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JPH024328B2 - - Google Patents
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JPH024328B2 - - Google Patents

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Publication number
JPH024328B2
JPH024328B2 JP13337085A JP13337085A JPH024328B2 JP H024328 B2 JPH024328 B2 JP H024328B2 JP 13337085 A JP13337085 A JP 13337085A JP 13337085 A JP13337085 A JP 13337085A JP H024328 B2 JPH024328 B2 JP H024328B2
Authority
JP
Japan
Prior art keywords
hollow fiber
fluid
pipe
hollow
filtration
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
Application number
JP13337085A
Other languages
Japanese (ja)
Other versions
JPS61291008A (en
Inventor
Munehiro Okumura
Kazuo Kuwabara
Shinichi Ishii
Osamu Yamamoto
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.)
Mitsubishi Rayon Engineering Co Ltd
Original Assignee
Mitsubishi Rayon Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Rayon Engineering Co Ltd filed Critical Mitsubishi Rayon Engineering Co Ltd
Priority to JP13337085A priority Critical patent/JPS61291008A/en
Priority to US06/875,728 priority patent/US4668401A/en
Priority to DE8686108349T priority patent/DE3666533D1/en
Priority to EP86108349A priority patent/EP0207379B1/en
Publication of JPS61291008A publication Critical patent/JPS61291008A/en
Publication of JPH024328B2 publication Critical patent/JPH024328B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は流体濾過用中空糸濾過モジユール及び
それを用いた濾過システムに関し、より詳しくは
大量の水中の懸濁物質の除去や空気中の浮遊物質
の除去等に適した中空糸濾過モジユール及びそれ
を用いた濾過システムに関する。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a hollow fiber filtration module for fluid filtration and a filtration system using the same. The present invention relates to a hollow fiber filtration module suitable for removing substances, etc., and a filtration system using the same.

[従来の技術] 中空糸濾過膜は優れた濾過機能を有しているた
めに従来より高純度の工業用水の製造や気体の濾
過等を始めとして種々の用途に広く用いられてき
ている。
[Prior Art] Hollow fiber filtration membranes have an excellent filtration function and have been widely used for various purposes including the production of high-purity industrial water and gas filtration.

中空糸濾過モジユールとしては中空糸の中空部
から外部へ向けて濾過するものと中空糸の外部か
ら中空部へ向けて濾過するものとの2通りがある
が、前者は中空糸の内部の通過抵抗が大きく、
又、懸濁物質が中空糸中空部に残存して目詰まり
を起し易いため、これらの用途には後者のタイプ
が多く用いられてきた。
There are two types of hollow fiber filtration modules: one that filters from the hollow part of the hollow fiber to the outside, and one that filters from the outside of the hollow fiber to the hollow part, but the former is based on the passage resistance inside the hollow fiber. is large,
Further, since suspended substances remain in the hollow portion of the hollow fiber and tend to cause clogging, the latter type has been often used for these applications.

[発明が解決しようとする問題点] これらのモジユールはその殆どが直管の中に中
空糸が収納され、被処理流体の出入口が直管の側
面に設けられており、複数のモジユールを直列に
連結して使用する場合には被処理流体の流れは複
雑に曲折する連結方式をとらざるをえず、被処理
流体の圧力損失が大きく必要以上のポンプ能力を
必要としたり、連結数の制限を受けたり、エネル
ギー損失が大きい等という不便があつた。
[Problems to be solved by the invention] Most of these modules have a hollow fiber housed in a straight pipe, and the inlet and outlet for the fluid to be treated are provided on the side of the straight pipe. When used in combination, the flow of the fluid to be treated must be connected in a complicated manner, resulting in a large pressure loss of the fluid to be treated, requiring more pumping capacity than necessary, or limiting the number of connections. There were inconveniences such as high energy loss and high energy loss.

本発明の目的は上述した問題点を解決した全く
新しい構造であつて、工業的流体処理に使用可能
な中空糸濾過モジユール及びそれを用いた濾過シ
ステムを提供することにある。
An object of the present invention is to provide a hollow fiber filtration module and a filtration system using the same, which has a completely new structure that solves the above-mentioned problems and can be used in industrial fluid processing.

[問題点を解決するための手段] 即ち、本発明の要旨はU字状に束ねた中空糸束
を側管を有する直管からなるハウジングに収納
し、中空糸の開口部を開口状態に保つたまま側管
端部に固定してなる、中空糸束が側管部と直管部
の一部に存在する中空糸濾過モジユールにあり、
さらに、複数個の該モジユールを各々の直管の端
部を介して直列に連結し、直列に連結されたモジ
ユール列の一方の端に被処理流体の入口、他方の
端に被処理流体の出口を設け、各々のモジユール
の側管出口を濾過流体出口とする濾過システムに
ある。
[Means for Solving the Problems] That is, the gist of the present invention is to house a hollow fiber bundle bundled in a U-shape in a housing consisting of a straight pipe having a side pipe, and to keep the openings of the hollow fibers in an open state. There is a hollow fiber filtration module in which a bundle of hollow fibers, which is fixed to the end of the side tube, is present in the side tube section and a part of the straight tube section.
Furthermore, a plurality of modules are connected in series through the ends of each straight pipe, and one end of the serially connected module row has an inlet for the fluid to be treated, and the other end has an outlet for the fluid to be treated. The filtration system is provided with a side tube outlet of each module as a filtrate fluid outlet.

上記中空糸モジユールのU字状に束ねた中空糸
束の代りに一端は中空糸の開口部を開口状態に保
ち他端は封鎖した中空糸束を用いることもでき
る。
Instead of the U-shaped hollow fiber bundle of the hollow fiber module described above, a hollow fiber bundle may be used in which one end of the hollow fibers is kept open and the other end is closed.

[発明を実施するための好適な態様] 以下、本発明の中空糸濾過モジユールにつき図
面を参照しつつ詳細に説明する。
[PREFERRED EMBODIMENTS FOR CARRYING OUT THE INVENTION] Hereinafter, the hollow fiber filtration module of the present invention will be described in detail with reference to the drawings.

第1図は本発明の中空糸濾過モジユールの1態
様例を示す一部欠載平面模式図であり、第2図及
び第3図は該中空糸濾過モジユールを直列に継い
でなる濾過システムの態様例の主要部分を示す断
面図(中空糸濾過膜図示せず)である。図におい
て側管を有する直管1の側管2の角度は10〜90゜
であることが好ましい。この角度は直管と接合す
る部分の角度であり、側管はその先で真直であつ
てもよく、適度に曲がつていてもよい。又、側管
を有する直管は一体で成型されていてもよく、エ
ルボ付き管と直管を接合したものであつてもよ
い。又、直管部の口径は全体にわたつて同一の口
径であつてもよく、途中で異なつた口径のものと
接続したものであつてもよい。この場合、複数の
モジユールを直列に接続することを考慮すればモ
ジユール両端の口径が一致していることが好まし
い。もちろん口径が一致していない場合でもジヨ
イントの形状を工夫すれば接続できることは明ら
かである。なお、直管と側管の接合部分は中空糸
を傷めないためになめらかであることが好まし
く、この部分にテーパがついていてもよい。又、
直管内において中空糸の保持や局所的に流速を高
める等のために圧損をそれほど大きくしない範囲
であれば絞りを入れてもよい。
FIG. 1 is a partially cutaway schematic plan view showing one embodiment of the hollow fiber filtration module of the present invention, and FIGS. 2 and 3 are embodiments of a filtration system formed by connecting the hollow fiber filtration modules in series. It is a sectional view (hollow fiber filtration membrane not shown) showing the main part of an example. In the figure, the angle of the side pipe 2 of the straight pipe 1 having a side pipe is preferably 10 to 90 degrees. This angle is the angle of the part that joins with the straight pipe, and the side pipe may be straight or appropriately curved at its tip. Further, the straight pipe having the side pipe may be integrally molded, or may be formed by joining an elbowed pipe and a straight pipe. Further, the diameter of the straight pipe portion may be the same throughout, or may be connected to pipes of different diameters along the way. In this case, considering that a plurality of modules are connected in series, it is preferable that the diameters of both ends of the modules are the same. Of course, it is clear that even if the diameters do not match, it is possible to connect by devising the shape of the joint. Note that the joining portion between the straight tube and the side tube is preferably smooth so as not to damage the hollow fibers, and this portion may be tapered. or,
A restriction may be inserted in the straight pipe in order to retain the hollow fibers or locally increase the flow velocity, as long as the pressure loss is not too large.

一本の直管に対する側管の数は2本以上あつて
もよい。この場合、側管相互の位置は何ら限定さ
れるものではなく、例えば直管の1つの円周上に
配置するとか直管の周囲に螺旋状に配置する等の
方法をとることができる。第5図は円周上に配置
した例である。複数の側管を有する場合その全て
に中空糸束が入つていてもよく、その一部に入つ
ていてもよい。中空糸束が入つていない側管があ
る場合はその側管の端を封鎖しておけばよい。
There may be two or more side pipes for one straight pipe. In this case, the mutual positions of the side tubes are not limited in any way; for example, the side tubes may be arranged on one circumference of the straight tube or arranged in a spiral around the straight tube. FIG. 5 shows an example of arrangement on the circumference. When having a plurality of side tubes, the hollow fiber bundle may be contained in all of them, or in some of them. If there is a side tube that does not contain a hollow fiber bundle, the end of that side tube may be sealed.

一本の直管に中空糸束を複数本装着するとマク
ロに見た直管内の流体の流れをより均一にするこ
とも可能となる。
By attaching a plurality of hollow fiber bundles to one straight pipe, it is also possible to make the flow of fluid in the straight pipe more uniform from a macroscopic perspective.

中空糸濾過膜3はU字状に束ねられた中空糸束
として又は一端は中空糸の開口部を開口状態に保
ち他端は封鎖した中空糸束として側管部から挿入
され、直管部まで延在している。中空糸の有効部
分の90%以上が直管部分にあることが濾過効率の
点から好ましい。中空糸の存在しない側の直管部
分4はスペース効率の点から少ない方が好まし
い。
The hollow fiber filtration membrane 3 is inserted from the side pipe section as a hollow fiber bundle bundled in a U-shape or as a hollow fiber bundle with one end of the hollow fibers kept open and the other end closed, and then inserted into the straight pipe section. Extending. From the viewpoint of filtration efficiency, it is preferable that 90% or more of the effective portion of the hollow fiber be located in the straight pipe portion. In terms of space efficiency, it is preferable that the number of straight pipe portions 4 on the side where no hollow fibers is present is small.

中空糸濾過膜としては柔軟性を有しているもの
が好ましく、このような中空糸の例としてポリオ
レフイン、弗素化ポリオレフイン、ポリスルフオ
ン、ポリアクリロニトリル等の素材からなる限外
濾過または精密濾過中空糸膜を挙げることができ
る。
The hollow fiber filtration membrane is preferably flexible, and examples of such hollow fibers include ultrafiltration or microfiltration hollow fiber membranes made of materials such as polyolefin, fluorinated polyolefin, polysulfone, and polyacrylonitrile. can be mentioned.

この中空糸膜は中空糸の開口部を開口状態に保
つたまま側管端部においてポリウレタン、エポキ
樹脂、不飽和ポリエステル樹脂、シリコン樹脂等
のポツテイング剤により液密に固定保持される。
中空糸の途中で曲がつたU字状を保持するために
適当な支持部材を用いてもよい。中空糸束は直管
の断面方向で均一に分散していることが好ましい
が、濾過の目的によつては一部に偏在していても
よい。該モジユールは直管部端aの部分から被処
理流体を導入し、膜で濾過された濾過流体は中空
糸内部を通つて側管端cから取出される。一方、
濾過されなかつた流体は直管の他の端bから取出
される。これにより被濾過流体の流れは直管内を
直線的に流れるため圧力損失が小さいという特徴
を有している。
This hollow fiber membrane is held liquid-tightly fixed at the end of the side tube by a potting agent such as polyurethane, epoxy resin, unsaturated polyester resin, silicone resin, etc. while keeping the opening of the hollow fiber in an open state.
A suitable support member may be used to maintain the bent U-shape in the middle of the hollow fiber. It is preferable that the hollow fiber bundles are uniformly distributed in the cross-sectional direction of the straight pipe, but depending on the purpose of filtration, they may be unevenly distributed in a part. The module introduces the fluid to be treated from the straight pipe end a, and the fluid filtered through the membrane is taken out from the side pipe end c through the hollow fiber. on the other hand,
Unfiltered fluid is removed from the other end b of the straight pipe. As a result, the fluid to be filtered flows linearly in the straight pipe, so it has a characteristic that pressure loss is small.

次に該モジユールを直列に接続してなる濾過シ
ステムにつき説明する。第2図は2つのモジユー
ルを接合直管部材を用いて結合した例であり、こ
のようにして必要な段数結合すればよい。結合の
方法は第2図に示した方法に限定されるものでな
く、例えば直管同士を直接嵌合させる方法を採つ
てもよい。第3図は直管を曲管で接合した例であ
り、直管の内径とほぼ同等又はそれ以上の内径を
有する曲管を用いれば圧力損失を大きくすること
なく、コンパクトにすることができる。なお、モ
ジユールの接続にあたつては中空糸束のU字端が
同じ方向を向くように結合し、中空糸束のU字端
部分が被処理流体の下流側(出口側)になるよう
に、直列につながれたモジユール列の一方の端を
被処理流体の入口とし、他方の端を被処理流体の
出口とすればよい。濾過流体の出口の濾過流体を
集める配管を設けて1箇所に集めてもよく、それ
ぞれで受けてもよい。
Next, a filtration system formed by connecting the modules in series will be explained. FIG. 2 shows an example in which two modules are connected using a joining straight pipe member, and in this way, the necessary number of stages can be connected. The method of coupling is not limited to the method shown in FIG. 2, and for example, a method of directly fitting straight pipes together may be used. FIG. 3 shows an example in which straight pipes are joined with a curved pipe, and if a curved pipe having an inner diameter approximately equal to or larger than the inner diameter of the straight pipe is used, the pipe can be made compact without increasing the pressure loss. When connecting the modules, connect the hollow fiber bundles so that the U-shaped ends face the same direction, and make sure that the U-shaped ends of the hollow fiber bundles are on the downstream side (outlet side) of the fluid to be treated. , one end of a series of modules connected in series may be used as an inlet for the fluid to be treated, and the other end may be used as an outlet for the fluid to be treated. A pipe for collecting the filtrate fluid at the outlet of the filtrate fluid may be provided to collect the fluid at one location, or the fluid may be received at each location.

第4図は本発明の中空糸濾過モジユールを用い
た濾過システムとポンプ及び付帯設備を一体化し
たプラントの実施態様例を示すものであり、この
例では原水は直管と循環ライン20とを循環する
ようになつている。即ち被処理流体(この例では
原水という)は供給ポンプ24により原水ライン
18に供給され、循環中の流体と合流して循環ポ
ンプ15を経由して直管内に入る。そこで中空糸
膜を接触して濾過された液は処理水ライン19を
通つて出る。濾過されなかつた流体は循環ライン
を通り循環ポンプにより循環する。各々の側管と
処理水ラインの間にはバルブ25が設けられてお
り、処理水の水質を確認しながらバルブを開いて
所定の水質の処理水のみ集めるようにすればよ
い。循環をしながら一定量の濃縮原水を抜き取つ
てもよく、循環をしないでワンパスで濃縮原水を
抜き取つてもよい。但しこのようなシステムでは
供給される原水の10倍以上の量を循環させること
が好ましい。濃縮原水は他の処理工程にまわして
もよく、原水タンクに戻してもよい。システムの
頂部にはエア抜き電磁弁が、底部にはスラツジ抜
き電磁弁が設けられている。
FIG. 4 shows an embodiment of a plant that integrates a filtration system using the hollow fiber filtration module of the present invention, a pump, and ancillary equipment. In this example, raw water is circulated through a straight pipe and a circulation line 20. I'm starting to do that. That is, the fluid to be treated (referred to as raw water in this example) is supplied to the raw water line 18 by the supply pump 24, merges with the circulating fluid, and enters the straight pipe via the circulation pump 15. There, the liquid that has been filtered by contacting the hollow fiber membrane exits through the treated water line 19. The unfiltered fluid is circulated through a circulation line by a circulation pump. A valve 25 is provided between each side pipe and the treated water line, and the valve 25 may be opened while checking the quality of the treated water to collect only the treated water of a predetermined quality. A fixed amount of concentrated raw water may be extracted while circulating, or concentrated raw water may be extracted in one pass without circulation. However, in such a system, it is preferable to circulate at least 10 times the amount of raw water supplied. The concentrated raw water may be sent to other treatment steps or returned to the raw water tank. There is an air bleed solenoid valve at the top of the system and a sludge bleed solenoid valve at the bottom.

[本発明の効果] 上述したように本発明の中空糸濾過モジユール
は構造が簡単であり、組立加工が容易であり、モ
ジユール同士の連結も簡単に行なえ、被処理流体
の通過抵抗が小さいという特徴を有しており、本
発明のシステムも連結が容易で圧力損失が従来の
モジユールに比べて非常に小さく、濾過分離され
た物質の回収が容易であり、接合曲管部材を用い
れば狭い場所にもコンパクトに配置できるという
優れたものである。この圧力損失が小さいという
特徴はポンプエネルギーを節約できるという効果
を発揮する。
[Effects of the present invention] As described above, the hollow fiber filtration module of the present invention has a simple structure, is easy to assemble, is easy to connect modules to each other, and has low passage resistance for the fluid to be treated. The system of the present invention is also easy to connect, the pressure loss is very small compared to conventional modules, the filtered and separated substances are easy to recover, and the use of jointed curved pipe members allows it to be installed in narrow spaces. It is also excellent in that it can be placed compactly. This feature of low pressure loss has the effect of saving pump energy.

本発明のシステムを垂直方向に立てて使用する
と、濾過分離された物質が最下段へ落下沈殿し、
容易に分離取出しができる。又最下段から加圧空
気水又は加圧空気を入れて中空糸束に付着した物
質を剥離して沈殿させたり加圧浮上させたりする
こともできる。又、本発明のシステムは圧損が小
さいため被濾過流体の流速を高めたり脈動流をお
こさせたりして洗浄するのも容易であり、薬剤に
よる洗浄も容易であるという特徴を有する。又、
中空糸束の交換、取りはずしての洗浄等も側管を
有する直管から中空糸束のみを取りはずすことが
できるため簡単となる。もちろんモジユールごと
交換することも可能である。
When the system of the present invention is used vertically, the filtered substances fall to the bottom and settle.
Can be easily separated and taken out. It is also possible to introduce pressurized water or pressurized air from the lowest stage to separate and precipitate substances attached to the hollow fiber bundle, or to float them under pressure. Furthermore, since the system of the present invention has a small pressure drop, it is easy to clean by increasing the flow rate of the fluid to be filtered or by creating a pulsating flow, and it is also easy to clean with chemicals. or,
Replacing the hollow fiber bundle, removing it and cleaning it, etc., becomes easy because only the hollow fiber bundle can be removed from the straight pipe having the side pipe. Of course, it is also possible to replace the entire module.

本発明のモジユール及びシステムは飲料水、工
業用水、医療用水、超純水、パイロジエンフリー
水等の各種用水の濾過、研磨廃水、含油排水、凝
集処理水、キレート反応処理水、生物処理水、濁
水、含金属粉廃水、脱脂液、含SS溶剤等の濾過、
金、銀等の有価金属粉末、フロツク等の濾過回
収、食品や製薬工業における有価液の回収等に好
適に用いることができる。
The module and system of the present invention can be used to filter various types of water such as drinking water, industrial water, medical water, ultrapure water, pyrogen-free water, polishing wastewater, oil-containing wastewater, flocculation treated water, chelate reaction treated water, biologically treated water, etc. Filtration of turbid water, metal-containing powder wastewater, degreasing liquid, SS-containing solvent, etc.
It can be suitably used for the filtration recovery of valuable metal powders such as gold and silver, flocs, etc., and the recovery of valuable liquids in the food and pharmaceutical industries.

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

第1図は本発明の中空糸濾過モジユールの1態
様例を示す一部欠載平面模式図であり、第2図及
び第3図は該中空糸濾過モジユールを直列に連結
してなる濾過システムの態様例の主要部分を示す
断面図である。第4図は本発明の中空糸濾過モジ
ユールを用いた濾過システムとポンプ及び付帯設
備を一体化したプラントの実施態様例を示すもの
であり、第5図は複数の側管を直管の円周上に配
置した例である。図において1は側管を有する直
管からなるハウジング、2は側管、3は中空糸濾
過膜、4は中空糸の存在しない側の直管部分、5
は接合部材、6は袋ナツトを示す。被処理流体は
aより入り、bより出る。濾過流体はCより出
る。第4図において11は側管付き直管、12は
コネクター、13は入口コネクター、14は出口
コネクター、15は循環ポンプ、16はエア抜き
電磁弁、17はスラツジ抜き電磁弁、18は原水
ライン、19は処理水ライン、20は循環ライ
ン、21は循環水流量計、22は処理水流量計、
23は入口圧力計、24は供給ポンプ、25〜2
9は流量調節バルブを示す。
FIG. 1 is a schematic plan view showing one embodiment of the hollow fiber filtration module of the present invention, and FIGS. 2 and 3 show a filtration system in which the hollow fiber filtration modules are connected in series. FIG. 3 is a cross-sectional view showing main parts of an embodiment. Figure 4 shows an embodiment of a plant that integrates a filtration system using the hollow fiber filtration module of the present invention, a pump, and ancillary equipment, and Figure 5 shows how a plurality of side pipes are connected to the circumference of a straight pipe. This is an example placed above. In the figure, 1 is a housing made of a straight pipe with a side pipe, 2 is a side pipe, 3 is a hollow fiber filtration membrane, 4 is a straight pipe part on the side where no hollow fiber is present, 5
6 indicates a joint member, and 6 indicates a cap nut. The fluid to be treated enters through a and exits through b. The filtrate fluid exits at C. In Fig. 4, 11 is a straight pipe with a side pipe, 12 is a connector, 13 is an inlet connector, 14 is an outlet connector, 15 is a circulation pump, 16 is an air vent solenoid valve, 17 is a sludge vent solenoid valve, 18 is a raw water line, 19 is a treated water line, 20 is a circulation line, 21 is a circulating water flow meter, 22 is a treated water flow meter,
23 is an inlet pressure gauge, 24 is a supply pump, 25-2
9 indicates a flow rate control valve.

Claims (1)

【特許請求の範囲】 1 U字状に束ねた中空糸束又は一端は中空糸の
開口部を開口状態に保ち他端は封鎖した中空糸束
を側管を有する直管からなるハウジングに収納
し、中空糸の開口部を開口状態に保つたまま側管
端部に固定してなる、中空糸束が側管部と直管部
の一部に存在する中空糸濾過モジユール。 2 U字状に束ねた中空糸束又は一端は中空糸の
開口部を開口状態に保ち他端は封鎖した中空糸束
を側管を有する直管からなるハウジングに収納
し、中空糸の開口部を開口状態に保つたまま側管
端部に固定してなる、中空糸束が側管部と直管部
の一部に存在する中空糸濾過モジユールの複数個
を各々の直管の端部を介して直列に連結し、直列
に連結されたモジユール列の一方の端に被処理流
体の入口、他方の端に複処理流体の出口を設け、
各々のモジユールの側管出口を濾過流体出口とす
る濾過システム。
[Claims] 1. A hollow fiber bundle bundled in a U-shape or a hollow fiber bundle with one end of the hollow fibers kept open and the other end closed is housed in a housing consisting of a straight pipe having a side pipe. , a hollow fiber filtration module in which a bundle of hollow fibers is present in a part of a side tube part and a part of a straight tube part, which is formed by fixing the opening of the hollow fibers to the end part of the side tube while keeping the openings in an open state. 2. A hollow fiber bundle bundled in a U-shape or a hollow fiber bundle with the opening of the hollow fibers at one end kept open and the other end closed is housed in a housing consisting of a straight tube having a side tube, and the opening of the hollow fibers is A plurality of hollow fiber filtration modules each having a hollow fiber bundle present in the side tube part and a part of the straight pipe part are fixed to the end part of the side pipe while keeping it in an open state. and providing an inlet for the fluid to be treated at one end of the serially connected module row and an outlet for the multi-processing fluid at the other end,
A filtration system in which the side pipe outlet of each module serves as a filtrate fluid outlet.
JP13337085A 1985-06-19 1985-06-19 Hollow yarn filter module and filtering system using the same Granted JPS61291008A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP13337085A JPS61291008A (en) 1985-06-19 1985-06-19 Hollow yarn filter module and filtering system using the same
US06/875,728 US4668401A (en) 1985-06-19 1986-06-18 Hollow-fiber filter module and filtration method using the same
DE8686108349T DE3666533D1 (en) 1985-06-19 1986-06-19 Hollow-fiber filter module and filtration method using the same
EP86108349A EP0207379B1 (en) 1985-06-19 1986-06-19 Hollow-fiber filter module and filtration method using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13337085A JPS61291008A (en) 1985-06-19 1985-06-19 Hollow yarn filter module and filtering system using the same

Publications (2)

Publication Number Publication Date
JPS61291008A JPS61291008A (en) 1986-12-20
JPH024328B2 true JPH024328B2 (en) 1990-01-26

Family

ID=15103137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13337085A Granted JPS61291008A (en) 1985-06-19 1985-06-19 Hollow yarn filter module and filtering system using the same

Country Status (1)

Country Link
JP (1) JPS61291008A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0671524B2 (en) * 1988-06-01 1994-09-14 株式会社クボタ Water purifier

Also Published As

Publication number Publication date
JPS61291008A (en) 1986-12-20

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