JPH08266872A - Production of hollow fiber membrane type separation module - Google Patents
Production of hollow fiber membrane type separation moduleInfo
- Publication number
- JPH08266872A JPH08266872A JP7382895A JP7382895A JPH08266872A JP H08266872 A JPH08266872 A JP H08266872A JP 7382895 A JP7382895 A JP 7382895A JP 7382895 A JP7382895 A JP 7382895A JP H08266872 A JPH08266872 A JP H08266872A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber membrane
- casing
- bundle
- resin
- 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.)
- Pending
Links
- 239000012510 hollow fiber Substances 0.000 title claims abstract 21
- 239000012528 membrane Substances 0.000 title claims abstract 20
- 238000000926 separation method Methods 0.000 title claims 7
- 238000004519 manufacturing process Methods 0.000 title claims 5
- 229920005989 resin Polymers 0.000 claims abstract 10
- 239000011347 resin Substances 0.000 claims abstract 10
- 239000000843 powder Substances 0.000 claims abstract 8
- 238000001816 cooling Methods 0.000 claims abstract 3
- 229920005992 thermoplastic resin Polymers 0.000 claims abstract 2
- 239000000463 material Substances 0.000 claims 3
- 230000001133 acceleration Effects 0.000 claims 2
- 239000002861 polymer material Substances 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 4
- 238000010438 heat treatment Methods 0.000 abstract 3
- 238000001704 evaporation Methods 0.000 abstract 1
- 239000000155 melt Substances 0.000 abstract 1
- 238000002844 melting Methods 0.000 abstract 1
- 230000008018 melting Effects 0.000 abstract 1
- 229920000098 polyolefin Polymers 0.000 abstract 1
- 229920005672 polyolefin resin Polymers 0.000 abstract 1
- 238000003756 stirring Methods 0.000 abstract 1
- 239000000725 suspension Substances 0.000 abstract 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、電子工業、食品工業、
医薬工業様等、低溶出性、耐薬品性を必要とする分野で
利用される中空糸膜型分離モジュ−ルの製造方法に関す
る。BACKGROUND OF THE INVENTION The present invention relates to the electronic industry, food industry,
The present invention relates to a method for producing a hollow fiber membrane type separation module which is used in fields requiring low elution and chemical resistance such as in the pharmaceutical industry.
【0002】[0002]
【従来の技術】中空糸膜分離モジュ−ルは複数本の中空
糸状多孔質膜を結束し、その端部を固定してハウジング
内に組み込み、ユニット化したものであるが、中空糸状
多孔質膜端部を固定化する手段としては、従来ポリウレ
タン系又はエポキシ系樹脂からなる接着剤が使用されて
いる。しかし、接着剤による固定化方法では接着剤から
の溶出物があり、耐熱性及び耐薬品性にも乏しいため、
浄水器用等の限定された用途にしか使用できない欠点が
あった。この接着剤による固定化に代る手段として熱融
着方法がある。この方法は、複数の中空糸状多孔質膜同
志の間隙にポリオレフィン樹脂のような熱融着性樹脂を
充填し、加熱して一体とするのであるが、樹脂の熱溶融
時に中空糸状多孔質膜の形状を維持することが困難で中
空糸状多孔質膜が潰れたり、或は中空糸膜の内径及び外
径の寸法に変化を生じる等の問題点があった。2. Description of the Related Art A hollow fiber membrane separation module is a unit in which a plurality of hollow fiber-like porous membranes are bound together and the ends are fixed and incorporated into a housing to form a unit. As a means for fixing the ends, an adhesive agent made of polyurethane-based or epoxy-based resin has been conventionally used. However, with the method of fixing with an adhesive, there is elution from the adhesive, and it is also poor in heat resistance and chemical resistance.
It has a drawback that it can only be used for limited applications such as water purifiers. There is a heat fusion method as an alternative to fixing with the adhesive. In this method, a space between a plurality of hollow fiber-like porous membranes is filled with a heat-fusible resin such as a polyolefin resin and heated to be integrated. There are problems that it is difficult to maintain the shape, the hollow fiber-shaped porous membrane is crushed, or the inner diameter and outer diameter of the hollow fiber membrane are changed.
【0003】この問題点を解決する手段として、特開平
1−293105号公報には熱溶融を行なう部分の中空
糸膜の内部を加熱の際に流動性を示さない物質で目止め
を行い、中空糸膜端部同士の隙間に熱可塑性樹脂を詰め
加熱溶融して接着したのち、目止め剤を除去する方法が
記載されている。そして具体的に補助部材を詰めた中空
糸状多孔質膜の糸束の外周に熱収縮性のテ−プを巻きつ
けて固定し、これを加熱することによって、補助部材が
完全に中空糸状多孔質膜同志の間隙を埋めると共に熱収
縮性テ−プの収縮によって糸束が締めつけられて液密的
に熱融着されることが示されている。As a means for solving this problem, Japanese Patent Application Laid-Open No. 1-293105 discloses that the inside of the hollow fiber membrane where heat is melted is sealed with a substance that does not flow when heated, A method is described in which a thermoplastic resin is filled in a gap between end portions of a yarn film, heated and melted to be bonded, and then a filling agent is removed. Then, specifically, a heat-shrinkable tape is wound around the outer periphery of the bundle of hollow fiber-shaped porous membranes packed with the auxiliary member to be fixed, and this is heated so that the auxiliary member is completely hollow-fiber-like porous. It has been shown that the yarn bundle is clamped and liquid-tightly heat-sealed by filling the gap between the membranes and shrinking the heat-shrinkable tape.
【0004】また、特開平4−63117号公報には中
空糸膜及び中空糸膜の結束端部における封止剤の材質を
オレフィン系樹脂を使用した中空糸膜分離ユニットが開
示されている。そして、この中空糸型膜分離ユニットの
製造方法として封止剤のポリオレフィン系樹脂の微粉末
の懸濁液をつくり、これに中空糸膜を結束し、結束端部
を浸漬し、封止剤の融点以上の温度に加熱して懸濁液の
液体を蒸発させ、封止剤微粉末が溶融流動状態になった
後、常温まで徐冷固化する方法が開示されている。しか
し、この製造方法では加熱溶融時に封止剤微粉末間の空
隙を埋めるための操作を行なわないため気泡の残存が多
く、初期シ−ル性及び耐熱くり返し圧力性の耐久性の保
証がしがたいという問題があった。Further, Japanese Patent Application Laid-Open No. 4-63117 discloses a hollow fiber membrane separation unit in which an olefin resin is used as the material of the hollow fiber membrane and the sealing agent at the binding end of the hollow fiber membrane. Then, as a method for manufacturing this hollow fiber type membrane separation unit, a suspension of fine powder of a polyolefin resin as a sealing agent is prepared, and the hollow fiber membrane is bound to this, and the binding end portion is dipped to remove the sealing agent. A method is disclosed in which the liquid of the suspension is evaporated by heating to a temperature equal to or higher than the melting point, the fine powder of the sealing agent is brought into a molten and fluidized state, and then slowly cooled and solidified to room temperature. However, in this manufacturing method, since the operation for filling the voids between the fine powders of the sealing agent is not performed at the time of heating and melting, many bubbles remain, so that the durability of the initial sealability and the heat and pressure resistance cannot be guaranteed. There was a problem of wanting.
【0005】これに対して前記特開平1−293105
号公報記載の方法では、熱収縮性のテ−プを巻きつけ、
これによって糸束は締めつけられ、熱溶融した補助部材
は中空糸状多孔質膜同志の隙間を埋めることができ、液
密的に熱溶融接着されるが、糸束外周にテ−プを巻きつ
ける等の操作を行わなければならず、しかも任意に巻き
つけるために収縮後の外径寸法が一定とならない。この
ようにして作られた濾過素子(中空糸膜分離モジュ−ル
素子)は、チュ−ブ状ケ−シング内に挿入されて使用さ
れるが、素子の端部外周とケ−シング内壁との間のシ−
ルは、Oリングパッキンを用いるか、または、再度補助
部材を用いて溶着する必要がある。従って、前者の場合
パッキン材の溶出、濾過素子の外径のバラツキからくる
パッキング材との間のシ−ル不良や耐久上の問題を生
じ、後者の場合外周部の接合不良、またあらかじめ接合
した中空糸膜間の再溶融に起因するシ−ル不良、更に製
造工程の増加等の問題を生ずる。On the other hand, the above-mentioned Japanese Patent Laid-Open No. 1-293105.
In the method described in the publication, a heat-shrinkable tape is wrapped,
As a result, the yarn bundle is tightened, and the heat-melted auxiliary member can fill the gap between the hollow fiber-shaped porous membranes and is heat-melt-bonded in a liquid-tight manner. The above-mentioned operation must be performed, and the outer diameter dimension after contraction is not constant because it is wrapped arbitrarily. The filtration element (hollow fiber membrane separation module element) produced in this way is used by inserting it into a tube-shaped casing. Between
The O-ring packing needs to be used again or the auxiliary member needs to be welded again. Therefore, in the former case, the packing material elutes, and the sealing material between the packing material comes out due to the variation in the outer diameter of the filter element and the durability problem occurs. This causes problems such as defective sealing due to remelting between the hollow fiber membranes and an increase in the number of manufacturing processes.
【0006】[0006]
【発明が解決しようとする課題】そこで、本発明者は上
記問題点を解決するために、種々検討した結果、本発明
を完成したもので、本発明の目的は、高分子材料から成
る複数本の中空糸膜が束ねられ、チュ−ブ状ケ−シング
内に高密度に組み込まれた中空糸膜型分離モジュ−ルに
おいて、中空糸膜の端部が潰れたり、或いは中空糸膜の
内径寸法に変化を生じることなく、その形状を維持して
液密的に一体に接合された中空糸膜モジュ−ルを提供す
るものである。Therefore, the present inventor has completed the present invention as a result of various studies in order to solve the above-mentioned problems, and an object of the present invention is to provide a plurality of polymer materials. In a hollow fiber membrane type separation module in which the hollow fiber membranes are bundled and incorporated in a tube-shaped casing at a high density, the end portions of the hollow fiber membranes are crushed, or the inner diameter of the hollow fiber membranes is measured. The present invention provides a hollow fiber membrane module liquid-tightly and integrally bonded to the hollow fiber membrane module, maintaining its shape without changing its shape.
【0007】[0007]
【課題を解決するための手段】本発明の要旨は、高分子
材料から成る複数本の中空糸膜が束ねられ、チュ−ブ状
ケ−シング内に高密度に組み込まれた中空糸膜型分離モ
ジュ−ルの製造方法において、高分子材料からなり、端
部が目止めされた複数本の中空糸膜の端部を熱可塑性樹
脂粉末で覆った後、束ねてチュ−ブ状ケ−シング内に挿
入して中空糸膜束とケ−シングの間隙及び中空糸膜同志
の間隙を前記樹脂粉末で満たした後、加熱して樹脂粉末
を熱溶融させて中空糸膜端部を溶融樹脂に埋設した後、
遠心加速度を与えつつ冷却固化して中空糸膜型分離モジ
ュ−ル端部を液密的に一体に接合することを特徴とする
中空糸膜型分離モジュ−ルの製造方法、又は、高分子材
料から成る複数本の中空糸膜が束ねられ、チュ−ブ状ケ
−シング内に高密度に組み込まれた中空糸膜型分離モジ
ュ−ルの製造方法において、高分子材料からなり、端部
が目止めされた複数本の中空糸膜の端部を溶融された樹
脂で覆ってた後、束ねてチュ−ブ状ケ−シング内に挿入
して中空糸膜束とケ−シングの間隙及び中空糸膜同志の
間隙を前記熱溶融した樹脂で満たし中空糸膜端部を溶融
樹脂に埋設した後、遠心加速度を与えつつ冷却固化して
中空糸膜型分離モジュ−ル端部を液密的に一体に接合す
ることを特徴とする中空糸膜型分離モジュ−ルの製造方
法である。SUMMARY OF THE INVENTION The gist of the present invention is a hollow fiber membrane type separation in which a plurality of hollow fiber membranes made of a polymer material are bundled and incorporated in a tube-shaped casing at a high density. In the method for producing a module, the ends of a plurality of hollow fiber membranes made of a polymer material and having their ends sealed are covered with a thermoplastic resin powder, and then bundled into a tube-shaped casing. After filling the hollow fiber membrane bundle and the casing and the gap between the hollow fiber membranes with the resin powder, the resin powder is heated to melt the resin powder and the end of the hollow fiber membrane is embedded in the molten resin. After doing
A method for producing a hollow fiber membrane-type separation module, characterized in that the hollow fiber membrane-type separation module ends are liquid-tightly joined by cooling and solidifying while imparting centrifugal acceleration, or a polymer material. In a method for producing a hollow fiber membrane-type separation module in which a plurality of hollow fiber membranes composed of is bundled in a tube-shaped casing at a high density, the hollow fiber membrane-type separation module is made of a polymer material, and the end portions are After covering the ends of the stopped hollow fiber membranes with a molten resin, the bundles are bundled and inserted into a tube-shaped casing, and the gap between the hollow fiber membrane bundle and the casing and the hollow fibers After filling the gap between the membranes with the hot-melt resin, the hollow fiber membrane end is buried in the molten resin, and then the hollow fiber membrane separation module end is liquid-tightly integrated by cooling and solidifying while applying centrifugal acceleration. The method for producing a hollow fiber membrane type separation module is characterized in that the hollow fiber membrane type separation module is joined.
【0008】即ち、本発明においては、中空糸膜束端部
の中空糸同志の隙間、及び中空糸膜束とケ−シングとの
隙間を樹脂粉末で満たした後、加熱して樹脂粉末を熱溶
融するか、或いは、中空糸膜束端部の中空糸同志の隙
間、及び中空糸膜束とケ−シングとの隙間を直接熱溶融
した樹脂で覆うかして上記隙間に熱溶融性樹脂を埋設し
た後、遠心力をかけつつ固化させる、いわゆる遠心冷却
により、溶融樹脂の冷却固化収縮時に発生するボイドを
無くすことができ、これによって中空糸膜束端部及び中
空糸膜束端部とケ−シングとの間に何らの気泡を生じる
こと無く完全に接合することができ、中空糸膜、接合樹
脂及びケ−シングを例えばポリオレフィン樹脂を使用し
た場合には完全なオ−ルポリオレフィン製中空糸膜型分
離モジュ−ルを形成することができる。That is, in the present invention, the gap between the hollow fibers at the end of the hollow fiber membrane bundle and the gap between the hollow fiber membrane bundle and the casing are filled with resin powder, and then heated to heat the resin powder. Either by melting or by directly covering the gap between the hollow fibers at the end of the hollow fiber membrane bundle and the gap between the hollow fiber membrane bundle and the casing with a heat-melted resin, a heat-meltable resin is filled in the gap. After embedding, by solidifying while applying centrifugal force, so-called centrifugal cooling, it is possible to eliminate voids that occur when the molten resin cools and solidifies and shrinks, and thus the hollow fiber membrane bundle end portion and the hollow fiber membrane bundle end portion -It can be completely bonded without generating any bubbles between it and the singing, and when the hollow fiber membrane, the bonding resin and the casing are made of, for example, a polyolefin resin, it is a perfect allol polyolefin hollow fiber. Forming a membrane-type separation module Rukoto can.
【0009】本発明の中空糸膜としては、特に限定され
るものではなく、通常中空糸膜型分離モジュ−ルに使用
されている中空糸膜の何れでもよく、例えばポリオレフ
ィン、ポリサルホン、ポリフッ化ビニリデン(PVD
F)、ポリテトラフルオロエチレン(PTFE)等であ
る。この中空糸膜同志、及び中空糸膜とケ−シングを接
合する熱溶融性樹脂としては使用する中空糸膜の材質に
より適宜選択すればよく、例えばポリオレフィン、ポリ
サルホンやポリフッ化ビニリデンの中空糸膜に対しては
ポリオレフィン系樹脂を、また、ポリテトラフルオロエ
チレンの中空糸膜に対してはパ−フルオロアルコキシア
ルカン(PFE)やテトラフルオロエチレン/ヘキサフ
ルオロプロピレン(FEP)を使用することが好まし
い。The hollow fiber membrane of the present invention is not particularly limited, and may be any of the hollow fiber membranes commonly used in hollow fiber membrane type separation modules, such as polyolefin, polysulfone and polyvinylidene fluoride. (PVD
F), polytetrafluoroethylene (PTFE) and the like. The hollow fiber membranes and the heat-melting resin for joining the hollow fiber membrane and the casing may be appropriately selected depending on the material of the hollow fiber membrane to be used. For example, a hollow fiber membrane of polyolefin, polysulfone or polyvinylidene fluoride may be used. On the other hand, it is preferable to use a polyolefin resin and, for the hollow fiber membrane of polytetrafluoroethylene, perfluoroalkoxyalkane (PFE) or tetrafluoroethylene / hexafluoropropylene (FEP).
【0010】中空糸膜の端部を溶融された樹脂で覆うに
先立って、中空糸膜の先端部を目止めを施こすことが好
ましく、各中空糸膜の目止めは、中空糸膜内端部に目止
め材を充填することによって行うが、材質や径によって
は、切断による端部のつぶれで目止めが可能である。ま
た、ケ−シングの熱変形を防止するためケ−シングの外
側に形状保持チュ−ブを取り付けることが好ましい。ま
た、必要量以上の樹脂が注入されないようにケ−シング
内面の先端部から10〜40mm付近の個所に環状突起
を設けて中空糸膜の束を絞ることが好ましい。また、突
起の代わりにリング状の別部品を用けたり、ケ−シング
の内径を途中から小さくして中空糸膜束を絞ってもよ
い。ケ−シング内面に環状突起を設けると中空糸膜束が
この部分で絞られた状態となるので、各中空糸膜間が密
となり、溶融樹脂はこの部分で止まり、それ以上中へ入
り込まず、従って環状突起より下方の部分の溶融樹脂が
より均一に注入された状態となってシ−ルがより確実に
なされる。Prior to covering the ends of the hollow fiber membranes with the molten resin, it is preferable to seal the tips of the hollow fiber membranes. The filling is performed by filling the portion with a sealing material, but depending on the material and the diameter, the sealing can be performed by crushing the end portion due to cutting. Further, in order to prevent thermal deformation of the casing, it is preferable to attach a shape holding tube to the outside of the casing. Further, it is preferable that an annular projection is provided at a position in the vicinity of 10 to 40 mm from the tip of the inner surface of the casing to prevent the resin from being injected in excess of the required amount so as to squeeze the bundle of hollow fiber membranes. Further, a ring-shaped separate component may be used instead of the protrusion, or the hollow fiber membrane bundle may be squeezed by reducing the inner diameter of the casing midway. When an annular projection is provided on the inner surface of the casing, the hollow fiber membrane bundle is squeezed at this portion, so that the hollow fiber membranes are closely packed and the molten resin stops at this portion and does not enter further. Therefore, the molten resin in the portion below the annular projection is more evenly injected, and the seal is made more reliable.
【0011】中空糸膜の端部を溶融樹脂中に埋設する方
法として、中空糸膜をバラバラにしてその端部に樹脂粉
末を付着させた後、これを束ねてケ−シング内に組み込
み中空糸膜間および中空糸膜とケ−シングの間に樹脂粉
末を充填した後加熱して溶融状態にして埋設するか、中
空糸膜端部に直接溶融樹脂を付着させて埋設する方法の
何れでもよい。中空糸膜端部に樹脂粉末を付着させる方
法としては、樹脂粉末の懸濁液中に中空糸膜端部を浸漬
して付着させる方法が好適である。また、中空糸膜端部
に直接溶融樹脂を付着させる方法としては、中空糸膜端
部をばらばらにして溶融樹脂を付着させた後、これをケ
−シング内に組み込むか、或いは中空糸膜の先端部をケ
−シング端部より外方に出した状態でケ−シング内に組
み込み、この状態で中空糸膜間に溶融樹脂が入り込みや
すいように中空糸膜の先端部を拡げて溶融樹脂浴中に浸
し中空糸膜に溶融樹脂を付着させて後、中空糸膜を完全
に組み込むことによって中空糸膜束端部を樹脂中に埋設
することができる。As a method of burying the end portions of the hollow fiber membrane in the molten resin, the hollow fiber membranes are separated and resin powder is adhered to the end portions, which are then bundled and incorporated in a casing. Either a method of filling the resin powder between the membranes or between the hollow fiber membrane and the casing and then heating it to be in a molten state for embedding or embedding by directly adhering the molten resin to the end of the hollow fiber membrane may be employed. . As a method for adhering the resin powder to the end of the hollow fiber membrane, a method of immersing the end of the hollow fiber membrane in a suspension of the resin powder and adhering it is suitable. As a method of directly attaching the molten resin to the end portions of the hollow fiber membranes, the end portions of the hollow fiber membranes are separated and the molten resin is attached thereto, or the molten resin is incorporated into the casing, or The tip of the hollow fiber membrane is incorporated into the casing with the tip of the hollow fiber membrane extending outward from the casing end. In this state, the tip of the hollow fiber membrane is expanded so that molten resin can easily enter between the hollow fiber membranes. It is possible to embed the hollow fiber membrane bundle end portion in the resin by completely immersing the hollow fiber membrane after immersing it in the hollow fiber membrane to attach the molten resin to the hollow fiber membrane.
【0012】続いて、中空糸膜束端部を溶融樹脂中に埋
設した後、遠心加速度を与えつつ冷却固化する所謂遠心
冷却によって溶融樹脂を固化する。遠心冷却によって溶
融樹脂を固化することによって、溶融樹脂の冷却固化収
縮時に発生するボイドを無くすことができ、これによっ
て中空糸膜束端部及び中空糸膜束端部とケ−シングとの
間に何らの気泡を生じること無く完全に接合することが
でる。遠心加速度としては100〜150G程度であ
る。冷却固化後、その先端部を切断して中空糸膜の開放
端を切断面上に出して中空糸膜分離モジュ−ルを得るこ
とができ、この端部にケ−シングと同質の合成樹脂より
なるキャップを溶着接合して使用に供される。Subsequently, the hollow fiber membrane bundle end portion is embedded in the molten resin, and then the molten resin is solidified by so-called centrifugal cooling in which it is cooled and solidified while applying centrifugal acceleration. By solidifying the molten resin by centrifugal cooling, it is possible to eliminate voids that occur when the molten resin cools and solidifies and shrinks, and thereby, between the hollow fiber membrane bundle end portion and the hollow fiber membrane bundle end portion and the casing. It is possible to bond completely without generating any bubbles. The centrifugal acceleration is about 100 to 150G. After cooling and solidification, the tip of the hollow fiber membrane is cut to expose the open end of the hollow fiber membrane on the cut surface to obtain a hollow fiber membrane separation module. At this end, a synthetic resin of the same quality as the casing is used. The cap is welded and joined for use.
【0013】[0013]
【実施例】次に図をもって本発明の実施例を示す。 実施例1 図1は本発明の製造方法の実施態様を説明した説明図で
ある。ポリオレフィンよりなり、外径1.2mmの中空
糸膜約400〜600本を束とし、その中央部を紐で束
ね(a)、この束を紐の部分でU字状に折り、2つ折り
した側から入口パイプ6を有するポリオレフィン製の外
径70mmのケ−シング(又はチュ−ブ)5内に、その
先端部を30〜80mm突出させて挿入する。なお、予
め中空糸膜の先端部は潰し、高濃度懸濁液が中空部内に
浸入するのを防止する。なお、ケ−シング5の内壁面に
は先端から10〜40mmのところに中空糸膜束を絞る
ため環状突起2が設けてあり、また、ケ−シング5の外
側にはケ−シング5の熱変形を制御する為の形状保持チ
ュ−ブ12が取付けられている(b)。他方、封止剤と
してポリオレフィン系樹脂(PP,PE,EVA等)微
粉末の適量を容器4に入れ、分散液(エタノ−ル)を加
え撹拌し、高濃度懸濁液8を作製する(c)。次に中空
糸膜1の束の突出部分の中空糸膜束を拡げて高濃度懸濁
液8に浸漬し(d)、中空糸のまわりに高濃度懸濁液を
十分に塗布した後、懸濁液浴より取り出し、中空糸膜束
1全体を中空糸膜束1を結束してある紐で引き上げ
(e)ポリオレフィン製のケ−シング5に引込め、ユニ
ットを形成する(f)。続いて、このユニットを、ポリ
オレフィン系樹脂よりも低い温度で加熱して分散媒のエ
タノ−ルを蒸発させる。次に、これを乾燥後、封止剤の
融点以上にヒ−タ−ブロック13によって端部を加熱、
封止剤を溶融させる(g)。その後、直ちに(1〜2m
in以内)遠心機10にセットし、100〜150Gの
遠心力を与えつつ冷却、固化させ(h)しかる後、遠心
機10から取り出した後、形状保持チュ−ブ12を外し
て溶着面の先端から5〜10mmを切断し、中空糸膜開
放端を切断面上に出して一方側に固定端部3を有するオ
−ルポリオレフィン製中空糸膜モジュ−ルを得た
(i)。該モジュ−ル端部にポリオレフィン製カバ−体
(キャップ)を溶着接合し、使用に供した(j)。EXAMPLE An example of the present invention will be shown with reference to the drawings. Example 1 FIG. 1 is an explanatory view illustrating an embodiment of the manufacturing method of the present invention. Approximately 400 to 600 hollow fiber membranes made of polyolefin and having an outer diameter of 1.2 mm are bundled into a bundle, the central part of which is bundled with a string (a), and the bundle is folded into a U-shape and folded in two. To the casing (or tube) 5 made of polyolefin and having an outer diameter of 70 mm and having an inlet pipe 6, the tip portion thereof is projected by 30 to 80 mm and inserted. The tip of the hollow fiber membrane is crushed in advance to prevent the high-concentration suspension from entering the hollow portion. An annular projection 2 is provided on the inner wall surface of the casing 5 at a distance of 10 to 40 mm from the tip for narrowing the hollow fiber membrane bundle, and the heat of the casing 5 is provided outside the casing 5. A shape holding tube 12 for controlling the deformation is attached (b). On the other hand, an appropriate amount of a polyolefin resin (PP, PE, EVA, etc.) fine powder as a sealing agent is put in a container 4, a dispersion liquid (ethanol) is added and stirred to prepare a high-concentration suspension 8 (c ). Next, the hollow fiber membrane bundle at the protruding portion of the bundle of hollow fiber membranes 1 is expanded and immersed in the high-concentration suspension 8 (d), and the high-concentration suspension is sufficiently applied around the hollow fibers, and then the suspension is suspended. The hollow fiber membrane bundle 1 is taken out from the suspension, and the whole hollow fiber membrane bundle 1 is pulled up by a string which binds the hollow fiber membrane bundle 1 (e) and drawn into the polyolefin casing 5 to form a unit (f). Subsequently, this unit is heated at a temperature lower than that of the polyolefin resin to evaporate the ethanol of the dispersion medium. Next, after drying this, the end portion is heated by the heater block 13 to a temperature above the melting point of the sealant,
Melt the sealant (g). Immediately thereafter (1-2 m
(within in) Set in the centrifuge 10, cool and solidify while applying a centrifugal force of 100 to 150 G (h), take out from the centrifuge 10, remove the shape-retaining tube 12, and remove the tip of the welding surface. 5 to 10 mm was cut, and the open end of the hollow fiber membrane was exposed on the cut surface to obtain an all-hollow polyolefin hollow fiber membrane module having a fixed end 3 on one side (i). A polyolefin cover body (cap) was welded to the end of the module and used (j).
【0014】実施例2 図2は本発明の製造方法の実施態様を説明した説明図で
ある。予め両端が目止めされ、中央部が紐で結束してあ
る中空糸膜束1(a)をその中央部で2つ折りにして、
2つ折りにした側からケ−シング5内に挿入する
(b)。なお、ケ−シング5の内壁面には先端から10
〜40mmのところに中空糸膜束を絞るため環状突起2
が設けてあり、また、ケ−シング5の外側にはケ−シン
グ5の熱変形を制御する為の形状保持チュ−ブ12が取
付けられている。目止めした中空糸膜束1の先端をケ−
シング5から約30〜50mm出し、この状態で紐を治
具9に固定する(c)。その際、中空糸膜同志の間に、
樹脂が入り込みやすい様に扇状に拡張させた。ヒ−タ−
ブロック13内にペレット状あるいは粉体の樹脂を徐々
に投入して溶融させ、溶融樹脂7浴中に浸漬した
(d)。使用した樹脂としてはポリオレフィンであっ
た。投入量は、ケ−シング端部から5〜10mm程度あ
け、ケ−シング端部に溶融樹脂が付着しない程度までと
した。中空糸膜間に溶融樹脂が付着して満たされた後、
治具9を上昇させて中空糸膜束1をケ−シング5内に引
き上げてケ−シング内に中空糸膜束を組込み、その端部
を樹脂内に埋設した。その後、直ちに(1〜2min以
内)遠心機10にセットし(e)、100〜150Gの
遠心力を与えつつ冷却、固化させてから、遠心機10か
ら取り出した後、形状保持チュ−ブ12を外して溶着面
の先端から5〜10mmを切断し、中空糸膜開放端を切
断面上に出すして一方側に固定短端部3を有するオ−ル
ポリオレフィン製中空糸膜モジュ−ルを得た(f)。該
モジュ−ルの端部及びケ−シングのもう一方の端部にポ
リオレフィン製カバ−体(キャップ)11を溶着接合
し、使用に供される(g)。Embodiment 2 FIG. 2 is an explanatory view explaining an embodiment of the manufacturing method of the present invention. The hollow fiber membrane bundle 1 (a) whose both ends are pre-sealed and the central portion is bound with a string is folded in two at the central portion,
Insert into the casing 5 from the folded side (b). In addition, on the inner wall surface of the casing 5, 10
Annular protrusion 2 to squeeze the bundle of hollow fiber membranes at ~ 40 mm
A shape holding tube 12 for controlling thermal deformation of the casing 5 is attached to the outside of the casing 5. The end of the hollow fiber membrane bundle 1 that has been stopped
About 30 to 50 mm is projected from the sing 5, and the string is fixed to the jig 9 in this state (c). At that time, between the hollow fiber membrane comrades,
The fan shape was expanded so that the resin could easily enter. Heater
Pellet or powder resin was gradually charged into the block 13 to be melted and immersed in a bath of molten resin 7 (d). The resin used was polyolefin. The charging amount was set to a distance of about 5 to 10 mm from the end of the casing so that the molten resin did not adhere to the end of the casing. After the molten resin is adhered and filled between the hollow fiber membranes,
The jig 9 was raised to pull up the hollow fiber membrane bundle 1 into the casing 5 to incorporate the hollow fiber membrane bundle into the casing, and the end portion thereof was embedded in the resin. Then, immediately (within 1 to 2 minutes), the centrifugal force is set in the centrifuge 10 (e), cooled and solidified while applying a centrifugal force of 100 to 150 G, and then taken out from the centrifuge 10 and then the shape-retaining tube 12 is removed. 5 to 10 mm from the tip of the welded surface is removed and the open end of the hollow fiber membrane is exposed on the cut surface to obtain an all-hollow polyolefin hollow fiber membrane module having a fixed short end portion 3 on one side. (F). A polyolefin-made cover body (cap) 11 is welded and joined to the end of the module and the other end of the casing, and is used (g).
【0015】本発明の製造方法によって得られた中空糸
膜型分離モジュ−ルとしてはケ−シング内に組み込まれ
た中空糸膜の一端がケ−シングと固定化され、その他端
はU字状に折り返されたもの、或いは、中空糸膜の両端
部がケ−シングに固定化されたものの何れでもよい。こ
れを図を以って表わすと、中空糸膜の一端がケ−シング
と固定化され、他端がU字状を呈しているものを図3
に、また、中空糸膜の両端部がケ−シングに固定化され
ているものを図4に示す。図3の場合は、ケ−シング内
に組み込まれた中空糸膜束1の一端がケ−シング5と固
定化され、その他端はU字状に折り返されたものであ
り、図4は中空糸膜束1の両端部がケ−シング5に固定
化されたものである。この中空糸膜束1の両端部を固定
する場合、端部の溶着は片方づつ行うがこれを実現する
には、ケ−シングを上下に分割し、上下ケ−シングがス
ライドできる構造にしておき他方を溶着するときは、溶
着されない方のケ−シングをスライドさせ中空糸膜の束
を突出させ前記したようにして溶着する。As the hollow fiber membrane type separation module obtained by the production method of the present invention, one end of the hollow fiber membrane incorporated in the casing is fixed to the casing and the other end is U-shaped. The hollow fiber membrane may be folded back, or both ends of the hollow fiber membrane may be fixed to the casing. This is illustrated in FIG. 3, in which one end of the hollow fiber membrane is fixed to the casing and the other end is U-shaped.
In addition, FIG. 4 shows that both ends of the hollow fiber membrane are fixed to the casing. In the case of FIG. 3, one end of the hollow fiber membrane bundle 1 incorporated in the casing is fixed to the casing 5, and the other end is folded back in a U shape, and FIG. 4 is a hollow fiber. Both ends of the membrane bundle 1 are fixed to the casing 5. When fixing both ends of the hollow fiber membrane bundle 1, the ends are welded one by one, but in order to realize this, the casing is divided into upper and lower parts, and the upper and lower casings can be slid. When the other is welded, the casing which is not welded is slid to protrude the bundle of hollow fiber membranes and welded as described above.
【0016】このようにして本願発明の方法で得られた
溶融樹脂接合部3は、中空糸膜同志の間隙、及び中空糸
膜束1とケ−シング5との隙間は溶融樹脂中に埋設され
た後、遠心冷却によって固化されたもので中空糸膜同志
及び中空糸膜束1とケ−シング5とは確実に固着一体化
している。そして、ケ−シング5は環状突起2を有し、
図3では一方の端部が、図4では両端部がそれぞれキャ
ップ体11によって封鎖されている。従って、処理され
る流体は一方の流体流入孔15より流入し、他方の流体
流出孔16より流出する。図3及び図4の14は空気抜
きポ−トで、図4の場合は14は空気抜きポ−トを兼ね
た濾過液出口である。In the molten resin joint portion 3 thus obtained by the method of the present invention, the gap between the hollow fiber membranes and the gap between the hollow fiber membrane bundle 1 and the casing 5 are embedded in the molten resin. After that, the hollow fiber membranes are solidified by centrifugal cooling, and the hollow fiber membrane bundle 1 and the hollow fiber membrane bundle 1 and the casing 5 are securely fixed and integrated. The casing 5 has the annular protrusion 2,
One end in FIG. 3 and both ends in FIG. 4 are closed by the cap body 11. Therefore, the fluid to be treated flows in through one fluid inflow hole 15 and flows out through the other fluid outflow hole 16. Reference numeral 14 in FIGS. 3 and 4 is an air vent port, and in the case of FIG. 4, 14 is a filtrate outlet which also serves as an air vent port.
【0017】[0017]
【発明の効果】以上述べたように、本発明の中空糸膜型
分離モジュ−ルは、溶融熱可塑性樹脂により、複数本の
中空糸状多孔質膜とケ−シングとを一体的に接合された
もののため、低溶出性で、耐薬品性、耐熱性、シ−ル性
に優れている。また中空糸状多孔質膜の端部固定が熱溶
着法のため、従来の接着剤法における接着剤溶出成分の
問題はなく、製造に当たっては、遠心冷却固化法を用い
たため、製造が極めて容易となり、ボイド、鬆がなくな
るため品質の安定したものを安価に提供出来る。As described above, in the hollow fiber membrane type separation module of the present invention, a plurality of hollow fiber-like porous membranes and a casing are integrally joined by a molten thermoplastic resin. Therefore, it has a low elution property and is excellent in chemical resistance, heat resistance and sealability. Further, since the end fixing of the hollow fiber-shaped porous membrane is a heat welding method, there is no problem of the adhesive agent elution component in the conventional adhesive method, and in the production, since the centrifugal cooling solidification method is used, the production becomes extremely easy, Since voids and voids are eliminated, stable quality products can be provided at low cost.
【図1】本発明にかかる実施例1の中空糸膜型分離モジ
ュ−ル製造方法の説明図FIG. 1 is an explanatory view of a method for producing a hollow fiber membrane type separation module of Example 1 according to the present invention.
【図2】本発明にかかる実施例2の中空糸膜型分離モジ
ュ−ル製造方法の説明図FIG. 2 is an explanatory view of a method for producing a hollow fiber membrane type separation module of Example 2 according to the present invention.
【図3】本発明にかかる中空糸膜型分離モジュ−ルの一
例の部分断面側面図FIG. 3 is a partial sectional side view of an example of a hollow fiber membrane type separation module according to the present invention.
【図4】本発明にかかる中空糸膜型分離モジュ−ルの他
の例の部分断面側面図FIG. 4 is a partial cross-sectional side view of another example of the hollow fiber membrane type separation module according to the present invention.
1 中空糸膜(束) 2 環状突起 3
溶融樹脂接合部 4 容器 5 ケ−シング 6
入口パイプ 7 溶融樹脂 8 懸濁液 9
紐固定治具 10 遠心機 11 カバ− 1
2 形状保持チュ−ブ 13 ヒ−タ−ブロック 14 空気抜きポ−ト 1
5 液体流入孔 16 液体流出孔 24 濾過液出口1 Hollow Fiber Membrane (Bundle) 2 Annular Protrusion 3
Molten resin joint 4 Container 5 Casing 6
Inlet pipe 7 Molten resin 8 Suspension 9
String fixing jig 10 Centrifuge 11 Cover 1
2 Shape-retaining tube 13 Heater block 14 Air vent port 1
5 Liquid inflow hole 16 Liquid outflow hole 24 Filtrate outlet
Claims (2)
束ねられ、チュ−ブ状ケ−シング内に高密度に組み込ま
れた中空糸膜型分離モジュ−ルの製造方法において、高
分子材料からなり、端部が目止めされた複数本の中空糸
膜の端部を熱可塑性樹脂粉末で覆った後、束ねてチュ−
ブ状ケ−シング内に挿入して中空糸膜束とケ−シングの
間隙及び中空糸膜同志の間隙を前記樹脂粉末で満たした
後、加熱して樹脂粉末を熱溶融させて中空糸膜端部を溶
融樹脂に埋設した後、遠心加速度を与えつつ冷却固化し
て中空糸膜型分離モジュ−ル端部を液密的に一体に接合
することを特徴とする中空糸膜型分離モジュ−ルの製造
方法。1. A method for producing a hollow fiber membrane-type separation module in which a plurality of hollow fiber membranes made of a polymeric material are bundled and incorporated in a tube-shaped casing at a high density. After covering the ends of a plurality of hollow fiber membranes made of a material and having their ends sealed with a thermoplastic resin powder, they are bundled together and
After being inserted into the hollow casing, the space between the hollow fiber membrane bundle and the casing and the space between the hollow fiber membranes are filled with the resin powder, the resin powder is heated to heat-melt the resin powder to end the hollow fiber membrane. The hollow fiber membrane type separation module is characterized in that after the portion is embedded in a molten resin, the hollow fiber membrane type separation module is joined in a liquid-tight manner by cooling and solidifying while applying centrifugal acceleration. Manufacturing method.
束ねられ、チュ−ブ状ケ−シング内に高密度に組み込ま
れた中空糸膜型分離モジュ−ルの製造方法において、高
分子材料からなり、端部が目止めされた複数本の中空糸
膜の端部を溶融された樹脂で覆った後、束ねてチュ−ブ
状ケ−シング内に挿入して中空糸膜束とケ−シングの間
隙及び中空糸膜同志の間隙を前記熱溶融した樹脂で満た
して中空糸膜端部を溶融樹脂に埋設した後、遠心加速度
を与えつつ冷却固化して中空糸膜型分離モジュ−ル端部
を液密的に一体に接合することを特徴とする中空糸膜型
分離モジュ−ルの製造方法。2. A method for producing a hollow fiber membrane-type separation module in which a plurality of hollow fiber membranes made of a polymer material are bundled and incorporated in a tube-shaped casing at a high density. After covering the ends of a plurality of hollow fiber membranes made of a material and having their ends sealed with molten resin, they are bundled and inserted into a tube-shaped casing to form a hollow fiber membrane bundle and a casing. -The hollow fiber membrane type separation module is filled with the molten resin by filling the space between the singing and the hollow fiber membranes with each other and burying the end portion of the hollow fiber membrane in the molten resin, and then cooling and solidifying while applying centrifugal acceleration. A method for producing a hollow fiber membrane type separation module, characterized in that the end portions are liquid-tightly joined together.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7382895A JPH08266872A (en) | 1995-03-30 | 1995-03-30 | Production of hollow fiber membrane type separation module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7382895A JPH08266872A (en) | 1995-03-30 | 1995-03-30 | Production of hollow fiber membrane type separation module |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08266872A true JPH08266872A (en) | 1996-10-15 |
Family
ID=13529405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7382895A Pending JPH08266872A (en) | 1995-03-30 | 1995-03-30 | Production of hollow fiber membrane type separation module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08266872A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006289156A (en) * | 2005-04-05 | 2006-10-26 | Mitsubishi Rayon Co Ltd | Method for producing hollow fiber membrane module |
| CN104474900A (en) * | 2014-11-10 | 2015-04-01 | 济南市水处理设备厂有限公司 | Hollow fiber ultrafiltration membrane module casting device, and casting method thereof |
-
1995
- 1995-03-30 JP JP7382895A patent/JPH08266872A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006289156A (en) * | 2005-04-05 | 2006-10-26 | Mitsubishi Rayon Co Ltd | Method for producing hollow fiber membrane module |
| CN104474900A (en) * | 2014-11-10 | 2015-04-01 | 济南市水处理设备厂有限公司 | Hollow fiber ultrafiltration membrane module casting device, and casting method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0768136A (en) | Hollow-fiber membrane type separation module and manufacture thereof | |
| JP2618820B2 (en) | Hollow fiber filter cartridge and manufacturing method | |
| JP4514959B2 (en) | Method for producing hollow fiber membrane | |
| US4767426A (en) | Membrane filter tube and method of preparation | |
| JPS61502102A (en) | Filter improvements | |
| EP1146944B1 (en) | Perfluorinated thermoplastic filter cartridge | |
| EP0942251B1 (en) | A thermoplastic, unibody transfer device | |
| JP2004016905A (en) | Separation membrane module having hollow fiber and method for producing the same | |
| JPH08266872A (en) | Production of hollow fiber membrane type separation module | |
| JPH08266871A (en) | Production of hollow fiber membrane type separation module | |
| EP3319713A1 (en) | Blended potting resins and use thereof | |
| JPS6168110A (en) | Filter element and its production | |
| JP2022501191A (en) | How to make a filtration and / or diffuser | |
| JP3196152B2 (en) | Hollow fiber membrane bundle unit, hollow fiber membrane type separation module, and method for producing them | |
| CN102639216A (en) | Method for making a hollow fiber filtration device enclosed by two thermoplastic parts | |
| KR960006213B1 (en) | Process for producing a filter element | |
| JPS5987115A (en) | Method of densely burying one or several membrane into thermoplastic material | |
| JPS5831205B2 (en) | Ekitaioyobi Kitairokasouchi | |
| JP2939644B2 (en) | Hollow fiber type membrane separation unit | |
| JPH03220B2 (en) | ||
| JPS61149220A (en) | filter element | |
| JPH0910560A (en) | Manufacture of mold-separable module of hollow fiber membranes | |
| JPH11197462A (en) | Hollow fiber membrane type separation element | |
| JP3174267B2 (en) | Method for manufacturing hollow fiber membrane separation unit | |
| JPH1099657A (en) | Hollow yarn type separation membrane module |