JPH0410371B2 - - Google Patents

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Publication number
JPH0410371B2
JPH0410371B2 JP8832184A JP8832184A JPH0410371B2 JP H0410371 B2 JPH0410371 B2 JP H0410371B2 JP 8832184 A JP8832184 A JP 8832184A JP 8832184 A JP8832184 A JP 8832184A JP H0410371 B2 JPH0410371 B2 JP H0410371B2
Authority
JP
Japan
Prior art keywords
cylinder
fibers
fiber bundle
hydrophilic
hollow
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
JP8832184A
Other languages
Japanese (ja)
Other versions
JPS60232208A (en
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 filed Critical
Priority to JP8832184A priority Critical patent/JPS60232208A/en
Publication of JPS60232208A publication Critical patent/JPS60232208A/en
Publication of JPH0410371B2 publication Critical patent/JPH0410371B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 技術分野 本発明は多孔質中空繊維を用いた過用モジユ
ールの処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a method for treating overused modules using porous hollow fibers.

更に詳しくは疎水性多孔質中空繊維を用いたモ
ジユールの任意の部分の中空繊維のみを親水化す
る方法に関する。
More specifically, the present invention relates to a method of hydrophilizing only the hollow fibers in an arbitrary portion of a module using hydrophobic porous hollow fibers.

従来技術 従来、水性液体(以下水と略称する)の過に
は微細孔を有する多孔質中空繊維を集束したもの
を筒内に封入した過モジユールが用いられ、水
は該微細孔を通して過され、該微細孔を通過で
きない水中の成分は別される。水が微細孔を通
過できるためには中空繊維がもともと親水性であ
るか、又は疎水性素材からなる場合は中空繊維の
管壁が親水化されている必要がある。しかし通常
の被処理水中には空気を主体とする気体(以外空
気と略称する)が混入されていることが多く、こ
れが親水化された管壁に達すると通常の圧力例え
ば1Kg/cm2程度では管壁を通過することができず
気泡として中空繊維の管壁に滞留し被処理水の浸
透を阻害する。従つてモジユールの過効率は時
間と共に低下し、最後には全く過不能の状態に
陥ることもある。
Prior Art Conventionally, a supermodule in which a bundle of porous hollow fibers having micropores is enclosed in a cylinder is used to pass through an aqueous liquid (hereinafter abbreviated as water), and the water is passed through the micropores. Components in the water that cannot pass through the micropores are separated. In order for water to pass through the micropores, the hollow fibers must originally be hydrophilic, or if they are made of a hydrophobic material, the tube walls of the hollow fibers must be made hydrophilic. However, ordinary water to be treated often contains gases mainly composed of air (abbreviated as air), and when this reaches the hydrophilized pipe wall, it will not react at a normal pressure of about 1 kg/ cm2 , for example. They cannot pass through the tube wall and remain as bubbles on the tube wall of the hollow fiber, inhibiting the permeation of the water to be treated. Therefore, the overefficiency of the module decreases over time, and it may eventually reach a state where it is completely ineffective.

かかる状態を改善するためにモジユールを構成
する中空繊維の一部を疎水性として前記混入気泡
が該疎水性部分を通じて中空内部へ浸透、前記開
口端から系外に脱出し得るようにすることが考え
られている。このように一部の繊維のみを疎水性
となし、他の繊維を親水性となすには予じめ親水
性の中空繊維と疎水性の中空繊維を所望の比率で
混合したものを繊維束としてモジユールを作る方
法が考えられている。この方法は親水性素材から
なる中空繊維と疎水性素材からなる中空繊維の両
方を準備する必要があり、製造コストは割高とな
る欠点がある。またもともと親水性の素材は微生
物により劣化され易いという欠点もある。
In order to improve this situation, it is considered that a part of the hollow fibers constituting the module is made hydrophobic so that the entrained air bubbles can penetrate into the hollow interior through the hydrophobic part and escape from the system through the open end. It is being In this way, in order to make only some fibers hydrophobic and other fibers hydrophilic, it is necessary to mix hydrophilic hollow fibers and hydrophobic hollow fibers in the desired ratio in advance and create a fiber bundle. A method of making modules is being considered. This method requires the preparation of both hollow fibers made of a hydrophilic material and hollow fibers made of a hydrophobic material, and has the disadvantage that the manufacturing cost is relatively high. Another drawback is that materials that are naturally hydrophilic are easily degraded by microorganisms.

勿論疎水性繊維を親水化処理によつて親水性と
なし、これと元の疎水性繊維とを所望の比率で混
合して繊維束となすことも可能であるが、繊維束
をモジユールに封入し繊維束の端部をポツテイン
グ材でハウジングに固定する際は乾燥状態で行な
う必要があるため、この場合の親水化処理は乾燥
状態でも親水性を保つような恒久親水化処理であ
ることが必要である。この方法としては親水性モ
ノマーグラフト、特殊条件でのプラズマ処理等が
知られているが面倒な方法であり、担当なコスト
アツプになる。
Of course, it is also possible to make hydrophobic fibers hydrophilic through a hydrophilic treatment and to mix them with the original hydrophobic fibers in a desired ratio to form a fiber bundle, but it is also possible to make a fiber bundle by enclosing the fiber bundle in a module. When fixing the end of the fiber bundle to the housing with potting material, it must be done in a dry state, so the hydrophilic treatment in this case must be a permanent hydrophilic treatment that maintains its hydrophilicity even in the dry state. be. Hydrophilic monomer grafting, plasma treatment under special conditions, and the like are known methods for this, but these methods are cumbersome and increase the cost.

発明の目的 本発明はこのような従来技術の欠点を克服する
ためになされたものであり疎水性中空繊維からな
る過モジユールを簡便に部分親水化する方法を
提供することにある。
OBJECTS OF THE INVENTION The present invention has been made in order to overcome the drawbacks of the prior art, and it is an object of the present invention to provide a method for easily partially hydrophilizing a permodule made of hydrophobic hollow fibers.

発明の構成 本発明の要旨は多数本の疎水性多孔質中空繊維
を集束してなる繊維束を筒内に収容し、該繊維束
の少なくとも一方の端部は該筒の一端においてそ
の中空内部が筒の外部と連通しているが繊維同士
の間及び繊維と筒内壁との間は水密に保持される
ようにポツテイング材によつて充填固定された開
口端を形成し、前記筒の一部を通じて筒内に供給
される被処理液体が繊維の多孔質管壁のみを通し
てその中空内部に浸透する際に過され、該過
水は該中空内部を経て前記開口端から筒外へ排出
されるようになされた過モジユールにおいて、
使用に先立つて前記開口端面の一部領域を通じて
適宜の親水化媒体を繊維束を構成する一部の中空
繊維の中空内部に圧入するか、又は親水化媒体を
中空繊維の中空内部に圧入して繊維束を親水化し
た後、適宜の疎水化触体を前記開口端面の一部領
域を通じて一部の中空繊維の中空内部に圧入しこ
れによつて親水性部分と疎水性部分を有する過
モジユールを得ることを特徴とする中空繊維を用
いた過モジユールの処理方法にある。
Structure of the Invention The gist of the present invention is that a fiber bundle formed by bundling a large number of hydrophobic porous hollow fibers is housed in a cylinder, and at least one end of the fiber bundle has a hollow interior at one end of the cylinder. An open end is formed that communicates with the outside of the cylinder, but is filled and fixed with a potting material so that the spaces between the fibers and between the fibers and the inner wall of the cylinder are maintained watertight, and the opening end is filled and fixed with a potting material to maintain watertightness between the fibers and between the fibers and the inner wall of the cylinder. The liquid to be treated that is supplied into the cylinder is passed through only the porous pipe wall of the fibers and permeates into the hollow interior thereof, and the superhydrous water is discharged from the open end to the outside of the cylinder through the hollow interior. In the supermodule made,
Prior to use, an appropriate hydrophilic medium is press-fitted into the hollow interior of some of the hollow fibers constituting the fiber bundle through a part of the open end surface, or a hydrophilic medium is press-fitted into the hollow interior of the hollow fibers. After making the fiber bundle hydrophilic, a suitable hydrophobizing contact is press-fitted into the hollow interior of some of the hollow fibers through a part of the open end surface, thereby forming a supermodule having a hydrophilic part and a hydrophobic part. A method of processing a permodule using hollow fibers is provided.

本発明において疎水性中空繊維としては疎水性
素材からなるものであればどのようなものでも用
いることが可能であり、ポリエチレン、ポリプロ
ピレン等のポリオレフイン、ポリテトラフルオロ
エチレン、ポリ弗化ビニリデン等の弗素化ポリオ
レフイン等を例示することができる。
In the present invention, any hydrophobic hollow fiber can be used as long as it is made of a hydrophobic material, including polyolefins such as polyethylene and polypropylene, and fluorinated fibers such as polytetrafluoroethylene and polyvinylidene fluoride. Examples include polyolefins.

本発明の対象となる過モジユールとしては全
量過型モジユールと部分過型モジユールのい
ずれも含まれる。
The permutation module to which the present invention is applied includes both full permutation modules and partial permutation modules.

本発明の親水性媒体としてはメチルアルコー
ル、エチルアルコール、プロピルアルコール等の
低級アルコール、界面活性剤水溶液等を用いるこ
とができるが、モジユールが医療用、飲食用の液
体処理用の場合は毒性、水置換後の親水性媒体の
除去の容易性等の点からエチルアルコールを用い
ることが好ましい。
As the hydrophilic medium of the present invention, lower alcohols such as methyl alcohol, ethyl alcohol, and propyl alcohol, surfactant aqueous solutions, etc. can be used. Ethyl alcohol is preferably used from the viewpoint of ease of removal of the hydrophilic medium after substitution.

疎水性媒体としてはフルオロカーボン等の化学
物質を用いることもできるが空気を用いるのが最
も簡便である。
Although chemical substances such as fluorocarbons can be used as the hydrophobic medium, it is most convenient to use air.

実施例 以下図面を参照して本発明を更に詳細に説明す
る。
EXAMPLES The present invention will be described in more detail below with reference to the drawings.

本発明の対象とする過用モジユールの構造の
一例を第1図及び第2図に示す。
An example of the structure of the overuse module to which the present invention is applied is shown in FIGS. 1 and 2.

第1図は全量過型モジユールの開口端面の一
部に親水化媒体又は疎水化媒体を注入するために
ノズルを押し当てた状態である。このモジユール
は中空構造を有する複数本の繊維1を平行に束ね
て繊維束となしたものを筒3内に軸方向に収容し
筒の一端において該繊維束の一方の端部をポツテ
イング材2によつて筒内壁に固定している。この
時各繊維1はその中空内部が閉塞されないよう
に、即ちその中空内部が出口5において外部と連
通可能に保持されると共に各繊維同士の間及び繊
維と筒内壁との間は完全に水密に充填固定されて
いることが必要である。又繊維束の他端部は筒3
の他端において密閉的に筒3に固定されている。
又筒3の外壁の一部には給水口4が設けられてい
る。第2図はこのモジユールの出口側から見た平
面図である。
FIG. 1 shows a state in which a nozzle is pressed against a part of the open end face of the full-flow module in order to inject a hydrophilic medium or a hydrophobic medium. In this module, a plurality of fibers 1 having a hollow structure are bundled in parallel to form a fiber bundle, which is housed in a cylinder 3 in the axial direction, and one end of the fiber bundle is attached to a potting material 2 at one end of the cylinder. It is fixed to the inner wall of the cylinder. At this time, each fiber 1 is held so that its hollow interior is not blocked, that is, its hollow interior can communicate with the outside at the outlet 5, and the spaces between each fiber and between the fibers and the inner wall of the cylinder are completely watertight. It is necessary that the filling is fixed. The other end of the fiber bundle is a tube 3.
The other end is hermetically fixed to the cylinder 3.
Further, a water supply port 4 is provided in a part of the outer wall of the tube 3. FIG. 2 is a plan view of this module as seen from the exit side.

中空繊維1の管壁は多数の微細孔を有してお
り、前記給水口4から筒3内に注入された被処理
水はこの微細孔を通して中空繊維1の中空部内に
浸透しその際管壁によつて不純物を過され、清
浄化された水は中空部を経て出口5から系外に排
出される。
The pipe wall of the hollow fiber 1 has a large number of micropores, and the water to be treated injected into the cylinder 3 from the water supply port 4 penetrates into the hollow part of the hollow fiber 1 through the micropores, and at this time, the water to be treated penetrates into the hollow part of the hollow fiber 1. The purified water is filtered out of impurities and is discharged out of the system from the outlet 5 through the hollow section.

第3図に示すものは過モジユールの別の例で
あり、中空繊維束は直線状ではなくU字状に湾曲
させられた状態で筒3内に収容され、両端部共そ
の中空内部が出口5において外部と連通可能に筒
3の一端において固定されている。この場合に
も、繊維同士の間及び繊維と筒内壁との間は水密
にポツテイング材2によつて充填されている。そ
の例においては給水口4は筒3の下端に設けられ
ており、前述の例と同様に筒内に供給された水は
繊維1の多孔質管壁を透過する際に過され、出
口5から系外に排出される。
The one shown in FIG. 3 is another example of a supermodule, in which the hollow fiber bundle is housed in a tube 3 not in a straight line but in a U-shaped curve, and the hollow interior of both ends is connected to the outlet 5. It is fixed at one end of the tube 3 so as to be able to communicate with the outside. In this case as well, the spaces between the fibers and between the fibers and the inner wall of the cylinder are filled with the potting material 2 in a watertight manner. In this example, the water supply port 4 is provided at the lower end of the tube 3, and as in the previous example, the water supplied into the tube is passed through the porous tube wall of the fiber 1, and then exits from the outlet 5. Exhausted from the system.

いずれの場合においても前述の通りモジユール
内の中空繊維はその管壁の一部、具体的には管壁
総面積の数%程度が疎水性であり、残りの部分は
親水性であることが被処理水中の混入空気を系外
に排出するために必要である。
In either case, as mentioned above, a part of the tube wall of the hollow fiber in the module, specifically about several percent of the total tube wall area, is hydrophobic, and the remaining portion is hydrophilic. Necessary to discharge air mixed in the treated water to the outside of the system.

かかる親疎比率を中空繊維に付与するため本発
明の一態様においては中空繊維として疎水性のも
のを用いてモジィユールを作製した後公知の方法
で親水化処理を行なう。これを用いて通常の方法
で過作業を行なうと前述のように混入空気が管
壁に滞溜し次第に過能力が低下し、気泡は順次
成長して筒内の空気だまり6(第3図)に蓄積さ
れ過効率が低下する。この欠点を防ぐため水を
充填したモジユールをあらかじめ、又は過途中
の気泡がたまつた時点で加圧空気供給源(図示し
ない)と接続された一定の出口断面積を有するノ
ズル7を筒3の出口端5の一部の領域に押しつけ
て加圧空気を繊維の中空部を通じて筒内に供給す
る。加圧空気はノズル7の押上てられた領域内の
中空繊維の管壁を内から外へ透過して筒内に排出
されその際に中空繊維の管壁内の水を排除しこれ
と置換される。疎水性の素材からなる多孔質中空
繊維の特性として一旦封入された空気は微細孔の
壁面に付着して捕捉されその部分が疎水化され
る。従つてこの処理後該疎水化部分を通じて水中
の空気が容易に繊維の中空部に透過し得るように
なり、気泡の滞溜のために他の部分の水過効率
が阻害されることが防止される。
In order to impart such a hydrophobicity ratio to the hollow fibers, in one embodiment of the present invention, a module is prepared using hydrophobic hollow fibers, and then a hydrophilic treatment is performed by a known method. When overwork is carried out in the normal manner using this, as mentioned above, the mixed air accumulates on the pipe wall, the overcapacity gradually decreases, and air bubbles grow one after another, causing air pockets 6 in the cylinder (Fig. 3). is accumulated and overefficiency decreases. In order to avoid this drawback, a nozzle 7 with a constant outlet cross-sectional area connected to a pressurized air supply source (not shown) is installed in the tube 3, either in advance or at the point where the air bubbles have accumulated during the course of filling the module with water. Pressurized air is supplied into the cylinder through the hollow part of the fiber by pressing against a certain area of the outlet end 5. The pressurized air passes through the tube wall of the hollow fiber in the region pushed up by the nozzle 7 from the inside to the outside and is discharged into the cylinder, at which time water in the tube wall of the hollow fiber is removed and replaced with water. Ru. As a characteristic of porous hollow fibers made of a hydrophobic material, once the air is encapsulated, it adheres to the walls of the micropores and is captured, making that part hydrophobic. Therefore, after this treatment, the air in the water can easily permeate into the hollow part of the fiber through the hydrophobized part, and the water permeation efficiency of other parts is prevented from being inhibited due to the accumulation of air bubbles. Ru.

本発明の方法によれば加圧空気を供給するため
のノズル7の出口面積を変えることによつて確実
に疎水化率をコントロールすることができ、又ノ
ズル7を押当てる領域を変えることによつえ所望
の個所の中空繊維を疎水化することができる。
According to the method of the present invention, the hydrophobization rate can be reliably controlled by changing the exit area of the nozzle 7 for supplying pressurized air, and by changing the area to which the nozzle 7 is pressed. The hollow fibers can be made hydrophobic at desired locations.

叙上の態様は次に示す実施例において更に明ら
かにされる。
The above aspects will be further elucidated in the following examples.

実施例 1 中空繊維としてポリエチレンからなる外径0.38
mm、孔径0.27mmのものを用い、これを960本束ね
たものを長さ120mmのU字型に曲げ、内径25mm、
厚さ3mm、長さ150mmのポリカーボネート製の筒
に収容し両者をポリウレタン系樹脂のポツテイン
グ材によつて固定して第3図に示す過モジユー
ルを作製した。使用に先立つてアルコール70%、
水30%のアルコール溶液を該モジユール内に圧入
し次いで水を圧入してこれと置換して繊維を親水
化した後、直径2.0mmのノズルを2個、モジユー
ルの出口5の繊維束の開口端に押しつけ、圧力4
Kg/cm2、温度約23℃の加圧空気を3分間供給し
た。これによつてノズルが押しつけられた部分に
開口端のある繊維が疎水化された。
Example 1 Hollow fiber made of polyethylene, outer diameter 0.38
mm, hole diameter 0.27 mm, a bundle of 960 pieces was bent into a U-shape with a length of 120 mm, an inner diameter of 25 mm,
The supermodule shown in FIG. 3 was prepared by housing the product in a polycarbonate cylinder having a thickness of 3 mm and a length of 150 mm, and fixing both together with a polyurethane resin potting material. 70% alcohol prior to use,
After pressurizing an alcohol solution containing 30% water into the module and then replacing it with water to make the fibers hydrophilic, two nozzles with a diameter of 2.0 mm are inserted into the open end of the fiber bundle at the outlet 5 of the module. pressure 4
Kg/cm 2 and pressurized air at a temperature of about 23° C. was supplied for 3 minutes. As a result, the fibers with open ends in the area against which the nozzle was pressed were made hydrophobic.

本発明の別の一態様はモジユールを構成するも
ともと疎水製の繊維をそのままの状態で残し、残
りの繊維のみを親水化して所定の親疎比率をもた
せるものである。即ち使用に先立つて一定の出口
断面積を有するノズル7を筒3の出口端5の一部
の領域に押しつけて該ノズル7からアルコールを
供給する。アルコールは該領域に開口を有する繊
維の中空部を通じて筒内に供給され、繊維の管壁
を透過してその微細孔を充填した上中空部外へ排
出され、給水口4から系外へ排出される。次にノ
ズル7から水を圧入すると繊維管壁内に残留して
いたアルコールは水と混じて排出され、管壁内は
水と置換されて親水性が付与される。かかる親水
化処理はノズル7が適用されている領域に開口を
有する繊維のみに対して施こされ、他の繊維は疎
水性のまま残されるので、前述の第1態様と同じ
くノズル7の出口面積を変えることによつて確実
に親疎比率をコントロールすることができ、又所
望の個所の中空繊維のみを選択的に親水化するこ
とができる。
Another embodiment of the present invention is to leave the originally hydrophobic fibers constituting the module as they are, and only the remaining fibers are made hydrophilic so as to have a predetermined affinity/phobicity ratio. That is, prior to use, a nozzle 7 having a constant outlet cross-sectional area is pressed against a part of the outlet end 5 of the cylinder 3, and alcohol is supplied from the nozzle 7. Alcohol is supplied into the cylinder through the hollow part of the fibers having openings in this region, passes through the pipe wall of the fibers, is discharged outside the upper hollow part filled with the fine pores, and is discharged to the outside of the system from the water supply port 4. Ru. Next, when water is injected from the nozzle 7, the alcohol remaining in the fiber tube wall is mixed with water and discharged, and the inside of the tube wall is replaced with water, thereby imparting hydrophilicity. This hydrophilic treatment is performed only on the fibers that have openings in the area where the nozzle 7 is applied, and the other fibers are left hydrophobic, so the exit area of the nozzle 7 is reduced as in the first embodiment. By changing the ratio, the affinity ratio can be reliably controlled, and only the hollow fibers at desired locations can be selectively made hydrophilic.

この第2態様は次に示す実施例において更に明
らかにされる。
This second aspect will be further elucidated in the following examples.

実施例 2 中空繊維としてポリエチレンからなる外径0.38
mm、孔径0.27mmのものを用い、これを1920本束ね
たものを直線状のまま、内径25mm、厚さ3mm、長
さ250mmのポリカーボネート製の筒に収容し、両
者をポリウレタン系樹脂のポツテイング材によつ
て固定し第1図に示す過モジユールを作製し
た。使用に先立つて内径8mmのノズル4個をモジ
ユールの出口5の繊維束の開口端に押しつけ、
200mlのアルコール70%、水30%のアルコール溶
液を圧入した後、水500mlを圧入してアルコール
溶液と置換し親水性となした。
Example 2 Hollow fiber made of polyethylene, outer diameter 0.38
25 mm in inner diameter, 3 mm in thickness, and 250 mm in length, 1,920 bundles of 1,920 bundles were placed in a polycarbonate tube with an inner diameter of 25 mm, a thickness of 3 mm, and a length of 250 mm, and both were placed in a potting material made of polyurethane resin. The supermodule shown in FIG. Prior to use, press four nozzles with an inner diameter of 8 mm against the open end of the fiber bundle at outlet 5 of the module.
After injecting 200 ml of an alcohol solution of 70% alcohol and 30% water, 500 ml of water was press-injected to replace the alcohol solution and make it hydrophilic.

親水比率は約40%であり、これはノズルの出口
断面積(π・82/4×4mm2)と筒の断面積 (π・252/4mm2)との比率と略々一致した。
The hydrophilic ratio was about 40%, which approximately matched the ratio of the nozzle exit cross-sectional area (π·8 2 /4×4 mm 2 ) and the cylinder cross-sectional area (π·25 2 /4 mm 2 ).

発明の効果 以上詳述した如く本発明によればモジユールの
開口端の一部領域にノズルを押し当てて親水化媒
体、又は疎水化媒体を圧入するのみで確実に所望
の比率で、且つ所望の個所の中空繊維を親水化又
は疎水化することが可能であり、従来の方法に比
し品質、コストの両面で遥かに優れたものであ
る。
Effects of the Invention As detailed above, according to the present invention, by simply pressing the nozzle against a partial area of the open end of the module and pressurizing the hydrophilic medium or the hydrophobic medium, the desired ratio can be reliably obtained. It is possible to make the hollow fibers hydrophilic or hydrophobic at certain points, and it is far superior to conventional methods in terms of both quality and cost.

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

第1図は本発明の第1実施態様を示すモジユー
ルの側断面図である。第2図は第1図のA−A線
に沿う平面断面図である。第3図は本発明の第2
実施態様を示すモジユールの側断面図である。 1……中空繊維、2……ポツテイング材、3…
…筒3,4……給水口、5……出口、6……空気
だまり、7……ノズル。
FIG. 1 is a side sectional view of a module showing a first embodiment of the present invention. FIG. 2 is a plan sectional view taken along line A--A in FIG. 1. Figure 3 shows the second embodiment of the present invention.
FIG. 2 is a side sectional view of a module showing an embodiment. 1...Hollow fiber, 2...Potting material, 3...
...Cylinder 3, 4...Water supply port, 5...Outlet, 6...Air pocket, 7...Nozzle.

Claims (1)

【特許請求の範囲】 1 多数本の疎水性多孔質中空繊維を集束してな
る繊維束を筒内に収容し、該繊維束の少なくとも
一方の端部は該筒の一端においてその中空内部が
筒の外部と連通しているが繊維同士の間及び繊維
と筒内壁との間は水密に保持されるようにポツテ
イング材によつて充填固定された開口端を形成
し、前記筒の一部を通じて筒内に供給される被処
理液体が繊維の多孔質管壁のみを通してその中空
内部に浸透する際に過され、該過水は該中空
内部を経て前記開口端から筒外へ排出されるよう
になされた過モジユールにおいて、使用に先立
つて前記開口端面の一部領域を通じて適宜の親水
化媒体を繊維束を構成する一部の中空繊維の中空
内部に圧入するか、又は親水化媒体を中空繊維の
中空内部に圧入して繊維束を親水化した後適宜の
疎水化媒体を前記開口端面の一部領域を通じて一
部の中空繊維の中空内部に圧入し、これによつて
親水性部分と疎水性部分を有する過モジユール
を得ることを特徴とする中空繊維を用いた過モ
ジユールの処理方法。 2 繊維束の前記開口端以外の端部が水密に密封
されている特許請求の範囲第1項に記載された処
理方法。 3 繊維束がU字状をなして筒内に収容され、該
繊維束の両端が共に前記開口端を形成している特
許請求の範囲第1項に記載された処理方法。 4 処理媒体として先ずアルコール類又は界面活
性剤を用いて繊維を処理した後、水と置換して疎
水性モジユールの一部を親水化する特許請求の範
囲第1項から第3項までのいずれか一項に記載さ
れた処理方法。 5 処理媒体として空気を用いて親水化されたモ
ジユールの一部を疎水化する特許請求の範囲第1
項から第3項までのいずれか一項に記載された処
理方法。
[Scope of Claims] 1. A fiber bundle formed by bundling a large number of hydrophobic porous hollow fibers is housed in a cylinder, and at least one end of the fiber bundle is arranged such that the hollow interior thereof forms a cylinder at one end of the cylinder. An open end is formed that communicates with the outside of the cylinder, but is filled and fixed with a potting material so that the spaces between the fibers and between the fibers and the inner wall of the cylinder are maintained watertight, and the cylinder is inserted through a part of the cylinder. The liquid to be treated that is supplied into the tube permeates into the hollow interior through only the porous tube wall of the fiber, and the permeable water passes through the hollow interior and is discharged from the open end to the outside of the tube. In the above module, prior to use, an appropriate hydrophilic medium is press-fitted into the hollow interior of some of the hollow fibers constituting the fiber bundle through a partial region of the open end surface, or a hydrophilic medium is press-fitted into the hollow interior of some of the hollow fibers constituting the fiber bundle. After making the fiber bundle hydrophilic by press-fitting it inside, a suitable hydrophobizing medium is press-fitted into the hollow interior of some of the hollow fibers through a part of the open end surface, thereby separating the hydrophilic part and the hydrophobic part. 1. A method for processing permodule using hollow fibers, characterized by obtaining permodule having the following properties. 2. The processing method according to claim 1, wherein the ends of the fiber bundle other than the open end are watertightly sealed. 3. The processing method according to claim 1, wherein the fiber bundle is housed in a cylinder in a U-shape, and both ends of the fiber bundle form the open end. 4. Any one of claims 1 to 3, in which the fibers are first treated using an alcohol or a surfactant as a treatment medium, and then replaced with water to make a part of the hydrophobic module hydrophilic. The processing method described in paragraph 1. 5 Claim 1 in which a part of the module that has been made hydrophilic is made hydrophobic using air as a treatment medium
The processing method described in any one of Items 1 to 3.
JP8832184A 1984-05-04 1984-05-04 Treatment of filter module using hollow fiber Granted JPS60232208A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8832184A JPS60232208A (en) 1984-05-04 1984-05-04 Treatment of filter module using hollow fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8832184A JPS60232208A (en) 1984-05-04 1984-05-04 Treatment of filter module using hollow fiber

Publications (2)

Publication Number Publication Date
JPS60232208A JPS60232208A (en) 1985-11-18
JPH0410371B2 true JPH0410371B2 (en) 1992-02-25

Family

ID=13939648

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8832184A Granted JPS60232208A (en) 1984-05-04 1984-05-04 Treatment of filter module using hollow fiber

Country Status (1)

Country Link
JP (1) JPS60232208A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02227123A (en) * 1989-02-28 1990-09-10 Material Eng Tech Lab Inc Microfiltration element
NL1023332C2 (en) * 2003-05-02 2004-11-03 Norit Proces Technologie Holdi Membrane filter with venting and method for its manufacture.
JP5115532B2 (en) * 2009-09-30 2013-01-09 東レ株式会社 Hollow fiber membrane module, method for producing hollow fiber membrane module, water purifier cartridge and water purifier
EP3580177B1 (en) 2017-02-13 2023-12-13 Merck Patent GmbH Method and system for producing ultrapure water
EP3580184A1 (en) * 2017-02-13 2019-12-18 Merck Patent GmbH A method for producing ultrapure water
CN110300735A (en) 2017-02-13 2019-10-01 默克专利股份公司 Method for producing ultrapure water
WO2018146318A1 (en) 2017-02-13 2018-08-16 Merck Patent Gmbh A method for producing ultrapure water
US11680239B2 (en) 2018-12-31 2023-06-20 Repligen Corporation Filter for mammalian cell culture perfusion and clarification with hydrophobic hollow fiber

Also Published As

Publication number Publication date
JPS60232208A (en) 1985-11-18

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