 is a perspective view for explaining a single-end water collection type hollow fiber membrane module applied to Fig. 1. 3 and 4 are schematic cross-sectional views for explaining a modification of the air cleaning type hollow fiber membrane filtration device shown in FIG.
FIG. 5 is a perspective view for explaining a hollow membrane module of both-ends water collection type installed in the apparatus shown in FIG. 4, and FIG. 6 is a cross-sectional view showing an example of a hollow fiber membrane filtration device with movable cleaning member A schematic diagram, FIG. 7 is a perspective view showing the configuration of a cleaning member and a hollow fiber membrane module, and FIG. 8 is a diagram for explaining a modification of the cleaning member movable hollow fiber membrane filtration device shown in FIG. 6. It is a cross-sectional schematic diagram. 1: Hollow fiber membrane filtration device 2: Hollow fiber membrane module 3: Diffusion device 4: Air pipe 5 Niblower 6: Raw water pump 7: Raw water inflow pipe 8: Washing pump 9: Washing pipe 10:
Treated water pipe 11: Drain valve 12: Exhaust pipe 13:
Drain valve 14: Drain pipe 15: Raw water pipe
16: Treated water tank - 17: Water collection section 18
: Hollow fiber 19: Hollow fiber folded part 20: Support rod 21.
22: Hollow fiber membrane filtration device 23: Both ends water collection type hollow fiber membrane Modineal 24: Hollow fiber 25. 26: Water collection section 101: Hollow fiber membrane filtration device 102: Hollow fiber membrane module 103: Cleaning member 104: Raw water Pump 105:
Raw water inflow pipe 106: Washing pump 107: Washing pipe
108: Treated water pipe 109: Treated water valve 1
10: Washing valve 111: Drain valve 112: Drain pipe 113: Raw water tank 114: Treated water tank 115:
Shaft water sealing part 116: Water collecting part 117: Hollow fiber
118; Hollow fiber folded part 119: Support rod
120: Connecting rod 121: Hollow fiber membrane filtration device

Claims (2)

【特許請求の範囲】[Claims] (1)複数の中空糸と、中空糸と連通した集水部とを有
する中空糸膜モジュールの1以上を槽内に少なくとも備
えた中空糸膜濾過装置において、該中空糸膜モジュール
の中空糸を水平方向に支持すると共に中空糸を洗浄する
ための散気装置および/または散水装置を配備したこと
を特徴とする中空糸膜濾過装置。
(1) In a hollow fiber membrane filtration device comprising at least one or more hollow fiber membrane modules each having a plurality of hollow fibers and a water collection portion communicating with the hollow fibers in a tank, the hollow fibers of the hollow fiber membrane module are A hollow fiber membrane filtration device characterized in that it supports the hollow fibers in a horizontal direction and is equipped with an aeration device and/or a water sprinkler device for cleaning the hollow fibers.
(2)複数の中空糸と、中空糸と連通した集水部とを有
する中空糸膜モジュールの1以上を槽内に少なくとも備
えた中空糸膜濾過装置において、中空糸膜モジュールの
中空糸を水平方向又は垂直方向に支持すると共に該装置
の外から部材を運動させることにより各モジュールの一
部又は全ての中空糸を運動させ、洗浄せしめるように該
部材を配備したことを特徴とする中空糸膜濾過装置。
(2) In a hollow fiber membrane filtration device including at least one or more hollow fiber membrane modules each having a plurality of hollow fibers and a water collection portion communicating with the hollow fibers in a tank, the hollow fibers of the hollow fiber membrane modules are horizontally disposed. A hollow fiber membrane characterized in that the member is arranged so as to support in the direction or perpendicular direction and to move a part or all of the hollow fibers of each module by moving the member from outside the device and cleaning it. Filtration device.
JP2308488A 1990-11-16 1990-11-16 Hollow fiber membrane filtration device Expired - Lifetime JPH0716589B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2308488A JPH0716589B2 (en) 1990-11-16 1990-11-16 Hollow fiber membrane filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2308488A JPH0716589B2 (en) 1990-11-16 1990-11-16 Hollow fiber membrane filtration device

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP6219574A Division JP2987546B2 (en) 1994-08-23 1994-08-23 Hollow fiber membrane filtration device

Publications (2)

Publication Number Publication Date
JPH04180821A true JPH04180821A (en) 1992-06-29
JPH0716589B2 JPH0716589B2 (en) 1995-03-01

Family

ID=17981621

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2308488A Expired - Lifetime JPH0716589B2 (en) 1990-11-16 1990-11-16 Hollow fiber membrane filtration device

Country Status (1)

Country Link
JP (1) JPH0716589B2 (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994011094A1 (en) * 1992-11-17 1994-05-26 Zenon Environmental Inc. Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
JPH07251043A (en) * 1994-01-28 1995-10-03 Toto Ltd Filtering method and filter device
WO2000007940A3 (en) * 1998-08-04 2000-05-11 Wehrle Werk Ag Method and device for separating biomass from water
US6245239B1 (en) 1998-10-09 2001-06-12 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
JP2003513784A (en) * 1999-11-18 2003-04-15 ゼノン、エンバイロンメンタル、インコーポレーテッド Immersion thin film elements and modules
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6620319B2 (en) 1995-08-11 2003-09-16 Zenon Enviromental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
JP2009183847A (en) * 2008-02-05 2009-08-20 Panasonic Electric Works Co Ltd Filtration apparatus
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
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009120384A2 (en) 2008-03-28 2009-10-01 Siemens Water Technologies Corp. Hybrid aerobic and anaerobic wastewater and sludge treatment systems and methods

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5627925U (en) * 1980-07-31 1981-03-16
JPS60261509A (en) * 1984-06-11 1985-12-24 Toshiba Corp Hollow yarn membrane module and filtration device using said module

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5627925U (en) * 1980-07-31 1981-03-16
JPS60261509A (en) * 1984-06-11 1985-12-24 Toshiba Corp Hollow yarn membrane module and filtration device using said module

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994011094A1 (en) * 1992-11-17 1994-05-26 Zenon Environmental Inc. Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
JPH07251043A (en) * 1994-01-28 1995-10-03 Toto Ltd Filtering method and filter device
US6620319B2 (en) 1995-08-11 2003-09-16 Zenon Enviromental Inc. 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
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. 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
US6682652B2 (en) 1995-08-11 2004-01-27 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes
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
US6964741B2 (en) 1995-08-11 2005-11-15 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
WO2000007940A3 (en) * 1998-08-04 2000-05-11 Wehrle Werk Ag Method and device for separating biomass from water
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7186343B2 (en) 1998-10-09 2007-03-06 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7198721B2 (en) 1998-10-09 2007-04-03 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7347942B2 (en) 1998-10-09 2008-03-25 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US6881343B2 (en) 1998-10-09 2005-04-19 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7625491B2 (en) 1998-10-09 2009-12-01 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US6245239B1 (en) 1998-10-09 2001-06-12 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US7820050B2 (en) 1998-10-09 2010-10-26 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US7922910B2 (en) 1998-10-09 2011-04-12 Zenon Technology Partnership Cyclic aeration system for submerged membrane modules
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
JP2003513784A (en) * 1999-11-18 2003-04-15 ゼノン、エンバイロンメンタル、インコーポレーテッド Immersion thin film elements and modules
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
JP2009183847A (en) * 2008-02-05 2009-08-20 Panasonic Electric Works Co Ltd Filtration apparatus

Also Published As

Publication number Publication date
JPH0716589B2 (en) 1995-03-01

Similar Documents

Publication Publication Date Title
JPH04180821A (en) Hollow yarn film filtration device
WO2001000307A2 (en) Self cleaning filter
JP2000189958A (en) Immersion type membrane filter device
JP2008229628A (en) Water treatment apparatus and water treatment method
JP3815645B2 (en) Immersion type flat membrane separator and control method thereof
JPH09215980A (en) Method for membrane separation and bioprocessing of waste water
JP2000343095A (en) Activated sludge treating device
JPH04222622A (en) Membrane filter for ultra or micro filtration of liquid particularly for water
JPH0947762A (en) Membrane module for waste water treatment and waste water treatment device and waste water treatment using the same
JP3440402B2 (en) Water treatment method
JP4188226B2 (en) Filtration device and filtration method using the filtration device
JP2987546B2 (en) Hollow fiber membrane filtration device
JPH0975970A (en) Dipping type membrane separation device using hollow fiber membrane
JP2003236349A (en) Method of operating membrane separator
JPH05154354A (en) Membrane filtration apparatus
JP2002239308A (en) Filter apparatus using floating filter medium and water treatment method
JP3583202B2 (en) Filtration device and filtration operation method
JPH09201519A (en) Flat membrane separator
JPH07275859A (en) Sewage treatment apparatus
JPH04187219A (en) Hollow yarn membrane module and filter
JP2002219484A (en) Dynamic filtration equipment
JP4818508B2 (en) Water treatment equipment
JP2592579Y2 (en) Wastewater treatment equipment using water treatment medium
JPH11128098A (en) Bath water purifying device
JPH09271613A (en) Sewage filtering apparatus