JPS618103A - Hydrophilic porous polyolefin hollow yarn - Google Patents
Hydrophilic porous polyolefin hollow yarnInfo
- Publication number
- JPS618103A JPS618103A JP12910084A JP12910084A JPS618103A JP S618103 A JPS618103 A JP S618103A JP 12910084 A JP12910084 A JP 12910084A JP 12910084 A JP12910084 A JP 12910084A JP S618103 A JPS618103 A JP S618103A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- hollow yarn
- acrylonitrile
- porous
- porous polyolefin
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〔技術分野〕
本発明は親水性に優れた多孔質ポリオレフィン中空糸に
関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to porous polyolefin hollow fibers with excellent hydrophilicity.
純水製造や水中のコロイド状物の濾過等にもちいる限外
濾過膜や精密濾過膜としては種々の膜が知られている。Various membranes are known as ultrafiltration membranes and precision filtration membranes used for producing pure water, filtering colloidal substances in water, and the like.
特に医療用、医薬品用、食品工業用、精密工業用の膜は
細菌を除去することが必要とされており、なかでも医療
用、医薬品用では発熱性物質をも除去できる膜が要望さ
れている。細菌を除去できる膜は数多く知られているが
、同時に発熱性物質をも除去できる限外濾過膜や精密濾
過膜は知られていない。In particular, membranes for medical, pharmaceutical, food, and precision industries are required to remove bacteria, and in particular, membranes that can also remove pyrogens are required for medical and pharmaceutical applications. . Although many membranes that can remove bacteria are known, there are no ultrafiltration membranes or microfiltration membranes that can simultaneously remove pyrogens.
発熱物質をも除去できる方法としては逆浸透法が知られ
ているが、逆浸透法は高い圧力を要する。Reverse osmosis is known as a method that can also remove pyrogens, but reverse osmosis requires high pressure.
ため設備費が高く、装置が大型となり、処理量を大きく
しないと経済性を満足し難いばかりでなく、処理済みの
水をためておいて、必要に応し少しずつその水を使うと
いう方法になる。水をためるのに種々の工夫をほどこし
ても処理済みの水に細菌や発熱性物質が混入してくると
いう欠点がある。Therefore, equipment costs are high, the equipment is large, and it is difficult to satisfy economic efficiency unless the processing capacity is increased.In addition, the method of storing treated water and using it little by little as needed Become. Even if various measures are taken to store water, there is a drawback that bacteria and pyrogens can contaminate the treated water.
特に細菌を阻止できるような微小な孔径を有する水処理
用の多孔質膜は親水性でないと、水を透過できないが、
親水性素材からなる膜は微生物の攻撃をうけて劣化し易
く、また阻止された側で細菌濃度が高くなるという問題
がある。In particular, porous membranes for water treatment, which have minute pores that can block bacteria, must be hydrophilic to allow water to pass through them.
Membranes made of hydrophilic materials tend to deteriorate when attacked by microorganisms, and there is also the problem that the concentration of bacteria increases on the side where they are attacked.
さきに、本出願人は、特公昭56−52123号及び特
開昭57−42919号において従来装置の欠点を解決
し、設備費およびエネルギー費が安く、しかも構造がN
単で、故障が少なく、かつ信願性の高い精密濾過装置用
の膜として、孔径0.01〜1μmの微小空孔が中空糸
の内壁面と外壁面との間を連通ずる多孔質ポリオレフィ
ン中空糸を提案した。しかしこれは疎水性の多孔質ポリ
オレフィン中空糸であるので、使用前にアルコール等で
一時的に親水化してそのまま水と置換して用いるが、水
を長期間濾過した後等、洗浄のために水を抜き取り、多
孔質ポリオレフィン中空糸表面を空気と接触させて乾燥
すると、濾水性が低下する問題があり、親水性に優れた
多孔質ポリオレフィン中空糸の開発が強く要望されてい
た。Previously, the present applicant solved the drawbacks of the conventional device in Japanese Patent Publication No. 56-52123 and Japanese Patent Application Laid-Open No. 57-42919, and achieved a structure with low equipment cost and energy cost.
As a membrane for precision filtration equipment that is simple, has few failures, and has high reliability, it is a porous polyolefin hollow fiber in which micropores with a pore diameter of 0.01 to 1 μm communicate between the inner wall surface and outer wall surface of the hollow fiber. I suggested thread. However, since this is a hydrophobic porous polyolefin hollow fiber, it is used by temporarily making it hydrophilic with alcohol etc. before use and replacing it with water. If the surface of the porous polyolefin hollow fiber is removed and dried by contacting with air, there is a problem that the freeness decreases, and there has been a strong demand for the development of a porous polyolefin hollow fiber with excellent hydrophilicity.
本発明の目的は安全、操作性に優れた親水化多孔質ポリ
オレフィン中空糸を提供することにある。An object of the present invention is to provide a hydrophilized porous polyolefin hollow fiber that is safe and has excellent operability.
本発明のL記目的は、中空糸のほぼ長手方向に配列した
多数のフィブリル相互間に形成されている微小空孔が、
中空糸の内壁面と外壁面との間を連通している多孔質ポ
リオレフィン中空糸であって、フィブリルの表面に、ア
クリロニトリル系またはポリウレタン系の樹脂からなる
膜が形成されていることを特徴とする親水化多孔質ポリ
オレフィン中空糸によって達成される。The L object of the present invention is that micropores formed between a large number of fibrils arranged approximately in the longitudinal direction of a hollow fiber are
A porous polyolefin hollow fiber that communicates between the inner wall surface and the outer wall surface of the hollow fiber, characterized in that a film made of an acrylonitrile-based or polyurethane-based resin is formed on the surface of the fibril. This is achieved by hydrophilic porous polyolefin hollow fibers.
多数のフィブリルによって形成された微小空孔が中空糸
の内壁面と外壁面との間を連通ずる多孔質ポリオレフィ
ン中空糸は上記特開昭57−42919号によって製造
することができる。このような多孔質ポリエチレン中空
糸を形成するフィブリルの表面にアクリロニトリル系ま
たはポリウレタン系の樹脂膜を形成して恒久的に親水化
された多孔質ポリエチレン中空糸を得る方法としては、
アクリロニトリル系またはポリウレタン系の樹脂を含有
する溶液を多孔質ポリエチレン中空糸のフィブリルの表
面に付着させた後、これらの樹脂を凝固剤溶液に浸漬し
、急速湿式凝固処理を行なうことによりアクリロニトリ
ル系又はポリウレタン系の樹脂膜を形成し、フィブリル
の表面に強固に付着させることができる。この場合アク
リロニトリル系多孔質膜を形成する場合は、使用するア
クリロニトリル系樹脂はアクリロニトリルを30重量%
以上含有する重合体を用いるアクリロニトリル含有量が
30重量%未満の重合体を用いると、アクリロニトリル
系膜は親水性が小さくなって好ましくない。なおアクリ
ロニトリル系樹脂はアクリロニトリル単独重合体あるい
は、アクリロニトリルと、酢酸ビニル、アクリル酸メチ
ル、メタクリル酸メチル、塩化ビニル、アクリルアミド
等との共重合体が好ましく用いられる。A porous polyolefin hollow fiber in which micropores formed by a large number of fibrils communicate between the inner wall surface and the outer wall surface of the hollow fiber can be manufactured according to the above-mentioned Japanese Patent Application Laid-Open No. 57-42919. A method for obtaining permanently hydrophilized porous polyethylene hollow fibers by forming an acrylonitrile or polyurethane resin film on the surface of the fibrils forming such porous polyethylene hollow fibers is as follows:
After a solution containing an acrylonitrile-based or polyurethane-based resin is attached to the surface of the fibrils of porous polyethylene hollow fibers, these resins are immersed in a coagulant solution and subjected to rapid wet coagulation treatment to form an acrylonitrile-based or polyurethane resin. A system resin film can be formed and firmly attached to the surface of fibrils. In this case, when forming an acrylonitrile-based porous membrane, the acrylonitrile resin used contains 30% by weight of acrylonitrile.
If a polymer having an acrylonitrile content of less than 30% by weight is used, the hydrophilicity of the acrylonitrile-based film becomes undesirable. As the acrylonitrile resin, an acrylonitrile homopolymer or a copolymer of acrylonitrile and vinyl acetate, methyl acrylate, methyl methacrylate, vinyl chloride, acrylamide, etc. is preferably used.
ポリウレタン系樹脂膜を形成する場合は、公知のものを
用いればよく、例えば末端に水酸基、カルボキシル基等
の活性水素を有する脂肪族ポリエーテルまたはポリエス
テルとジイソシアネートとの縮重合体等を挙げることが
できる。When forming a polyurethane resin film, a known resin may be used, such as a condensation polymer of aliphatic polyether or polyester having active hydrogen such as a hydroxyl group or a carboxyl group at the terminal and a diisocyanate. .
これらのアクリロニトリル系またばポリウレタン系の樹
脂膜は多孔質中空糸のフィブリルの表面に、できるだけ
均一にしかもその固着量を最少限度に止め、固着処理に
よる中空糸の開孔部分の閉塞をできるだけ少なくするこ
とが好ましい。These acrylonitrile-based or polyurethane-based resin films are adhered as uniformly as possible to the surface of the fibrils of the porous hollow fibers, and the amount of adhesion is kept to a minimum, thereby minimizing clogging of the open pores of the hollow fibers due to adhesion treatment. It is preferable.
アクリロニトリル系膜やポリウレタン系膜は優れた親水
性を示す。従ってフィブリルの表面にアクリロニトリル
系またはポリウレタン系の膜が固着した多孔質ポリオレ
フィン中空糸は優れた親水性を示すことになる。Acrylonitrile-based films and polyurethane-based films exhibit excellent hydrophilicity. Therefore, a porous polyolefin hollow fiber having an acrylonitrile or polyurethane membrane adhered to the fibril surface exhibits excellent hydrophilicity.
本発明の親水性多孔質ポリオレフィン中空糸を用いてモ
ジュールを製造するには、多孔質中空糸を用いた一般的
な既知のモジュール製法をそのまま応用すればよく、多
孔質中空糸の外壁側から内壁側に、または内壁側から外
壁側に向がって液体または気体を濾過するものであれば
、どのような形態のモジュールでもよい。本発明の親水
化多孔質ポリオレフィン中空糸を使用すればコロイド状
物質、細菌類ならびに発熱性物質の除去が可能であり、
常に安全操作性を保つと共に、従来装置に比べ設備費、
エネルギー費が安く、構造が簡単で故障が少なく、信頼
性の高い精密濾過を可能にするものである。In order to manufacture a module using the hydrophilic porous polyolefin hollow fiber of the present invention, it is sufficient to apply the general known module manufacturing method using porous hollow fiber as is, from the outer wall side of the porous hollow fiber to the inner wall side. Any form of module may be used as long as it filters liquid or gas from the side or from the inner wall to the outer wall. By using the hydrophilized porous polyolefin hollow fiber of the present invention, it is possible to remove colloidal substances, bacteria, and pyrogenic substances,
In addition to always maintaining safe operability, equipment costs and costs are reduced compared to conventional equipment.
The energy cost is low, the structure is simple, there are few failures, and highly reliable precision filtration is possible.
以下、本発明を実施例によって説明する。 Hereinafter, the present invention will be explained by examples.
実施例1
アクリロニトリル93重量%と酢酸ビニル7重量%とか
らなる粉末状のアクリロニトリル系共重合体1重量部を
、ジメ・チルホルムアミド99重量部で溶解した25℃
の溶液に、多孔質ポリエチレン中空糸(三菱レイヨン側
製、商品名E HF )を浸漬した後絞液し、中空糸に
対する溶液の付着量を80%owfとし、引続き60℃
の熱水中に浸漬して、アクリロニトリル系共重合体の急
速凝固処理による多孔質化と脱溶剤処理とを行なった後
、十分に水洗して乾燥し、中空糸のフィブリルの表面に
アクリロニトリル系膜が形成されて親水化多孔質ポリエ
チレン中空糸を得た。Example 1 1 part by weight of a powdered acrylonitrile-based copolymer consisting of 93% by weight of acrylonitrile and 7% by weight of vinyl acetate was dissolved in 99 parts by weight of dimethyl thylformamide at 25°C.
A porous polyethylene hollow fiber (manufactured by Mitsubishi Rayon, trade name EHF) was immersed in the solution, and then squeezed to make the amount of solution attached to the hollow fiber 80% owf, and then heated at 60°C.
The acrylonitrile copolymer is immersed in hot water to make it porous by rapid solidification and to remove the solvent.Then, the acrylonitrile copolymer is thoroughly washed with water and dried, and an acrylonitrile film is applied to the surface of the fibrils of the hollow fibers. was formed to obtain hydrophilized porous polyethylene hollow fibers.
この親水化多孔質ポリエチレン中空糸100本をU字型
に束ね、中空糸用開口部分を樹脂で固め、樹脂包埋部の
長さ4cm、中空糸有効長IQcmのモジュールが好ま
しく用いられる。A module is preferably used in which 100 of these hydrophilized porous polyethylene hollow fibers are bundled in a U-shape, the opening for the hollow fibers is hardened with resin, and the length of the resin-embedded part is 4 cm and the effective length of the hollow fibers is IQ cm.
この親水化多孔質ポリエチレン中空糸の外側から25℃
のエタノールを入れて多孔質ポリエチレン中空糸の内部
にエタノールを含浸させた後、中空糸の外側から圧力3
80mHgの下で51の水を濾過した後、水を抜取り5
時間中空糸の外側を空気と接触させた後、再び中空糸の
外側から、圧力3801mHHの下で水を濾過した結果
、本発明の親水化多孔質ポリエヂレン中空糸使用モジュ
ールは濾過速度に変化は認められなかった。25°C from the outside of this hydrophilized porous polyethylene hollow fiber.
of ethanol to impregnate the inside of the porous polyethylene hollow fiber, and then apply pressure of 3.5 mL from the outside of the hollow fiber.
After filtering the water of 51 under 80 mHg, the water was extracted and
After the outside of the hollow fiber was brought into contact with air for a period of time, water was again filtered from the outside of the hollow fiber under a pressure of 3801 mHH. As a result, the module using the hydrophilized porous polyethylene hollow fiber of the present invention did not notice any change in the filtration rate. I couldn't.
比較例1
上記親水処理をしていない多孔質ポリエチレン中空糸を
用い、実施例1と同じ方法で通常のモジュールを作成し
、実施例1と同じ方法で濾過実験した。この未処理の多
孔質ポリエチレン中空糸を使用したモジュールは、5時
間の空気との接触で濾過速度が32%低下した。Comparative Example 1 A normal module was prepared in the same manner as in Example 1 using the porous polyethylene hollow fibers that had not been subjected to the hydrophilic treatment, and a filtration experiment was conducted in the same manner as in Example 1. A module using this untreated porous polyethylene hollow fiber had a 32% reduction in filtration rate after 5 hours of contact with air.
実施例2
アジピン酸と1−4ブタンジオールとから合成したポリ
エステル(分子it 1500 ) 10000重量4
−4′ジフ工ニルメタンジイソシアネート29重量部を
加え、窒素気流下80℃で3時間反応させてポリウレタ
ンを得た。このポリウレタン0.5重量部をジメチルホ
ルムアミド99.5重量部で溶解した25“Cの溶液に
、実施例1で用いたものと同じ多孔質ポリエチレン中空
糸を浸漬した後、絞液し、中空糸に対する溶液の付着量
を330%owfとし、引き続き60℃の水中に浸漬し
てポリウレタンの急速凝固処理による多孔質化と脱溶剤
処理とを行なった後、十分水洗して乾燥し、中空糸のフ
ィブリルの表面にポリウレタン膜を固着した親水化多孔
質ポリエチレン中空糸を得た。この親水化多孔質ポリエ
チレン中空糸100本をU字型に束ね、中空糸用開口部
分を樹脂で固め、樹脂包埋部の長さ4cm、中空糸有効
長IQcn+のモジュールを作成した。Example 2 Polyester synthesized from adipic acid and 1-4 butanediol (molecules it 1500) 10000 weight 4
29 parts by weight of -4' diphenylmethane diisocyanate was added, and the mixture was reacted at 80° C. for 3 hours under a nitrogen stream to obtain polyurethane. The same porous polyethylene hollow fiber as used in Example 1 was immersed in a 25"C solution prepared by dissolving 0.5 parts by weight of this polyurethane in 99.5 parts by weight of dimethylformamide, and the hollow fiber was squeezed. The adhesion amount of the solution was set to 330% owf, and the solution was subsequently immersed in water at 60°C to make the polyurethane porous by rapid coagulation and to remove the solvent. After that, it was thoroughly washed with water and dried to form hollow fiber fibrils. A hydrophilic porous polyethylene hollow fiber was obtained with a polyurethane film fixed to the surface of the fiber.100 of the hydrophilic porous polyethylene hollow fibers were bundled into a U-shape, the opening for the hollow fiber was hardened with resin, and the resin-embedded part was A module with a length of 4 cm and a hollow fiber effective length IQcn+ was created.
この親水化多孔質ポリエチレン中空糸の外側から25°
Cのエタノールを入れ、多孔質ポリエチレン中空糸の内
部にエタノールを含浸させた後、中空糸の外側から圧力
380++mHgの下で5βの水を濾過した後、水を抜
取り、5時間中空糸の外側を空気と接触させた後、再び
中空糸の外側から圧力380i11(gの下で水を濾過
した結果、濾過速度に変化は認められなかった。25° from the outside of this hydrophilic porous polyethylene hollow fiber
After adding ethanol C to impregnate the inside of the porous polyethylene hollow fiber with ethanol, 5β water was filtered from the outside of the hollow fiber under a pressure of 380++ mHg, the water was extracted, and the outside of the hollow fiber was filtered for 5 hours. After contact with air, the water was again filtered from the outside of the hollow fiber under a pressure of 380 i11 (g), and no change in filtration rate was observed.
此l≧」λ
比較例1と同様に親水化処理していない多孔質ポリエチ
レン中空糸を用い、実施例2と同じ方法で通常のモジュ
ールを作成した。この未処理の多孔質ポリエチレン中空
糸を使用したモジュールは5時間の空気との接触で濾過
速度が32%低下した。This l≧”λ As in Comparative Example 1, a normal module was prepared in the same manner as in Example 2 using porous polyethylene hollow fibers that had not been subjected to hydrophilic treatment. The filtration rate of the module using this untreated porous polyethylene hollow fiber decreased by 32% after 5 hours of contact with air.
本発明の親水性多孔質ポリオレフィン中空糸を使用した
中空糸モジュールは、濾過を中断して中空糸を空気接触
させた後も濾過速度が低下することなく、安定した信頼
性をもって濾過を反復することができる。The hollow fiber module using the hydrophilic porous polyolefin hollow fibers of the present invention is capable of repeating filtration with stable reliability without decreasing the filtration rate even after filtration is interrupted and the hollow fibers are brought into contact with air. I can do it.
Claims (1)
相互間に形成されている微小空孔が、中空糸の内壁面と
外壁面との間を連通している多孔質ポリオレフィン中空
糸であって、フィブリルの表面に、アクリロニトリル系
またはポリウレタン系の樹脂からなる膜が形成されてい
ることを特徴とする親水化多孔質ポリオレフィン中空糸
。1. A porous polyolefin hollow fiber in which micropores formed between a large number of fibrils arranged substantially in the longitudinal direction of the hollow fiber communicate between the inner wall surface and the outer wall surface of the hollow fiber. , a hydrophilic porous polyolefin hollow fiber characterized in that a membrane made of acrylonitrile or polyurethane resin is formed on the surface of the fibrils.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12910084A JPS618103A (en) | 1984-06-25 | 1984-06-25 | Hydrophilic porous polyolefin hollow yarn |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12910084A JPS618103A (en) | 1984-06-25 | 1984-06-25 | Hydrophilic porous polyolefin hollow yarn |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS618103A true JPS618103A (en) | 1986-01-14 |
JPH0534046B2 JPH0534046B2 (en) | 1993-05-21 |
Family
ID=15001066
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12910084A Granted JPS618103A (en) | 1984-06-25 | 1984-06-25 | Hydrophilic porous polyolefin hollow yarn |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS618103A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61161103A (en) * | 1985-01-10 | 1986-07-21 | Terumo Corp | Hydrophilic porous membrane and its preparation |
US5096640A (en) * | 1986-05-16 | 1992-03-17 | Imperial Chemical Industries Plc | Method of producing porous hollow fibrous tubes |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54102292A (en) * | 1978-01-30 | 1979-08-11 | Mitsubishi Rayon Co Ltd | Composite hollow yarn and gas selective permeating method used above yarn |
-
1984
- 1984-06-25 JP JP12910084A patent/JPS618103A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54102292A (en) * | 1978-01-30 | 1979-08-11 | Mitsubishi Rayon Co Ltd | Composite hollow yarn and gas selective permeating method used above yarn |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61161103A (en) * | 1985-01-10 | 1986-07-21 | Terumo Corp | Hydrophilic porous membrane and its preparation |
JPH0451214B2 (en) * | 1985-01-10 | 1992-08-18 | Terumo Corp | |
US5096640A (en) * | 1986-05-16 | 1992-03-17 | Imperial Chemical Industries Plc | Method of producing porous hollow fibrous tubes |
Also Published As
Publication number | Publication date |
---|---|
JPH0534046B2 (en) | 1993-05-21 |
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