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JPS6365361B2 - - Google Patents
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JPS6365361B2 - - Google Patents

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Publication number
JPS6365361B2
JPS6365361B2 JP60006677A JP667785A JPS6365361B2 JP S6365361 B2 JPS6365361 B2 JP S6365361B2 JP 60006677 A JP60006677 A JP 60006677A JP 667785 A JP667785 A JP 667785A JP S6365361 B2 JPS6365361 B2 JP S6365361B2
Authority
JP
Japan
Prior art keywords
container
hollow fiber
resin
rod
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
JP60006677A
Other languages
Japanese (ja)
Other versions
JPS61167407A (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 JP667785A priority Critical patent/JPS61167407A/en
Publication of JPS61167407A publication Critical patent/JPS61167407A/en
Publication of JPS6365361B2 publication Critical patent/JPS6365361B2/ja
Granted legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 中空糸濾過膜(以下中空糸という)は、膜充填
密度が高く、過装置の小型軽量化を図ることが
できるため純水製造、食品加工その他の分野で分
野で多く用いられている。
[Detailed description of the invention] Hollow fiber filtration membranes (hereinafter referred to as hollow fibers) have a high membrane packing density and can make filtration equipment smaller and lighter, so they are widely used in pure water production, food processing, and other fields. It is used.

通常過原液は中空糸の内部へ圧入され過液
は外側へ取り出すことが多いが、極く清澄な原液
から微量の微粒子を除去する際には中空糸の外側
から原液を圧入し中空糸の内側へ過液を取り出
すいわゆる外圧方式の方が効率的な過が行え有
利である。
Normally, the undiluted liquid is forced into the inside of the hollow fiber, and the filtrated liquid is often taken out to the outside, but when removing trace amounts of fine particles from an extremely clear undiluted solution, the undiluted liquid is forced into the hollow fiber from the outside and inside the hollow fiber. The so-called external pressure method in which the filtrate is taken out is more advantageous because it can perform filtration more efficiently.

通常この様な方式により過を行う場合には、
複数本の中空糸を束ね、その両端を樹脂などで結
着封止した後、少なくともその一端を切断し中空
糸の端部を開口せしめたモジユールを、円筒状の
容器に中空糸の内部と外部が液密になる様に取り
付け、該容器の側面から過液を中空糸の外部へ
圧入し中空糸の内部に滲出する過液を中空糸の
開口端より取り出して過を行うものである。
Normally, when carrying out the procedure using this method,
After bundling multiple hollow fibers and binding and sealing both ends with resin etc., cut off at least one end of the hollow fibers and leave the ends of the hollow fibers open.The module is placed in a cylindrical container and the inside and outside of the hollow fibers are sealed. The filtrate is attached so as to be liquid-tight, and the filtrate is forced into the outside of the hollow fiber from the side of the container, and the filtrate seeped into the inside of the hollow fiber is taken out from the open end of the hollow fiber for filtration.

かかる方法では過原液はその圧力により中空
糸束を締めつけることとなり、その結果中空糸は
束の中側では隣接中空糸と密着して過原液と接
触できないため、束の外側の中空糸のみが過に
寄与することとなり、効率が低下するのが欠点で
あつた。
In such a method, the excessive stock solution tightens the hollow fiber bundle due to its pressure, and as a result, the hollow fibers in the inside of the bundle are in close contact with adjacent hollow fibers and cannot contact the superstock solution, so that only the hollow fibers on the outside of the bundle are The drawback was that the efficiency decreased.

この様な欠点を改良するため第1図に示す様な
過器が考えられた。
In order to improve these drawbacks, an overheater as shown in FIG. 1 was devised.

第1図は本発明の過器の断面を模式的にあら
わしたものである。中空糸束2の一端は樹脂3に
よつて封止結着されているが、該樹脂には中空糸
束2の中側に開口する貫通孔5が所定個数設けら
れている。中空糸の他端は開口した状態で樹脂6
によつて結着されこの様に構成されたモジユール
はハウジング4に中空糸の内部と外部が液密にな
る様に取り付けられる。ハウジング4には原液圧
入口1、過液流出口7および空気排出弁8が取
り付けられる。
FIG. 1 schematically shows a cross section of the overpass device of the present invention. One end of the hollow fiber bundle 2 is sealed and bound by a resin 3, and the resin is provided with a predetermined number of through holes 5 that open to the inside of the hollow fiber bundle 2. The other end of the hollow fiber is left open with resin 6.
The module thus constructed is attached to the housing 4 so that the inside and outside of the hollow fibers are liquid-tight. A raw liquid pressure inlet 1 , an excess liquid outlet 7 and an air exhaust valve 8 are attached to the housing 4 .

この様に構成された過器で過を行う際には
原液は流入口1より貫通孔5を経て中空糸束2の
中側へ供給される。従つて中空糸束2は外側から
締めつけられることなく、むしろ中側より拡げら
れる形で過が行なわれるため隣接する中空糸は
互に密着することなく過原液と接触するため束
を構成する中空糸は無駄なくすべて過に寄与す
ることとなり過の効率を飛躍的に向上させるこ
とが出来る。中空糸の内部へ滲出した過液は
液流出口7より取り出される。
When carrying out filtration with the filtration device constructed in this way, the stock solution is supplied from the inlet 1 to the inside of the hollow fiber bundle 2 through the through hole 5. Therefore, the hollow fiber bundle 2 is not tightened from the outside, but rather is spread out from the inside, so that adjacent hollow fibers do not come into close contact with each other and come into contact with the stock solution, so that the hollow fibers forming the bundle are Since all of the components contribute to the surplus without any wastage, the efficiency of the surplus can be dramatically improved. The filtrate that has seeped into the hollow fiber is taken out from the liquid outlet 7.

貫通孔5は必要により空気などを導入して容器
4の内部に気泡を生ぜしめ中空糸を振動する際に
も有用である。
The through holes 5 are also useful when introducing air or the like to create bubbles inside the container 4 and vibrating the hollow fibers, if necessary.

かかる構造の過器において貫通孔5の配置を
中空糸束2の中側に規則的に所定の位置に設ける
ことが肝要であるが従来では極めて困難な作業で
あり多くの時間と労力を要するものであつた。
In a device having such a structure, it is important to arrange the through holes 5 at regular predetermined positions inside the hollow fiber bundle 2, but this is an extremely difficult task and requires a lot of time and effort. It was hot.

本発明者等は鋭意検討の結果、かかるモジユー
ルの製造を容易にする本発明を完成するに到つた
ものである。
As a result of intensive studies, the present inventors have completed the present invention, which facilitates the manufacture of such modules.

本発明は周壁部と底面板よりなる容器の底面板
の所定位置に所定個数の細孔を設け、該細孔と同
一断面形状を有し、非接着性表面を有する棒材又
は管材を細孔に差し込み所定本数の中空糸よりな
る中空糸束の一端を該容器の開口部より容器中に
挿入し架橋性樹脂を該棒材又は管材を覆わぬ様に
上端より下の位置まで容器に充填し該樹脂を架橋
硬化し中空糸を結着封止した後、容器の底面側よ
り該棒材又は管材を抜去して貫通孔を設け、次い
で、硬化した架橋性樹脂成形物を容器の底面板と
共に周壁部から抜き出し、一方、前記中空糸束の
他端側は架橋性樹脂で結着した後、端部を切断し
て中空糸を開口状態とすることを特徴とする中空
糸過膜モジユールの製造方法である。
The present invention provides a predetermined number of pores at predetermined positions in a bottom plate of a container consisting of a peripheral wall and a bottom plate, and a rod or tube having the same cross-sectional shape as the pores and a non-adhesive surface. Insert one end of the hollow fiber bundle consisting of a predetermined number of hollow fibers into the container from the opening of the container, and fill the container with crosslinkable resin to a position below the top end without covering the rod or tube material. After cross-linking and curing the resin and binding and sealing the hollow fibers, the rod or tube is removed from the bottom side of the container to form a through hole, and then the cured cross-linkable resin molding is placed together with the bottom plate of the container. Manufacture of a hollow fiber membrane module characterized in that the hollow fibers are pulled out from the peripheral wall, the other end of the hollow fiber bundle is bound with a crosslinking resin, and then the end is cut to leave the hollow fibers in an open state. It's a method.

以下実施例により本発明を詳細に説明する。 The present invention will be explained in detail below with reference to Examples.

中空糸として内径1.0mm、外径1.6mm、長さ1300
mm、初期透水率1200l/m2・hr・atmのポリスル
ホン中空糸800本を用いた。
As hollow fiber, inner diameter 1.0mm, outer diameter 1.6mm, length 1300
800 polysulfone hollow fibers with an initial water permeability of 1200 l/m 2 hr atm were used.

容器として第2図に示すアクリル樹脂製内径74
mm、外径78mm、高さ30mmの円筒状容器の周壁部9
の底面板12に直径3mmの細孔10を放射状に9
個設けテフロン(4ふつ化エチレン樹脂、デユポ
ン社の商品名)製の直径3mmの棒材11を該細孔
に差し込んだ。容器としては円筒状に限らず必要
により箱状、その他形状とすることができる。又
第1図に示すハウジング4の一端に底面をとりつ
けて容器として用いても良い。又棒材は管材でも
よく素材はテフロンに限らず非接着性表面を有す
るポリオレフイン類又は離型処理を施したその他
の素材を用いることができる。
The container is made of acrylic resin with an inner diameter of 74 as shown in Figure 2.
Peripheral wall part 9 of a cylindrical container with an outer diameter of 78 mm and a height of 30 mm.
Pores 10 with a diameter of 3 mm are radially arranged 9 in the bottom plate 12 of the
An individual rod 11 made of Teflon (tetrafluoroethylene resin, trade name of DuPont) and having a diameter of 3 mm was inserted into the pore. The container is not limited to a cylindrical shape, but can be box-shaped or other shapes as necessary. Alternatively, the bottom surface may be attached to one end of the housing 4 shown in FIG. 1 and used as a container. Further, the rod material may be a tube material, and the material is not limited to Teflon, but polyolefins having a non-adhesive surface or other materials subjected to mold release treatment can be used.

中空糸束は一端を切り揃えた後第3図に示す様
に容器中に均一に挿入した。既に棒材11により
貫通孔5の位置が規定されているため中空糸束2
を均一に挿入することは極めて容易であつた。挿
入後容器開口部よりエポキシ樹脂を容器内に充填
し、架橋硬化せしめ中空糸束を結着封止した後、
容器の底面側(図面下方)より棒材11を除去し
て貫通孔5を形成せしめた。この際孔が樹脂層を
貫通するためにエポキシ樹脂を容器に充填する際
棒材11の上端より下の位置までとし樹脂が棒材
11を覆わぬことが肝要である。
After trimming one end of the hollow fiber bundle, it was inserted uniformly into a container as shown in FIG. Since the position of the through hole 5 is already defined by the rod 11, the hollow fiber bundle 2
It was extremely easy to insert the tube evenly. After insertion, epoxy resin is filled into the container from the opening of the container, cross-linked and cured, and the hollow fiber bundle is bound and sealed.
The rod 11 was removed from the bottom side of the container (lower side in the drawing) to form a through hole 5. At this time, since the holes penetrate through the resin layer, when filling the container with epoxy resin, it is important that the resin does not cover the rod 11 to a position below the upper end of the rod 11.

中空糸束の他端は所定の長さに切り揃えた後通
常の方法により中空糸が開口した状態でエポキシ
樹脂により径78mm、高さ約30mmの円筒状に成形し
た中空糸を結着し、モジユール全長を1060mmとし
た。
The other end of the hollow fiber bundle was trimmed to a predetermined length, and with the hollow fibers open, the hollow fibers were shaped into a cylinder with a diameter of 78 mm and a height of approximately 30 mm using epoxy resin, and then bound together using an epoxy resin. The total length of the module is 1060mm.

この様にして製造されたモジユールは内径80
mm、外径88mmの塩化ビニル製ハウジングの内部に
装着し両端部をエポキシ樹脂によりハウジングに
液密になる様に接着した。
The module manufactured in this way has an inner diameter of 80
It was mounted inside a vinyl chloride housing with an outer diameter of 88 mm, and both ends were glued to the housing with epoxy resin to make it liquid-tight.

この様に構成したハウジングの両端に原液圧入
口、濾過液流出口および空気排出弁をとりつけ、
第1図と類似の構成より成る過器を製造した。
A raw liquid pressure inlet, a filtrate outlet, and an air discharge valve are attached to both ends of the housing configured in this way.
A superconductor having a configuration similar to that shown in FIG. 1 was manufactured.

かかる過器は貫通孔が所定の配置となつてお
り中空糸が均一に分布していることが認められ
た。以上のように、本発明の方法によれば極く簡
単な型を用いて、濾過原液の入口となる貫通孔と
中空糸が均一に分布した中空糸膜モジユール容易
に得ることができ、また、樹脂成形後の棒材又は
管材の抜去や脱型の際に、中空糸に不要な引り力
が加わることがなく、中空糸膜モジユールの製造
方法として有用である。
It was observed that such a filter had through holes in a predetermined arrangement and hollow fibers were uniformly distributed. As described above, according to the method of the present invention, it is possible to easily obtain a hollow fiber membrane module in which through-holes and hollow fibers, which serve as inlets for filtration stock solution, are evenly distributed, using an extremely simple mold, and This method is useful as a method for producing hollow fiber membrane modules because no unnecessary pulling force is applied to the hollow fibers when the rod or tube material is removed or demolded after resin molding.

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

第1図は本発明による過器の断面を模式的に
示した図である。 図中1…過原液流入口、2…中空糸束、3…
中空糸結着封止する架橋性樹脂、4…ハウジン
グ、5…貫通孔、6…中空糸開口端部結着封止す
る架橋性樹脂、7…過原液流出口、8…空気排
出弁、 第2図は本実施例において用いたアクリル樹脂
容器を模式的に示した図面であり、Aは側断面
図、Bは底面を示す。 図中9…周壁部、10…細孔、11…細孔10
に差し込んだテフロン製丸棒、12…底面板、 第3図はアクリル樹脂容器の細孔に丸棒を差し
込み中空糸の一端を均一に容器内に挿入し、架橋
性樹脂を容器内に充填した状態および架橋硬化後
丸棒を除去して貫通孔を形成する状態を模式的に
示した図である。
FIG. 1 is a diagram schematically showing a cross section of a superconductor according to the present invention. In the figure, 1...excess stock solution inlet, 2...hollow fiber bundle, 3...
Crosslinkable resin for binding and sealing the hollow fiber, 4...Housing, 5...Through hole, 6...Crosslinking resin for binding and sealing the opening end of the hollow fiber, 7...Excess stock solution outlet, 8...Air discharge valve, Figure 2 is a drawing schematically showing the acrylic resin container used in this example, where A is a side sectional view and B is a bottom view. In the figure, 9...peripheral wall part, 10...pore, 11...pore 10
A Teflon round rod inserted into the 12 bottom plate. Figure 3 shows a round rod inserted into the pore of an acrylic resin container, one end of the hollow fiber inserted uniformly into the container, and the crosslinkable resin filled into the container. FIG. 3 is a diagram schematically showing the state and the state in which the round rod is removed after crosslinking and curing to form a through hole.

Claims (1)

【特許請求の範囲】[Claims] 1 周壁部と底面板よりなる容器の底面板に細孔
を設け、該細孔と同一断面形状を有し非接着性表
面を有するプラスチツク製の棒材又は管材を該細
孔に差し込み、中空糸束の一端側を該容器の開口
部より容器中に挿入し、架橋性樹脂を該棒材又は
管材の上端より下の位置まで容器に充填し、該樹
脂を架橋硬化し中空糸を結着封止した後、容器の
底面側より該棒材又は管材を抜去して貫通孔を設
け、次いで、硬化した架橋性樹脂成形物を容器の
底面板と共に周壁部から抜き出し、一方、前記中
空糸束の他端側は架橋性樹脂で結着した後、端部
を切断して中空糸を開口状態とすること特徴とす
る中空糸過膜モジユールの製造方法。
1. A pore is provided in the bottom plate of a container consisting of a peripheral wall and a bottom plate, and a plastic rod or tube having the same cross-sectional shape as the pore and a non-adhesive surface is inserted into the pore to form a hollow fiber. One end of the bundle is inserted into the container through the opening of the container, and the container is filled with crosslinkable resin to a position below the upper end of the rod or tube material, and the resin is crosslinked and cured to bind and seal the hollow fibers. After stopping, the rod or tube is removed from the bottom side of the container to form a through hole, and then the cured crosslinkable resin molded product is removed from the peripheral wall along with the bottom plate of the container, while the hollow fiber bundle is removed from the bottom of the container. A method for manufacturing a hollow fiber membrane module, characterized in that the other end is bound with a crosslinkable resin and then the end is cut to leave the hollow fiber in an open state.
JP667785A 1985-01-19 1985-01-19 Preparation of hollow yarn filtration membrane module Granted JPS61167407A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP667785A JPS61167407A (en) 1985-01-19 1985-01-19 Preparation of hollow yarn filtration membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP667785A JPS61167407A (en) 1985-01-19 1985-01-19 Preparation of hollow yarn filtration membrane module

Publications (2)

Publication Number Publication Date
JPS61167407A JPS61167407A (en) 1986-07-29
JPS6365361B2 true JPS6365361B2 (en) 1988-12-15

Family

ID=11644991

Family Applications (1)

Application Number Title Priority Date Filing Date
JP667785A Granted JPS61167407A (en) 1985-01-19 1985-01-19 Preparation of hollow yarn filtration membrane module

Country Status (1)

Country Link
JP (1) JPS61167407A (en)

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EP2900356A1 (en) 2012-09-27 2015-08-05 Evoqua Water Technologies LLC Gas scouring apparatus for immersed membranes
EP3052221B1 (en) 2013-10-02 2022-12-14 Rohm & Haas Electronic Materials Singapore Pte. Ltd Device for repairing a membrane filtration module
WO2017011068A1 (en) 2015-07-14 2017-01-19 Evoqua Water Technologies Llc Aeration device for filtration system

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JPS6010643Y2 (en) * 1978-05-30 1985-04-11 荏原インフイルコ株式会社 Permeable membrane module

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