JPH0938470A - Filter - Google Patents

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Publication number
JPH0938470A
JPH0938470A JP18922895A JP18922895A JPH0938470A JP H0938470 A JPH0938470 A JP H0938470A JP 18922895 A JP18922895 A JP 18922895A JP 18922895 A JP18922895 A JP 18922895A JP H0938470 A JPH0938470 A JP H0938470A
Authority
JP
Japan
Prior art keywords
partition plate
container
pipe
liquid
supply pipe
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
JP18922895A
Other languages
Japanese (ja)
Other versions
JP3349015B2 (en
Inventor
Michio Murase
道雄 村瀬
Kiyoshi Fujimoto
清志 藤本
Masato Kobayashi
政人 小林
Seiichi Kazama
誠一 風間
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP18922895A priority Critical patent/JP3349015B2/en
Publication of JPH0938470A publication Critical patent/JPH0938470A/en
Application granted granted Critical
Publication of JP3349015B2 publication Critical patent/JP3349015B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • B01D65/08Prevention of membrane fouling or of concentration polarisation
    • 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
    • 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
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/20By influencing the flow
    • B01D2321/2033By influencing the flow dynamically
    • B01D2321/2058By influencing the flow dynamically by vibration of the membrane, e.g. with an actuator

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide an inexpensive filter having a simple structure, which is capable of evenly supplying a gas for cleaning to plural hollow yarn membrane modules. SOLUTION: A parting plate 20 is provided below the bottom end of a module cylinder 14 in a vessel 11 and a ventilation hole 21 is provided directly below the module cylinder 14 of the parting plate 20 in one-to-one. Water pipes 22 are provided among the plural ventilation holes (for example, one water pipe 22 to 3 ventilation holes 21 are provided). An intake gas pipe 16 is connected to a vessel 11 below the parting plate 20 and an intake gas diffusing pipe 10 having plural intake gas holes 31 is connected to the intake gas pipe 16. At the time of purifying, the gas supplied from the intake gas pipe 16 forms a gas layer having uniform thickness at the lower part of the parting plate 20 and uniformly flows into the respective module cylinders 14 through the ventilation holes 21 to give an adequate vibration to a hollow yarn membrane 13 to remove impurities.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、浄化する液体を複数の
濾過モジュ−ルに通じることにより被浄化液を濾過する
濾過装置に係り、特に、濾過モジュ−ルを簡単な構造で
洗浄するに好適な濾過装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter device for filtering a liquid to be purified by passing a liquid to be purified through a plurality of filtration modules, and more particularly to cleaning the filtration module with a simple structure. It relates to a suitable filtration device.

【0002】[0002]

【従来の技術】被浄化液を濾過する濾過装置において
は、長時間の浄化によって濾過モジュ−ルの濾過性能が
低下すると、洗浄して再使用する。中空糸膜モジュ−ル
を用いた濾過装置では、中空糸膜モジュ−ルの下方から
空気などの気体を流入して中空糸をゆらせて洗浄する。
このとき、各中空糸膜モジュ−ルに供給する気体流量が
少なすぎると洗浄効果が低下し、多すぎると中空糸の寿
命が低下するため、各中空糸膜モジュ−ルに均等に気体
を供給する必要がある。
2. Description of the Related Art In a filtration device for filtering a liquid to be purified, if the filtration performance of a filtration module deteriorates due to long-term purification, it is washed and reused. In a filtration device using a hollow fiber membrane module, a gas such as air is introduced from below the hollow fiber membrane module to shake the hollow fibers for cleaning.
At this time, if the gas flow rate to be supplied to each hollow fiber membrane module is too low, the cleaning effect will be reduced, and if it is too high, the life of the hollow fiber will be reduced, so that the gas is evenly supplied to each hollow fiber membrane module. There is a need to.

【0003】中空糸膜モジュ−ルを用いた従来の濾過装
置の典型として、特開昭61−222509号公報に記
載のものがある。この公知技術は、各中空糸膜モジュ−
ルの直下に被浄化液の出口を有する仕切板を設け、この
仕切板の下側の流出口に上下が開口した筒を接続してい
る。この筒の側壁には複数の小孔を長さ方向に付設して
いる。洗滌時には仕切板より下方にある給気管から供給
した圧縮気体を仕切板の下に層状に溜めた後、筒の小孔
と仕切板の流出口を通して各中空糸膜モジュ−ルに給気
するものである。
As a typical example of a conventional filtration device using a hollow fiber membrane module, there is one described in JP-A-61-222509. This known technique is based on each hollow fiber membrane module.
A partition plate having an outlet for the liquid to be purified is provided directly under the partition, and a cylinder having upper and lower openings is connected to the lower outlet of the partition plate. A plurality of small holes are attached to the side wall of the cylinder in the length direction. During cleaning, the compressed gas supplied from the air supply pipe below the partition plate is accumulated in layers under the partition plate, and then it is supplied to each hollow fiber membrane module through the small hole in the cylinder and the outlet of the partition plate. Is.

【0004】また、異なるタイプとして、特告平4−6
2770号公報記載のものがある。この公知技術は、上
記例のように仕切板や通水の筒を設けず、中空糸膜モジ
ュ−ルの各列に対して給気管を配置するとともに、各中
空糸膜モジュ−ルの直下において給気管に小孔を設け、
この小孔を通して、各中空糸膜モジュ−ルに直接、給気
するものである。
As a different type, Japanese Patent Application No. 4-6
There is one described in Japanese Patent No. 2770. According to this known technique, a partition plate or a water passage tube is not provided as in the above example, an air supply pipe is arranged for each row of hollow fiber membrane modules, and the pipes are provided directly under each hollow fiber membrane module. A small hole is provided in the air supply pipe,
Air is directly supplied to each hollow fiber membrane module through the small holes.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記公
知技術には以下の課題が存在する。
However, the above-mentioned known technology has the following problems.

【0006】すなわち、特開昭61−222509号の
技術においては、浄化運転時の被浄化液の通水と洗浄時
の給気を仕切板に接続した筒で兼用している。この方式
による各中空糸膜モジュ−ルへの給気は最終的には浮力
で行われるため、中空糸膜モジュ−ル1個に対してその
直下に1個の筒が必要であり、仕切板には多数の筒が取
付けられる。しかも、給気時には筒の内部が気液二相と
なり流れが不安定化するとともに、給気のための静水頭
が低下するため筒を長くする必要があるなど、設備費が
高くなる。
That is, in the technique disclosed in JP-A-61-222509, the cylinder connected to the partition plate serves both as the passage of the liquid to be purified during the cleaning operation and the supply of air during the cleaning. Since air supply to each hollow fiber membrane module by this system is ultimately performed by buoyancy, one hollow fiber membrane module needs one cylinder immediately below it, and the partition plate A large number of cylinders are attached to the. Moreover, during air supply, the inside of the cylinder becomes a gas-liquid two-phase and the flow becomes unstable, and the hydrostatic head for air supply decreases, so that the cylinder needs to be lengthened, resulting in high equipment costs.

【0007】また、特告平4−62770号の技術にお
いては、中空糸膜モジュ−ルの1列毎に給気管を設け
る。このため、容器の内容積が増大するとともに、容器
底部の検査時に給気管を取外しするための構造が複雑に
なるなど、同様に設備費が高くなる。
Further, in the technique of Japanese Patent Application No. 4-62770, an air supply pipe is provided for each row of hollow fiber membrane modules. Therefore, the inner volume of the container increases, and the structure for removing the air supply pipe at the time of inspecting the bottom of the container becomes complicated.

【0008】本発明の目的は、複数の中空糸膜モジュ−
ルに浄化時には被浄化液を、洗浄時には気体を供給で
き、構成が簡単で安価な濾過装置を提供することにあ
る。
The object of the present invention is to provide a plurality of hollow fiber membrane modules.
It is an object of the present invention to provide a filtration device which can supply a liquid to be purified at the time of cleaning and a gas at the time of cleaning and which has a simple structure and is inexpensive.

【0009】[0009]

【課題を解決するための手段】本発明の上記の目的は、
容器と、前記容器内に隔離板と前記隔離板に接続した複
数の濾過モジュ−ルと、前記容器内に被浄化液を供給す
る給水管及び気体を供給する給気管とを有し、前記被浄
化液を前記濾過モジュ−ルに通じて前記被浄化液を浄化
する濾過装置において、その下側に供給気体の層を形成
するための仕切板を前記濾過モジュ−ルの下方で前記給
水管及び前記給気管より上方に略水平に備え、前記濾過
モジュ−ルに対応してその直下の前記仕切板に通気孔を
設けるとともに、前記被浄化液を前記仕切板の上方に通
じる通水部を前記通気孔と分離して設けたことにより達
成される。
SUMMARY OF THE INVENTION The above objects of the present invention are as follows.
A container, a separator plate inside the container, a plurality of filtration modules connected to the separator plate, a water supply pipe for supplying the liquid to be purified and an air supply pipe for supplying gas into the container, In a filtration device for purifying the liquid to be purified by passing a purification liquid through the filtration module, a partition plate for forming a layer of supply gas is provided below the filtration module under the filtration module. It is provided substantially horizontally above the air supply pipe, a ventilation hole is provided in the partition plate immediately below it corresponding to the filtration module, and a water passage portion that communicates the liquid to be purified above the partition plate is provided. This is achieved by providing it separately from the ventilation hole.

【0010】前記通水部は、前記通気孔を含まないよう
に通気孔間の仕切板に配置、もしくは、仕切板の外周部
を開放して容器との間隙部で形成することを特徴とす
る。
The water passage portion is arranged in a partition plate between the ventilation holes so as not to include the ventilation holes, or is formed in a gap portion with the container by opening the outer peripheral portion of the partition plate. .

【0011】また、前記通水部は、上下を開放し上端を
前記仕切板に接続した通水管を、複数の前記通気孔の間
に配置したことを特徴とする。
Further, the water passage portion is characterized in that a water passage pipe whose upper and lower sides are opened and an upper end thereof is connected to the partition plate is arranged between the plurality of ventilation holes.

【0012】また、複数の前記通気孔が前記仕切板の平
面上で千鳥状に配置され、隣接する3の通気孔を頂点と
する三角形の中央部に前記通水管の上端を配置したこと
を特徴とする。
Further, a plurality of the ventilation holes are arranged in a staggered manner on the plane of the partition plate, and the upper end of the water pipe is arranged at the central portion of a triangle having the three ventilation holes adjacent to each other as vertices. And

【0013】また、複数の前記通気孔に、それぞれ異な
る長さの通気管の上端を接続したことを特徴とする。
Further, the upper ends of the ventilation pipes having different lengths are connected to the plurality of ventilation holes.

【0014】また、前記容器に内接するとともに前記仕
切板の外周より小さい開口を有して前記仕切板を取外し
可能に支持する支持板を設け、さらには、前記支持板に
上端を接続したドレン管を設けたことを特徴とする。
Further, there is provided a support plate which is inscribed in the container and has an opening smaller than the outer periphery of the partition plate to detachably support the partition plate, and further, a drain pipe having an upper end connected to the support plate. Is provided.

【0015】また、前記給気管に接続して、容器と給気
管との接続部より上方に出口を有する給気流出管を設
け、前記開口が洗滌時に前記仕切板の下方に形成される
気体層の開口することを特徴とする。
Further, there is provided an air supply outflow pipe which is connected to the air supply pipe and has an outlet above a connecting portion between the container and the air supply pipe, and the opening forms a gas layer formed below the partition plate during cleaning. It is characterized by opening.

【0016】[0016]

【作用】以上のように、本発明の構成においては、容器
内の濾過モジュ−ルの下端より下方に仕切板を略水平
(気体層がほぼ均等になる程度の水平)に設け、濾過モ
ジュ−ルに対応して仕切板の各濾過モジュ−ル直下に通
気孔を設けている。さらに、被浄化液を仕切板下方から
上方へ通じる通水部を前記通気孔とは独立して配置して
いる。通水部は、仕切板の複数の通気孔の間に設けた開
口部に上端を接続した複数の通水管で構成し、あるい
は、仕切板の外周部と容器の間を開放する構成として、
前記通気孔と独立した通水部を実現できる。
As described above, in the structure of the present invention, a partition plate is provided below the lower end of the filtration module in the container substantially horizontally (horizontally so that the gas layer is substantially even), and the filtration module is provided. Ventilation holes are provided directly below each filtration module of the partition plate corresponding to each module. Further, a water passage portion for communicating the liquid to be purified upward from below the partition plate is arranged independently of the ventilation hole. The water passage portion is composed of a plurality of water pipes whose upper ends are connected to the openings provided between the plurality of ventilation holes of the partition plate, or as a configuration for opening between the outer peripheral portion of the partition plate and the container,
It is possible to realize a water passage portion independent of the ventilation hole.

【0017】濾過モジュ−ルの洗浄時には、容器に接続
した給気管から供給された気体は仕切板の下方に気体層
を形成し、仕切板に設けた通気孔を通って各濾過モジュ
−ルに流入する。このとき、通気孔を出た気体は仕切板
上側の水中の浮力によって濾過モジュ−ルに流入するの
で、本発明のように濾過モジュ−ルの直下に通気孔を設
けることで給気が可能になる。一方、浄化時の被浄化液
を供給する通水部は、濾過モジュ−ルの直下であること
も、濾過モジュ−ルと一対一であることも必要としない
ので、本発明のように通気孔と分離され、独立した構成
が可能になる。
At the time of cleaning the filtration module, the gas supplied from the air supply pipe connected to the container forms a gas layer below the partition plate, and passes through the ventilation holes provided in the partition plate to reach each filtration module. Inflow. At this time, the gas that has exited the ventilation hole flows into the filtration module by the buoyancy of water in the upper side of the partition plate, so that it is possible to supply air by providing the ventilation hole directly below the filtration module as in the present invention. Become. On the other hand, since the water passage for supplying the liquid to be purified at the time of purification does not need to be directly under the filtration module or one-to-one with the filtration module, the ventilation hole as in the present invention. It is separated from the above, and an independent configuration becomes possible.

【0018】このような本発明によれば、通水部の設計
の自由度が高まり、通水管の本数を削減したり、仕切板
に通水管を有しない構成も可能となるので、濾過装置の
構造が簡単になり、小型化や設備費の低減が可能にな
る。
According to the present invention as described above, the degree of freedom in designing the water passage portion is increased, the number of water passage pipes can be reduced, and a construction in which the partition plate does not have a water passage pipe is possible. The structure is simple, and it is possible to downsize and reduce the equipment cost.

【0019】また、通水部の内部は常に液単相であり、
流れが安定で給気のための静水頭も大きくなるため、通
水部を短くできる。
Further, the inside of the water passage is always a liquid single phase,
Since the flow is stable and the static head for air supply is large, the water passage can be shortened.

【0020】また、各濾過モジュ−ル直下に設けた通気
孔を複数とし、それぞれ異なる長さの通気管を前記通気
孔に接続する。これにより、給気流量を増加する場合、
仕切板の下方の通水部を除く部分に形成される気体層が
厚くなるが、短い通気管から順番に気体が流れるため気
体が流れる通気管の数が増加し、気体層厚さの急激な増
加を抑制できる。この結果、給気流量が多い場合にも通
水部を短くできる。
Further, a plurality of ventilation holes are provided immediately below each filtration module, and ventilation pipes having different lengths are connected to the ventilation holes. As a result, when increasing the air supply flow rate,
The gas layer formed under the partition plate excluding the water passage portion becomes thicker, but the gas flows in order from the short ventilation pipes, so the number of ventilation pipes through which the gas flows increases, and the gas layer thickness increases rapidly. The increase can be suppressed. As a result, the water passage portion can be shortened even when the supply air flow rate is large.

【0021】さらに、容器に内接するとともに仕切板の
外周より小さい開口を有する仕切板の支持板を設け、上
下を開放し上端を支持板に接続したドレン管を設けるこ
とにより、容器底部の点検時に仕切板を容易に取外しで
きるとともに、支持板の上に溜る液体や不純物をドレン
管から容易に排水できる。
Further, by providing a support plate for the partition plate which is inscribed in the container and has an opening smaller than the outer circumference of the partition plate, and by providing a drain pipe whose upper and lower sides are opened and whose upper end is connected to the support plate, at the time of inspecting the container bottom part. The partition plate can be easily removed, and liquids and impurities accumulated on the support plate can be easily drained from the drain pipe.

【0022】また、容器と給気管との接続部より上方に
開口を有する給気流出管を設けることにより、給気流量
が少なく仕切板の下方の通水部を除く部分に形成される
気体層が薄い場合においても、給気流出管の開口が気体
層内に露出し液面を乱すことがなく、各濾過モジュ−ル
への給気量を安定化するとともに均等化することができ
る。
Further, by providing the air supply outflow pipe having an opening above the connecting portion between the container and the air supply pipe, the gas supply flow rate is small and the gas layer formed below the partition plate excluding the water passage part. Even when the thickness is small, the opening of the supply air outflow pipe is not exposed in the gas layer and disturbs the liquid surface, and the supply air amount to each filtration module can be stabilized and equalized.

【0023】さらに、給気管に接続し、複数の開口を有
する給気分散管を容器内に設けることにより、仕切板の
下方に形成される気体層の厚さを均一化し、各濾過モジ
ュ−ルへの給気量を均等化することができる。
Further, by providing an air supply dispersion pipe having a plurality of openings, which is connected to the air supply pipe, in the container, the thickness of the gas layer formed below the partition plate is made uniform, and each filtration module is provided. It is possible to equalize the amount of air supplied to.

【0024】[0024]

【実施例】以下、本発明の実施例を図面に従って詳細に
説明する。なお、各図を通して同じ部品には同一符号を
付している。
Embodiments of the present invention will now be described in detail with reference to the drawings. The same parts are denoted by the same reference numerals throughout the drawings.

【0025】本発明の第一の実施例を図1〜図3により
説明する。図1は第1の実施例による濾過装置の縦断面
図、図2は図1のA−A矢視図、図3は水平板の部分詳
細図である。
A first embodiment of the present invention will be described with reference to FIGS. 1 is a longitudinal sectional view of a filter device according to a first embodiment, FIG. 2 is a view taken along the line AA of FIG. 1, and FIG. 3 is a partial detailed view of a horizontal plate.

【0026】濾過装置は、容器11と、容器11内に配
置され、濾過機能をもつ中空糸膜13とモジュ−ル筒1
4で構成される中空糸膜モジュ−ルと、中空糸膜モジュ
−ルを支持する隔離板12と、中空糸膜モジュ−ル下端
より下方に配置され、通気孔21と通水管22とを有す
る仕切板20と、浄化する液体を供給する給水管15
と、中空糸膜13を洗浄する際に供給する気体の給気管
16と、容器11の上部に接続された流出管17と、隔
離板12の下方に接続された排気管18と、容器11の
下部に接続された排水管19を有している。
The filtration device comprises a container 11, a hollow fiber membrane 13 arranged inside the container 11 and having a filtering function, and a module cylinder 1.
4, a hollow fiber membrane module, a separator 12 for supporting the hollow fiber membrane module, a ventilator 21 and a water pipe 22 arranged below the lower end of the hollow fiber membrane module. Partition plate 20 and water supply pipe 15 for supplying liquid to be purified
An air supply pipe 16 for supplying gas when cleaning the hollow fiber membrane 13, an outflow pipe 17 connected to the upper part of the container 11, an exhaust pipe 18 connected below the separator 12, and an exhaust pipe 18 of the container 11. It has a drainage pipe 19 connected to the bottom.

【0027】本実施例の濾過装置において、通常の浄化
運転時には、被浄化液は給水管15から流入し、仕切板
20に接続した通水管22を通って各モジュ−ル筒14
内に均等に流入し、中空糸膜13でクラッドなどの不純
物を濾過された後、流出管17から流出する。このよう
な濾過運転により中空糸膜13に不純物が捕獲され、中
空糸膜13の濾過機能が低下すると、被浄化液の供給を
中止し、気体(通常は空気)を給気管16と給気分散管
30とを通して供給する。このとき、隔離板12より下
部の容器内は満水状態となっている。
In the filtration apparatus of this embodiment, during the normal purification operation, the liquid to be purified flows in from the water supply pipe 15 and passes through the water pipe 22 connected to the partition plate 20 to each module cylinder 14.
It evenly flows into the inside, and after impurities such as clad are filtered by the hollow fiber membrane 13, it flows out from the outflow pipe 17. When impurities are captured in the hollow fiber membranes 13 by such a filtration operation and the filtration function of the hollow fiber membranes 13 deteriorates, the supply of the liquid to be purified is stopped and the gas (usually air) is supplied to the air supply pipe 16 and the air supply dispersion. Supply through tube 30. At this time, the inside of the container below the separator 12 is full of water.

【0028】供給された気体により容器11内の仕切板
20下方で通水管22を除く部分に気体層24が形成さ
れ、仕切板20の通気孔21から流出した気体は被浄化
液中での浮力によって直上のモジュ−ル筒14に流入
し、気体の流れで中空糸膜13をゆらして捕獲された不
純物を離脱させ、洗浄終了後に不純物を被浄化液ととも
に排水管19から排出する。各濾過モジュ−ルに供給さ
れた気体は、モジュ−ルに筒14の上部に設けた孔から
流出し、排気管18から排気される。モジュ−ル筒14
に流入する気体流量は、少なすぎると中空糸膜13の洗
浄効果が弱くなり、多すぎると中空糸膜13の寿命が低
下するため、各濾過モジュ−ルに均等に供給されること
が重要である。
The supplied gas forms a gas layer 24 below the partition plate 20 in the container 11 except the water pipe 22, and the gas flowing out from the ventilation hole 21 of the partition plate 20 has a buoyancy force in the liquid to be purified. Then, the hollow fiber membrane 13 is caused to flow into the module cylinder 14 immediately above by the flow of the gas, the trapped impurities are removed, and after the cleaning is completed, the impurities are discharged from the drain pipe 19 together with the liquid to be purified. The gas supplied to each filtration module flows out from the hole provided in the upper part of the cylinder 14 in the module and is exhausted from the exhaust pipe 18. Module tube 14
If the flow rate of gas flowing into the filter is too low, the cleaning effect on the hollow fiber membranes 13 will be weak, and if it is too high, the life of the hollow fiber membranes 13 will be shortened. Therefore, it is important that the gas flow rates are uniformly supplied to each filtration module. is there.

【0029】仕切板20には、モジュ−ル筒14の直下
に通気孔21が設けられ、複数の通気孔21の間(本実
施例では3個の通気孔)の開口23に通水管22の上端
が接続されて、通水部を構成している。給気管16には
複数の給気孔31を有する給気分散管30が接続されて
いる。
Ventilation holes 21 are provided in the partition plate 20 immediately below the module cylinder 14, and water passages 22 are provided in openings 23 between the plurality of ventilation holes 21 (three ventilation holes in this embodiment). The upper end is connected to form a water passage. An air supply dispersion pipe 30 having a plurality of air supply holes 31 is connected to the air supply pipe 16.

【0030】通常の浄化運転時には、被浄化液は給水管
15から流入し、仕切板20に接続した通水管22を通
って各モジュ−ル筒14内に流入するが、通水管22は
通気孔21と独立であるため、モジュ−ル筒14毎に通
水管22を設ける必要がない。本実施例のように、例え
ば3本のモジュ−ル筒14に1個の通水管22で十分で
あり、通水管22の員数を低減できる。例えば、容器1
1の径が1.5m程度の場合で、通水管の径は10cm
程度、通気孔21の径は1cm程度であり、通水管の減
少による効果の大きいことが窺えるであろう。
During normal purification operation, the liquid to be purified flows in from the water supply pipe 15 and into each module cylinder 14 through the water passage pipe 22 connected to the partition plate 20, but the water passage pipe 22 has a vent hole. Since it is independent of 21, it is not necessary to provide the water pipe 22 for each module cylinder 14. As in this embodiment, for example, one water pipe 22 for three module cylinders 14 is sufficient, and the number of water pipes 22 can be reduced. For example, container 1
When the diameter of 1 is about 1.5 m, the diameter of the water pipe is 10 cm
The diameter of the vent hole 21 is about 1 cm, and it can be seen that the effect of reducing the number of water passages is great.

【0031】また、通気孔と通水管を独立する構成によ
り設計の自由度が大きくなる。通常、水平断面内の占有
率を高めて容器11を小型化するために、濾過モジュー
ルは三角格子状(あるいは千鳥状)に配置されている。
この場合、図示のように、3本のモジュール筒14を頂
点として形成される三角形(点線)の中央部に、通水管
を1本配置する構成とする。通水管22を通った被浄化
液は周囲の3つのモジュール14に分散して供給される
が、通水管22と各モジュール14は最短且つ等距離に
配置されているので、被浄化液は各モジュールに均等に
分配されるとともに、容器内の水の擾乱を防止できる利
点がある。
Moreover, the degree of freedom in design is increased by the structure in which the vent hole and the water pipe are independent. Usually, the filtration modules are arranged in a triangular lattice (or zigzag) in order to increase the occupation rate in the horizontal section and downsize the container 11.
In this case, as shown in the figure, one water pipe is arranged at the center of a triangle (dotted line) formed with the three module tubes 14 as vertices. The liquid to be purified that has passed through the water pipe 22 is dispersed and supplied to the three modules 14 in the surroundings, but since the water pipe 22 and each module 14 are arranged at the shortest distance and at the same distance, the liquid to be purified is to be supplied to each module. There is an advantage that it can be evenly distributed in the container and that the disturbance of the water in the container can be prevented.

【0032】ところで、洗滌時の定常状態において、給
気管16からの総給気量と通気孔21の全通過量は、数
1式の関係によってバランスし、そのときの気体層の厚
さはHとなる。
By the way, in the steady state at the time of cleaning, the total amount of air supplied from the air supply pipe 16 and the total amount of air passing through the vent hole 21 are balanced by the relationship of the equation 1, and the thickness of the gas layer at that time is H Becomes

【0033】[0033]

【数1】ρ・g・H=1/2・ζ・ρg・Vg2 ここで、ζ:通気孔21の抵抗係数、ρg:気体の密
度、ρ:通水部23の流体の密度、g:重力加速度、V
g:通気孔21からの気体の流出速度である。これよ
り、洗浄時におけるVgは、
## EQU1 ## ρ.g.H = 1 / 2..zeta..rho.g.Vg 2 where ζ is the resistance coefficient of the vent hole 21, ρg is the gas density, ρ is the fluid density of the water passage portion 23, g : Gravity acceleration, V
g: outflow rate of gas from the vent hole 21. From this, Vg at the time of washing is

【0034】[0034]

【数2】(Vg)2=(2/ζ)・(ρ/ρg)・g・H と、表わすことができる。## EQU2 ## It can be expressed as (Vg) 2 = (2 / ζ)  (ρ / ρg) gH

【0035】上記の従来技術では、通水管に通気孔を設
けているので、通水管内部が気液二相となって流体密度
ρが減少する。しかし、本実施例では、通水管22の内
部は液単相であり、流体密度ρは液体の密度になる。こ
の結果、同一の流出速度Vgを得るための気体層24の
厚さHを薄くでき、その分だけ通水管を短くすることが
できる。
In the above-mentioned conventional technique, since the water passage is provided with the vent hole, the inside of the water passage becomes a gas-liquid two phase and the fluid density ρ decreases. However, in this embodiment, the inside of the water flow pipe 22 is a liquid single phase, and the fluid density ρ is the density of the liquid. As a result, the thickness H of the gas layer 24 for obtaining the same outflow velocity Vg can be reduced, and the water pipe can be shortened accordingly.

【0036】また、複数の給気孔31を有する給気分散
管30によって、気体を分散して供給し、気体層24の
厚さ分布を均一化し、各モジュ−ル筒14への給気量を
均一化することができる。給気孔31はクラッドが入ら
ないように、主として給気分散管30の側面に設けられ
るが、給気開始後の排水のために先端近くの下面に、給
気終了後の排気のために上面にも設けられる。
Further, the gas is dispersed and supplied by the air supply dispersion pipe 30 having a plurality of air supply holes 31, the thickness distribution of the gas layer 24 is made uniform, and the amount of air supplied to each module cylinder 14 is adjusted. It can be made uniform. The air supply hole 31 is provided mainly on the side surface of the air supply dispersion pipe 30 so that the clad does not enter, but is provided on the lower surface near the tip for drainage after the start of air supply, and on the upper surface for exhaust after the end of air supply. Is also provided.

【0037】以上説明したように、本実施例の濾過装置
によれば、仕切板20の通気孔21と通水管22を独立
に設けることができるので、通水管22の員数を低減で
きるとともに、通水管22の内部が液単相となるので通
水管22を短くでき、経済性を向上することができる。
As described above, according to the filtration device of this embodiment, the ventilation hole 21 and the water passage 22 of the partition plate 20 can be provided independently, so that the number of water passages 22 can be reduced and Since the inside of the water pipe 22 becomes a liquid single phase, the water pipe 22 can be shortened and the economical efficiency can be improved.

【0038】図4は、第1の一実施例の変形例による濾
過装置の部分詳細図である。本変形例において、第1の
一実施例と異なる点は、複数の通気孔21a,21b,
21cを有し、通気孔21b,21cには異なる長さの
通気管27b,27cを接続し、各通気孔21a,21
b,21cの長さが異なることである。
FIG. 4 is a partial detailed view of a filter device according to a modification of the first embodiment. This modification is different from the first embodiment in that a plurality of ventilation holes 21a, 21b,
21c, and ventilation pipes 27b and 27c of different lengths are connected to the ventilation holes 21b and 21c, respectively.
That is, the lengths of b and 21c are different.

【0039】一般に、中空糸膜の洗浄時の給気量は一定
である。しかし、例えば、給気量を大幅に増加する必要
が生じた場合、(数1)から明らかなように気体層24
の厚さHは給気量の二乗に比例して急増する。本変形例
においては、給気量が大幅に増加して気体層24の厚さ
が増加すると、気体を供給する通気孔の数が21a,2
1b,21cのように順次増加する。このため、気体層
24の厚さの増加を抑制でき、給気量が大幅に変化する
場合においても、通水管22を短くできる。
Generally, the amount of air supplied during cleaning of the hollow fiber membrane is constant. However, for example, when it becomes necessary to greatly increase the supply air amount, the gas layer 24 becomes clear from (Equation 1).
The thickness H of the abruptly increases in proportion to the square of the air supply amount. In this modification, when the supply amount of air is significantly increased and the thickness of the gas layer 24 is increased, the number of ventilation holes for supplying gas is 21a, 2a.
It increases sequentially like 1b and 21c. Therefore, the increase in the thickness of the gas layer 24 can be suppressed, and the water pipe 22 can be shortened even when the supply amount of air changes significantly.

【0040】次に、本発明の第2の実施例を図5〜図7
により説明する。
Next, a second embodiment of the present invention will be described with reference to FIGS.
This will be described below.

【0041】図5は本発明の第2の実施例による濾過装
置の縦断面図、図6は図5のA−A矢視図、図7は仕切
板の部分詳細図である。
FIG. 5 is a longitudinal sectional view of a filter device according to a second embodiment of the present invention, FIG. 6 is a view taken along the line AA of FIG. 5, and FIG. 7 is a partial detailed view of a partition plate.

【0042】本実施例において、第1の実施例と異なる
点は、第1の実施例の給気分散管30を設けず、代わり
に複数の給気管16を容器11に接続したことにある。
また、1本のモジュ−ル筒14に対してほぼ1個の通水
管22を設けている。この点は好適例ではあるが必要条
件ではない。
The present embodiment is different from the first embodiment in that the air supply dispersion pipe 30 of the first embodiment is not provided and a plurality of air supply pipes 16 are connected to the container 11 instead.
Further, one water pipe 22 is provided for one module cylinder 14. This is a preferable example, but it is not a necessary condition.

【0043】中空糸膜13の洗浄時に、複数の給気管1
6から分散して供給された気体は、仕切板20の下部に
気体層24を形成し、通気孔21を通って各モジュ−ル
筒14に供給される。
When cleaning the hollow fiber membranes 13, a plurality of air supply pipes 1
The gas dispersedly supplied from 6 forms a gas layer 24 in the lower part of the partition plate 20, and is supplied to each module cylinder 14 through the ventilation hole 21.

【0044】本実施例の特徴は、通水管22の員数が多
く、給気分散管30の配置に困難があるような場合に、
気体層24の厚さ分布を均一化し、各モジュ−ル筒14
への給気量を均一化するのに有効である。なお、通水管
22の員数を増やすと、管内の流速を低下させることが
できる。
The feature of this embodiment is that when the number of the water flow pipes 22 is large and it is difficult to arrange the air supply dispersion pipes 30,
The thickness distribution of the gas layer 24 is made uniform, and each module cylinder 14
It is effective to make the air supply to the air uniform. It should be noted that increasing the number of water passage pipes 22 can reduce the flow velocity in the pipes.

【0045】図8は、第2の実施例の変形例による濾過
装置の下方から見た水平断面図、図9はその部分縦断面
図、図10はその別の位置での部分縦断面図である。
FIG. 8 is a horizontal sectional view of a filter device according to a modification of the second embodiment as seen from below, FIG. 9 is a partial vertical sectional view thereof, and FIG. 10 is a partial vertical sectional view at another position thereof. is there.

【0046】本変形例において、第2の実施例と異なる
第1点は、仕切板20を支持する支持板125を設け、
支持板125にドレン管126を設けたことである。仕
切板20と支持板125は、図示していない締結手段に
よって係止される。第2点は、給気管16に開口が給気
管16と容器11との接続部より高い位置に、出口13
3を有する給気流出管132を設けたことである。な
お、これら第1点と第2点は、互いに他を必要条件とは
していない。
In this modification, the first difference from the second embodiment is that a support plate 125 for supporting the partition plate 20 is provided,
That is, the drain pipe 126 is provided on the support plate 125. The partition plate 20 and the support plate 125 are locked by fastening means (not shown). The second point is that the opening of the air supply pipe 16 is higher than the connecting portion between the air supply pipe 16 and the container 11, and the outlet 13
That is, the supply air outflow pipe 132 having No. 3 is provided. Note that these first and second points do not require each other as a necessary condition.

【0047】容器11に接続する支持板125を仕切板
20とを分離することにより、容器11の底部を点検す
る際に仕切板20を容易に取り外すことができる。この
場合、容器11と仕切板20の間の支持板125上に液
体や不純物が溜るが、支持板125に接続したドレン管
126により排水でき、また、ドレン管126の長さを
通水管22の長さと同じにすることにより、中空糸膜の
洗浄時に気体が流出することもない。
By separating the support plate 125 connected to the container 11 from the partition plate 20, the partition plate 20 can be easily removed when the bottom of the container 11 is inspected. In this case, liquids and impurities are collected on the support plate 125 between the container 11 and the partition plate 20, but the drain pipe 126 connected to the support plate 125 can drain the liquid and impurities, and the length of the drain pipe 126 can increase the length of the water passage pipe 22. By making the length the same, the gas does not flow out when the hollow fiber membrane is washed.

【0048】また、第2の実施例(図7)においては、
給気量が小さく空気層24の厚さが薄くなり水面が給気
管16より高くなると、給気によって液面が乱れ通気孔
21からの通気量が変動する。本変形例においては、図
9に示すように給気流出管132が上部方向に曲折され
て、その先端にある出口133の位置が給気管16との
接続位置より高いため、給気量が小さく空気層24の厚
さが薄くなっても通気孔21からの通気量が変動するこ
となく安定して供給できる。
In addition, in the second embodiment (FIG. 7),
When the air supply amount is small and the air layer 24 is thin and the water surface is higher than the air supply pipe 16, the liquid surface is disturbed by the air supply, and the air flow amount from the ventilation hole 21 is changed. In this modification, the supply air outflow pipe 132 is bent upward as shown in FIG. 9, and the position of the outlet 133 at the tip thereof is higher than the connection position with the supply air pipe 16, so that the supply air amount is small. Even if the thickness of the air layer 24 becomes thin, the amount of ventilation from the ventilation hole 21 does not fluctuate, and stable supply is possible.

【0049】図11は、第2の実施例の他の変形例によ
る部分縦断面図で、図9に相当する図である。
FIG. 11 is a partial longitudinal sectional view of another modification of the second embodiment, which is equivalent to FIG.

【0050】本変形例において、図9の変形例と異なる
点は、給気流出管132の上向きの先端を閉じ、先端付
近の管壁で容器11の中心部側に出口134を設けたこ
とである。これによれば、給気流出管132の出口13
4から気体が水平に流出し、仕切板20の下方に拡がり
易くなるため、気体層の厚さ分布を均一化し、各モジュ
−ル筒14に均等に気体を供給することができる。
In this modification, the difference from the modification of FIG. 9 is that the upward end of the supply air outflow pipe 132 is closed and the outlet 134 is provided on the center side of the container 11 by the pipe wall near the end. is there. According to this, the outlet 13 of the supply air outflow pipe 132
Since the gas flows out horizontally from 4 and easily spreads below the partition plate 20, the thickness distribution of the gas layer can be made uniform, and the gas can be evenly supplied to each module cylinder 14.

【0051】次に、本発明の第3の実施例を図12〜図
14により説明する。図12は第3の実施例による濾過
装置の縦断面図、図13は図12のA−A矢視図、図1
4は仕切板の部分詳細図である。
Next, a third embodiment of the present invention will be described with reference to FIGS. 12 is a vertical sectional view of a filter device according to a third embodiment, FIG. 13 is a view taken along the line AA of FIG. 12, and FIG.
4 is a partial detailed view of the partition plate.

【0052】本実施例において、第1の実施例や第2の
実施例と異なる点は、仕切板20に設けていた通水管2
2がなく、仕切板20の外縁部に下向きに設けた外周板
201と容器11の間に通水部220を形成したことで
ある。
This embodiment is different from the first and second embodiments in that the water pipe 2 provided on the partition plate 20 is different.
That is, there is no 2 and the water passage portion 220 is formed between the outer peripheral plate 201 provided downward on the outer edge portion of the partition plate 20 and the container 11.

【0053】本実施例では、他で仕切板20に設けてい
た多数の通水管を持たないので、極めてシンプルな構造
となり、設備費を低減でき、小型化も可能になる。ただ
し、通水部220を出た後で容器11の中心部に向かう
横流れが生じるため、モジュ−ル筒14への流体力が増
加するため、被浄化液の処理流量に制約を生じる。
In this embodiment, since the other large number of water pipes provided in the partition plate 20 are not provided, the structure is extremely simple, the equipment cost can be reduced, and the size can be reduced. However, since a lateral flow toward the center of the container 11 occurs after leaving the water passage 220, the fluid force on the module cylinder 14 increases, and thus the treatment flow rate of the liquid to be purified is restricted.

【0054】さらに、本実施例では、給気管16を複数
(図では2個)設け、給気管16に接続する給気分散管
230をヘッダ状としている。図示のように、給気分散
管230のヘッダ部は外周板201の内側に円弧状に形
成し、複数の給気孔231を設けている。通水管などの
障害物がないので、多数の給気孔から分散して供給され
た気体は、仕切板20の下部に均等な厚さ分布の気体層
24を形成し、通気孔21を通って各モジュ−ル筒14
に供給される。この構成によれば、容器下部の点検も容
易になる。
Further, in this embodiment, a plurality of (two in the figure) air supply pipes 16 are provided, and the air supply dispersion pipe 230 connected to the air supply pipes 16 is formed in a header shape. As shown in the figure, the header portion of the air supply dispersion pipe 230 is formed in an arc shape inside the outer peripheral plate 201 and is provided with a plurality of air supply holes 231. Since there are no obstructions such as water passages, the gas distributed and supplied from a large number of air supply holes forms a gas layer 24 having a uniform thickness distribution in the lower part of the partition plate 20, and passes through the air holes 21 to form a gas layer 24. Module tube 14
Is supplied to. With this configuration, it is easy to inspect the lower part of the container.

【0055】以上、本発明の第1の実施例から第3の実
施例まで、異なる形状の通水部や給気部などを適用した
が、これらのいかなる組合せでもよいことは自明であ
る。
As described above, the water passage portion and the air supply portion having different shapes are applied from the first embodiment to the third embodiment of the present invention, but it is obvious that any combination thereof may be used.

【0056】[0056]

【発明の効果】本発明によれば、容器内の中空糸膜モジ
ュ−ルの下端より下方に水平の仕切板を設け、中空糸膜
モジュ−ルに一対一にその直下の仕切板に通気孔を設
け、この通気孔とは独立して仕切板の下部から上部へ通
じる通水部を設けているので、設計の自由度が高まり、
仕切板下部の通気孔の間に設ける通水管の員数を低減し
たり、通水管を排除して仕切板の周縁部に通水部を形成
したりでき、濾過装置の構造を簡単にして小型化したり
設備費を低減する効果がある。
According to the present invention, a horizontal partition plate is provided below the lower end of the hollow fiber membrane module in the container, and the hollow fiber membrane module has a one-to-one ventilation hole in the partition plate immediately below. Since a water passage that connects the lower part of the partition plate to the upper part is provided independently of this ventilation hole, the degree of freedom in design is increased,
The number of water pipes provided between the ventilation holes at the bottom of the partition plate can be reduced, or the water pipes can be eliminated to form water passages at the peripheral edge of the partition plate, simplifying the structure of the filtration device and making it smaller. It also has the effect of reducing equipment costs.

【0057】また、給気管に接続した給気流出管の開口
の位置を給気管と容器との接続位置より高くすることに
より、給気量が少なく気体層の厚さが薄い場合において
も液面を乱すことがなく供給でき、あるいは給気分散管
によって気体を分散して供給でき、気体層の厚さ分布を
均一化し、各中空糸膜モジュ−ルへの給気量を均等化し
て、濾過装置の洗滌能力を向上することができる。
Further, by making the position of the opening of the supply air outflow pipe connected to the supply air pipe higher than the connection position between the supply air pipe and the container, the liquid level can be obtained even when the amount of supply air is small and the gas layer is thin. Can be supplied without disturbing, or the gas can be dispersed and supplied by the air supply dispersion pipe, the thickness distribution of the gas layer is made uniform, the air supply amount to each hollow fiber membrane module is made uniform, and filtration is performed. The cleaning ability of the device can be improved.

【0058】さらに、仕切板を支持板によって取外し可
能に設けたり、給気分散管のヘッダを仕切板の周部に沿
って円弧状に設けるので、容器底部の点検が容易になる
効果がある。
Further, since the partition plate is detachably provided by the support plate and the header of the air supply dispersion pipe is provided in an arc shape along the peripheral portion of the partition plate, there is an effect that the bottom of the container can be easily inspected.

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

【図1】本発明の第1の実施例による濾過装置の縦断面
図。
FIG. 1 is a longitudinal sectional view of a filtration device according to a first embodiment of the present invention.

【図2】本発明の第1の実施例による濾過装置の水平断
面図。
FIG. 2 is a horizontal sectional view of the filtering device according to the first embodiment of the present invention.

【図3】本発明の第1の実施例による仕切板の部分詳細
図。
FIG. 3 is a partial detailed view of a partition plate according to the first embodiment of the present invention.

【図4】第1の実施例の変形例による部分詳細図。FIG. 4 is a partial detailed view of a modification of the first embodiment.

【図5】本発明の第2の実施例による濾過装置の縦断面
図。
FIG. 5 is a vertical sectional view of a filtering device according to a second embodiment of the present invention.

【図6】本発明の第2の実施例による濾過装置の水平断
面図。
FIG. 6 is a horizontal sectional view of a filter device according to a second embodiment of the present invention.

【図7】本発明の第2の実施例による仕切板の部分詳細
図。
FIG. 7 is a partial detailed view of a partition plate according to a second embodiment of the present invention.

【図8】第2の実施例の変形例による水平断面図。FIG. 8 is a horizontal sectional view according to a modification of the second embodiment.

【図9】第2の実施例の変形例による部分縦断面図。FIG. 9 is a partial vertical sectional view according to a modification of the second embodiment.

【図10】第2の実施例の変形例による別位置の部分縦
断面図。
FIG. 10 is a partial vertical cross-sectional view of another position according to a modification of the second embodiment.

【図11】第2の実施例の別の変形例による部分縦断面
図。
FIG. 11 is a partial vertical sectional view according to another modification of the second embodiment.

【図12】本発明の第3の実施例による濾過装置の縦断
面図。
FIG. 12 is a vertical sectional view of a filter device according to a third embodiment of the present invention.

【図13】本発明の第3の実施例による濾過装置の水平
断面図。
FIG. 13 is a horizontal sectional view of a filter device according to a third embodiment of the present invention.

【図14】本発明の第3の実施例による仕切板の部分詳
細図。
FIG. 14 is a partial detailed view of a partition plate according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

11…容器、13…中空糸膜、14…モジュ−ル筒、1
5…給水管、16…給気管、20…仕切板、21…通気
孔、22…通水管、23…開口、24…気体層、27…
通気管、30…給気分散管、31…給気孔、125…支
持板、126…ドレン管、132…給気流出管、133
…出口、134…出口、201…外周板、220…通水
部、230…給気分散管、231…給気孔。
11 ... Container, 13 ... Hollow fiber membrane, 14 ... Module cylinder, 1
5 ... Water supply pipe, 16 ... Air supply pipe, 20 ... Partition plate, 21 ... Vent hole, 22 ... Water supply pipe, 23 ... Opening, 24 ... Gas layer, 27 ...
Vent pipe, 30 ... Air supply dispersion pipe, 31 ... Air supply hole, 125 ... Support plate, 126 ... Drain pipe, 132 ... Air supply outflow pipe, 133
Outlet, 134 ... Outlet, 201 ... Outer peripheral plate, 220 ... Water passage part, 230 ... Air supply dispersion pipe, 231 ... Air supply hole.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 風間 誠一 茨城県日立市幸町三丁目1番1号 株式会 社日立製作所日立工場内 ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Seiichi Kazama 3-1-1, Sakaicho, Hitachi City, Ibaraki Prefecture Inside Hitachi, Ltd. Hitachi Plant

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 容器と、前記容器内に隔離板と前記隔離
板に接続した複数の濾過モジュ−ルと、前記容器内に被
浄化液を供給する給水管及び気体を供給する給気管とを
有し、前記被浄化液を前記濾過モジュ−ルに通じて前記
被浄化液を浄化する濾過装置において、 その下側に供給気体の層を形成するための仕切板を前記
濾過モジュ−ルの下方で前記給水管及び前記給気管より
上方に略水平に備え、前記濾過モジュ−ルに対応してそ
の直下の前記仕切板に通気孔を設けるとともに、前記被
浄化液を前記仕切板の上方に通じる通水部を前記通気孔
と分離して設けたことを特徴とする濾過装置。
1. A container, a separator in the container, a plurality of filtration modules connected to the separator, a water supply pipe for supplying a liquid to be purified and an air supply pipe for supplying gas into the container. In the filtration device for purifying the liquid to be purified by passing the liquid to be purified to the filtration module, a partition plate for forming a layer of supply gas is provided below the filtration module. Is provided substantially horizontally above the water supply pipe and the air supply pipe, a ventilation hole is provided in the partition plate immediately below the water supply pipe and the air supply pipe, and the liquid to be purified is communicated above the partition plate. A filtering device, wherein a water passage portion is provided separately from the ventilation hole.
【請求項2】 容器と、前記容器内に隔離板と前記隔離
板に接続した複数の濾過モジュ−ルと、前記容器内に被
浄化液を供給する給水管及び気体を供給する給気管とを
有し、前記被浄化液を前記濾過モジュ−ルに通じて前記
被浄化液を浄化する濾過装置において、 前記容器内の前記濾過モジュ−ルの下端より下方で前記
給水管及び前記給気管より上方に略水平に仕切板を備
え、前記濾過モジュ−ルに対応してその直下に通気孔
を、前記通気孔を含まないように通水部をそれぞれ前記
仕切板に設けたことを特徴とする濾過装置。
2. A container, a separator in the container, a plurality of filtration modules connected to the separator, a water supply pipe for supplying a liquid to be purified and an air supply pipe for supplying gas into the container. A filtration device for purifying the liquid to be purified by passing the liquid to be purified to the filtration module, wherein the liquid is below the lower end of the filtration module in the container and above the water supply pipe and the air supply pipe. A substantially horizontal partition plate, corresponding to the filtration module, a ventilation hole is provided directly below the filtration module, and a water passage portion is provided on the partition plate so as not to include the ventilation hole. apparatus.
【請求項3】 請求項2記載の濾過装置において、 前記通水部は、前記仕切板の複数の前記通気孔の間に設
けた開口に、通水管の上端を接続したことを特徴とする
濾過装置。
3. The filtration device according to claim 2, wherein the water passage portion has an upper end of a water pipe connected to an opening provided between the plurality of ventilation holes of the partition plate. apparatus.
【請求項4】 請求項2記載の濾過装置において、 複数の前記通気孔が前記仕切板の平面上で千鳥状に配置
され、隣接する3の通気孔を頂点とする三角形の中央部
に前記通水管を配置したことを特徴とする濾過装置。
4. The filtering device according to claim 2, wherein the plurality of ventilation holes are arranged in a staggered pattern on a plane of the partition plate, and the ventilation holes are provided in a central portion of a triangle having three ventilation holes adjacent to each other. A filtering device having a water pipe.
【請求項5】 請求項2または3または4記載の濾過装
置において、 複数の前記通気孔に、それぞれ異なる長さの通気管を接
続したことを特徴とする濾過装置。
5. The filtering device according to claim 2, 3 or 4, wherein ventilation pipes having different lengths are connected to the plurality of ventilation holes, respectively.
【請求項6】 請求項2から5記載のいずれかの濾過装
置において、 前記容器に内接するとともに前記仕切板の外周より小さ
い開口を有して前記仕切板を取外し可能に支持する支持
板を設けたことを特徴とする濾過装置。
6. The filtering device according to claim 2, further comprising a support plate that is inscribed in the container and has an opening that is smaller than an outer circumference of the partition plate and that detachably supports the partition plate. A filtering device characterized in that
【請求項7】 請求項6記載の濾過装置において、 前記支持板に上端を接続したドレン管を設けたことを特
徴とする濾過装置。
7. The filtering device according to claim 6, wherein a drain pipe having an upper end connected to the support plate is provided.
【請求項8】 容器と、前記容器内に隔離板と前記隔離
板に接続した複数の濾過モジュ−ルと、前記容器内に被
浄化液を供給する給水管及び気体を供給する給気管とを
有し、前記被浄化液を前記濾過モジュ−ルに通じて前記
被浄化液を浄化する濾過装置において、 前記容器内の前記濾過モジュ−ルの下端より下方で前記
給水管及び前記給気管より上方の前記容器内に略水平に
仕切板を備え、前記濾過モジュ−ルに対応してその直下
の前記仕切板に通気孔を設け、前記仕切板の縁部を下方
に延設した外周部と前記容器との間で前記被浄化液を前
記仕切板上方に通じる通水部を形成したことを特徴とす
る濾過装置。
8. A container, a separator in the container, a plurality of filtration modules connected to the separator, a water supply pipe for supplying a liquid to be purified and an air supply pipe for supplying gas into the container. A filtration device for purifying the liquid to be purified by passing the liquid to be purified to the filtration module, wherein the liquid is below the lower end of the filtration module in the container and above the water supply pipe and the air supply pipe. The container is provided with a partition plate substantially horizontally, a ventilation hole is provided in the partition plate immediately below the partition plate corresponding to the filtration module, and an outer peripheral portion in which an edge portion of the partition plate is extended downward and the A filtration device, wherein a water passage portion is formed between the container and the liquid to be purified above the partition plate.
【請求項9】 請求項1から8記載のいずれかの濾過装
置において、 前記給気管に接続して、容器と給気管との接続部より上
方に出口を有する給気流出管を設け、前記出口が洗滌時
に前記仕切板の下側に形成される気体層に開口すること
を特徴とする濾過装置。
9. The filtration device according to claim 1, further comprising: an air supply outflow pipe that is connected to the air supply pipe and has an outlet above a connecting portion between the container and the air supply pipe. Is opened in a gas layer formed below the partition plate during washing.
【請求項10】 請求項9記載の濾過装置において、 前記給気流出管に複数の出口を設けたことを特徴とする
濾過装置。
10. The filtering device according to claim 9, wherein the supply air outflow pipe is provided with a plurality of outlets.
【請求項11】 請求項1から10記載のいずれかの濾
過装置において、 前記濾過モジュ−ルは中空糸膜モジュ−ルであり、中空
糸膜と前記中空糸膜を取り囲むモジュ−ル筒とで構成さ
れていることを特徴とする濾過装置。
11. The filtration device according to claim 1, wherein the filtration module is a hollow fiber membrane module and includes a hollow fiber membrane and a module tube surrounding the hollow fiber membrane. A filtering device characterized by being configured.
JP18922895A 1995-07-25 1995-07-25 Filtration device Expired - Fee Related JP3349015B2 (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18922895A JP3349015B2 (en) 1995-07-25 1995-07-25 Filtration device

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Publication Number Publication Date
JPH0938470A true JPH0938470A (en) 1997-02-10
JP3349015B2 JP3349015B2 (en) 2002-11-20

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