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JPH0798135B2 - Hollow fiber type membrane module and manufacturing method thereof - Google Patents
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JPH0798135B2 - Hollow fiber type membrane module and manufacturing method thereof - Google Patents

Hollow fiber type membrane module and manufacturing method thereof

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Publication number
JPH0798135B2
JPH0798135B2 JP62329236A JP32923687A JPH0798135B2 JP H0798135 B2 JPH0798135 B2 JP H0798135B2 JP 62329236 A JP62329236 A JP 62329236A JP 32923687 A JP32923687 A JP 32923687A JP H0798135 B2 JPH0798135 B2 JP H0798135B2
Authority
JP
Japan
Prior art keywords
hollow fiber
membrane module
type membrane
fiber type
adhesive
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 - Lifetime
Application number
JP62329236A
Other languages
Japanese (ja)
Other versions
JPH01171608A (en
Inventor
和久 熊見
勝昭 福永
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.)
Daicel Corp
Original Assignee
Daicel Chemical Industries 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 Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP62329236A priority Critical patent/JPH0798135B2/en
Publication of JPH01171608A publication Critical patent/JPH01171608A/en
Publication of JPH0798135B2 publication Critical patent/JPH0798135B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、不純物の溶出が少ない中空糸型膜モジュール
及びその製造方法に関し、さらに詳細には接着封止部内
の中空糸膜に不純物を蓄積させない中空糸型膜モジュー
ル及びその製造方法に関する。
Description: TECHNICAL FIELD The present invention relates to a hollow fiber type membrane module in which impurities are hardly eluted and a method for producing the same, and more specifically, impurities are accumulated in a hollow fiber membrane in an adhesive sealing part. TECHNICAL FIELD The present invention relates to a hollow fiber type membrane module and a method for manufacturing the same.

〔従来の技術〕[Conventional technology]

近年、膜技術の進展には著しいものがあり、逆浸透型、
精密濾過型、限外濾過型等の種々の分離特性を有する分
離膜が開発されている。これに伴い膜を収容する膜モジ
ュールも各種の膜に応じて、スパイラル型、中空糸型等
の種々の形態を有するものが製造されている。
In recent years, there have been significant advances in membrane technology, including reverse osmosis,
Separation membranes having various separation characteristics such as microfiltration type and ultrafiltration type have been developed. Along with this, as membrane modules for accommodating membranes, those having various forms such as spiral type and hollow fiber type are manufactured according to various membranes.

このうち、中空糸型膜モジュールは、コンパクトであ
り、プライミング容積が小さい等の利点があるため広範
な分野で用いられている。例えば、電子工業の分野にお
いては、超純水のユースポイントの直前に限外濾過用と
して使用されている。
Among them, the hollow fiber type membrane module is used in a wide range of fields because it is compact and has advantages such as a small priming volume. For example, in the field of electronics industry, it is used for ultrafiltration just before the point of use of ultrapure water.

このような中空糸型膜モジュールは、長さ200〜1000m
m、外径0.05〜2mmφ程度の中空糸を数千本〜数万本束ね
て円筒状のケースに挿入し、その端部を主としてエポキ
シ系接着剤により接着封止して硬化後、端部の切断を行
ない、さらにキャップを接着等して取りつけて製造され
る。
Such a hollow fiber type membrane module has a length of 200 to 1000 m.
Thousands to tens of thousands of hollow fibers with m and outer diameter of 0.05 to 2 mmφ are bundled and inserted into a cylindrical case, and the ends are adhesively sealed mainly with an epoxy adhesive to cure and It is manufactured by cutting and then attaching a cap and the like.

ところでこのようにして得られた膜モジュールが一旦不
純物等に汚染されると、不純物の排出は容易でない。か
かる不純物は被分離液中に含まれるものと、モジュール
内の構成部材等から発生するものがあり、モジュール内
の各部に残留して濾液を汚染させる。
By the way, once the membrane module thus obtained is contaminated with impurities or the like, it is not easy to discharge the impurities. Some of these impurities are contained in the liquid to be separated and some are generated from the constituent members in the module, etc., and remain in each part in the module to contaminate the filtrate.

このため上記の製造工程においては、モジュールからの
不純物の溶出を低減するためのモジュールの部材や封止
剤等が厳選されている。また、モジュールの構造につい
ても不純物の滞留しやすいO−リングなどのシール部分
付近や透過液ノズルと接着封止部間の水の滞留部分等を
改良した構造が採用されている。
Therefore, in the above manufacturing process, the members of the module, the sealant and the like are carefully selected in order to reduce the elution of impurities from the module. In addition, as for the structure of the module, a structure is adopted in which the vicinity of a seal portion such as an O-ring where impurities easily accumulate and the water retention portion between the permeate nozzle and the adhesive sealing portion are improved.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、上記のようなモジュールの構成部材の選
択や構造上の改良がなされても、中空糸型膜モジュール
からの不純物の溶出が問題となる場合がある。本発明者
らが調査したところによると、このような不純物の滞留
部分はモジュールの容器端部に接着封止された中空糸膜
内部であることが判明した。
However, even if the components of the module are selected and the structure is improved as described above, the elution of impurities from the hollow fiber type membrane module may be a problem. According to the investigation conducted by the present inventors, it was found that such a portion where impurities are accumulated is inside the hollow fiber membrane that is adhesively sealed at the end of the container of the module.

そこで、本発明の目的は、上記のような原因による中空
糸型膜モジュールからの不純物溶出が生じない中空糸型
膜モジュールを開発することにある。
Therefore, an object of the present invention is to develop a hollow fiber type membrane module in which impurities are not eluted from the hollow fiber type membrane module due to the above causes.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは上記問題点を解決するために鋭意検討・研
究を重ねた結果、中空糸型膜モジュールを製造する際、
封止剤部分にある中空糸に以下の如き処理を施すことに
よって、かかる部分に不純物が滞留しないようにして溶
出不純物を低減することができる中空糸型膜モジュール
を開発することに成功した。
The present inventors have conducted extensive studies and research to solve the above problems, and as a result, when manufacturing a hollow fiber type membrane module,
We have succeeded in developing a hollow fiber type membrane module that can reduce the eluted impurities by preventing the impurities from accumulating in the hollow fiber in the sealant portion by the following treatment.

即ち、本発明は、中空糸束を収容する円筒状容器の両端
部が中空糸を互いに隔離して接着封止してなる中空糸型
膜モジュールであって、 該接着封止部内の中空糸内表面が非透水性であることを
特徴とする中空糸型膜モジュールを提供するものであ
る。
That is, the present invention provides a hollow fiber type membrane module in which both ends of a cylindrical container for accommodating a hollow fiber bundle separate and seal the hollow fibers from each other. The present invention provides a hollow fiber type membrane module having a surface that is impermeable to water.

さらに本発明は、上記の中空糸型膜モジュールの製造方
法をも提供するものである。
Furthermore, the present invention also provides a method for producing the above hollow fiber membrane module.

本発明において、中空糸の非透水化とは、中空糸膜の表
面の多孔質部に濾液を実質的に進入させないようにする
ことを意味する。かかる非透水化の方法としては、例え
ば、中空糸を溶剤に浸透させる方法、中空糸表面に接着
剤を塗布または浸漬した後余分な接着剤を取り去り硬化
させる方法、中空糸を水に浸漬後乾燥させる方法等が挙
げられるが、特に接着剤を中空糸内表面に塗布する本願
方法では、中空糸の内表面が完全に非透水化するため、
効果が大きい。使用する接着剤は、例えば、エポキシ系
の接着剤、ウレタン系の接着剤が挙げられ、特にこれら
に限定されずどのようなものでもよい。
In the present invention, making the hollow fiber water impermeable means that the filtrate is not substantially allowed to enter the porous portion on the surface of the hollow fiber membrane. Examples of such water-impermeable methods include, for example, a method of infiltrating the hollow fiber with a solvent, a method of applying or dipping an adhesive on the surface of the hollow fiber and then removing excess adhesive to cure the hollow fiber, and dipping the hollow fiber in water and then drying. In particular, in the method of the present invention in which an adhesive is applied to the inner surface of the hollow fiber, the inner surface of the hollow fiber is completely impermeable to water.
Great effect. The adhesive used is, for example, an epoxy adhesive or a urethane adhesive, and is not particularly limited to these and any adhesive may be used.

上記のような非透水化処理は、膜モジュールを作製後に
接着封止されている部分に上記処理を施す。
In the water-impermeable treatment as described above, the above-mentioned treatment is applied to the portion that is adhesively sealed after the membrane module is manufactured.

本発明に使用する中空糸膜の材質としては、例えば、ポ
リスルホン系樹脂、ポリエーテルスルホン系樹脂、ポリ
イミド樹脂、ポリアクリロニトリル樹脂、ポリメチルメ
タクリル樹脂あるいは酢酸セルロース系樹脂等が挙げら
れるが、特に限定されない。
Examples of the material of the hollow fiber membrane used in the present invention include, but are not particularly limited to, polysulfone-based resin, polyether sulfone-based resin, polyimide resin, polyacrylonitrile resin, polymethylmethacryl resin or cellulose acetate-based resin. .

また、膜モジュールの材質、形状についても、特に限定
されずどのようなものでも使用できる。
The material and shape of the membrane module are not particularly limited, and any one can be used.

本発明において上記の非透水化を行う工程以外の膜モジ
ュールの製造方法は、特に限定されず通常の製造方法を
用いることができる。
In the present invention, the method for producing the membrane module other than the step of making the water impermeable is not particularly limited, and a usual production method can be used.

上記のようにして得られた本発明の中空糸型膜モジュー
ルは、接着剤封止部のある中空糸膜内表面の多孔質部分
が非透水性であるため不純物を含む濾液が進入せず、か
かる部分に不純物が滞留することはない。
The hollow fiber type membrane module of the present invention obtained as described above, the porous portion of the inner surface of the hollow fiber membrane having the adhesive sealing portion is impermeable so that the filtrate containing impurities does not enter, Impurities do not accumulate in such portions.

〔実施例〕〔Example〕

以下、本発明を実施例により説明するが、本発明はこれ
らに何等限定されない。
Hereinafter, the present invention will be described with reference to examples, but the present invention is not limited thereto.

中空糸型膜モジュールの製造例 内径89mmφ、厚さ5mm、長さ320mmのポリスルホン製ケー
スに内径500μm、外径800μmのポリエーテルスルホン
製中空糸5000本よりなる糸束を挿入し、これを遠心シー
ル機の中にセットして耐熱性のエポキシ接着剤を注入
し、遠心シールして硬化させた。これをとり出してケー
スの端末部の切断後100℃にて接着剤を十分に硬化させ
た。
Example of manufacturing hollow fiber membrane module A bundle of 5000 hollow fibers made of polyethersulfone with an inner diameter of 500 μm and an outer diameter of 800 μm is inserted into a polysulfone case with an inner diameter of 89 mmφ, a thickness of 5 mm, and a length of 320 mm, which is centrifugally sealed. It was set in the machine and a heat resistant epoxy adhesive was injected and centrifugally sealed to cure. This was taken out, and after cutting the end portion of the case, the adhesive was sufficiently cured at 100 ° C.

実施例1 上記の製造例で得られた中空糸型膜モジュールの一方の
端末部に第1図に示す様にエポキシ接着剤6を少なくと
も接着封止部内の中空糸2内に充填する様に塗布した
後、直ちに他方のケース端末部から加圧空気を送り込ん
で中空糸の中空部に充填されていた余分のエポキシ接着
剤6を排出させた。余分の接着剤をふきとった後接着剤
を90℃に加温して硬化させた。この後同様にしてもう一
方のケース端末部も処理して接着封止部内の中空糸膜を
非透水化させた。
Example 1 As shown in FIG. 1, epoxy adhesive 6 is applied to one end of the hollow fiber type membrane module obtained in the above production example so as to fill at least the hollow fiber 2 in the adhesive sealing portion. Immediately after that, pressurized air was sent from the other end of the case to discharge the excess epoxy adhesive 6 filled in the hollow portion of the hollow fiber. After wiping off the excess adhesive, the adhesive was heated to 90 ° C. and cured. After that, the other case end portion was treated in the same manner to make the hollow fiber membrane in the adhesive sealing portion impermeable to water.

このように処理した膜モジュールについて、不純物の滞
留性を評価するために以下のような試験を行った。
The membrane module treated in this manner was subjected to the following tests in order to evaluate the retention of impurities.

上記の中空糸型膜モジュールに不純物として5%ホルム
アルデヒド水溶液を充填し、室温で1時間放置した。そ
の後純水をモジュール内に25℃で400l/hの流量で通水
(透過水側を360l/h、濃縮水側を40l/h)して、透過水
のホルムアルデヒド濃度をホルムアルデヒドテストワコ
ー(和光純薬)で測定した。通水開始10分後のホルムア
ルデヒド濃度を第1表に示した。
The above hollow fiber type membrane module was filled with a 5% aqueous formaldehyde solution as an impurity and left at room temperature for 1 hour. Then, pure water is passed through the module at 25 ° C at a flow rate of 400 l / h (360 l / h on the permeate side and 40 l / h on the concentrated side) to determine the formaldehyde concentration of the permeate in the formaldehyde test Wako (Wako Pure Drug). The formaldehyde concentration 10 minutes after the start of water flow is shown in Table 1.

比較例1 上記の製造例で得られた膜モジュールにつき非透水化処
理を施さなかった以外は、実施例1と同様にしてホルム
アルデヒドによる滞留性の評価試験を行った。得られた
結果を第1表に示す。
Comparative Example 1 A retention test with formaldehyde was conducted in the same manner as in Example 1 except that the membrane module obtained in the above Production Example was not subjected to the water-impermeable treatment. The results obtained are shown in Table 1.

上記試験の結果からすれば、非透水化の処理がされてい
ない膜では、不純物の溶出量が高く膜モジュールの封止
剤部分内にある中空糸の多孔質内に不純物が滞留してい
るものと考えられる。
From the results of the above test, in the membrane that has not been subjected to the water-impermeable treatment, the amount of impurities eluted is high, and the impurities are retained in the porous hollow fiber in the sealant portion of the membrane module. it is conceivable that.

〔発明の効果〕〔The invention's effect〕

以上説明してきたように、本発明により得られた中空糸
型膜モジュールは、不純物の溶出が極めて少なく、高純
度の製品を得るための分離に好適である。
As described above, the hollow fiber type membrane module obtained by the present invention has very little elution of impurities, and is suitable for separation to obtain a high-purity product.

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

第1図は、実施例1において中空糸に非透水化処理を施
す様子を示した概念図である。 〔主な参照番号〕 1……中空糸型膜モジュール、2……中空糸、4……接
着封止部、6……接着剤
FIG. 1 is a conceptual diagram showing how a hollow fiber is subjected to a water-impermeable treatment in Example 1. [Main reference numbers] 1 ... Hollow fiber type membrane module, 2 ... Hollow fiber, 4 ... Adhesive sealing part, 6 ... Adhesive

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】中空糸束を収容する円筒状容器の両端部が
中空糸を互いに隔離して接着封止してなる中空糸型膜モ
ジュールであって、 該接着封止部内の中空糸内表面が非透水性であることを
特徴とする中空糸型膜モジュール。
1. A hollow fiber type membrane module in which both ends of a cylindrical container for accommodating a hollow fiber bundle are separated from each other and adhesively sealed, and an inner surface of the hollow fiber in the adhesively sealed portion. Is a water-impermeable hollow fiber membrane module.
【請求項2】中空糸束を収容する円筒状容器の両端部が
中空糸を互いに隔離して接着封止してなる中空糸型膜モ
ジュールの製造方法において、 組立られた中空糸型膜モジュールの接着封止部内にある
中空糸の内表面に接着剤を塗布し、硬化して非透水化す
ることを特徴とする中空糸型膜モジュールの製造方法。
2. A method for producing a hollow fiber type membrane module in which both ends of a cylindrical container for accommodating a hollow fiber bundle separate hollow fibers from each other and adhere and seal the hollow fiber type membrane module. A method for producing a hollow fiber type membrane module, characterized in that an adhesive is applied to the inner surface of the hollow fiber in the adhesive sealing portion and cured to make it impermeable.
JP62329236A 1987-12-25 1987-12-25 Hollow fiber type membrane module and manufacturing method thereof Expired - Lifetime JPH0798135B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62329236A JPH0798135B2 (en) 1987-12-25 1987-12-25 Hollow fiber type membrane module and manufacturing method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62329236A JPH0798135B2 (en) 1987-12-25 1987-12-25 Hollow fiber type membrane module and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JPH01171608A JPH01171608A (en) 1989-07-06
JPH0798135B2 true JPH0798135B2 (en) 1995-10-25

Family

ID=18219169

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62329236A Expired - Lifetime JPH0798135B2 (en) 1987-12-25 1987-12-25 Hollow fiber type membrane module and manufacturing method thereof

Country Status (1)

Country Link
JP (1) JPH0798135B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5230270B2 (en) * 1973-12-17 1977-08-06
JPS6197005A (en) * 1984-10-18 1986-05-15 Mitsubishi Rayon Co Ltd Manufacturing method of hollow fiber membrane module

Also Published As

Publication number Publication date
JPH01171608A (en) 1989-07-06

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