JPS6297981A - Method for making hydrophobic porous membrane hydrophilic - Google Patents

Method for making hydrophobic porous membrane hydrophilic

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Publication number
JPS6297981A
JPS6297981A JP60236943A JP23694385A JPS6297981A JP S6297981 A JPS6297981 A JP S6297981A JP 60236943 A JP60236943 A JP 60236943A JP 23694385 A JP23694385 A JP 23694385A JP S6297981 A JPS6297981 A JP S6297981A
Authority
JP
Japan
Prior art keywords
water
membrane
porous membrane
hydrophilic
hydrophobic porous
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.)
Pending
Application number
JP60236943A
Other languages
Japanese (ja)
Inventor
元 伊藤
和民 三谷
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP60236943A priority Critical patent/JPS6297981A/en
Publication of JPS6297981A publication Critical patent/JPS6297981A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は水処理や血液浄化等の分野で使用さ扛る疎水性
多孔質膜の親水化方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for hydrophilizing a hydrophobic porous membrane used in fields such as water treatment and blood purification.

し従来の技術〕 疎水性多孔質膜は磯緘的性質や耐薬品性か優扛ているた
めに、その適用分野が急速に拡大している。しかし、疎
水性多孔質膜は水を透過させることが僻しく、水を始め
とする親水性液体を透過させるためには親水化処理が必
要である。
BACKGROUND ART Hydrophobic porous membranes have excellent barrier properties and chemical resistance, so the fields of their application are rapidly expanding. However, it is difficult for hydrophobic porous membranes to allow water to pass through them, and a hydrophilic treatment is required to allow water and other hydrophilic liquids to pass through them.

疎水性物質の表面改質による親水化法については、棹々
の方法が検討さnているが、表面形状が複雑な多孔質族
の親水化に対して表面が滑らかなフィルム状物等の親水
化法を単純に適用することは出来ない。
As for the method of making hydrophilic materials by surface modification of hydrophobic substances, several methods have been studied, but in contrast to making porous materials with complex surface shapes, hydrophilic materials such as film-like materials with smooth surfaces have been studied. It is not possible to simply apply the conversion method.

疎水性多孔’J[膜の親水化法とじてに、(1)有機溶
剤湿潤・水置換法、(2)物理的吸着法、及び(3)化
学的表面変性法が知らnている。有機溶剤湿潤・水置換
法は、水との相溶性が艮好なアルコールやケトン等の有
機溶剤によってポリオレフィン等の疎水性多孔質膜の微
細孔部金倉めた表面全体を湿潤処理した後、該有機溶剤
を水で置換する方法であるが、この方法では保存中や使
用中に細孔内の水が抜けるとその部分に書度水會光窺す
ことかできなくなるので、多孔質膜の周囲に常時水を光
たしておくことが必要であり、取り扱いが煩雑である。
Hydrophobic pores [Methods for making membranes hydrophilic include (1) organic solvent wetting/water displacement method, (2) physical adsorption method, and (3) chemical surface modification method. The organic solvent wetting/water displacement method involves wetting the entire surface of a hydrophobic porous membrane such as polyolefin with an organic solvent such as alcohol or ketone that is highly compatible with water, and then applying the This method replaces the organic solvent with water, but with this method, if the water in the pores escapes during storage or use, it becomes impossible to see the water in that area, so the surrounding area of the porous membrane is It is necessary to keep water shining at all times, and handling is complicated.

物理的吸着法は特開昭54−153872号や特開昭5
9−24732号に記載さnているが、ポリエチレング
リコールや界面活性剤等の親水性物質?多孔質膜の表面
に吸着させて多孔質膜に親水性を付与する方法であり、
操作が簡単であるという利点を有している。
The physical adsorption method is described in JP-A-54-153872 and JP-A-5.
Although it is described in No. 9-24732, is it a hydrophilic substance such as polyethylene glycol or surfactant? This is a method to impart hydrophilicity to a porous membrane by adsorbing it to the surface of the porous membrane.
It has the advantage of being easy to operate.

しかし、界面活性剤やポリエチレングリコール金吸着さ
せた多孔質膜を用いて血液処理等を行なう場合は、該吸
着物質の脱離・溶出が問題となるので、これらの親水性
物質の使用は好ましくない。
However, when blood treatment is performed using a porous membrane adsorbed with surfactant or polyethylene glycol gold, the use of these hydrophilic substances is not recommended because the desorption and elution of the adsorbed substances becomes a problem. .

化学的表面変性法としては、オゾンや過マンガン酸塩等
の酸化剤あるいはコロナ放電を利用して多孔質膜表面を
酸化変性する方法が知られているが、膜基質の酸化劣化
か不可避であり、多孔質膜の強度が低下するという欠点
を有している。
As a chemical surface modification method, a method is known in which the porous membrane surface is oxidized and modified using an oxidizing agent such as ozone or permanganate or corona discharge, but oxidative deterioration of the membrane substrate is inevitable. However, it has the disadvantage that the strength of the porous membrane is reduced.

〔発明か解決しようとする問題点3 以上述べ友ように、有機溶剤湿潤・水置換法や物理的吸
着法では親水性の寿命不足、酸化法でt1膜基質の頻度
低下等が問題であり、現在のところ疎水性多孔質膜に対
する有効な親水化法は確立さnていない。
[Problem to be Solved by the Invention 3] As mentioned above, organic solvent wetting/water displacement methods and physical adsorption methods have problems such as insufficient hydrophilic life, and oxidation methods have problems such as a decrease in the frequency of t1 membrane substrates. At present, no effective method for imparting hydrophilic properties to hydrophobic porous membranes has been established.

本発明の目的は、従来技術が持つ酊述の問題点を解消し
、疎水性多孔質膜の強度低下を招くことなく、細孔内部
′に含めた表面全体にわたって親水化処理することり能
にし友ポリオレフィン多孔質膜の親水化法を提供するこ
とにある。
The purpose of the present invention is to solve the problem of drunkenness in the prior art, and to provide a hydrophobic porous membrane that can be hydrophilized over the entire surface contained in the pores without reducing the strength of the membrane. An object of the present invention is to provide a method for making a porous polyolefin membrane hydrophilic.

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

上記の目的金違取するため、本発明省等に工程が簡単な
物理的吸着法について詳細な検討を進め本発明に到達し
た。本発明の要旨は、疎水性多孔質膜を水溶性蛋白質で
処理すること全特徴とする疎水性多孔質膜の親水化方法
にめる・本発明の疎水性多孔質膜に用いらnる疎水性材
料としては、エチレン、プロピレン、4−メチル−1−
ペンテン、3−メチル−1−ブテン、テトラフルオロエ
チレン、フッ化ビニリデン等の群から選ばnる重合体や
共i置体を挙げることができる。
In order to solve the above-mentioned problem, the Ministry of the Invention and others conducted a detailed study on a physical adsorption method with a simple process and arrived at the present invention. The gist of the present invention is to provide a method for making a hydrophobic porous membrane hydrophilic, which is characterized by treating the hydrophobic porous membrane with a water-soluble protein. Ethylene, propylene, 4-methyl-1-
Examples include polymers selected from the group of pentene, 3-methyl-1-butene, tetrafluoroethylene, vinylidene fluoride, and co-positional polymers.

また水溶性蛋白質としてはアルブミン、グロブリン、プ
ロラミン、グルテリン、ヒストン、プロタミン、硬タン
パン質等t−挙げることができるが、こnらの中でも特
に血清、乳あるいは卵白中のアルブミンやグロブリンか
好適である。
Examples of water-soluble proteins include albumin, globulin, prolamin, glutelin, histone, protamine, and hard protein, among which albumin and globulin found in serum, milk, or egg white are particularly preferred. .

本発明は水浴性蛋白質全官有する溶液上用いて、疎水性
多孔質Mを処理することにより実施することができる。
The present invention can be carried out by treating the hydrophobic porous M using a solution containing all of the water bathing proteins.

水浴性蛋白質を溶解させる溶媒としては水または生理的
食塩水を用いることかできる。溶液中の該蛋白質の濃度
はおよそα1〜10重量係が適当であり、濃度かこの範
囲より小さいと十分な親水化が達成できない@ま文濃度
がこの範囲より大きくても親水化効果は特別に増大せず
、むしろ過剰に吸着さnた蛋白質あるいは細孔内に残留
している蛋白質が多孔質膜の透水性能を低下させる場合
が多いので好ましくない。処理方法としては、疎水性多
孔質膜を該溶液中に浸漬する方法、あるいはモジュール
化した疎水性多孔質膜に該浴液を圧入する方法金挙げる
ことかできるが、必ずしもこnらの方法に限定さnない
Water or physiological saline can be used as a solvent for dissolving the water bath protein. The appropriate concentration of the protein in the solution is approximately α1 to 10 by weight, and if the concentration is lower than this range, sufficient hydrophilization cannot be achieved. Even if the concentration is higher than this range, the hydrophilization effect will be particularly Proteins that do not increase but are excessively adsorbed or proteins that remain in the pores often deteriorate the water permeability of the porous membrane, which is not preferable. Treatment methods include a method of immersing a hydrophobic porous membrane in the solution, or a method of pressurizing the bath liquid into a modularized hydrophobic porous membrane, but these methods do not necessarily apply. Not limited.

本発明の親水化法の特徴としては、(1)水または生理
的食塩水を溶媒として使用できること、(2)水溶性蛋
白質が界面活性に’FjL疎水性多孔質膜の細孔部分に
浸透して表面に吸着するので疎水性多孔質膜のほぼ全面
に親水性を付与でさること、(3)該吸着力が強大であ
るので、水中あるいは有機溶剤中においても水浴性蛋白
質は多孔質膜から容易には脱離せず、はぼ恒久的な親水
性全保持できること、(4)水浴性蛋白質が生体適合v
lJ5にであり、人体に対する有害性がないので仮に脱
離・浴出しても全く問題が生じないこと等を挙げること
ができる。
The characteristics of the hydrophilization method of the present invention include (1) water or physiological saline can be used as a solvent, and (2) water-soluble proteins penetrate into the pores of the FjL hydrophobic porous membrane due to surface activity. (3) Since the adsorption power is strong, bathing proteins can be absorbed from the porous membrane even in water or organic solvents. (4) The water-bathable protein is biocompatible;
1J5 and is not harmful to the human body, so even if it were to be desorbed or bathed, no problems would occur.

し実施例〕 以下実施例によって本発明を具体的に説明する。Example] EXAMPLES The present invention will be specifically explained below with reference to Examples.

尚、実施例において透水圧、水透過率及びアルコール親
水化法での水透過率はそn(Jn有効膜面積か163d
の試験膜モジュールを用い矢の方法により、1九引張破
断強度も次の方法により求め九〇 (1)  透水圧:試験膜モジュールの一方(中空糸膜
の場合は中空糸膜の内側)から水圧を上げながら25℃
の水を供給し、透過水量が30−と5011&tになる
時の水圧金側足する0絖いて横軸に水圧を、また縦軸に
透過水量をプロットし、プロットした2点を結ぶ直線が
横軸と交わる点の圧力個を求めその値を透水圧とする。
In addition, in the examples, water permeability, water permeability, and water permeability in the alcohol hydrophilization method are calculated as follows:
19 Tensile breaking strength was also determined by the following method using the test membrane module of 25℃ while increasing
Water is supplied, and the water pressure when the amount of permeated water becomes 30- and 5011 Find the pressure at the point where it intersects with the axis and use that value as the hydraulic pressure.

(2)水迅過単:試験膜モジュールの一方(中空糸膜の
場合は中空糸膜の内側)から25℃の水ft61tし、
膜間差圧が50mmHg  になる時の透過水量を測定
し、その石から水透過率(1重mt−hr−IllIH
g)を求める。
(2) Water flow: 61 tons of 25°C water from one side of the test membrane module (inside the hollow fiber membrane in the case of a hollow fiber membrane),
Measure the amount of permeated water when the transmembrane pressure is 50 mmHg, and calculate the water permeability (1 mt-hr-IllIH) from the stone.
Find g).

(3)  アルコール親水化法での水透過率:親水化処
理していない試験膜モジュールの一方(中空糸膜の場合
は中空糸膜の内N)刀為らエタノールf 25 tag
/ minの流量で15分曲圧入して多孔質膜の細孔部
まで充分にエタノールで湿潤さぞた後、水を100 d
/minの流量で15分間流し、細孔内部に存在するエ
タノール金水で置換する。続いて(2)に記載し九方法
により水透過率全測定する。
(3) Water permeability by alcohol hydrophilization method: One of the test membrane modules that has not been hydrophilized (in the case of a hollow fiber membrane, the inner part of the hollow fiber membrane) is ethanol f 25 tag
/min for 15 minutes to fully wet the pores of the porous membrane with ethanol, and then add 100 d of water.
/min for 15 minutes to replace the ethanol and gold water present inside the pores. Subsequently, the total water permeability was measured by the nine methods described in (2).

(4)引張破断強度:引張試験器音用い試長を100■
、引張速度を50■/ m i nとして引張破断時の
応力値を測定し、こfL’に引張破断強度とする。
(4) Tensile breaking strength: using a tensile tester with a test length of 100cm
The stress value at tensile breakage was measured at a tensile speed of 50 mm/min, and this fL' was defined as the tensile strength at break.

実施例1 空孔率70チ、膜厚42μmのポリエチレン多孔質平膜
を血清アルブミン會1重is言肩する生理的食塩水浴液
中に2分間浸漬し友。続いて該多孔質膜を流水中で48
時間洗浄した後、常温減圧下で乾燥して親水化処理さr
Lzポリエチレン多孔質膜を得た。次に、試験膜モジュ
ールによって透水圧及び水透過率を測定し第1表の結果
を得た。第1表において、親水化処理後の透水圧は親水
化処理前と比較すると著しく低下しており、また親水化
処理後の水透過率はアルコール親水化法による水透過も
と殆んど同程度であり、本実施例の親水化処理が極めて
有効であることかわかる。
Example 1 A polyethylene porous flat membrane with a porosity of 70 mm and a membrane thickness of 42 μm was immersed for 2 minutes in a physiological saline bath solution with a serum albumin concentration. Subsequently, the porous membrane was soaked in running water for 48 hours.
After washing for several hours, it is dried at room temperature and under reduced pressure to make it hydrophilic.
An Lz polyethylene porous membrane was obtained. Next, the water permeability pressure and water permeability were measured using the test membrane module, and the results shown in Table 1 were obtained. In Table 1, the water permeability after the hydrophilic treatment is significantly lower than before the hydrophilic treatment, and the water permeability after the hydrophilic treatment is almost the same as that by the alcohol hydrophilic method. It can be seen that the hydrophilic treatment of this example is extremely effective.

次に親水化処理品の耐久性評価全目的として該親水化処
理後の試験膜モジュールを用いて流950 ml/ m
i nにて200時間水k fjtLした後、エタノー
ル中に1分間浸漬し、常温減圧下で乾保し、同様にして
透水圧を水透過率全測定し、第1表の1[k得た。第1
表においてエタノール洗浄後の透水圧と水透過率は親水
化処理直後の頓と殆んど同じであり、本実施例親水化処
理品の耐久性が十分であることがわかる。
Next, for the purpose of evaluating the durability of the hydrophilized product, a flow rate of 950 ml/m was applied using the test membrane module after the hydrophilic treatment.
After soaking in water for 200 hours, it was immersed in ethanol for 1 minute, kept dry under reduced pressure at room temperature, and the water permeability and water permeability were measured in the same manner. . 1st
In the table, the water permeability pressure and water permeability after ethanol washing are almost the same as those immediately after the hydrophilic treatment, and it can be seen that the durability of the hydrophilized product of this example is sufficient.

実施例2 空孔量68%、膜厚60μm1内径2° 、ir/1の
ポリエチレン斧孔質中空糸J[−用いて、1(゛効膜面
槓165iの試験膜モジュールを製作し、該中空糸膜の
内側から卵白アルブミン七2重f[%含有する水浴液t
−25vd/minで5分間圧入徴用した。絖いて、同
様にして該中空糸膜の内側から水i 100−/min
で1重分間圧入洗浄した彼、常温減圧下で乾燥すること
によって親水化処理さnたポリエチレン多孔質中空糸膜
を得た。
Example 2 A test membrane module with an effective membrane surface of 165 i was fabricated using a polyethylene ax porous hollow fiber J[-] with a pore content of 68%, a membrane thickness of 60 μm, an inner diameter of 2°, and an IR/1. A water bath solution containing ovalbumin 72 times F [%] from the inside of the thread membrane.
Pressure was applied for 5 minutes at −25 vd/min. Similarly, water was added from the inside of the hollow fiber membrane at a rate of 100-/min.
A polyethylene porous hollow fiber membrane which had been subjected to a hydrophilic treatment was obtained by press-fitting the membrane for 1 minute and drying it at room temperature under reduced pressure.

次に親水化処理前後の試験膜モジュールによって透水圧
を測定し、纂1表の結果を得た◎第1表において、親水
化後の透水圧は親水化前の透水圧と比較すると著しく低
下しており、十分に親水化さnていることかわかる。
Next, we measured the permeability pressure using the test membrane module before and after the hydrophilic treatment, and obtained the results shown in Table 1.◎In Table 1, the permeable pressure after the hydrophilic treatment was significantly lower than that before the hydrophilic treatment. It can be seen that it has been sufficiently hydrophilized.

次に実施例1と全く同様にして、親水化処理後の試験膜
モジュールを用いてエタノール洗浄、常温減圧乾燥を実
施し、透水圧と水透過率を測定した。第1表においてエ
タノール洗浄後の透水圧と水透過率は親水化処理直後の
値と殆んど同じであり、本実施例親水化処理品の耐久性
か十分であることがわかる。
Next, in exactly the same manner as in Example 1, the test membrane module after the hydrophilic treatment was washed with ethanol and dried under reduced pressure at room temperature, and the water permeability pressure and water permeability were measured. In Table 1, the water permeability pressure and water permeability after ethanol washing are almost the same as the values immediately after the hydrophilization treatment, which indicates that the durability of the hydrophilization treated product of this example is sufficient.

ま友親水化処理前後の膜の引張破断強度全開=。Full tensile breaking strength of the membrane before and after hydrophilic treatment.

定したところ、両省とも7.5 K9/ 踵2であり梗
水化処理によって膜強度か低下しないことを確認した。
As a result, it was confirmed that the membrane strength was 7.5 K9/heel 2 in both cases, and the membrane strength did not decrease as a result of the water infestation treatment.

実施例3 空孔率45%、M厚22 pm、内径20011mのポ
リプロピレン多孔質中空糸膜と血清グロブリン全2重t
%含有する生理的食塩水浴液音用い、その他の条件は実
施例2と全く四−にして親水化処理、エタノール洗浄、
及び性能評価を実施し、第1表の結果を得九〇第1表よ
り本実施例親水化処理品の透水圧は良好であり、耐久性
が優nていることがわかる。
Example 3 Polypropylene porous hollow fiber membrane with porosity 45%, M thickness 22 pm, inner diameter 20011 m and serum globulin full double layer t
% of physiological saline bath solution was used, and the other conditions were the same as in Example 2. Hydrophilization treatment, ethanol washing,
and performance evaluation, and obtained the results shown in Table 1. From Table 1, it can be seen that the hydrophilic treated product of this example had good water permeability pressure and excellent durability.

〔発明の効果〕〔Effect of the invention〕

実施例の結果から明らかであるが、本発明の疎水性多孔
質膜の親水化法を採用することにより以下の効果か生じ
る。
As is clear from the results of the Examples, the following effects are produced by employing the method of making a hydrophobic porous membrane hydrophilic according to the present invention.

(1)アルコール親水化法と同程度の4&n7を親水性
を付与できる。
(1) Hydrophilicity can be imparted to 4&n7 to the same extent as with the alcohol hydrophilization method.

(2)吸着さnx水浴性蛋白質の脱離速度が非常に遅い
ので、長時間の使用が可能である。
(2) Since the rate of desorption of adsorbed nx water bath protein is very slow, it can be used for a long time.

(3)  水溶性蛋白質に人体に対して安全であるので
、仮に脱離・溶出し九としても全く問題が生じない。
(3) Water-soluble proteins are safe for the human body, so even if they are detached and eluted, no problems will occur.

Claims (1)

【特許請求の範囲】 1、疎水性多孔質膜を水溶性蛋白質で処理することを特
徴とする疎水性多孔質膜の親水化方法。 2、水溶性蛋白質がアルブミンまたはグロブリンである
ことを特徴とする特許請求の範囲第1項記載の疎水性多
孔質膜の親水化方法。
[Scope of Claims] 1. A method for making a hydrophobic porous membrane hydrophilic, which comprises treating the hydrophobic porous membrane with a water-soluble protein. 2. The method for making a hydrophobic porous membrane hydrophilic according to claim 1, wherein the water-soluble protein is albumin or globulin.
JP60236943A 1985-10-23 1985-10-23 Method for making hydrophobic porous membrane hydrophilic Pending JPS6297981A (en)

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JP60236943A JPS6297981A (en) 1985-10-23 1985-10-23 Method for making hydrophobic porous membrane hydrophilic

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Application Number Priority Date Filing Date Title
JP60236943A JPS6297981A (en) 1985-10-23 1985-10-23 Method for making hydrophobic porous membrane hydrophilic

Publications (1)

Publication Number Publication Date
JPS6297981A true JPS6297981A (en) 1987-05-07

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JP60236943A Pending JPS6297981A (en) 1985-10-23 1985-10-23 Method for making hydrophobic porous membrane hydrophilic

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62176508A (en) * 1985-11-01 1987-08-03 モンサント コンパニ− Surface modification of predetermined polymeric support material
JPH01242984A (en) * 1988-03-24 1989-09-27 Mitsubishi Electric Corp Beam profile monitor
WO1997000994A1 (en) * 1995-06-23 1997-01-09 Kimberly-Clark Worldwide, Inc. Modified polymeric material having improved wettability
JP2008510856A (en) * 2004-08-18 2008-04-10 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Amphiphilic and proteinaceous coatings on nanoporous polymers
JP2008307454A (en) * 2007-06-13 2008-12-25 Tosoh Corp Method for hydrophilizing substrate surface, hydrophilic member, and container and apparatus for handling microparticles employing the same
JP2018504507A (en) * 2014-11-14 2018-02-15 アテンズ ヘルスケア プロダクツ インコーポレイテッド Synthetic surfactant-free finishing agents, sheets with synthetic surfactant-free finishing agents, articles having sheets with synthetic surfactant-free finishing agents, and related methods

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62176508A (en) * 1985-11-01 1987-08-03 モンサント コンパニ− Surface modification of predetermined polymeric support material
JPH01242984A (en) * 1988-03-24 1989-09-27 Mitsubishi Electric Corp Beam profile monitor
WO1997000994A1 (en) * 1995-06-23 1997-01-09 Kimberly-Clark Worldwide, Inc. Modified polymeric material having improved wettability
JP2008510856A (en) * 2004-08-18 2008-04-10 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Amphiphilic and proteinaceous coatings on nanoporous polymers
JP2008307454A (en) * 2007-06-13 2008-12-25 Tosoh Corp Method for hydrophilizing substrate surface, hydrophilic member, and container and apparatus for handling microparticles employing the same
JP2018504507A (en) * 2014-11-14 2018-02-15 アテンズ ヘルスケア プロダクツ インコーポレイテッド Synthetic surfactant-free finishing agents, sheets with synthetic surfactant-free finishing agents, articles having sheets with synthetic surfactant-free finishing agents, and related methods

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