JP3349015B2 - Filtration device - Google Patents

Filtration device

Info

Publication number
JP3349015B2
JP3349015B2 JP18922895A JP18922895A JP3349015B2 JP 3349015 B2 JP3349015 B2 JP 3349015B2 JP 18922895 A JP18922895 A JP 18922895A JP 18922895 A JP18922895 A JP 18922895A JP 3349015 B2 JP3349015 B2 JP 3349015B2
Authority
JP
Japan
Prior art keywords
partition plate
container
liquid
pipe
air supply
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.)
Expired - Fee Related
Application number
JP18922895A
Other languages
Japanese (ja)
Other versions
JPH0938470A (en
Inventor
道雄 村瀬
清志 藤本
政人 小林
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)

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 filtration apparatus for filtering a liquid to be purified by passing a liquid to be purified through a plurality of filtration modules, and more particularly to a method for cleaning a 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 apparatus for filtering a liquid to be purified, if the filtration performance of the filtration module is reduced by long-time purification, the module 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, and the hollow fiber is shaken and washed.
At this time, if the gas flow rate supplied to each hollow fiber membrane module is too small, the cleaning effect is reduced, and if the gas flow rate is too large, the life of the hollow fiber is reduced, so that gas is uniformly 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。洗浄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。
A typical example of a conventional filtration device using a hollow fiber membrane module is disclosed in Japanese Patent Application Laid-Open No. Sho 61-222509. This publicly known technique is applied to each hollow fiber membrane module.
A partition plate having an outlet for the liquid to be purified is provided immediately below the partition plate, and a vertically open cylinder is connected to an outlet on the lower side of the partition plate. A plurality of small holes are provided in the side wall of the cylinder in the length direction. During washing , compressed gas supplied from an air supply pipe below the partition plate is stored in a layer below the partition plate and then supplied to each hollow fiber membrane module through a small hole in the cylinder and an outlet of the partition plate. It 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。
[0004] As a different type, Japanese Patent Application Laid-Open No.
No. 2770 is disclosed. According to this known technique, an air supply pipe is arranged for each row of hollow fiber membrane modules without providing a partition plate or a water passage cylinder as in the above-described example, and the air supply pipe is provided immediately below each hollow fiber membrane module. Make a small hole in the air supply pipe,
Through these small holes, air is directly supplied to each hollow fiber membrane module.

【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 of Japanese Patent Application Laid-Open No. 61-222509, the cylinder connected to the partition plate is used for both the flow 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 method is finally performed by buoyancy, one hollow fiber membrane module requires one cylinder immediately below the hollow fiber membrane module. A large number of cylinders are attached to. In addition, at the time of air supply, the interior of the cylinder becomes a gas-liquid two-phase and the flow becomes unstable, and the hydrostatic head for air supply is reduced, so that the cylinder needs to be lengthened, thereby increasing the equipment cost.

【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。
In the technique disclosed in Japanese Patent Publication No. 4-62770, an air supply pipe is provided for each row of hollow fiber membrane modules. For this reason, the internal 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。
An 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 simple and inexpensive filtration device which can supply a liquid to be purified during cleaning and a gas during cleaning.

【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 in the container, a plurality of filtration modules connected to the separator, a water supply pipe for supplying a liquid to be purified into the container, and an air supply pipe for supplying gas; In a filtration device for purifying the liquid to be purified by passing the purified liquid through the filtration module, a partition plate for forming a layer of supply gas is formed below the water supply pipe below the filtration module and the partition plate. The partition plate is provided substantially horizontally above the air supply pipe, and a ventilation hole is provided in the partition plate immediately below the filter module, and a water passage for communicating the liquid to be purified above the partition plate is provided. This is achieved by providing the air vent separately from the vent.

【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。
[0010] The water passage section may be disposed on a partition plate between the vent holes so as not to include the vent hole, or may be formed in a gap with a container by opening an 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。
[0011] Further, the water passage section is characterized in that a water passage pipe whose upper and lower sides are opened and whose upper end is connected to the partition plate is arranged between the plurality of vent 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。
A plurality of the ventilation holes are arranged in a zigzag pattern on the plane of the partition plate, and the upper end of the water pipe is disposed at the center of a triangle having three adjacent ventilation holes 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。
[0013] The present invention is characterized in that upper ends of ventilation pipes having different lengths are connected to the plurality of ventilation holes, respectively.

【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。
[0014] Further, a support plate which is inscribed in the container and has an opening smaller than the outer periphery of the partition plate and which detachably supports the partition plate is provided, and 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、前記開口が洗浄時に前記仕切板の下方に形成される
気体層開口することを特徴とする。
[0015] Further, an air supply outflow pipe having an outlet above a connection portion between the container and the air supply pipe is provided to be connected to the air supply pipe, and the opening is formed below the partition plate at the time of washing. It is characterized in that it is opened at the 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 construction of the present invention, the partition plate is provided substantially horizontally (horizontally so that the gas layer becomes substantially uniform) below the lower end of the filtration module in the container. A ventilation hole is provided directly below each filter module of the partition plate corresponding to the partition plate. Further, a water passage for passing the liquid to be purified upward from below the partition plate is arranged independently of the vent hole. The water passage section is constituted by a plurality of water pipes connected to the upper end to an opening provided between the plurality of ventilation holes of the partition plate, or as a configuration that opens between the outer peripheral portion of the partition plate and the container,
A water passage independent of the vent can be realized.

【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 washing 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 each filter module. Inflow. At this time, the gas that has exited from the ventilation hole flows into the filtration module due to the buoyancy in the water above the partition plate, so that air can be supplied by providing the ventilation hole immediately below the filtration module as in the present invention. Become. On the other hand, the water supply section for supplying the liquid to be purified at the time of purification does not need to be directly below the filtration module or one-to-one with the filtration module. 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, the degree of freedom in designing the water passage section is increased, the number of water passage pipes can be reduced, and a structure without a water passage pipe in the partition plate can be realized. The structure is simplified, and downsizing and equipment cost can be reduced.

【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。
The inside of the water passage is always a single liquid phase,
Since the flow is stable and the hydrostatic head for air supply is large, the water flow section 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。
In addition, 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,
Although the gas layer formed in the part except the water passage part below the partition plate becomes thicker, the gas flows in order from the shorter one, so the number of gas pipes through which the gas flows increases, and the gas layer thickness becomes sharp. Increase can be suppressed. As a result, even when the air supply flow rate is large, the water passage section can be shortened.

【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 of a partition plate inscribed in the container and having an opening smaller than the outer periphery of the partition plate, and providing a drain pipe which is opened up and down and has an upper end connected to the support plate, the inspection of the bottom of the container can be performed. The partition plate can be easily removed, and the liquid 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 an air supply outflow pipe having an opening above a connection portion between the container and the air supply pipe, a gas layer formed in a portion having a small air supply flow rate and excluding a water passage below the partition plate. Even when the thickness is small, the opening of the air supply / outflow pipe is not exposed in the gas layer and does not disturb the liquid level, so that the air supply 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 distribution pipe having a plurality of openings in the container connected to the air supply pipe, the thickness of the gas layer formed below the partition plate is made uniform, and each filtration module is provided. The amount of air supply to the air can be equalized.

【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 be described below 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. FIG. 1 is a longitudinal sectional view of a filtration device according to a first embodiment, FIG. 2 is a view taken along the line AA in 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 filtering device comprises a container 11, a hollow fiber membrane 13 having a filtering function and disposed in the container 11, and a module cylinder 1.
4, a separator 12 for supporting the hollow fiber membrane module, and a vent 21 and a water pipe 22 disposed below the lower end of the hollow fiber membrane module. Partition plate 20 and water supply pipe 15 for supplying liquid to be purified
A gas supply pipe 16 for supplying the 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, It has a drain pipe 19 connected to the lower part.

【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 the present embodiment, during a normal purification operation, the liquid to be purified flows in from the water supply pipe 15, passes through the water pipe 22 connected to the partition plate 20, and passes through each module cylinder 14.
After the impurities such as the clad are filtered by the hollow fiber membrane 13, they flow out of the outflow pipe 17. When impurities are trapped in the hollow fiber membrane 13 by such a filtration operation and the filtration function of the hollow fiber membrane 13 is reduced, the supply of the liquid to be purified is stopped, and gas (usually air) is distributed to the air supply pipe 16 and the air supply dispersion. Feed through tube 30. At this time, the inside of the container below the separator 12 is full.

【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 for the water pipe 22, and the gas flowing out from the vent hole 21 of the partition plate 20 has a buoyancy in the liquid to be purified. Then, the gas flows into the module cylinder 14 immediately above, and the trapped impurities are released by shaking the hollow fiber membrane 13 by the flow of gas, and after the washing is completed, the impurities are discharged from the drain pipe 19 together with the liquid to be purified. The gas supplied to each filter module flows out of a 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 the gas flowing into the filter is too small, the cleaning effect of the hollow fiber membrane 13 is weakened, and if it is too large, the life of the hollow fiber membrane 13 is shortened. 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。
The partition plate 20 is provided with a vent hole 21 immediately below the module tube 14, and a water passage pipe 22 is provided between the plurality of vent holes 21 (three vent holes in this embodiment). The upper ends are connected to form a water passage section. An air supply distribution 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 a normal purifying operation, the liquid to be purified flows from the water supply pipe 15 and flows into each module cylinder 14 through the water pipe 22 connected to the partition plate 20, but the water pipe 22 has a vent hole. Since it is independent of the module 21, there is no need to provide a water pipe 22 for each module cylinder 14. As in this embodiment, for example, one water pipe 22 is sufficient for three module cylinders 14, and the number of water pipes 22 can be reduced. For example, container 1
When the diameter of 1 is about 1.5m, the diameter of the water pipe is 10cm
The diameter of the vent hole 21 is about 1 cm, and it can be seen that the effect of the reduction of the water pipe 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つのモジュール筒14に分散して供給され
るが、通水管22と各モジュール筒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。
Further, since the ventilation hole and the water pipe are independent of each other, the degree of freedom in design is increased. Usually, in order to increase the occupancy in the horizontal section and reduce the size of the container 11, the filtration modules are arranged in a triangular lattice (or staggered).
In this case, as shown in the drawing, one water pipe is disposed 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 surrounding module cylinders 14. Since the water pipe 22 and each module cylinder 14 are arranged at the shortest and equidistant distance, the liquid to be purified is There is an advantage that the components are evenly distributed to each module and the disturbance of water in the container can be prevented.

【0032】ところで、洗浄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 following equation (1). 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、
Ρ · g · H = 1 / · ζ · ρg · Vg 2 where ζ: resistance coefficient of the vent hole 21, ρg: gas density, ρ: fluid density of the water passage 23, g : Gravity acceleration, V
g: Outflow velocity of gas from the vent hole 21. From this, Vg during cleaning is

【0034】[0034]

【数2】(Vg)2=(2/ζ)・(ρ/ρg)・g・H と、表わすことができる。(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 prior art, since the water pipe has the ventilation hole, the inside of the water pipe becomes a gas-liquid two-phase, and the fluid density ρ decreases. However, in this embodiment, the inside of the water pipe 22 is a single liquid 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 an air supply distribution 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 reduced. It can be made uniform. The air supply hole 31 is provided mainly on the side surface of the air supply distribution pipe 30 so that the clad does not enter, but on the lower surface near the tip for drainage after the start of air supply, and on the upper surface for exhaust after the air supply ends. 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 filtering device of the present embodiment, the ventilation hole 21 of the partition plate 20 and the water passage 22 can be provided independently, so that the number of water passages 22 can be reduced and the number of passages can be reduced. Since the inside of the water pipe 22 has a single liquid phase, the water pipe 22 can be shortened, and the economic 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 partially detailed view of a filtering device according to a modification of the first embodiment. This modified example 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.
b and 21c have different lengths.

【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 supply during the cleaning of the hollow fiber membrane is constant. However, for example, when it becomes necessary to greatly increase the amount of supplied air, as is apparent from (Equation 1), the gas layer 24
Increases rapidly in proportion to the square of the air supply amount. In this modification, when the amount of air supply is greatly increased and the thickness of the gas layer 24 is increased, the number of vent holes for supplying gas is increased to 21a, 2
It increases sequentially like 1b and 21c. For this reason, an increase in the thickness of the gas layer 24 can be suppressed, and the water pipe 22 can be shortened even when the supplied air amount 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 filtration device according to a second embodiment of the present invention, FIG. 6 is a view taken in the direction of arrows AA in 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 differs from the first embodiment in that the air supply distribution pipe 30 of the first embodiment is not provided, and a plurality of air supply pipes 16 are connected to the container 11 instead.
In addition, one water pipe 22 is provided for one module cylinder 14. This is a preferred but not 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。
At the time of cleaning the hollow fiber membrane 13, a plurality of air supply pipes 1
The gas dispersed and supplied from 6 forms a gas layer 24 below the partition plate 20, and is supplied to each module cylinder 14 through the vent 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 water pipes 22 is large and there is difficulty in arranging the air supply distribution pipe 30,
The thickness distribution of the gas layer 24 is made uniform, and each module cylinder 14
This is effective for equalizing the amount of air supplied to the pump. When the number of the water pipes 22 is increased, the flow velocity in the pipes can be reduced.

【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 filtering device according to a modification of the second embodiment viewed from below, FIG. 9 is a partial longitudinal sectional view thereof, and FIG. 10 is a partial longitudinal sectional view of 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 the present modification, a first point different from the second embodiment is that a support plate 125 for supporting the partition plate 20 is provided.
That is, the drain tube 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 outlet 13 is located at a position where the opening of the air supply pipe 16 is higher than the connection between the air supply pipe 16 and the container 11.
3 is provided. Note that the first point and the second point do not require any other conditions.

【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 inspecting the bottom of the container 11. In this case, liquid and impurities accumulate on the support plate 125 between the container 11 and the partition plate 20, but can be drained by the drain pipe 126 connected to the support plate 125, and the length of the drain pipe 126 is By making the length the same, 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 the second embodiment (FIG. 7),
When the air supply amount is small and the thickness of the air layer 24 becomes thin and the water surface becomes higher than the air supply pipe 16, the liquid surface is disturbed by the air supply, and the air flow amount from the air holes 21 fluctuates. In this modification, as shown in FIG. 9, the air supply / outflow pipe 132 is bent upward and the position of the outlet 133 at the tip thereof is higher than the position of connection with the air supply pipe 16, so that the air supply amount is small. Even if the thickness of the air layer 24 becomes thin, the air can be supplied stably without changing the amount of air flow from the air holes 21.

【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 according to another modification of the second embodiment, and corresponds 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。
This modification is different from the modification of FIG. 9 in that the upward end of the air supply / outflow pipe 132 is closed, and an outlet 134 is provided at the center of the container 11 on the pipe wall near the end. is there. According to this, the outlet 13 of the air supply outflow pipe 132
Since the gas flows out horizontally from 4 and spreads easily below the partition plate 20, the thickness distribution of the gas layer can be made uniform and the gas can be supplied to each module cylinder 14 evenly.

【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. FIG. 12 is a longitudinal sectional view of a filtration device according to a third embodiment, FIG. 13 is a view taken along the line AA of 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 in the partition plate 20 is different from the first embodiment.
2 is that a 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 a large number of water pipes provided on the partition plate 20 are not provided, the structure becomes 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 is generated after exiting the water passage section 220, the fluid force to the module cylinder 14 is increased, so that the processing 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 (two in the figure) of the air supply pipes 16 are provided, and the air supply distribution pipe 230 connected to the air supply pipe 16 has a header shape. As shown in the figure, the header portion of the air supply distribution pipe 230 is formed in an arc shape inside the outer peripheral plate 201, and a plurality of air supply holes 231 are provided. Since there is no obstacle such as a water pipe, the gas dispersed and supplied from the large number of air supply holes forms a gas layer 24 having a uniform thickness distribution at the lower portion of the partition plate 20, Module tube 14
Supplied to According to this configuration, inspection of the lower part of the container is also facilitated.

【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 first embodiment to the third embodiment of the present invention employ different shapes of the water passage section and the air supply section, 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−ルに一対一に対応して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 a vent hole is formed in the partition plate in one-to-one correspondence with the hollow fiber membrane module. Is established,
Since the water passage that communicates from the lower part to the upper part of the partition plate is provided independently of this vent hole, the degree of freedom of design is increased, and the number of water pipes provided between the vent holes at the lower part of the partition plate can be reduced. In addition, a water passage can be formed at the peripheral edge of the partition plate by eliminating the water passage pipe, which has the effect of simplifying the structure of the filtration device, reducing its size, and 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、濾過装置の洗浄能力を向上することができる。
Further, by setting the position of the opening of the supply air outlet pipe connected to the air supply pipe higher than the connection position between the air supply pipe and the container, the liquid level can be reduced even when the air supply amount is small and the thickness of the gas layer is thin. The gas can be supplied without disturbing the gas, or the gas can be supplied by dispersing the gas through an air supply distribution 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 the filtration is performed. The cleaning ability of the device can be improved.

【0058】[0058]

【図面の簡単な説明】[Brief description of the 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 filtration 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 longitudinal sectional view of a filtration 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 filtration 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 of 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 longitudinal 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 longitudinal 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 longitudinal sectional view according to another modified example 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 longitudinal sectional view of a filtration 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 filtration 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 pipe, 23 ... opening, 24 ... gas layer, 27 ...
Ventilation pipe, 30 ... air supply distribution 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 supply part, 230 ... air supply distribution pipe, 231 ... air supply hole.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小林 政人 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 (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 (56)参考文献 特開 昭61−293504(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 61/00 - 65/10 C02F 1/44 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Masato Kobayashi 3-1-1, Sachimachi, Hitachi-shi, Ibaraki Pref. Hitachi, Ltd. Hitachi Plant (72) Inventor Seiichi Kazama 3-1-1 Sachimachi, Hitachi-shi, Ibaraki No. 1 Hitachi, Ltd. Hitachi Plant (56) References JP-A-61-293504 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) B01D 61/00-65/10 C02F 1/44

Claims (10)

(57)【特許請求の範囲】(57) [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、前記濾過モジュールのモジュール筒より下方に間隙を介
して仕切板を略水平に 備え、かつ前記仕切板は前記給水
管及び前記給気管より上方に設けられて供給気体の層の
形成を可能にし、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 to the container. In the filtering device for purifying the liquid to be purified by passing the liquid to be purified through the filtration module, a gap is provided below the module cylinder of the filtration module through a gap.
The partition plate is provided substantially horizontally , and the partition plate is provided with the water supply.
Pipe and a supply gas layer provided above the air supply pipe.
And a ventilation hole is provided in the partition plate immediately below the filter module corresponding to the filtration module , and a water passage through which the liquid to be purified passes above the partition plate is separated from the ventilation hole. A filtration device characterized by being provided.
【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、前記濾過モジュールのモジュール筒より下方に間隙を介
して仕切板を略水平に 備え、かつ前記仕切板は前記給水
管及び前記給気管より上方に設けられて供給気体の層の
形成を可能にし、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を含
まないように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 to the container, and an air supply pipe for supplying gas. In the filtering device for purifying the liquid to be purified by passing the liquid to be purified through the filtration module, a gap is provided below the module cylinder of the filtration module through a gap.
The partition plate is provided substantially horizontally , and the partition plate is provided with the water supply.
Pipe and a supply gas layer provided above the air supply pipe.
And a ventilation hole is provided in the partition plate immediately below the filter module corresponding to the filtration module ,
Filtration device, characterized in that the water passing portion communicating the liquid above the partition plate is provided in front Symbol partition plate so as not to include the vent.
【請求項3】 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、前記濾過モジュールのモジュール筒より下方に間隙を介
して仕切板を略水平に 備え、かつ前記仕切板は前記給水
管及び前記給気管より上方に設けられて供給気体の層の
形成を可能にし、前記複数の濾過モジュ−ルの各々に対
応した複数の通気孔とともに、前記通気孔を含まないよ
うに配置される通水部を前記仕切板に設けたことを特徴
とする濾過装置。
3. 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 to the container, and an air supply pipe for supplying gas. In the filtering device for purifying the liquid to be purified by passing the liquid to be purified through the filtration module, a gap is provided below the module cylinder of the filtration module through a gap.
The partition plate is provided substantially horizontally , and the partition plate is provided with the water supply.
Pipe and a supply gas layer provided above the air supply pipe.
To allow the formation, said plurality of filtration modules - with a plurality of vent holes corresponding to each of the le, characterized in that the water passing portion arranged so as not to include ventilation holes provided in the partition plate filtration apparatus.
【請求項4】 請求項1、2または3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。
4. The filtering device according to claim 1, wherein the water-passing portion connects an upper end of a water-passing pipe to an opening provided between the plurality of ventilation holes of the partition plate. Characteristic filtration device.
【請求項5】 請求項4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または
三角格子状に配置され、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。
5. The filtering device according to claim 4, wherein the plurality of ventilation holes are arranged in a staggered or triangular lattice on the plane of the partition plate, and the center of a triangle having three adjacent ventilation holes as vertices. A filtration device, wherein the water pipe is arranged in a part.
【請求項6】 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、前記濾過モジュールのモジュール筒より下方に間隙を介
して仕切板を略水平に 備え、かつ前記仕切板は前記給水
管及び前記給気管より上方に設けられて供給気体の層の
形成を可能にし、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。
6. 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 to the container. In the filtering device for purifying the liquid to be purified by passing the liquid to be purified through the filtration module, a gap is provided below the module cylinder of the filtration module through a gap.
The partition plate is provided substantially horizontally , and the partition plate is provided with the water supply.
Pipe and a supply gas layer provided above the air supply pipe.
The partition plate immediately below the filter module is provided with a vent hole corresponding to the filter module, and the purifying is performed between the outer peripheral portion extending downward at the edge of the partition plate and the container. A filtration device, wherein a water-passing portion for passing a liquid above the partition plate is formed.
【請求項7】 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、前記濾過モジュールのモジュール筒より下方に間隙を介
して仕切板を略水平に 備え、かつ前記仕切板は前記給水
管及び前記給気管より上方に設けられて供給気体の層の
形成を可能にし、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、前記仕切板の外縁部に
設けられ該仕切板から下向きに延びた外周部と前記容器
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。
7. 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 to the container. In the filtering device for purifying the liquid to be purified by passing the liquid to be purified through the filtration module, a gap is provided below the module cylinder of the filtration module through a gap.
The partition plate is provided substantially horizontally , and the partition plate is provided with the water supply.
Pipe and a supply gas layer provided above the air supply pipe.
A ventilation hole is provided in the partition plate directly below the filter module in correspondence with the filter module, and provided between the outer peripheral portion provided at the outer edge of the partition plate and extending downward from the partition plate and the container. A filter for passing the liquid to be purified above the partition plate.
【請求項8】 請求項1から7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たことを特徴とする
濾過装置。
8. The filter device according to claim 1, further comprising a supply air outlet pipe connected to the air supply pipe and having an outlet above a connection between the container and the air supply pipe. Characteristic filtration device.
【請求項9】 請求項8記載の濾過装置において、 前記給気流出管の前記出口が、洗浄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 filtering device according to claim 8, wherein the outlet of the air supply / outflow pipe opens to a gas layer formed below the partition plate during cleaning.
【請求項10】 請求項1から9記載のいずれかの濾過
装置において、 前記給気管は2個設けられ、前記容器の周方向において
対向する2箇所に配置されていることを特徴とする濾過
装置。
10. The filtering device according to claim 1, wherein two air supply pipes are provided and arranged at two locations facing each other in a circumferential direction of the container. .
JP18922895A 1995-07-25 1995-07-25 Filtration device Expired - Fee Related JP3349015B2 (en)

Priority Applications (1)

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

Applications Claiming Priority (1)

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

Publications (2)

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

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ID=16237738

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