JPS6142304A - Removal method - Google Patents
Removal methodInfo
- Publication number
- JPS6142304A JPS6142304A JP16406384A JP16406384A JPS6142304A JP S6142304 A JPS6142304 A JP S6142304A JP 16406384 A JP16406384 A JP 16406384A JP 16406384 A JP16406384 A JP 16406384A JP S6142304 A JPS6142304 A JP S6142304A
- Authority
- JP
- Japan
- Prior art keywords
- cellulose acetate
- hollow yarn
- hollow fiber
- porous
- filtering
- 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
- 238000000034 method Methods 0.000 title description 5
- 229920002301 cellulose acetate Polymers 0.000 claims abstract description 17
- 239000012528 membrane Substances 0.000 claims abstract description 17
- 229920000098 polyolefin Polymers 0.000 claims abstract description 17
- 239000012510 hollow fiber Substances 0.000 claims description 38
- 239000004698 Polyethylene Substances 0.000 abstract description 11
- 238000001914 filtration Methods 0.000 abstract description 11
- -1 polyethylene Polymers 0.000 abstract description 11
- 229920000573 polyethylene Polymers 0.000 abstract description 11
- 230000015271 coagulation Effects 0.000 abstract description 3
- 238000005345 coagulation Methods 0.000 abstract description 3
- 239000000701 coagulant Substances 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 241000894006 Bacteria Species 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 239000011148 porous material Substances 0.000 description 4
- 239000002510 pyrogen Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 241000972773 Aulopiformes Species 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000001698 pyrogenic effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 235000019515 salmon Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
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
ているか、逆浸透法は高い圧力を要するため設備費が高
く、装置が大盤となり、処堺量を大きくしないと鮭済性
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、必要に応じ少しずつその水を使うという方法になる
。Reverse osmosis is a well-known method that can also remove pyrogens, but because reverse osmosis requires high pressure, equipment costs are high, the equipment is large, and salmon quality cannot be satisfied unless the processing volume is increased. Not only is this difficult, but the method involves storing treated water and using it little by little as needed.
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。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な有する水処理
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’&5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 a problem in that the concentration of bacteria increases on the side where the membranes 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<、シかも構造が簡
単で、故障が少なく、かつ信頼性の高い精密濾過装置用
の膜として、孔径Q、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, in Japanese Patent Publication No. 56-52123 and Japanese Patent Application Laid-Open No. 57-42919, the present applicant solved the drawbacks of conventional devices, and developed a system with low equipment and energy costs, a simple structure, and fewer failures. As a highly reliable membrane for precision filtration equipment, we proposed a porous polyolefin hollow fiber in which micropores with a pore diameter Q of 0.1 to 1 μm communicate between the inner and outer wall surfaces of the hollow fiber. 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@
〔問題点を解決するための手段〕
本発明の上記目的は、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、酢
酸セルロースからなる膜が形成されていることt%徴と
する親水化多孔質ポリオレフィン中空糸によつ℃達成さ
れる。An object of the present invention is to provide a hydrophilized porous polyolefin hollow fiber that is safe and has excellent operability. The micropores formed between many arranged fibrils are
A porous polyolefin hollow fiber that communicates between the inner wall surface and the outer wall surface of the hollow fiber, the hydrophilic porous material having a t% characteristic that a film made of cellulose acetate is formed on the surface of the fibril. ℃ achieved by 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
ン中空糸は例えば上記特開昭57−42919号等によ
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酢酸セルロー
ス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、例えば酢酸セルロースを
含有する溶液を多孔質ポリエチレン中空糸に含浸させた
後、該酢酸セルロースの凝固剤溶液に浸漬し、急速湿式
凝固処理な行なうことKよりフィブリル表面に酢酸セル
ロース膜を形成させる方法をとることができる。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 produced, for example, according to the above-mentioned Japanese Patent Application Laid-Open No. 57-42919. As a method for obtaining permanently hydrophilic porous polyethylene hollow fibers by forming cellulose acetate membranes on the surfaces of fibrils forming such porous polyethylene hollow fibers, for example, a solution containing cellulose acetate is made into a porous polyethylene hollow fiber. After impregnating polyethylene hollow fibers, a method can be used in which a cellulose acetate film is formed on the surface of the fibril by immersing it in a coagulant solution of the cellulose acetate and performing a rapid wet coagulation treatment.
この場合、本発明で使用する酢酸セルロースはフィルム
形成能を有するものであればどのようなものも用いるこ
とができる。酢酸セルロースはフィブリル表面にできる
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。酢酸セルロース 膜は優れ
た親水性を示す。従ってフィブリルの表面に酢酸セルロ
ース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0
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
壁側に向かって液体または気体な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、a1m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 this case, any cellulose acetate used in the present invention can be used as long as it has film-forming ability. It is preferable that the cellulose acetate be fixed as uniformly as possible on the surface of the fibrils, and that the amount of the cellulose acetate should be kept to a minimum, so as to minimize the clogging of the pores of the hollow fibers due to the fixation treatment. Cellulose acetate membranes exhibit excellent hydrophilic properties. Therefore, a porous polyolefin hollow fiber in which a cellulose acetate membrane is adhered to the fibril surface exhibits excellent hydrophilicity. It is sufficient to apply the general known module manufacturing method using threads as is, and as long as liquid or gas is filtered from the outer wall side of the porous hollow fibers to the inner wall side, or from the inner wall side to the outer wall side, Any form of module may be used. By using the hydrophilized porous polyolefin hollow fiber of the present invention, it is possible to remove colloidal substances, A1Ms, and pyrogenic substances, and while maintaining safe operability at all times, equipment costs and energy costs are lower than conventional equipment. The structure is simple, there are few failures, and it enables highly reliable precision filtration.
以下、本発明を実施例によって説明する〇ジアセテート
繊維製造用の酢酸セルロースフレーク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℃の浴液中に
1多孔質ポリエチレン中空糸(三菱レイヨン(株)製、
商品名EHF)を浸漬した後絞液し、溶液の中空糸に対
する付着量を310 % owfとし、引続き60℃の
水中に浸漬して酢酸セルロースの急速凝固処理による脱
溶剤処理を行ない中空糸の積層構造表面に酢酸セルロー
スの薄膜が固着された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10αのモジュールを作成した。Hereinafter, the present invention will be explained with reference to Examples.〇 One porous polyethylene hollow fiber (Mitsubishi Rayon Co., Ltd. ) made,
After dipping in EHF (trade name), the solution was squeezed to make the amount of solution attached to the hollow fibers 310% owf, and then immersed in water at 60°C to remove the solvent by rapid coagulation of cellulose acetate, and then stack the hollow fibers. A porous polyethylene hollow fiber with a thin film of cellulose acetate fixed to the structural surface was obtained. 100 of these hydrophilized porous polyethylene hollow fibers were bundled in a U-shape and the openings of the hollow fibers were solidified with resin to create a module with a resin-embedded portion of 4 cm in length and a hollow fiber effective length of 10α.
このモジュール内部に25℃のエタノールを入れ、多孔
質ポリエチレン中空糸内部にエタノールを含浸させた後
、中空糸外壁側から圧力380mHfで5tの水を1遇
させた後、水を抜き取り、5時間中空糸外壁部を空気と
接触させた後、再び中空糸外壁側から圧力680■Hf
で水を1遇させた結果、空気と接触させた前後でf過速
度に変化がみもれなかった。After filling the inside of this module with ethanol at 25°C and impregnating the inside of the porous polyethylene hollow fiber with ethanol, 5 tons of water was applied to the outer wall of the hollow fiber at a pressure of 380 mHf. After bringing the fiber outer wall into contact with air, a pressure of 680■Hf is applied from the hollow fiber outer wall again.
When exposed to water, no change was observed in f overspeed before and after contact with air.
比較例1
上記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1と同じ方法で通常のモジュールを作成し
、通水、水抜き、再通水を行すった。このモジュールは
空気接触後は32チ濾過速度が低下した。Comparative Example 1 A normal module was prepared in the same manner as in Example 1 using the above-mentioned porous polyethylene hollow fibers that had not been subjected to the hydrophilic treatment, and water was passed through the module, water was drained, and water was passed through the module again. The filtration rate of this module decreased by 32 cm after 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
糸であつて、フィブリルの表面に、酢酸セルロースから
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 hydrophilized porous polyolefin hollow fiber characterized in that a membrane made of cellulose acetate is formed on the surface of the fibrils.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16406384A JPS6142304A (en) | 1984-08-03 | 1984-08-03 | Removal method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16406384A JPS6142304A (en) | 1984-08-03 | 1984-08-03 | Removal method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6142304A true JPS6142304A (en) | 1986-02-28 |
| JPH0534047B2 JPH0534047B2 (en) | 1993-05-21 |
Family
ID=15786074
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16406384A Granted JPS6142304A (en) | 1984-08-03 | 1984-08-03 | Removal method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6142304A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4969661A (en) * | 1987-08-24 | 1990-11-13 | Nissan Motor Co., Ltd. | Vehicular rear suspension system and rear end construction including same |
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
- 1984-08-03 JP JP16406384A patent/JPS6142304A/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 (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4969661A (en) * | 1987-08-24 | 1990-11-13 | Nissan Motor Co., Ltd. | Vehicular rear suspension system and rear end construction including same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0534047B2 (en) | 1993-05-21 |
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