JPH0259032A - Surface modified film made of polysulfone and preparation thereof - Google Patents
Surface modified film made of polysulfone and preparation thereofInfo
- Publication number
- JPH0259032A JPH0259032A JP20956888A JP20956888A JPH0259032A JP H0259032 A JPH0259032 A JP H0259032A JP 20956888 A JP20956888 A JP 20956888A JP 20956888 A JP20956888 A JP 20956888A JP H0259032 A JPH0259032 A JP H0259032A
- Authority
- JP
- Japan
- Prior art keywords
- polysulfone
- membrane
- filtering
- irradiation
- ultraviolet rays
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野]
本発明はポリサルフオン製高分子多孔質膜の表面改質法
に関するものである。、疎水性基体であるポリサルフォ
ンからなる多孔質膜は機械的にも強く、熱的にも安定で
あり、′a過技術の多くの範囲に利用されている。しか
し、疎水性基体からなる股は、蛋白質の吸着を回避でき
ず、蛋白質による膜の孔の閉塞による濾過速度の急激な
低下は避けられないものであった。[Detailed Description of the Invention] "Industrial Application Field" The present invention relates to a method for surface modification of a porous polymer membrane made of polysulfone. It is strong and thermally stable, and is used in a wide range of membrane filtration technologies. However, the crotch made of a hydrophobic substrate cannot avoid protein adsorption, and the membrane pores are blocked by proteins. A sudden drop in the filtration rate was inevitable.
[従来の技術〕
ポリサルフォンを含む高分子多孔質膜の表面改質法は多
数報告されているが、代表的な例としてグラフト重合技
術を用いた例がある。高分子多孔質膜と重合性用M体と
適当な架橋剤を用いて表面処理する方法においては、膜
細孔の閉塞を回避しながら、表面特性を改質することは
困難である。[Prior Art] Many methods for surface modification of porous polymer membranes containing polysulfone have been reported, and a representative example is one using graft polymerization technology. In a surface treatment method using a porous polymer membrane, a polymerizable M-form, and an appropriate crosslinking agent, it is difficult to modify the surface properties while avoiding clogging of the membrane pores.
また、プラズマ放電処理を用いた表面グラフト法(特開
昭62−2G2705号公報、特開昭133−140(
i号公報)では、真空下での処理を必要とし、処理工程
、処理装置が繁雑であり工業的生産は非常に困難である
。In addition, surface grafting methods using plasma discharge treatment (JP-A-62-2G2705, JP-A-133-140)
Publication No. I) requires processing under vacuum, and the processing steps and processing equipment are complicated, making industrial production very difficult.
[発明が解決しようとする課題]
本発明は疎水性基体であるポリサルフォンの特徴である
物理的強度、耐薬品性を維持し、かつポリサルフォンか
ら形成される多孔質膜の大きな欠点である蛋白質の吸z
1による濾過速度の急激な低ドを解決し、高い濾過速度
を維持する表面改質膜及びその製造方法を提供するもの
である。[Problems to be Solved by the Invention] The present invention maintains the physical strength and chemical resistance that are characteristic of polysulfone, which is a hydrophobic substrate, and also eliminates protein absorption, which is a major drawback of porous membranes formed from polysulfone. z
The purpose of the present invention is to provide a surface-modified membrane that solves the sudden drop in filtration rate caused by No. 1 and maintains a high filtration rate, and a method for manufacturing the same.
[課題を解決するための手段]
本発明者は1−記の如き現状に鑑み鋭意研究した結果、
本発明に到達した。[Means for Solving the Problem] As a result of intensive research in view of the current situation as described in 1-1, the present inventor has found that
We have arrived at the present invention.
即ち、本発明はポリサルフォン製多孔質膜の多孔質(1
η造を閉塞により破壊することなく、多孔質膜表面に限
って表面改質することにより、ポリサルフォンの特徴で
ある物理的強度、耐薬品性を維持した高濾過速度を有す
る表面改質膜及びその製造)j法を提供するものである
。That is, the present invention provides a porous membrane made of polysulfone (1
By surface-modifying only the porous membrane surface without destroying the structure due to blockage, we have developed a surface-modified membrane that maintains the physical strength and chemical resistance that are characteristic of polysulfone, and has a high filtration rate. (manufacturing) method.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
ポリザルフォン製多孔質膜を水洗したのち、続いて紫外
線を照射することにより表面改質を行う。After washing the polysulfone porous membrane with water, the surface is modified by irradiating it with ultraviolet light.
表面改質に用いる紫外線源は10W程度のものから10
0[)W以」二のものまで適当な照射距離、照射時間を
用いることにより使用可能である。紫外線の照射は常1
M + 常圧下において行うものであり、特別な条件を
必要としないため、処理装置、処理工程も非常に簡便な
ものである。The ultraviolet light source used for surface modification ranges from about 10W to 10W.
It is possible to use up to 0[)W or more by using an appropriate irradiation distance and irradiation time. UV irradiation is always 1
M + Since it is carried out under normal pressure and does not require special conditions, the processing equipment and processing steps are also very simple.
紫外線の照射時間は紫外線の照射距離1強度に依存する
が、例えば紫外線強度GOOW、照射距離25cmの場
合、1〜20分間の照射処理が適当であり、−ガに好ま
しくは3〜IO分間である。照射時間が短ずぎるとその
効果はあられれず、長すぎると表面親水化がさまたげら
れ、]]的とする性能が現れない。The irradiation time of ultraviolet rays depends on the irradiation distance and intensity of ultraviolet rays, but for example, when the intensity of ultraviolet rays is GOOW and the irradiation distance is 25 cm, irradiation treatment for 1 to 20 minutes is appropriate, and for -ga, it is preferably 3 to IO minutes. . If the irradiation time is too short, the effect will not be achieved, and if the irradiation time is too long, surface hydrophilization will be hindered, and the desired performance will not be achieved.
本発明で得られる表面改質膜の表面の純水による接触角
は60°以下、好ましくは35°以下である。また、護
膜は、蛋白質に対する親和力が極めて小さく、疎水性基
体であるポリサルフォン製多孔質膜の大きな欠点である
蛋白質の吸着による濾過速度の急激な低下を解決し、高
濾過速度を維持する。The contact angle of the surface of the surface-modified membrane obtained by the present invention with pure water is 60° or less, preferably 35° or less. In addition, the protective membrane has extremely low affinity for proteins and maintains a high filtration rate by solving the major drawback of porous membranes made of polysulfone, which is a hydrophobic substrate, by adsorbing proteins and causing a rapid decrease in filtration rate.
[発明の効果]
本発明によれば、常温3常圧下においてポリサルフォン
製多孔質膜に紫外線を照射するのみで多孔質膜表面の改
質が可能である。また、本発明により得られる表面の改
質されたポリサルフォン製多孔質膜は未処理のポリサル
フォン製多孔質膜に比較して、非常に高い濾過速度を維
持するものであるので護膜を用いることにより、蛋白質
の濾過など広範囲の濾過操作における濾過時間の大幅な
1d縮が可能である。[Effects of the Invention] According to the present invention, the surface of a porous membrane can be modified by simply irradiating the polysulfone porous membrane with ultraviolet rays at room temperature and pressure. In addition, since the surface-modified porous polysulfone membrane obtained by the present invention maintains a much higher filtration rate than an untreated polysulfone porous membrane, the use of a protective membrane It is possible to significantly reduce the filtration time by 1d in a wide range of filtration operations such as protein filtration.
[実施例]
本発明を更に詳細に説明するために、実施例を挙げるか
、本発明はこれら実施例に限定されるものではない。[Examples] Examples will be given to explain the present invention in more detail, but the present invention is not limited to these Examples.
実施例1
直径43111111.分画分子量300,000のポ
リサルフォン膜を水洗し、常温、常圧下において、紫外
線照射装置(ウシオ電気株式会社製、ミニキュア450
)を用い、紫外線強度eoow、照射距Is、25cm
にて1゜3.5.7分間紫外線照射処理を行った。得ら
れた4種類の膜に対し、0.5%γ−グロブリン。Example 1 Diameter 43111111. A polysulfone membrane with a molecular weight cut-off of 300,000 was washed with water and exposed to ultraviolet irradiation equipment (manufactured by Ushio Electric Co., Ltd., MiniCure 450) at room temperature and under normal pressure.
), UV intensity eoow, irradiation distance Is, 25cm
Ultraviolet irradiation treatment was performed at 1° for 3.5.7 minutes. 0.5% γ-globulin for the four types of membranes obtained.
0.3596牛血清アルブミン、 0.12%ミオグロ
ビン。0.3596 bovine serum albumin, 0.12% myoglobin.
(1、Ol 9jiビタミンB1□を生理食塩水に溶解
した蛋白質混合溶液50m1を用い、濾過装置(アドバ
ンテックン1.製、ウルトラホルダー 〇IIP−43
)により圧力1 kg l’/cfiにて限外d!i過
を行い、濾過速度の変化を調べ未処理膜との比較を行っ
た。(1. Using 50 ml of protein mixed solution in which Ol 9ji vitamin B1 □ was dissolved in physiological saline, use a filtration device (manufactured by Advantechn 1., Ultra Holder 〇IIP-43)
), the limit d! at a pressure of 1 kg l'/cfi! The membrane was subjected to i-filtration, and changes in filtration rate were examined and compared with untreated membranes.
未処理ポリサルフ+ン膜と表面改質膜の純水による接触
角を測定したところ表1に示すように、紫外線照射時間
が長くなるに従い、接触角は小さくなり紫外線照射時間
5分で接触角か最小値をとり膜表面が親水化され表面改
質か行イ〕れていることか確認できた。The contact angle of untreated polysulfone film and surface-modified film with pure water was measured, and as shown in Table 1, the contact angle decreased as the UV irradiation time increased, and the contact angle decreased after 5 minutes of UV irradiation. By taking the minimum value, it was confirmed that the membrane surface was made hydrophilic and surface modification was carried out.
表1
また、未処理ポリサルフォン膜と表面改質膜の濾過速度
をflll+定したところ図1に示すように、表面改質
膜においては、未処理膜に比べ常に高い濾過速度を維持
しており、蛋白質による膜孔の閉塞が抑制されているこ
とが確認でき、接触角が最小(1(〜を示した紫外線1
(−(対時間5分において濾過速度の最大値がみられた
。Table 1 In addition, when the filtration rates of the untreated polysulfone membrane and the surface-modified membrane were determined as shown in Figure 1, the surface-modified membrane always maintained a higher filtration rate than the untreated membrane. It was confirmed that the blockage of membrane pores by proteins was suppressed, and the contact angle was the minimum (1 (~1)
(-(The maximum value of the filtration rate was observed at 5 minutes relative to the time.
゛実施例2
直径43n++++、分画分子量1,000,000の
ポリサルフォン膜を水洗し、常温、常圧下において、紫
外線強+ieoow、照射距+t125cmにて5分間
紫外線照射処理を行った。得られた膜に対し、0.1%
−ブルーデキストラン(分子量2,000,000 )
溶液50歳を用い、濾過装置(アトバンチツク社製、ウ
ルトラホルダー UIIP−43) +、:より、圧力
1 kg r/cd f、: ”C限外濾過を行い、濾
過速rUの変化を調べ未処理膜との比十′ンを?−1っ
jこ。Example 2 A polysulfone membrane having a diameter of 43n+++ and a molecular weight cut off of 1,000,000 was washed with water and subjected to ultraviolet irradiation treatment for 5 minutes at room temperature and pressure at a strong ultraviolet ray +ieoow and an irradiation distance of 125 cm. 0.1% for the obtained film
-Blue dextran (molecular weight 2,000,000)
Using a 50-year-old solution, a filtration device (Ultra Holder UIIP-43 manufactured by Atvanchik Co., Ltd.) +,:, pressure 1 kg r/cd f,: "C ultrafiltration was performed, and changes in filtration rate rU were examined. The ratio with the membrane is ?-1.
未処理ポリサリフオン膜と表面改質膜の濾過速度を41
1定したところ図2に示すように、表面改質膜において
は、未処理膜に比べ常に高い濾過速度を維持しており、
表面改質膜の有効性が認められた。The filtration rate of untreated polysaliphon membrane and surface-modified membrane was 41
As shown in Figure 2, the surface-modified membrane always maintains a higher filtration rate than the untreated membrane.
The effectiveness of the surface modified membrane was confirmed.
実施例3
直径43 mm 、分画分子=to、oooのポリサル
フオン膜を水洗し、常温、常圧下において、紫外線強度
tioOW、照射距離25cmにて1,3.5分間紫外
線照射処理を行った。得られた3種類の膜に対し、実施
例1と同様の試料溶液50m1を用い、圧力1kgf/
e4にて限外濾過を行い、濾過速度の変化を調べ未処理
膜との比較を行った。Example 3 A polysulfon membrane having a diameter of 43 mm and molecular fractions of to and ooo was washed with water and subjected to ultraviolet irradiation treatment at room temperature and pressure at an ultraviolet intensity of tioOW and an irradiation distance of 25 cm for 1.3.5 minutes. For the three types of membranes obtained, 50ml of the same sample solution as in Example 1 was used, and a pressure of 1kgf/
Ultrafiltration was performed using e4, and changes in filtration rate were examined and compared with untreated membranes.
未処理ポリサルフォン膜と表面改質膜の濾過速度を測定
したところ図3に示すように、表面改質膜においては、
未処理膜に比べ非常に高い濾過速1ヶを維持しており、
蛋白質による膜孔の閉塞が抑制されていることが確認で
きる。The filtration rates of the untreated polysulfone membrane and the surface-modified membrane were measured, and as shown in Figure 3, the surface-modified membrane had a
It maintains a very high filtration rate compared to untreated membranes,
It can be confirmed that the clogging of membrane pores by proteins is suppressed.
図1.2.3はそれぞれ実施例1,2.3における表面
改質膜と未処理膜の濾過時間に伴う濾過速度の変化を示
すものである。
図1
図2
O:未処理膜
・:紫外線5分照射Figures 1.2.3 show changes in filtration rate with filtration time for the surface-modified membrane and untreated membrane in Examples 1 and 2.3, respectively. Figure 1 Figure 2 O: Untreated film: UV irradiation for 5 minutes
Claims (2)
。(1) A surface-modified polysulfone membrane with a hydrophilic surface.
とを特徴とする特許請求の範囲第(1)項記載の表面改
質膜の製造方法。(2) The method for producing a surface-modified membrane according to claim (1), which comprises irradiating the polysulfone porous membrane with ultraviolet rays.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20956888A JPH0259032A (en) | 1988-08-25 | 1988-08-25 | Surface modified film made of polysulfone and preparation thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20956888A JPH0259032A (en) | 1988-08-25 | 1988-08-25 | Surface modified film made of polysulfone and preparation thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0259032A true JPH0259032A (en) | 1990-02-28 |
Family
ID=16574987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20956888A Pending JPH0259032A (en) | 1988-08-25 | 1988-08-25 | Surface modified film made of polysulfone and preparation thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0259032A (en) |
-
1988
- 1988-08-25 JP JP20956888A patent/JPH0259032A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6319404B1 (en) | Process for the preparation of porous material and porous material | |
| US4675384A (en) | Fractionation/purification of plasma by ion exchange chromatography | |
| US5667684A (en) | Material for removing HIV and its related substances | |
| EP1439212B1 (en) | Hydrophilic material and process for producing the same | |
| EP3141296A1 (en) | Hollow fiber membrane module and manufacturing method thereof | |
| JP2001524878A (en) | Method and substance for purifying physiological fluid of an organism and method for producing the substance | |
| EP0561379A1 (en) | Filter medium having a limited surface negative charge for treating a blood material | |
| US5187010A (en) | Membrane having high affinity for low density lipoprotein-cholesterol from whole blood | |
| JPS62179540A (en) | Nonadsorptive hydrophilic membrane | |
| EP0424698B1 (en) | Adsorbent for removing biomacromolecules, particularly LDL and endotoxines, from whole blood in extracorporeal circuit | |
| JP5332230B2 (en) | Blood processing column | |
| JP2686949B2 (en) | Selective adsorption functional microfilter and its manufacturing method | |
| JP2006198611A (en) | Separation membrane production method and separation membrane module production method using the separation membrane | |
| JPH0259029A (en) | Porous membrane having hydrophilic surface and preparation thereof | |
| GB2025385A (en) | Activated carbon and apparatus for hemoperfusion | |
| EP4316646A1 (en) | Porous adsorbent material, separation column using same for purifying biopharmaceutical, and method for manufacturing biopharmaceutical | |
| JPH02132132A (en) | Porous membrane having selective adsorptivity of anion and production thereof | |
| JPS631406A (en) | Nonadsorptive hydrophilic semipermeable membrane and its production | |
| JPS6331501A (en) | Composite semipermeable membrane and its production | |
| JP3810664B2 (en) | Method for producing perforated hollow fiber | |
| JP4569315B2 (en) | Modified hollow fiber membrane | |
| JP3648261B2 (en) | Method for treating hemoglobin-containing aqueous solution | |
| RU2325944C1 (en) | Method of production of track membrane | |
| JP3246681B2 (en) | Transthyretin adsorbent | |
| JPH0611325B2 (en) | Porous hollow fiber membrane |