JPH02293031A - Hydrophilic porous hollow fiber membrane - Google Patents
Hydrophilic porous hollow fiber membraneInfo
- Publication number
- JPH02293031A JPH02293031A JP11200689A JP11200689A JPH02293031A JP H02293031 A JPH02293031 A JP H02293031A JP 11200689 A JP11200689 A JP 11200689A JP 11200689 A JP11200689 A JP 11200689A JP H02293031 A JPH02293031 A JP H02293031A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber membrane
- porous hollow
- water
- 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
Links
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 112
- 239000012528 membrane Substances 0.000 title claims abstract description 89
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 45
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 45
- 229910052709 silver Inorganic materials 0.000 claims abstract description 39
- 239000004332 silver Substances 0.000 claims abstract description 39
- 239000010409 thin film Substances 0.000 claims description 40
- 239000011148 porous material Substances 0.000 abstract description 37
- 239000003651 drinking water Substances 0.000 abstract description 10
- 235000020188 drinking water Nutrition 0.000 abstract description 10
- 235000013305 food Nutrition 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 81
- 238000001914 filtration Methods 0.000 description 53
- 235000018102 proteins Nutrition 0.000 description 41
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 33
- 230000035699 permeability Effects 0.000 description 33
- 239000005018 casein Substances 0.000 description 28
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 28
- 235000021240 caseins Nutrition 0.000 description 28
- 230000002209 hydrophobic effect Effects 0.000 description 19
- 238000000034 method Methods 0.000 description 19
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 15
- 230000003385 bacteriostatic effect Effects 0.000 description 15
- -1 polyethylene Polymers 0.000 description 14
- 235000019441 ethanol Nutrition 0.000 description 11
- 239000007864 aqueous solution Substances 0.000 description 10
- 230000000844 anti-bacterial effect Effects 0.000 description 9
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 8
- 239000004698 Polyethylene Substances 0.000 description 7
- 229920000573 polyethylene Polymers 0.000 description 7
- 239000002344 surface layer Substances 0.000 description 7
- 239000011347 resin Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 239000010408 film Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 239000010410 layer Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 229910001961 silver nitrate Inorganic materials 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 230000035622 drinking Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 229920002492 poly(sulfone) Polymers 0.000 description 3
- 244000068988 Glycine max Species 0.000 description 2
- 235000010469 Glycine max Nutrition 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 230000001112 coagulating effect Effects 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000007772 electroless plating Methods 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 235000013336 milk Nutrition 0.000 description 2
- 239000008267 milk Substances 0.000 description 2
- 210000004080 milk Anatomy 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 239000012460 protein solution Substances 0.000 description 2
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- 108010076119 Caseins Proteins 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 108010058643 Fungal Proteins Proteins 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 241000084978 Rena Species 0.000 description 1
- 241000191967 Staphylococcus aureus Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 150000003457 sulfones Chemical class 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000001771 vacuum deposition Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
Landscapes
- External Artificial Organs (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Artificial Filaments (AREA)
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、水の′I11通用として好適な多孔質中空糸
Mに関し、詳しくは、多孔質膜の細孔表面に蛋白質薄膜
が形成されていることによって、良好な親水性を継続的
に安定して有し、かつ飲料水製造用の濾過モジュールの
濾過膜としても好適な多孔質中空糸膜に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a porous hollow fiber M suitable for use with water. The present invention relates to a porous hollow fiber membrane which continuously and stably has good hydrophilicity due to the presence of water, and which is also suitable as a filtration membrane for a filtration module for producing drinking water.
[従来の技術]
従来より、多孔質中空糸を水の濾過膜として用いる場合
、例えばポリエチレン、ボリプロビレン、ボリスルホン
、ポリカーボネート、ポリフッ化ビニリデン、ポリテト
ラフルオルエチレン等からなる疎水性の多孔質中空糸に
おいては、使用而にアルコール等の親水化剤で親水化す
る必要がある。[Prior Art] Conventionally, when porous hollow fibers are used as water filtration membranes, for example, in hydrophobic porous hollow fibers made of polyethylene, polypropylene, borisulfone, polycarbonate, polyvinylidene fluoride, polytetrafluoroethylene, etc. must be made hydrophilic with a hydrophilic agent such as alcohol before use.
ところが、このような方法で処理した多孔質中空糸の親
木性は不安定であり、例えば、水を長期間!2!!通し
た後の洗浄処理時に濾過器から水を抜き取り、これを一
時的に放置し、多孔質中空糸を乾燥させた場合,親水性
が大きく低下して良好な透水性が得られなくなるという
欠点がある。However, the wood-philicity of porous hollow fibers treated with this method is unstable; for example, if water is not used for a long period of time! 2! ! If the water is removed from the filter during the washing process after passing through the filter and left temporarily to dry the porous hollow fibers, the disadvantage is that the hydrophilicity will be greatly reduced and good water permeability will not be obtained. be.
そこで、このような欠点がなく、親水性を継続的に安定
して有する多孔質中空糸の開発が強く要望されていた。Therefore, there has been a strong demand for the development of porous hollow fibers that do not have such drawbacks and have continuous and stable hydrophilicity.
この要望に答えるために、本発明者らは、疎水性の多孔
質中空糸に恒久親水性を付与した中空糸、すなわち、疎
水性多孔質中空糸の細孔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薄n党が形成されてな
る恒久親水性多孔質中空糸膜[特願昭59−12910
0号(特開昭61−810:J″+)]、疎水性多孔質
中空糸の細孔表面に酢酸セルロースからなる薄膜が形成
されてなる恒久親水性多孔質中空糸[特願昭59−16
4063号(特開昭61−42304号)]、疎水性中
空糸の細孔表面にセルロースからなる薄膜か形成されて
なる恒久親水性多孔質中空糸[特願昭59−15954
3号(特開昭61−35804号)]、疎水性多孔質中
空糸の細孔表面にエチレン・ビニルアルコール系樹脂か
らなる薄膜が形成されてなる恒久親水性多孔質中空糸[
特願昭59−245606号(特開昭61−12540
8号)])を開示した。In order to meet this demand, the present inventors created a hollow fiber that gave permanent hydrophilicity to a hydrophobic porous hollow fiber. Permanent hydrophilic porous hollow fiber membrane formed of a thin layer consisting of
No. 0 (Japanese Unexamined Patent Publication No. 61-810: J''+)], a permanent hydrophilic porous hollow fiber in which a thin film of cellulose acetate is formed on the pore surface of a hydrophobic porous hollow fiber [Patent Application No. 59-81- 16
No. 4063 (Japanese Unexamined Patent Publication No. 61-42304)], a permanent hydrophilic porous hollow fiber in which a thin film of cellulose is formed on the pore surface of a hydrophobic hollow fiber [Patent Application No. 15954-1982]
No. 3 (Japanese Unexamined Patent Publication No. 61-35804)], a permanent hydrophilic porous hollow fiber in which a thin film made of ethylene/vinyl alcohol resin is formed on the pore surface of a hydrophobic porous hollow fiber [
Patent Application No. 59-245606 (Japanese Patent Application No. 12540-1983
No. 8)]) was disclosed.
一方、従来より、銀は優れた制菌性を示し、銀表面では
細菌等の微生物が繁殖できないことが知られている。On the other hand, it has been known that silver exhibits excellent bactericidal properties and that microorganisms such as bacteria cannot grow on the silver surface.
この銀の特性を利用し、多孔質中空糸に制菌性を付与す
ることが可能である。Utilizing this characteristic of silver, it is possible to impart antibacterial properties to porous hollow fibers.
そのための方法として、例えば本発明者らによる特開昭
60−261502号公報(特願昭59−116572
号)には、多孔買ポリオレフィン中空糸の外壁面側表層
にある細孔表面に銀の薄膜を形成して制菌性を付与した
多孔質中空糸を水の濾通膜として用いた中空糸濾過モジ
ュールが本発明者らにより開示されている。As a method for this purpose, for example, the method disclosed in Japanese Patent Application Laid-Open No. 60-261502 (Japanese Patent Application No. 59-116572) by the present inventors
No.) describes hollow fiber filtration using porous hollow fibers, which have antibacterial properties by forming a thin silver film on the surface of the pores on the outer wall side of porous polyolefin hollow fibers, as a membrane for water filtration. A module is disclosed by the inventors.
更に、特開昭62−298406号公報(特願昭59−
142301号)には、中空糸の外壁面側表層にある細
孔表面への銀の薄膜形成をスパッタリングによって行な
う方法が開示されている。Furthermore, Japanese Patent Application Laid-Open No. 1983-298406 (Japanese Patent Application No. 1983-
No. 142301) discloses a method of forming a thin silver film on the surface of pores in the surface layer on the outer wall side of a hollow fiber by sputtering.
また、多孔質中空糸に銀を吸着させて制菌性を付与する
方法として、無電解メッキによって、中空糸壁の外壁面
側表層から中空部側圏層までの多孔買構造の全域にわた
って銀を固着させる方法も知られている。In addition, as a method for imparting antibacterial properties by adsorbing silver to porous hollow fibers, electroless plating is used to coat silver throughout the entire porous structure from the surface layer on the outer wall side of the hollow fiber wall to the sphere layer on the side of the hollow fiber. A method of fixing is also known.
[発明が解決しようとする課題]
上述のように、アルコール等の親水化剤で処理した多孔
質中空糸における欠点を解消するために、恒久親水性を
疎水性多孔質中空糸に付与する種々の方法が知られてい
る。[Problems to be Solved by the Invention] As mentioned above, in order to eliminate the drawbacks of porous hollow fibers treated with hydrophilic agents such as alcohol, various methods have been developed to impart permanent hydrophilicity to hydrophobic porous hollow fibers. method is known.
しかしながら、従来の方法によって恒久親水性が付与さ
れた多孔質中空糸の飲料水製造用の濾過膜としての使用
では生物に対する安全性は未だ確認されていないのが現
状である。However, the safety of porous hollow fibers imparted with permanent hydrophilicity by conventional methods as filtration membranes for producing drinking water has not yet been confirmed.
例えば、上述の本発明者らによって提供された恒久親水
性中空糸は、いずれも優れた恒久親水性を有しており、
工業用、特に精密機器工業用の水の濾通処理に有用であ
るが、これらの中空糸を用いて濾過処理した水が飲料水
用として安全かどうかについては未だ確認されていない
。For example, the permanent hydrophilic hollow fibers provided by the present inventors mentioned above all have excellent permanent hydrophilicity,
Although they are useful for filtering water for industrial use, especially for precision equipment, it has not yet been confirmed whether water filtered using these hollow fibers is safe for drinking water.
すなわち、これらの中空糸は、疎水性中空糸の多孔質細
孔表面に、上述した親水性樹脂の薄膜を形成した構成を
有するが、これら親水性樹脂が水の濾過過程で多孔質構
造表面から万一剥離して脱落し、それか濾過水中に混入
された場合、濾過水か飲料用として安全かどうかは確認
されていない。In other words, these hollow fibers have a structure in which a thin film of the above-mentioned hydrophilic resin is formed on the surface of the porous pores of the hydrophobic hollow fiber, but these hydrophilic resins are removed from the surface of the porous structure during the water filtration process. It has not been confirmed whether the filtered water is safe for drinking if it were to peel off and fall off, or if it were mixed into the filtered water.
そこで、飲料用としても安全な水を提供できる恒久親水
性を有する多孔質中空糸の開発が強く要望されている。Therefore, there is a strong demand for the development of porous hollow fibers with permanent hydrophilicity that can provide water that is safe for drinking.
一方、上述のように、多孔質中空糸に銀を利用して制菌
性を付与するための種々の方法が従来より検討されてい
るか、従来の方法はなお改善すべき問題を有している。On the other hand, as mentioned above, various methods have been studied for imparting antibacterial properties to porous hollow fibers using silver, and conventional methods still have problems that need to be improved. .
例えば、多孔質中空糸として前述のように疎水性のもの
が主に利用され、かつ金属銀自体も疎水性であるので、
銀が固定された多孔質中空糸は疎水性を示し、これを水
濾過に用いる際にはアルコール等の親水化剤による前処
理が必要となる。For example, as mentioned above, hydrophobic porous hollow fibers are mainly used, and metallic silver itself is also hydrophobic, so
The porous hollow fibers to which silver is fixed exhibit hydrophobicity, and when used for water filtration, pretreatment with a hydrophilic agent such as alcohol is required.
しかも、アルコール等の親水化剤によって付与された親
木性は前述したように安定性に欠ける。Furthermore, the wood-philicity imparted by a hydrophilizing agent such as alcohol lacks stability as described above.
また、前記特開昭60−261502号公報に記載され
ている真空蒸着法による多孔質中空糸の外壁面側表層へ
の銀の固定方法では、表層全域にわたって銀を均一に固
着させることが困難であり、銀の薄膜が形成されていな
い部分の発生が避けられない場合が多い。Furthermore, in the method of fixing silver to the surface layer on the outer wall side of the porous hollow fiber using the vacuum evaporation method described in JP-A-60-261502, it is difficult to fix silver uniformly over the entire surface layer. In many cases, the occurrence of areas where a thin silver film is not formed is unavoidable.
一方、特開昭62−298406号公報に記載さわてい
るスパッタリングによる銀の固定方法においても、多孔
質中空糸の外壁面側表層の全域にわたって銀を均一に固
着させることが困難であり、$11菌性が完全であると
はいえない。On the other hand, even in the method of fixing silver by sputtering described in JP-A-62-298406, it is difficult to fix silver uniformly over the entire surface layer on the outer wall side of the porous hollow fibers, and the cost is $11. It cannot be said that it is completely bacteriostatic.
更に、無電解メッキ法によって中空糸壁の全域にわたっ
て銀を固着させる方法では、細孔内において銀が還元析
出ざれるが、各細孔内における銀の析出量を中空糸壁の
全域にわたって調節することがむずかしく、析出した銀
による細孔の閉塞による透水性の著しい低下が避けられ
ない。Furthermore, in the method of fixing silver over the entire hollow fiber wall by electroless plating, silver is reduced and precipitated within the pores, but the amount of silver deposited within each pore is adjusted over the entire hollow fiber wall. This is difficult, and a significant decrease in water permeability due to the clogging of pores by precipitated silver is unavoidable.
本発明の目的は、上記した水濾過用として利用される従
来の多孔質中空糸における問題を解決し、継続的に安定
した親水性を有し、かつ飲料水製造用としての安全性に
ついても問題がない多孔質中空系膜を提供することにあ
る。The purpose of the present invention is to solve the above-mentioned problems with the conventional porous hollow fibers used for water filtration, to have continuously stable hydrophilicity, and to have safety problems for producing drinking water. The object of the present invention is to provide a porous hollow system membrane without any porosity.
本発明の他の目的は、銀による制菌性の付与に好通な構
造を有する水濾過用として好適な親水性多孔質中空糸膜
を提供することにある。Another object of the present invention is to provide a hydrophilic porous hollow fiber membrane suitable for water filtration and having a structure suitable for imparting bactericidal properties with silver.
本発明の他の目的は、継続的に安定した親水性及び飲料
水製造用としての安全性を有し、かつ制閑性においても
優れた水濾過用として好適な多孔質中空糸膜を提供する
ことにある。Another object of the present invention is to provide a porous hollow fiber membrane suitable for water filtration that has continuously stable hydrophilicity and safety for producing drinking water, and has excellent dryness control properties. There is a particular thing.
[課題を解決するための手段]
本発明の親水性多孔質中空糸膜は、多孔貿膜の少なくと
も一部の表面に蛋白質薄膜が形成されてなるものである
。[Means for Solving the Problems] The hydrophilic porous hollow fiber membrane of the present invention has a protein thin film formed on at least a portion of the surface of the porous fiber membrane.
本発明の親水性多孔質中空糸膜に保持された蛋白質薄膜
には必要に応じて銀を結合させることによって、制菌性
に優れた親水性多孔質中空糸膜を得ることができる。A hydrophilic porous hollow fiber membrane with excellent bacteriostatic properties can be obtained by bonding silver to the protein thin film held in the hydrophilic porous hollow fiber membrane of the present invention, if necessary.
本発明における多孔質膜の細孔表面には、中空糸壁の多
孔質構造からなる部分の細孔内表面及び細孔外表面が含
まれる。細孔外表面とは、具体的には中空糸壁の外壁面
及び中空部側内壁面に位置する表面である。The pore surface of the porous membrane in the present invention includes the pore inner surface and the pore outer surface of the porous structure portion of the hollow fiber wall. Specifically, the outer surface of the pore is a surface located on the outer wall surface of the hollow fiber wall and the inner wall surface on the hollow side.
又、少なくとも一部の細孔表面とは細孔内表面と外表面
の全部又は一部をいう。Moreover, at least a part of the pore surface refers to all or part of the inner surface and outer surface of the pore.
本発明の親水性多孔質中空糸膜の形成に用い得る多孔質
中空糸膜としては、例えば、ポリエチレン、ボリブロビ
レン、ボリスルホン、ポリエーテルスルホン、ポリカー
ボネート、ボリフッ化ビニリデン、ポリテトラフル才口
エチレン、ポリアミド、ポリイミド、ポリ塩化ビニル、
ポリメチルメタクリレート、セルロースアセテート等か
らなる微少空孔が中空糸壁の内壁面から外壁面へ相互に
つながる疎水性多孔質中空糸膜を好適なものとして挙げ
ることができる。Porous hollow fiber membranes that can be used to form the hydrophilic porous hollow fiber membrane of the present invention include, for example, polyethylene, polypropylene, polysulfone, polyethersulfone, polycarbonate, polyvinylidene fluoride, polytetrafluoroethylene, polyamide, polyimide, PVC,
Preferred examples include hydrophobic porous hollow fiber membranes in which micropores made of polymethyl methacrylate, cellulose acetate, etc. are interconnected from the inner wall surface to the outer wall surface of the hollow fiber wall.
疎水性多孔質中空糸膜に、均一・な蛋白質薄膜を形成さ
せるため、該蛋白質薄膜の形成処理に先立ち、一時的な
親水化処理を行なう方法が好ましく用いられる。In order to form a uniform protein thin film on a hydrophobic porous hollow fiber membrane, a method is preferably used in which a temporary hydrophilic treatment is performed prior to the protein thin film formation treatment.
多孔質中空糸膜の細孔表面に形成される蛋白質薄膜を構
成するタンパク質としては、例えば大qカゼイン、牛乳
カゼイン、ゼラチン、酵母蛋白質、とうもろこし蛋白質
、石油資化徴生物由来の蛋白質等の水に不溶性の蛋白質
が利用でき、なかでも工業的な生産性等を考慮した場合
、大豆カゼイン、牛乳カゼインか好適である。しかしな
がら、本発明において目的とされる蛋白質薄膜が形成で
きるものであれば、これらに限定されない。Examples of proteins constituting the protein thin film formed on the pore surface of the porous hollow fiber membrane include large q casein, milk casein, gelatin, yeast protein, corn protein, and proteins derived from petroleum-utilizing organisms. Insoluble proteins can be used, and soybean casein and milk casein are particularly suitable when considering industrial productivity. However, it is not limited to these as long as it can form the protein thin film aimed at in the present invention.
多孔質膜の細孔表面への蛋白質薄膜の形成は、例えば、
細孔表面に蛋白質の溶液を接触させて付着させ、その状
態で蛋白質を凝固させるための溶液に浸漬し、凝固蛋白
質の薄膜を細孔表面に被覆1−る方法によって行なうこ
とができる。Formation of a protein thin film on the pore surface of a porous membrane can be achieved by, for example,
This can be carried out by contacting and adhering a protein solution to the pore surface, immersing it in a solution for coagulating the protein, and coating the pore surface with a thin film of coagulated protein.
この方法における蛋白質溶液のpHや蛋白質濃度、凝固
剤の種類及びその濃度、凝固処理におけるpHや温度等
の条件などは、用いる蛋白質の種類に応じて適宜選択さ
れる。In this method, the pH and protein concentration of the protein solution, the type and concentration of the coagulant, and the conditions such as pH and temperature in the coagulation process are appropriately selected depending on the type of protein used.
例えば、カゼインの凝固薄膜を形成する場合、カセイン
のアルカリ性水溶液を多孔貿膜の細孔表面に接触させて
付着させた後、これを酸性水溶液等の凝固剤溶液に浸漬
してカセインを凝固させ、引き続き、水洗して乾燥させ
ることにより多孔貿膜の細孔表面にカゼインの薄膜を形
成させることができる。For example, when forming a coagulated thin film of casein, an alkaline aqueous solution of casein is brought into contact with the pore surface of the porous membrane, and then this is immersed in a coagulant solution such as an acidic aqueous solution to coagulate casein. Subsequently, by washing with water and drying, a thin film of casein can be formed on the surface of the pores of the porous membrane.
この場合、使用するカセインの濃度は0.5〜3ti%
の範囲が好ましい。In this case, the concentration of casein used is 0.5-3ti%
A range of is preferred.
カゼインの濃度が0.5重量%未満の場合には、多孔質
構造の有する表面均−なカゼインの薄1漠を形成するこ
とができず、良好な親水性の付与が困難である。When the concentration of casein is less than 0.5% by weight, it is impossible to form a thin layer of casein having a porous structure with a uniform surface, making it difficult to impart good hydrophilicity.
また、カゼインの濃度が3重量%を越える場合には、凝
固カゼイン量が多くなりすぎて、透水性の低下の原因と
なる孔の閉塞が生じゃすくなるので好ましくない。Further, when the concentration of casein exceeds 3% by weight, the amount of coagulated casein becomes too large, which is not preferable because the pores are likely to be clogged, which causes a decrease in water permeability.
なお、カゼイン以外の蛋白質においても、その濃度等を
適宜選択することによって、多孔質膜の細孔表面への均
一な蛋白質薄膜形成が可能となる。In addition, even for proteins other than casein, by appropriately selecting the concentration etc., it is possible to form a uniform protein thin film on the pore surface of the porous membrane.
上記構成を有する本発明の多孔質中空糸膜は、多孔質膜
の細孔表面に、アミノ基,カルボキシル基、水酸基等の
親水性の官能基に富む蛋白質の薄膜が形成されているた
めに優れた親水性を有し、良好な透水性を発揮できる。The porous hollow fiber membrane of the present invention having the above structure is excellent because a thin film of protein rich in hydrophilic functional groups such as amino groups, carboxyl groups, and hydroxyl groups is formed on the pore surface of the porous membrane. It has high hydrophilicity and can exhibit good water permeability.
蛋白質薄膜は、多孔質膜の細孔表面に均一に、しかもな
るべく薄く形成されることが、濾過における細孔の有効
容量を減少させず、良好な透水性を維持する上で好まし
い。It is preferable that the protein thin film be formed uniformly and as thinly as possible on the pore surface of the porous membrane in order to maintain good water permeability without reducing the effective capacity of the pores for filtration.
このような観点から、例えばカゼインの薄膜を形成する
場合には、上述したカゼインのアルカリ性水溶液を付着
させた多孔質膜の細孔表面を酸性水溶液中で湿式凝固処
理した後、水洗、乾燥させる方冫去が好適である。From this point of view, for example, when forming a thin film of casein, the pore surface of the porous membrane to which the above-mentioned alkaline aqueous casein solution is attached is subjected to wet coagulation treatment in an acidic aqueous solution, followed by washing with water and drying. Death is preferred.
この方法を用いれば、多孔質膜の細孔表面に少量の蛋白
質により均一な薄膜を形成させることが可能となり、良
好な遣水性を維持することができる。By using this method, it becomes possible to form a uniform thin film with a small amount of protein on the pore surface of the porous membrane, and good water repellency can be maintained.
本発明の多孔質中空糸膜において蛋白質薄膜は、多孔質
膜の細孔表面に対して良好な密着性を有し、濾過モジュ
ールに組み込んで水濾過に使用した際にも容易に剥離す
ることない。In the porous hollow fiber membrane of the present invention, the protein thin film has good adhesion to the pore surface of the porous membrane, and does not easily peel off when incorporated into a filtration module and used for water filtration. .
また、濾過モジュールの洗浄処理等において一旦乾燥し
た場合でも、本発明の蛋白質薄膜が保持された多孔質中
空糸1摸は引き続き良好な親水性を有しており、アルコ
ール等での親水化処理は不要である。In addition, even if the porous hollow fiber retaining the protein thin film of the present invention is once dried during the cleaning process of the filtration module, it continues to have good hydrophilicity, and hydrophilic treatment with alcohol etc. Not necessary.
更に、本発明における蛋白質薄膜は、いずれも食用とし
て供給されている材料からなるものであるので、例えば
飲料水の製造において、万一蛋白質薄膜が剥離して脱落
し、それが飲料用として供給される濾過水内に混入した
場合でも、該濾過水の飲料水としての安全性に問題はな
い。Furthermore, since the protein thin film in the present invention is made of materials that are supplied as food, for example, in the production of drinking water, in the unlikely event that the protein film peels off and falls off, it may not be supplied as a drink. Even if it is mixed into filtered water, there is no problem with the safety of the filtered water as drinking water.
一方、本発明の親水性多孔質中空糸膜は、多孔質膜の細
孔表面への銀の固定によって制菌性を得るのに好通な構
造を有する。On the other hand, the hydrophilic porous hollow fiber membrane of the present invention has a structure suitable for obtaining bacteriostatic properties by fixing silver to the pore surfaces of the porous membrane.
すなわち、蛋白質は銀イオンと結合しやすく、蛋白質を
硝酸銀水溶液中に浸漬すると銀イオンは蛋白質とキレー
ト結合し、蛋白質を凝固させる性質を有する。That is, protein easily binds to silver ions, and when the protein is immersed in an aqueous silver nitrate solution, the silver ions form a chelate bond with the protein and have the property of coagulating the protein.
従って、多孔質中空糸膜の細孔表面に形成さわた蛋白質
薄膜を銀イオンと接触させることによって、銀を蛋白質
薄膜に斑な〈結合させることができ、優れた制菌性を有
する多孔質中空糸膜を容易に得ることができる。Therefore, by contacting the protein thin film formed on the pore surface of the porous hollow fiber membrane with silver ions, silver can be unevenly bonded to the protein thin film, and the porous hollow fiber membrane has excellent bactericidal properties. Thread membranes can be easily obtained.
しかも、銀の蛋白質薄膜への結合によって多孔質中空糸
膜の親水性が損なわれることがないので、優れた親水性
、透水性及び制菌性を有する多孔買中空糸膜を得ること
ができる。Moreover, since the hydrophilicity of the porous hollow fiber membrane is not impaired by the binding of silver to the protein thin film, it is possible to obtain a porous hollow fiber membrane having excellent hydrophilicity, water permeability, and bacteriostatic properties.
蛋白質薄膜への銀の結合には、例えば、多孔質1liの
細孔表面に形成された蛋白質薄膜を銀塩の水溶液に接触
させる方法が好適に利用できる。For bonding silver to the protein thin film, for example, a method in which the protein thin film formed on the pore surface of the porous 1li is brought into contact with an aqueous solution of a silver salt can be suitably used.
この銀塩としては、硝酸銀を好適に利川できる。As this silver salt, silver nitrate can be suitably used.
例えば、硝酸銀0.02重1%を含有する25℃の水溶
液中に蛋白質薄膜が形成された多孔質中空糸11Qをl
O分間程度浸漬し後、水洗、乾燥させることにより、銀
を蛋白質薄膜に斑な〈結合させることができる。For example, a porous hollow fiber 11Q with a protein thin film formed in an aqueous solution at 25°C containing 0.02% by weight of silver nitrate is used.
After immersing for about 0 minutes, washing with water and drying, silver can be bonded unevenly to the protein thin film.
[実施例]
以下本発明を実施例及び比較例によって更に詳細に説明
する。[Examples] The present invention will be explained in more detail below using Examples and Comparative Examples.
なお、以下の実施例及び比較例における制菌性及び透水
性は以下の方法により測定した。In addition, the bacteriostatic property and water permeability in the following Examples and Comparative Examples were measured by the following methods.
(1)制菌性の測定:
黄色ブドウ状菌(江吐h江皿胚里aureus)を植種
した寒天培地上に艮さlcmの供試多孔質中空糸膜を並
べて置き、37℃で24時間の培養を行ない、供試試料
表面での細菌の成育の有無を観察し、制菌効果を判定し
た。(1) Measurement of bacteriostatic property: A 1cm sample of porous hollow fiber membranes was placed side by side on an agar medium inoculated with Staphylococcus aureus (S. aureus), and incubated at 37°C for 24 hours. After culturing for a period of time, the presence or absence of bacterial growth on the surface of the test sample was observed to determine the bacteriostatic effect.
(判定) ○:試料表面には細菌の生育は認められなか
った。(Judgment) ○: No bacterial growth was observed on the sample surface.
×:試料表面に細菌の生育が認めら れな。×: Bacterial growth was observed on the sample surface. Rena.
(2)透水付の測定;
供試多孔質中空糸膜400本をU字状に束ね、それぞれ
の中空糸膜開口部を樹脂で固め、第1図に示す構造の容
器内の所定位置に固定して濾過モジュールを製作した。(2) Measurement with water permeability: 400 sample porous hollow fiber membranes were bundled in a U-shape, the opening of each hollow fiber membrane was solidified with resin, and fixed at a predetermined position in a container with the structure shown in Figure 1. A filtration module was manufactured.
なお、供試多孔質中空糸膜の有効長は16cm、樹脂3
内での埋没部の長さはlcmであった。The effective length of the porous hollow fiber membrane tested was 16 cm, and the resin 3
The length of the buried part within was 1 cm.
この濾過モジュール1に通水口4から水を供給し、各中
空糸膜2の外壁面から中空部へ向けて、水圧1 kg/
cm”で1分間の透水を行ない、通水口5から排出され
る水の量を測定し、その結果から中空糸膜単位表面積あ
たりの水の透過量を算出し、通水性(mjl /min
.−cm2)とした。Water is supplied to this filtration module 1 from the water inlet 4 and directed from the outer wall surface of each hollow fiber membrane 2 to the hollow part at a water pressure of 1 kg/
cm" for 1 minute, measure the amount of water discharged from the water inlet 5, calculate the amount of water permeated per unit surface area of the hollow fiber membrane from the results, and calculate the water permeability (mjl/min).
.. -cm2).
なお、下記の比較例における疎水性多孔買中空糸膜の透
水性の測定では、透水に先立って、疎水性多孔質中空糸
膜を25℃のエチルアルコールに30分間浸漬して親水
化した後、水洗した。In addition, in the measurement of water permeability of a hydrophobic porous hollow fiber membrane in the following comparative example, prior to water permeation, the hydrophobic porous hollow fiber membrane was immersed in ethyl alcohol at 25 ° C. for 30 minutes to make it hydrophilic. Washed with water.
実施例1
疎水性多孔質ポリエチレン中空糸膜(商品名EHF27
0T、外径380μ戯、内径270鱗、三菱レイヨン株
式会社製)を25℃のエチルアルコール中に5分間浸漬
した後、25℃の流水中に30分間浸漬して引き上げ、
次いで大豆カゼイン1重量%及び水酸化ナトリウム0.
3重量%を含有するカゼインのアルカリ性水溶液中に2
5℃で8時間浸漬して、多孔質構造の有する表面にカセ
インのアルカリ性水溶液を付着させた後、引き上げた。Example 1 Hydrophobic porous polyethylene hollow fiber membrane (trade name EHF27
0T, outer diameter 380μ, inner diameter 270 scales, manufactured by Mitsubishi Rayon Co., Ltd.) was immersed in ethyl alcohol at 25°C for 5 minutes, then immersed in running water at 25°C for 30 minutes and pulled out.
Then 1% by weight of soybean casein and 0% sodium hydroxide.
2 in an alkaline aqueous solution of casein containing 3% by weight.
The sample was immersed at 5° C. for 8 hours to adhere an alkaline aqueous solution of casein to the surface of the porous structure, and then pulled out.
次に、このカゼインのアルカリ性水溶液を保持させた多
孔質中空糸膜を、酢酸1重量%を含有する25℃の酸性
水溶液中に1分間浸漬し、カゼインの凝固処理を行なっ
た後、充分水洗して、乾燥させて、親水性多孔質ポリエ
チレン中空糸膜を得た。Next, the porous hollow fiber membrane holding this alkaline aqueous solution of casein was immersed for 1 minute in an acidic aqueous solution at 25°C containing 1% by weight of acetic acid to coagulate the casein, and then thoroughly washed with water. The membrane was dried to obtain a hydrophilic porous polyethylene hollow fiber membrane.
得られた親水性多孔質中空糸膜外表面を電子顕微鏡で観
察したところ、中空糸壁の多孔貿構造の有する表面にむ
らなくカゼインの薄膜が形成されているのが観察された
。When the outer surface of the obtained hydrophilic porous hollow fiber membrane was observed using an electron microscope, it was observed that a thin film of casein was evenly formed on the surface of the porous structure of the hollow fiber wall.
この親水性多孔質中空糸膜の透水性の測定結果を表1に
示す。Table 1 shows the results of measuring the water permeability of this hydrophilic porous hollow fiber membrane.
表1の結果から明らかなように本実施例で得られた親水
性多孔質中空糸膜は良好な透水性を有し、該親水性多孔
質中空糸膜を組み込んだ′tLAモジュールは、使用前
のアルコール等による親水化処理は不要であり、そのま
ま水の濾過処理に利用可能であった。As is clear from the results in Table 1, the hydrophilic porous hollow fiber membrane obtained in this example has good water permeability, and the 'tLA module incorporating the hydrophilic porous hollow fiber membrane was No hydrophilic treatment with alcohol or the like was required, and the product could be used as it was for water filtration.
更に、濾通処理に使用した後に、濾過モジュールを洗浄
し、乾燥させてから水濾過に再利用し、透水性を測定し
たところ、良好な透水性が維持されていた。Furthermore, after being used for filtration treatment, the filtration module was washed, dried, and reused for water filtration, and its water permeability was measured, and it was found that good water permeability was maintained.
実施例2
疎水性多孔質ボリスルホン中空糸膜(外径440μs、
内径330μ廊)を用いる以外は、実施例1と同様にし
て、カゼイン薄膜を多孔貿構造の有する表面に形成し、
親水化された多孔質ボリスルホン中空糸+iを得た。Example 2 Hydrophobic porous boris sulfone hollow fiber membrane (outer diameter 440 μs,
A thin casein film was formed on the surface of the porous structure in the same manner as in Example 1, except that the inner diameter was 330 μm.
A hydrophilized porous borisulfone hollow fiber +i was obtained.
得られた親水性多孔質中空糸膜の透水性の測定結果を表
1に示す。Table 1 shows the results of measuring the water permeability of the obtained hydrophilic porous hollow fiber membrane.
表1の結果から明らかなように本実施例で得ら九た親水
性多孔質中空糸膜もまた良好な透水性を有し、この中空
糸膜を組み込んだ濾過モジュールも、使用前のアルコー
ル等による親水化処理は不要であり、そのまま水の濾過
処理に利川可能であった。As is clear from the results in Table 1, the hydrophilic porous hollow fiber membrane obtained in this example also has good water permeability, and the filtration module incorporating this hollow fiber membrane also No hydrophilic treatment was required, and the water could be directly filtered.
更に、濾過処理に使用した後に、濾過モジュールを洗浄
し、乾燥させてから水濾過に再利用し、透水性を測定し
たところ、良好な透水性が維持されていた。Furthermore, after being used for filtration, the filtration module was washed, dried, and reused for water filtration, and its water permeability was measured, and it was found that good water permeability was maintained.
実施例3
実施例1で得たカゼイン薄膜を有する親水性多孔質ポリ
エチレン中空糸膜を、25℃の硝酸銀の0.02重量%
水溶液に5分間浸漬して銀をカゼイン薄膜に結合させた
後、超音波洗浄機を用いて25℃でlO分間水洗処理し
、次いで真空乾燥機を用いて40℃で24時間真空乾燥
を行ない、カゼイン薄膜の表層に銀が結合されて灰色に
着色された親水性多孔質ポリエチレン中空糸膜を得た。Example 3 The hydrophilic porous polyethylene hollow fiber membrane having the casein thin film obtained in Example 1 was treated with 0.02% by weight of silver nitrate at 25°C.
After immersing in an aqueous solution for 5 minutes to bond silver to the casein thin film, washing with water at 25 ° C. for 10 minutes using an ultrasonic cleaner, then vacuum drying at 40 ° C. for 24 hours using a vacuum dryer, Silver was bonded to the surface layer of the casein thin film to obtain a hydrophilic porous polyethylene hollow fiber membrane colored gray.
得られた親水性多孔質中空糸膜の透水性及び制菌性の結
果を表1に示す。Table 1 shows the results of the water permeability and bacteriostatic properties of the obtained hydrophilic porous hollow fiber membrane.
表1の結果から明らかなように本実施例で得られた親水
性多孔質中空糸膜もまた良好な透水性を有し、この中空
糸膜を組み込んだ濾過モジュールも、使用前のアルコー
ル等による親水化処理は不要であり、そのまま水の濾過
処理に利用可能であった。As is clear from the results in Table 1, the hydrophilic porous hollow fiber membrane obtained in this example also has good water permeability, and the filtration module incorporating this hollow fiber membrane also No hydrophilic treatment was required, and it could be used as it was for water filtration treatment.
更に、濾過処理に使用した後に、濾過モジュールを洗浄
し、乾燥させてから水濾過に再利用し、透水性及び制菌
性を測定したところ、良好な透水性及び制菌性が維持さ
れていた。Furthermore, after being used for filtration, the filtration module was washed, dried, and reused for water filtration, and its water permeability and bacteriostatic properties were measured, and it was found that good water permeability and bacteriostatic properties were maintained. .
実施例4
実施例2で得たカセイン薄膜を有する親水性多孔質ポリ
スルホン中空糸膜を用いる以外は実施例3と同様にして
、カセイン薄膜の表層に銀が結合された親水性多孔質ポ
ソスルホン中空糸膜を得た。Example 4 A hydrophilic porous pososulfone hollow fiber with silver bonded to the surface layer of the casein thin film was prepared in the same manner as in Example 3 except that the hydrophilic porous polysulfone hollow fiber membrane having the casein thin film obtained in Example 2 was used. A membrane was obtained.
得られた親水性多孔質中空糸膜の透水性及び制菌性の結
果を表1に示す。Table 1 shows the results of the water permeability and bacteriostatic properties of the obtained hydrophilic porous hollow fiber membrane.
表1の結果から明らかなように本実施例で得られた親水
性多孔質中空糸膜もまた良好な透水性を有し、この中空
糸膜な組み込んだ濾過モジュールも、使用前のアルコー
ル等による親水化処理は不要であり、そのまま水の濾過
処理に利用可能であった。As is clear from the results in Table 1, the hydrophilic porous hollow fiber membrane obtained in this example also has good water permeability, and the filtration module incorporating this hollow fiber membrane also No hydrophilic treatment was required, and it could be used as it was for water filtration treatment.
更に、濾過処理に使用した後に、濾過モジュールを洗浄
し、乾燥させてから水濾過に再利用し、透水性及び制菌
性を測定したところ、良好な透水性及び制菌性が維持ざ
れていた。Furthermore, after using it for filtration treatment, the filtration module was washed, dried, and reused for water filtration, and its water permeability and bacteriostatic properties were measured, and it was found that good water permeability and bacteriostatic properties were maintained. .
比較例1
実施例1で用いた疎水性多孔質ポリエチレン中空糸膜の
透水性及び制菌性を測定したところ表1に示す結果を得
た。Comparative Example 1 The water permeability and antibacterial properties of the hydrophobic porous polyethylene hollow fiber membrane used in Example 1 were measured, and the results shown in Table 1 were obtained.
次に、この疎水性多孔質中空糸膜を組み込んだ濾過モジ
ュールをエチルアルコールでの親水化処理を行なってか
ら濾過処理に使用した後に、濾過モジュールを洗浄し、
乾燥させてから水濾過に再利用し、透水性を測定したと
ころ、透水性は低下していた。Next, the filtration module incorporating this hydrophobic porous hollow fiber membrane is subjected to hydrophilization treatment with ethyl alcohol and used for filtration treatment, and then the filtration module is washed,
After drying, it was reused for water filtration and its water permeability was measured, and it was found that the water permeability had decreased.
比較例2
実施例2で用いた疎水性多孔質ボリスルホン中空糸膜の
透水性及び制菌性を測定したところ表1に示す結果を得
た。Comparative Example 2 The water permeability and bacteriostatic properties of the hydrophobic porous polysulfone hollow fiber membrane used in Example 2 were measured, and the results shown in Table 1 were obtained.
次に、この疎水性多孔質中空糸膜を組み込んだ濾過モジ
ュールをエチルアルコールでの親水化処埋を行なってか
ら濾過処理に使用した後に、濾過モジュールを洗浄し、
乾燥させてから水濾過に再利用し、透水性を測定したと
ころ、透水性は低下していた。Next, the filtration module incorporating this hydrophobic porous hollow fiber membrane is subjected to hydrophilic treatment with ethyl alcohol and used for filtration treatment, and then the filtration module is washed,
After drying, it was reused for water filtration and its water permeability was measured, and it was found that the water permeability had decreased.
表 1
[発明の効果]
本発明の親水性多孔質中空糸膜においては、蛋白質薄膜
が多孔質構造の有する表面に形成されていることによっ
て優れた親水性を繕続的に安定して有し、これを用いて
作製した濾過モジュールは、アルコール等の親水化剤に
よる而処理の必要がなく,水の濾過に直接利用でき、一
旦乾燥させた後でも直接再利用町能である。Table 1 [Effects of the Invention] The hydrophilic porous hollow fiber membrane of the present invention has excellent hydrophilicity continuously and stably because the protein thin film is formed on the surface of the porous structure. The filtration module made using this does not require treatment with a hydrophilic agent such as alcohol, can be used directly for water filtration, and can be directly reused even after being dried.
本発明の親水性多孔質中空糸膜における蛋白質薄膜は,
安全面において問題のない蛋白質から構成されているの
で、これを用いて作製した濾過モジュールを飲料水製造
に利用する際にも、安全で、衛生的な飲t1用の濾過水
を提供できる。The protein thin film in the hydrophilic porous hollow fiber membrane of the present invention is
Since it is composed of proteins that pose no safety problems, even when a filtration module made using this is used for producing drinking water, it is possible to provide safe and sanitary filtered water for drinking t1.
更に,本発明の親水性多孔質中空糸膜の有する蛋白質薄
膜は銀の結合能に優れ、必要に応じて銀を結合して制菌
性を得る場合に好適な構造を有する。従って、この親水
性多孔質中空糸膜を用いれば、銀の結合によって優れた
jttlJ菌性が付与された親水性多孔質中空糸膜を極
めて容易に形成できる。しかも、本発明の親水性多孔質
中空糸膜は、蛋白質薄膜に銀が結合された場合でも、上
述の特性が損なわれることがないという利点を有する。Furthermore, the protein thin film of the hydrophilic porous hollow fiber membrane of the present invention has an excellent silver binding ability and has a structure suitable for obtaining bacteriostatic properties by binding silver as necessary. Therefore, by using this hydrophilic porous hollow fiber membrane, a hydrophilic porous hollow fiber membrane imparted with excellent jttlJ bactericidal properties due to silver binding can be formed very easily. Moreover, the hydrophilic porous hollow fiber membrane of the present invention has the advantage that the above-mentioned properties are not impaired even when silver is bonded to the protein thin film.
この銀が結合された蛋白質薄1摸を有する親水性多孔質
中空糸膜を濾過膜として用いた濾過モジュールによる濾
過においては、中空糸壁に捕獲された細菌等の微生物の
繁殖か抑制され、細菌等の微生物の繁殖による水の変質
や異臭の発生、更には中空糸の細孔の閉塞が効果的に防
止され、常に安全で、衛生的な状態を保持した信頼性の
高い鯖密濾過が可能となる。In filtration by a filtration module using a hydrophilic porous hollow fiber membrane having a thin layer of silver-bonded protein as a filtration membrane, the growth of microorganisms such as bacteria captured on the hollow fiber wall is suppressed, and the bacteria It effectively prevents the deterioration of water, the generation of odor, and the clogging of the hollow fiber pores due to the proliferation of microorganisms such as microorganisms, enabling highly reliable filtration that maintains safe and sanitary conditions at all times. becomes.
第1図は透水性の測定の際に製作した濾過モジュールの
構成を示す模式的断面図である。
1:濾過モジュール
2:多孔質中空糸膜
3:樹脂
4、5:通水口
特許出願人 三菱レイヨン株式会社FIG. 1 is a schematic cross-sectional view showing the configuration of a filtration module manufactured when measuring water permeability. 1: Filtration module 2: Porous hollow fiber membrane 3: Resin 4, 5: Water port Patent applicant Mitsubishi Rayon Co., Ltd.
Claims (1)
成されてなる親水性多孔質中空糸膜。 2)蛋白質薄膜に銀が結合されてなる請求項1記載の親
水性多孔質中空糸膜。[Scope of Claims] 1) A hydrophilic porous hollow fiber membrane having a protein thin film formed on at least a portion of the surface of the porous membrane. 2) The hydrophilic porous hollow fiber membrane according to claim 1, wherein silver is bonded to a protein thin membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11200689A JPH02293031A (en) | 1989-05-02 | 1989-05-02 | Hydrophilic porous hollow fiber membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11200689A JPH02293031A (en) | 1989-05-02 | 1989-05-02 | Hydrophilic porous hollow fiber membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02293031A true JPH02293031A (en) | 1990-12-04 |
Family
ID=14575606
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11200689A Pending JPH02293031A (en) | 1989-05-02 | 1989-05-02 | Hydrophilic porous hollow fiber membrane |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02293031A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2803126C2 (en) * | 2018-05-03 | 2023-09-06 | Пак Витаэ (Прайвит) Лимитед | Hollow fibre membrane for liquid filtration |
-
1989
- 1989-05-02 JP JP11200689A patent/JPH02293031A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2803126C2 (en) * | 2018-05-03 | 2023-09-06 | Пак Витаэ (Прайвит) Лимитед | Hollow fibre membrane for liquid filtration |
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