JPH01300961A - Preparation of membrane type filter apparatus - Google Patents

Preparation of membrane type filter apparatus

Info

Publication number
JPH01300961A
JPH01300961A JP63132266A JP13226688A JPH01300961A JP H01300961 A JPH01300961 A JP H01300961A JP 63132266 A JP63132266 A JP 63132266A JP 13226688 A JP13226688 A JP 13226688A JP H01300961 A JPH01300961 A JP H01300961A
Authority
JP
Japan
Prior art keywords
water
porous membrane
membrane
hot water
pressure
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.)
Granted
Application number
JP63132266A
Other languages
Japanese (ja)
Other versions
JPH0759250B2 (en
Inventor
Yasushi Shimomura
下村 泰志
Kenji Takeshita
健次 武下
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP63132266A priority Critical patent/JPH0759250B2/en
Publication of JPH01300961A publication Critical patent/JPH01300961A/en
Publication of JPH0759250B2 publication Critical patent/JPH0759250B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the title apparatus capable of being used simply and safely and excellent in water permeability and filterability, by allowing hot water at predetermined temp. or more to fill and applying pressure through hot water to allow water to penetrate in the pores of a porous membrane. CONSTITUTION:A membrane type filter apparatus having a porous membrane, which is composed of a hydrophobic polymer and provided with pores having an average pore size of 0.01-10mum, mounted therein and also having the introducing and lead-out ports of an aqueous solution and a filtrate lead-out port is prepared. Each of the spaces partitioned by said porous membrane of this apparatus if filled with hot water of 60 deg.C or more and pressure is applied through hot water to allow water to penetrate in the pores of the porous membrane.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は膜型濾過装置の製造方法に関するものであり、
更に詳しくは使用に際して簡便で安全に用いることかて
きる疎水性ポリマーよりなる多孔質膜を内蔵した濾過装
置の製造方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing a membrane filtration device,
More specifically, the present invention relates to a method for manufacturing a filtration device incorporating a porous membrane made of a hydrophobic polymer, which is simple and safe to use.

尚、ここでいう濾過装置とは、医用、工業用および一般
用に用いられる濾過装置をいう。
Note that the filtration device here refers to a filtration device used for medical, industrial, and general purposes.

医用としては、血液より血球成分と血漿成分を分離する
血漿分層器、血漿成分を更に分子ら:により分画する血
漿成分分離器、血液より水分のみを分離する血液儂縮塁
、■・ナーからの血液より血漿成分を献血・採取するた
めの血漿成分採取器等が挙げられる。また、工業用とし
ては精密波過カー1ヘリッジ、フィルター笠の木あるい
は水系溶液の濾過装置、−・般用としては家庭用浄水器
、携帯用浄水器等が挙げられる。
For medical use, there are plasma separators that separate blood cells and plasma components from blood, plasma component separators that further fractionate plasma components by molecules, blood thinners that separate only water from blood, and Examples include plasma component collectors for donating and collecting plasma components from blood from people. Examples of industrial use include a precision wave filter car 1 hedge, a filter shade made of wood or a filtration device for aqueous solutions, and general use such as household water purifiers and portable water purifiers.

[従来の技術] 疎水性ポリマーよりなる多孔質膜においては、血液のよ
うな水性液体は疎水性ポリマーを濡らさないため、多孔
質膜の微細孔への水性液体浸透か困難てあり、このよう
な疎水性ポリマーからなる多孔質膜を内蔵する医用濾過
装置はそのままでは使用することかできない。そのため
、疎水性ポリマーよりなる多孔質膜を予め親木化処理す
ることか提案されており、これら親木化処理方法とlノ
では、 (1)水にii(溶な低界面張力有機溶剤を微細孔内に
浸透させた後、水と置換する方法、 ■界面活性剤て多孔質膜を処理する方法、■多孔質膜表
面に親木性基を化学的に導入する方法、 ■親木性ポリマーを多孔質膜表面にコーティングする方
法、また ■水を5 kg/cm2以上の圧力で微細孔内に浸入さ
せる方法(特開昭61−92675号、同61−946
62号および同61−109573号各公報参照)か知
られている。
[Prior art] In porous membranes made of hydrophobic polymers, aqueous liquids such as blood do not wet the hydrophobic polymers, so it is difficult for aqueous liquids to penetrate into the micropores of the porous membrane. Medical filtration devices incorporating porous membranes made of hydrophobic polymers cannot be used as is. For this reason, it has been proposed to preliminarily treat porous membranes made of hydrophobic polymers to make them lignophilic, and in these lignophilic treatment methods, (1) using a low interfacial tension organic solvent that is soluble in water; Method of infiltrating into micropores and then replacing with water, ■ Method of treating porous membrane with surfactant, ■ Method of chemically introducing wood-philic groups onto the surface of porous membrane, ■ Wood-philicity A method of coating the surface of a porous membrane with a polymer, and a method of infiltrating water into micropores at a pressure of 5 kg/cm2 or more (JP-A-61-92675, JP-A-61-946).
No. 62 and No. 61-109573) are known.

[発明か解決しようとする課題] しかしなから、上記■の低界面張力有機溶剤を微細孔内
に浸透させた抜水と置換する方法ては。
[Problems to be Solved by the Invention] However, there is no method for replacing water with a low interfacial tension organic solvent infiltrated into micropores as described in (2) above.

低界面張力有機溶剤を洗浄除去するのに大量の水を必要
とする欠点かある。また、■の界面活性剤て処理する方
法ては、導入水および濾液に界面活性剤か溶出し、使用
上諸液汚染の問題がある。
One drawback is that a large amount of water is required to wash and remove the low interfacial tension organic solvent. In addition, in the method (2) of treating with a surfactant, the surfactant is eluted into the introduced water and the filtrate, resulting in the problem of contamination of various liquids during use.

又、■の多孔質膜表面に親木性基を化学的に導入する方
法も、反応残存、溶媒等か残留しやすに前記■と同様に
使用上問題があり、[株]の親木性ポリマーをコーティ
ングする方法も、コーティングに使用した溶媒か残留し
やすく、使用上問題かあるばかりでなく、特に医用に用
いる場合、疎水性多孔質膜が有する生体適合性、補体お
よび血小板等の活性化か低い等の血液への良適合性か、
疎水性1模の表面を別のポリマーでコーティングするこ
とにより失われてしまうという欠点かある。
In addition, the method of chemically introducing wood-loving groups onto the surface of the porous membrane in (2) also has the same problems in use as in (2) above, as reaction residues, solvents, etc. tend to remain. The method of coating polymers not only causes problems in use, as the solvent used for coating tends to remain, but especially when used for medical purposes, the hydrophobic porous membrane has biocompatibility, complement and platelet activities, etc. Good compatibility with blood, such as low
One drawback is that the hydrophobic surface is lost by coating it with another polymer.

更に、上記■の水を5 kg/cm2以上の圧力で微細
孔内に浸入させる方法では、上記のかかる問題はないか
、5 kg/c+s2以上という高い圧力をかけると膜
や容器が破損する確率が大きくなり、また破損しないま
でも高い圧力により多孔質膜の孔径が変化するという欠
点かあった。
Furthermore, with the above method of injecting water into the micropores at a pressure of 5 kg/cm2 or more, is there a possibility that the membrane or container will be damaged if a high pressure of 5 kg/c+s2 or more is applied? However, even if the membrane does not break, the pore diameter of the porous membrane changes due to the high pressure.

[課題を解決するための手段] そこで、本発明者らはこれら疎水性ポリマーよりなる多
孔質膜を内蔵する医用濾過装置の欠点を解決すべく鋭意
検討した結果、本発明に達した。
[Means for Solving the Problems] Therefore, the present inventors conducted extensive studies to solve the drawbacks of medical filtration devices incorporating porous membranes made of these hydrophobic polymers, and as a result, they arrived at the present invention.

すなわち、本発明は、疎水性ポリマーよりなり、微細孔
の平均孔径が0.01〜10ミクロンである多孔質膜を
内蔵し、水系溶液の導入口および導出口ならびに濾液の
導出口を有する膜型濾過装置を用意し、前記多孔質膜で
隔てられる各空間を60℃以上の温水で充填し、該温水
を介して圧力をかけることにより水を前記多孔質膜の微
細孔内に浸入させることを特徴とする膜型症過装鐙の製
造方法、を提供するものである。
That is, the present invention provides a membrane-type membrane that is made of a hydrophobic polymer, has a built-in porous membrane with an average pore size of 0.01 to 10 microns, and has an inlet and an outlet for an aqueous solution and an outlet for a filtrate. Prepare a filtration device, fill each space separated by the porous membrane with hot water of 60°C or higher, and apply pressure through the hot water to cause water to infiltrate into the micropores of the porous membrane. The present invention provides a method for manufacturing a characteristic membrane-type overloaded stirrup.

本発明で製造される膜型濾過装置は、親木化処理剤とし
ての有機溶剤、界面活性剤を用いず、多孔質膜の微細孔
に水か充填されているので、濾過装置4内に親木化剤か
残留することがなく医用の場合、安全であり、また工業
用、一般用においても濾液汚染の問題かない。
The membrane-type filtration device manufactured according to the present invention does not use an organic solvent or a surfactant as a wood-loving treatment agent, and the micropores of the porous membrane are filled with water, so that the inside of the filtration device 4 does not contain water. It is safe for medical use because no lignifying agent remains, and there is no problem of filtrate contamination for industrial or general use.

本発明において使用される疎水性ポリマーよりなる多孔
質膜としては、特にその種類を制限するものではなく、
例えばポリエチレン、ポリプロピレン、ポリ4−メチル
ペンテン−1、ポリスルフォン、ポリエーテJレスルフ
オン、ポリフッ化ヒ′ニリデン、ポリマ1〜ラフルオロ
エチレン、ポリジメチルシロキサン、ポリエチレンテレ
フタレート、ナイロンなどの材質のものが挙げられる。
The porous membrane made of a hydrophobic polymer used in the present invention is not particularly limited in its type;
For example, materials such as polyethylene, polypropylene, poly4-methylpentene-1, polysulfone, polyether J resulfone, polyhynylidene fluoride, polymer 1-lafluoroethylene, polydimethylsiloxane, polyethylene terephthalate, and nylon can be used.

本発明において使用される多孔質膜の形態は特に限定さ
れるものてはなく、例えば中空糸状、平膜状のものか用
いられる。
The form of the porous membrane used in the present invention is not particularly limited, and for example, a hollow fiber or flat membrane may be used.

また、多孔質膜の製造法についても特に制限はなく、延
伸法、湿式相分離法、溶融相分離法、溶媒抽出法等、公
知の製造法が採用される。
Further, there are no particular limitations on the method for producing the porous membrane, and known production methods such as a stretching method, a wet phase separation method, a melt phase separation method, and a solvent extraction method can be employed.

本発明において用いられる水系溶液としては、木のほか
、水を主成分とし界面張力を低下させる物質以外の有害
でない溶質を含むものも用いることがてきる。これには
純水、蒸留水、注射用蒸留水、パイロジエンフリー水、
生理食塩水などが挙げられる。
In addition to wood, the aqueous solution used in the present invention may also be one that has water as its main component and contains non-toxic solutes other than substances that reduce interfacial tension. This includes pure water, distilled water, distilled water for injection, pyrogen-free water,
Examples include physiological saline.

また、本発明においては、平均孔径か0.01〜10ミ
クロン(pm)(バブルポイント法による測定)の多孔
質膜を対象としている。0.01ミクロンより小さい平
均孔径の多孔質膜では微細孔内に温水が浸入し難く、1
0ミクロンより大きい平均孔径の多孔質膜ては、通常の
方法で多孔質膜の微細孔に水を流入させることができる
からである。
In addition, the present invention targets porous membranes having an average pore diameter of 0.01 to 10 microns (pm) (measured by bubble point method). In porous membranes with an average pore diameter smaller than 0.01 micron, hot water is difficult to penetrate into the micropores;
This is because, in a porous membrane having an average pore diameter larger than 0 microns, water can be caused to flow into the fine pores of the porous membrane using a conventional method.

本発明の方法な、従来公知である5 kg/cm2以−
hの圧力をか【Jて多孔質■りの微細孔に木を浸入さゼ
る方法と比較して述べると、本発明は、加温された場合
の水の界面張力の低下を積極的に利用することにより、
例えば特開昭61−92675号、同61−94662
号、同61−109573号−各公報等に示された公知
の方法よりも低、圧゛(多孔質膜の微細孔内に水を浸入
させることができる。
In the method of the present invention, the conventionally known
Comparing this with the method of infiltrating wood into the fine pores of a porous material using a pressure of By using
For example, JP-A-61-92675, JP-A No. 61-94662
No. 61-109573 - Water can penetrate into the micropores of a porous membrane at a lower pressure than the known methods disclosed in various publications.

多孔質膜を用いた濾過装置、特に医用として用いられる
濾過装置の場合、膜を固定する接着剤にポリウレタン樹
脂、濾過装置の容器としてポリマーか使用され、又実際
の使用上ではかなり低圧の一過圧で使われることか多く
、接着部、容器に使用I−の圧力範囲よりか(Jはなれ
た耐圧性を持たせることは経済的に得策でない。また高
い圧力により膜孔径が変化することも有り得る。従って
、可能な限り低圧で多孔質膜の微細孔内に木を浸入させ
ることが好ま1〕いのである。さらに、水を60℃以l
−に加温1.て使用するため、細菌の繁殖を軒減するこ
とかでき、汚染の問題も減することかてきる。
In the case of filtration devices using porous membranes, especially those used for medical purposes, polyurethane resin is used as the adhesive to fix the membrane, and polymer is used as the container of the filtration device, and in actual use, filtration at a fairly low pressure is used. It is often used under high pressure, and it is not economically advisable to provide adhesives and containers with pressure resistance that is outside the pressure range of I- (J).Also, high pressure may change the membrane pore diameter. Therefore, it is preferable to infiltrate the wood into the micropores of the porous membrane at as low a pressure as possible.
-Heat to 1. Since it is used in a vacuum, the growth of bacteria can be reduced and the problem of contamination can also be reduced.

なお、この濾過装置を高温状態のまま密封して高圧蒸気
滅菌することにより、完全に無菌てバイロンJ、ンフリ
ーの濾過装置を提供することができ、好ましい。
Note that it is preferable to seal the filtration device in a high-temperature state and sterilize it with high-pressure steam, since it is possible to provide a completely sterile, Byron-free filtration device.

使用する温水の温度としては、60’C以−1−1好ま
しくは80〜・−97℃てあり、加圧水を使用する場合
には100℃以−[、の温度の温水も使用することかで
きる。温水か60℃より低い場合、温水を介I)゛C圧
力をかけても、低圧では木がIIりの微細孔内に浸入し
難く、効果が低い。
The temperature of the hot water used is 60°C or higher, preferably 80 to -97°C, and if pressurized water is used, hot water at a temperature of 100°C or higher can also be used. . If the temperature of the hot water is lower than 60°C, even if pressure is applied through the hot water, the wood will be difficult to penetrate into the fine pores of II at low pressure, and the effect will be low.

また、温水を介1ノでかける圧力は、従来公知の方法で
用いる圧力より低くてよく、2〜5kg/cl112の
圧力範囲か好ましく、2.5−へ−4,5kg/cm2
の圧力範囲か特に好ましい。
Further, the pressure applied to the hot water may be lower than the pressure used in conventionally known methods, preferably in the pressure range of 2 to 5 kg/cl112, and 2.5 to 4.5 kg/cm2.
Particularly preferred is the pressure range.

又、本発明においCは、減圧ドて膜型濾過装置内の多孔
質膜で隔てられる名字間のn[気を排除1)、次いで該
空間に60℃以−1−の温水を充填し、温水を介1ノで
圧力をかけることか好ましいものである。
In addition, in the present invention, C is a space between the names separated by a porous membrane in a membrane-type filtration device under reduced pressure (1), and then the space is filled with hot water of 60°C or higher -1-, It is preferable to apply pressure through hot water.

[実施例] 以下、本発明を実施例に基いて更に詳細に説明するか、
本発明はこれら実施例に限られるものではない。
[Examples] Hereinafter, the present invention will be explained in more detail based on Examples.
The present invention is not limited to these examples.

(実施例) ポリプロピレン(UBE−PP−F l 09K、商品
名:宇部興産株製、M F I = 9g/10分)を
、中空糸製造用ノズルを使用し、紡糸温度210′Cで
紡糸した。得られたポリプロピレン中空糸を145℃の
加熱空気槽で30分間加熱処理し、次いで135℃の温
度で初期長さに対し400%、歪速度8.33%/分て
延伸し、延伸状態を保ったまま145℃の加熱空気槽内
で15分間熱処理を行ない多孔質ポリプロピレン中空糸
を製造した。得られた多孔質ポリプロピレンは内径32
04t、 m、膜厚55pmであった。また、ハツルボ
イントυ、(エタノール使用)で測定した」・−膜孔径
は0.48jLmて、空隙率は75%であった。
(Example) Polypropylene (UBE-PP-F l 09K, trade name: manufactured by Ube Industries, Ltd., M FI = 9 g/10 minutes) was spun at a spinning temperature of 210'C using a nozzle for manufacturing hollow fibers. . The obtained polypropylene hollow fibers were heat-treated in a heated air bath at 145°C for 30 minutes, and then stretched at a temperature of 135°C to 400% of the initial length and at a strain rate of 8.33%/min, and the stretched state was maintained. Heat treatment was performed for 15 minutes in a heated air bath at 145° C. to produce porous polypropylene hollow fibers. The obtained porous polypropylene had an inner diameter of 32
The film thickness was 55 pm. Further, the membrane pore diameter was 0.48 lm, and the porosity was 75%, as measured by Hatsuruboint υ (using ethanol).

この多孔質膜をポリカーボネート製ハウシングに収容し
、両端をポリウレタン接着剤で固定し、0.51112
の膜面積を有Jるポリプロピレン多孔質膜t!過装置を
作製1ノだ。この濾過装置の内部空間を真空ポンプて減
圧に1ノだ後、94℃の温水を濾過装置の各空間に充填
1ノ、多孔質膜で隔てられた各空間から温水を介して3
 kg/cm2の圧力で加圧した。
This porous membrane was housed in a polycarbonate housing, and both ends were fixed with polyurethane adhesive.
A porous polypropylene membrane having a membrane area of t! This is the first step in making a transceiver device. After reducing the pressure in the internal space of this filtration device for 1 time using a vacuum pump, warm water at 94°C is filled into each space of the filtration device for 1 time, and hot water is passed through each space separated by a porous membrane for 3 times.
Pressure was applied at a pressure of kg/cm2.

この濾過装置を用いて、木の透水量を測定したところ、
301 / Ilin−m”kg/cm′の高透水−7
iを示した。
When we measured the water permeability of wood using this filtration device, we found that
301/Ilin-m"kg/cm' high water permeability-7
i was shown.

(比較例) 実施例と同様に作製した濾過装置の内部空間を真空ポン
プて減圧にした後、25℃の無菌水を濾過装置の各空間
に充填1ノ、室温で水圧により濾過装置の各空間を4 
J/cm2て加圧した。この濾過装置を用いて、水の透
水量を測定したところ、2 、2 X 10−’4 /
min−m2・kg/cIl12の透水量を示し、実用
可能な透水量は得られなかった。
(Comparative example) After reducing the pressure in the internal space of a filtration device produced in the same manner as in the example, using a vacuum pump, sterile water at 25°C was filled into each space of the filtration device for 1 hour, and each space of the filtration device was heated at room temperature using water pressure. 4
Pressure was applied at J/cm2. When the water permeability was measured using this filtration device, it was found to be 2.2 x 10-'4/
The water permeability amount was min-m2·kg/cIl12, and a practically usable water permeation amount was not obtained.

[発明の効果〕 以−■−説明したように、本発明によれば、60’C以
上の温水で充填し、該温水を介して圧力をかけて水を多
孔質膜の微細孔内に浸入させて濾過装置を製造するため
、簡便且つ安全に使用することができ、しかも透水性、
濾過性に優れた膜型濾過装置を得ることができる。
[Effects of the Invention] As explained below, according to the present invention, the porous membrane is filled with hot water of 60'C or more, and pressure is applied through the hot water so that the water infiltrates into the micropores of the porous membrane. Since the filtration device is manufactured using the same method, it is easy and safe to use, and has high water permeability and
A membrane type filtration device with excellent filtration performance can be obtained.

Claims (1)

【特許請求の範囲】[Claims] (1)疎水性ポリマーよりなり、微細孔の平均孔径が0
.01〜10ミクロンである多孔質膜を内蔵し、水系溶
液の導入口および導出口ならびに濾液の導出口を有する
膜型濾過装置を用意し、前記多孔質膜で隔てられる各空
間を60℃以上の温水で充填し、該温水を介して圧力を
かけることにより水を前記多孔質膜の微細孔内に浸入さ
せることを特徴とする膜型濾過装置の製造方法。
(1) Made of hydrophobic polymer, the average pore diameter of micropores is 0.
.. A membrane-type filtration device is prepared which incorporates a porous membrane having a diameter of 01 to 10 microns and has an inlet and an outlet for an aqueous solution and an outlet for a filtrate. A method for manufacturing a membrane filtration device, characterized in that the porous membrane is filled with hot water and pressure is applied through the hot water to allow water to enter the micropores of the porous membrane.
JP63132266A 1988-05-30 1988-05-30 Membrane type filtration device manufacturing method Expired - Lifetime JPH0759250B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63132266A JPH0759250B2 (en) 1988-05-30 1988-05-30 Membrane type filtration device manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63132266A JPH0759250B2 (en) 1988-05-30 1988-05-30 Membrane type filtration device manufacturing method

Publications (2)

Publication Number Publication Date
JPH01300961A true JPH01300961A (en) 1989-12-05
JPH0759250B2 JPH0759250B2 (en) 1995-06-28

Family

ID=15077264

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63132266A Expired - Lifetime JPH0759250B2 (en) 1988-05-30 1988-05-30 Membrane type filtration device manufacturing method

Country Status (1)

Country Link
JP (1) JPH0759250B2 (en)

Also Published As

Publication number Publication date
JPH0759250B2 (en) 1995-06-28

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