JP3282334B2 - Method for hydrophilizing polysulfone hollow fiber membrane - Google Patents
Method for hydrophilizing polysulfone hollow fiber membraneInfo
- Publication number
- JP3282334B2 JP3282334B2 JP32609793A JP32609793A JP3282334B2 JP 3282334 B2 JP3282334 B2 JP 3282334B2 JP 32609793 A JP32609793 A JP 32609793A JP 32609793 A JP32609793 A JP 32609793A JP 3282334 B2 JP3282334 B2 JP 3282334B2
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber membrane
- polysulfone
- water
- hydrophilizing
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、ポリスルホン中空糸膜
の親水化方法に関する。更に詳しくは、恒久親水化を可
能ならしめるポリスルホン中空糸膜の加熱処理方法に関
する。The present invention relates to a method for hydrophilizing a polysulfone hollow fiber membrane. More specifically, the present invention relates to a method for heat-treating a polysulfone hollow fiber membrane which enables permanent hydrophilicization.
【0002】[0002]
【従来の技術】疎水性のポリスルホンから親水性の中空
糸膜を製造する場合、親水性の高分子物質であるポリビ
ニルピロリドンなどを混和して、親水性を付与すること
が行われている。しかしながら、このような方法で得ら
れた中空糸膜に通水すると、親水性高分子物質が徐々に
溶出し、やがて中空糸膜の親水性が失われるようにな
る。2. Description of the Related Art When a hydrophilic hollow fiber membrane is produced from hydrophobic polysulfone, hydrophilicity is imparted by mixing a hydrophilic polymer substance such as polyvinylpyrrolidone. However, when water is passed through the hollow fiber membrane obtained by such a method, the hydrophilic polymer substance is gradually eluted, and the hydrophilicity of the hollow fiber membrane is eventually lost.
【0003】[0003]
【発明が解決しようとする課題】本発明の目的は、親水
性の高分子物質であるポリビニルピロリドンを添加した
ポリスルホン中空糸膜において、そこに恒久親水性を付
与せしめるポリスルホン中空糸膜の加熱処理方法を提供
することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a polysulfone hollow fiber membrane to which polyvinylpyrrolidone which is a hydrophilic polymer substance is added, and a method for heat-treating the polysulfone hollow fiber membrane in which permanent hydrophilicity is imparted thereto. Is to provide.
【0004】[0004]
【課題を解決するための手段】かかる本発明の目的は、
約0.1〜10重量%のポリビニルピロリドンを添加したポリ
スルホン紡糸原液から中空糸膜を乾湿式紡糸した後、約
110℃以上の水中で加圧加熱処理することによって達成
される。SUMMARY OF THE INVENTION The object of the present invention is as follows.
After dry-wet spinning of a hollow fiber membrane from a polysulfone spinning stock solution containing about 0.1 to 10% by weight of polyvinylpyrrolidone,
This is achieved by performing pressure heating in water at 110 ° C. or higher.
【0005】親水性高分子物質として添加されるポリビ
ニルピロリドンとしては、分子量が約10000(K-15)〜120
0000(K-90)のものが、紡糸原液中約0.1〜10重量%、好ま
しくは約0.1〜6重量%程度占めるような割合で用いられ
る。[0005] Polyvinylpyrrolidone added as a hydrophilic polymer substance has a molecular weight of about 10,000 (K-15) to 120.
0000 (K-90) is used in such a ratio that it occupies about 0.1 to 10% by weight, preferably about 0.1 to 6% by weight in the spinning dope.
【0006】このようなポリビニルピロリドンが添加さ
れる紡糸溶液は、約10〜30重量%、好ましくは約13〜20
重量%を占めるような量のポリスルホンを、ジメチルホ
ルムアミド、ジエチルホルムアミド、ジメチルアセトア
ミド、ジエチルアセトアミド、ジメチルスルホキシド、
N-メチル-2-ピロリドン、トリエチルホスフェート等の
非プロトン性極性溶媒中に溶解させて用いられる。The spinning solution to which such polyvinylpyrrolidone is added is about 10 to 30% by weight, preferably about 13 to 20% by weight.
% By weight of polysulfone in dimethylformamide, diethylformamide, dimethylacetamide, diethylacetamide, dimethylsulfoxide,
It is used by dissolving it in an aprotic polar solvent such as N-methyl-2-pyrrolidone and triethyl phosphate.
【0007】ポリスルホン、ポリビニルピロリドンおよ
び非プロトン性極性溶媒等から形成される紡糸原液中に
は、必要に応じて増孔剤あるいは増粘剤として分子量約
400〜6000程度のポリエチレングリコールなどを、約1〜
20重量%、好ましくは約13〜20重量%程度添加することも
できる。[0007] The spinning dope formed from polysulfone, polyvinylpyrrolidone and an aprotic polar solvent, etc., may have a molecular weight of approximately
Polyethylene glycol of about 400 to 6000, about 1 to
20% by weight, preferably about 13 to 20% by weight can be added.
【0008】かかる紡糸原液を用いての中空糸膜化は、
二重環状ノズルから押出し、空走させた後、一般に水が
用いられる水性凝固浴中でゲル化させるという通常の方
法に従って行われる。[0008] The formation of a hollow fiber membrane using such a spinning solution is as follows.
It is extruded from a double annular nozzle, run idle, and then gelled in an aqueous coagulation bath generally using water.
【0009】水性凝固浴中でゲル化させたポリスルホン
中空糸膜は、約110℃以上、好ましくは121℃程度の水中
での加熱処理に付される。この加熱処理は、当然加圧条
件下で行われるのでオートクレーブ等を用いて、約5分
間以上、好ましくは約15〜60分間程度行われ、その際洗
浄も同時に行われる。The polysulfone hollow fiber membrane gelled in an aqueous coagulation bath is subjected to a heat treatment in water at about 110 ° C. or higher, preferably about 121 ° C. Since this heat treatment is naturally performed under a pressurized condition, it is performed using an autoclave or the like for about 5 minutes or more, preferably for about 15 to 60 minutes, and at the same time, washing is performed at the same time.
【0010】[0010]
【発明の効果】親水性高分子物質としてのポリビニルピ
ロリドンを添加したポリスルホン中空糸膜に、水中での
高温加熱処理を行うことにより、親水性高分子物質の溶
出が少なく、従って恒久親水性の付与されたポリスルホ
ン中空糸膜が得られる。The polysulfone hollow fiber membrane to which polyvinylpyrrolidone is added as a hydrophilic polymer substance is subjected to a high-temperature heat treatment in water, so that the elution of the hydrophilic polymer substance is small, and thus a permanent hydrophilic property is imparted. The obtained polysulfone hollow fiber membrane is obtained.
【0011】[0011]
【実施例】次に、実施例について本発明を説明する。Next, the present invention will be described with reference to examples.
【0012】実施例1 ポリスルホン 14重量部 ポリエチレングリコール(分子量600) 14 〃 ポリビニルピロリドン(分子量40000) 1 〃 ジメチルホルムアミド 71 〃 以上の各成分からなる紡糸原液を二重環状ノズルから押
出し、水凝固浴でゲル化させる乾湿式紡糸法によって、
ポリスルホン中空糸膜を製造した。Example 1 Polysulfone 14 parts by weight Polyethylene glycol (molecular weight 600) 14 << polyvinylpyrrolidone (molecular weight 40000) 1 << dimethylformamide 71 >> A spinning stock solution comprising the above components was extruded from a double annular nozzle, and was extruded from a water coagulation bath. By dry-wet spinning method to gel,
A polysulfone hollow fiber membrane was manufactured.
【0013】その際、 A:水凝固浴でゲル化させた中空糸膜 B:水凝固浴でゲル化させた後、約2時間水洗した中空
糸膜 C:水凝固浴でゲル化させた後、そのままオートクレー
ブ中に入れ、121℃の水中で20分間処理した中空糸膜 D:上記Cの中空糸膜を更に約2時間水洗した中空糸膜 について、それぞれ一旦乾燥させた後、エタノールで一
度濡らしてから純水に置換したときの純水透過係数に対
する乾燥中空糸膜の純水透過係数の100分率を親水化度
として測定すると、次のような結果が得られ、水中での
加熱処理により恒久親水性化が達成されることが分か
る。 At this time, A: a hollow fiber membrane gelled in a water coagulation bath B: a hollow fiber membrane gelled in a water coagulation bath and then washed with water for about 2 hours C: after a gelation in a water coagulation bath The hollow fiber membrane was placed in an autoclave as it was, and treated in water at 121 ° C. for 20 minutes. D: The hollow fiber membrane obtained by washing the hollow fiber membrane of the above C for about 2 hours was dried once and then wetted once with ethanol. When the percentage of the pure water permeability coefficient of the dry hollow fiber membrane relative to the pure water permeability coefficient when replaced with pure water is measured as the degree of hydrophilicity, the following results are obtained. It can be seen that permanent hydrophilization is achieved.
【0014】実施例2 実施例1において、ポリビニルピロリドン量を0.5重量
部に変更した。その際、 E:水凝固浴でゲル化させた中空糸膜 F:水凝固浴でゲル化させた後、そのままオートクレー
ブ中に入れ、121℃の水中で20分間処理した中空糸膜 G:上記Fの中空糸膜を更に2時間水洗した中空糸膜 について、親水化度を測定すると、次のような結果が得
られた。 Example 2 In Example 1, the amount of polyvinylpyrrolidone was changed to 0.5 parts by weight. At this time, E: hollow fiber membrane gelled in a water coagulation bath F: gelled in a water coagulation bath, then placed in an autoclave as it is and treated in water at 121 ° C. for 20 minutes G: F above The following results were obtained by measuring the degree of hydrophilicity of the hollow fiber membrane obtained by further washing the hollow fiber membrane with water for 2 hours.
【0015】比較例 実施例1において、ポリビニルピロリドンが用いられな
かった。その際、 H:水凝固浴でゲル化させた中空糸膜 I:水凝固浴でゲル化させた後、そのままオートクレー
ブ中に入れ、121℃の水中で20分間処理した中空糸膜 について、親水化度を測定すると、次のような結果が得
られた。 Comparative Example In Example 1, no polyvinylpyrrolidone was used. At that time, H: hollow fiber membrane gelled in a water coagulation bath I: gelled in a water coagulation bath, then put directly into an autoclave and treated in water at 121 ° C. for 20 minutes to obtain a hydrophilic fiber When the degree was measured, the following results were obtained.
Claims (1)
添加したポリスルホン紡糸原液から中空糸膜を乾湿式紡
糸した後、110℃以上の水中で加圧加熱処理することを
特徴とするポリスルホン中空糸膜の親水化方法。1. A After dry-wet spinning of hollow fiber membrane from 0.1 to 10 wt% of polyvinylpyrrolidone polysulfone spinning solution was added, polysulfone hollow fiber membrane, characterized by pressurizing and heating treatment in water above 110 ° C. Method for hydrophilization.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32609793A JP3282334B2 (en) | 1993-11-30 | 1993-11-30 | Method for hydrophilizing polysulfone hollow fiber membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32609793A JP3282334B2 (en) | 1993-11-30 | 1993-11-30 | Method for hydrophilizing polysulfone hollow fiber membrane |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07155573A JPH07155573A (en) | 1995-06-20 |
JP3282334B2 true JP3282334B2 (en) | 2002-05-13 |
Family
ID=18184071
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32609793A Expired - Lifetime JP3282334B2 (en) | 1993-11-30 | 1993-11-30 | Method for hydrophilizing polysulfone hollow fiber membrane |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3282334B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100416134B1 (en) * | 2001-01-12 | 2004-01-31 | 주식회사 코오롱 | A polysulfone based hollow fiber membranes with high strength and performance, and a process of preparing for the same |
-
1993
- 1993-11-30 JP JP32609793A patent/JP3282334B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH07155573A (en) | 1995-06-20 |
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