JP2008062127A5 - Separation membrane manufacturing method and separation membrane for water treatment - Google Patents

Separation membrane manufacturing method and separation membrane for water treatment Download PDF

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JP2008062127A5
JP2008062127A5 JP2006239964A JP2006239964A JP2008062127A5 JP 2008062127 A5 JP2008062127 A5 JP 2008062127A5 JP 2006239964 A JP2006239964 A JP 2006239964A JP 2006239964 A JP2006239964 A JP 2006239964A JP 2008062127 A5 JP2008062127 A5 JP 2008062127A5
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separation membrane
oxygen
manufacturing
perfluorocarbon
containing substance
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JP5082347B2 (en
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本発明者は上記課題を解決するべく鋭意検討し、多孔質膜の表面に、通常は互いに相容れない特性である、親水性と撥油性を併せ持つ表面特性を付与できる方法を見出した。そして、該方法を用いて多孔質膜の表面に親水撥油性を付与することにより、優れた透水性、耐ファウリング性および易洗浄性を兼ね備えた分離膜を実現できることを知見して本発明を完成するに至った。
すなわち本発明の分離膜の製造方法は、多孔質膜の表面を、(A)パーフルオロカーボンと、(B)酸素原子を有し、C−H結合およびハロゲン原子のいずれも有しない酸素含有物質とが存在する雰囲気中で放電処理する工程を有することを特徴とする。
前記(A)パーフルオロカーボンが重合性炭素−炭素二重結合を有していることが好ましい。
前記(A)パーフルオロカーボンにおけるフッ素原子と炭素原子の存在比(F/C)が1.5以上であることが好ましい。
前記(B)酸素含有物質が、酸素、オゾン、二酸化炭素、水、一酸化窒素、二酸化窒素、二酸化硫黄および三酸化硫黄からなる群から選択される1種以上であることが好ましい。
前記(A)パーフルオロカーボンがテトラフルオロエチレンまたはヘキサフルオロプロピレンであり、前記(B)酸素含有物質が酸素であることが好ましい。
前記雰囲気中に存在する酸素原子の原子数とフッ素原子の原子数の比(O/F比)が0.05〜100であることが好ましい。
前記雰囲気中における(A)パーフルオロカーボンおよび(B)酸素含有物質の含有割合の合計が50モル%以上であることが好ましい。
前記多孔質膜の孔径が0.01〜5μmであることが好ましい。
前記多孔質膜の材質が、ポリオレフィン、ポリスルホン、ポリエーテルスルホン、ポリカーボネート、ポリアミド、ポリイミド、ポリアクリロニトリル、ポリビニルアルコール、酢酸セルロース、ポリテトラフルオロエチレン、エチレンテトラフルオロエチレン共重合体、ポリクロロトリフルオロエチレン、またはポリフッ化ビニリデンであることが好ましい。
本発明は、本発明の方法で製造される水処理用分離膜を提供する。

The present inventor has intensively studied to solve the above problems, and has found a method capable of imparting surface characteristics having both hydrophilicity and oil repellency, which are usually incompatible characteristics, to the surface of the porous membrane. The present invention is based on the knowledge that a separation membrane having excellent water permeability, fouling resistance and easy washing can be realized by imparting hydrophilic oil repellency to the surface of the porous membrane using the method. It came to be completed.
That is, in the method for producing a separation membrane of the present invention, the surface of the porous membrane comprises (A) perfluorocarbon and (B) an oxygen-containing substance having oxygen atoms and having neither C—H bonds nor halogen atoms. It has the process of carrying out an electrical discharge treatment in the atmosphere which exists.
The (A) perfluorocarbon preferably has a polymerizable carbon-carbon double bond.
The abundance ratio (F / C) of fluorine atoms to carbon atoms in the (A) perfluorocarbon is preferably 1.5 or more.
The (B) oxygen-containing substance is preferably at least one selected from the group consisting of oxygen, ozone, carbon dioxide, water, nitric oxide, nitrogen dioxide, sulfur dioxide and sulfur trioxide.
The (A) perfluorocarbon is preferably tetrafluoroethylene or hexafluoropropylene, and the (B) oxygen-containing substance is preferably oxygen.
The ratio of the number of oxygen atoms and the number of fluorine atoms (O / F ratio) in the atmosphere is preferably 0.05 to 100.
The total content of (A) perfluorocarbon and (B) oxygen-containing substance in the atmosphere is preferably 50 mol% or more.
It is preferable that the porous membrane has a pore diameter of 0.01 to 5 μm.
The material of the porous membrane is polyolefin, polysulfone, polyethersulfone, polycarbonate, polyamide, polyimide, polyacrylonitrile, polyvinyl alcohol, cellulose acetate, polytetrafluoroethylene, ethylenetetrafluoroethylene copolymer, polychlorotrifluoroethylene, Or it is preferable that it is a polyvinylidene fluoride.
The present invention provides a separation membrane for water treatment produced by the method of the present invention.

Claims (10)

多孔質膜の表面を、(A)パーフルオロカーボンと、(B)酸素原子を有し、C−H結合およびハロゲン原子のいずれも有しない酸素含有物質とが存在する雰囲気中で放電処理する工程を有することを特徴とする分離膜の製造方法。   A step of performing a discharge treatment on the surface of the porous film in an atmosphere in which (A) perfluorocarbon and (B) an oxygen-containing substance having an oxygen atom and neither a C—H bond nor a halogen atom are present. A method for producing a separation membrane, comprising: 前記(A)パーフルオロカーボンが重合性炭素−炭素二重結合を有している、請求項1記載の分離膜の製造方法。 The method for producing a separation membrane according to claim 1 , wherein the (A) perfluorocarbon has a polymerizable carbon-carbon double bond. 前記(A)パーフルオロカーボンにおけるフッ素原子と炭素原子の存在比(F/C)が1.5以上である、請求項1または2に記載の分離膜の製造方法。The manufacturing method of the separation membrane of Claim 1 or 2 whose abundance ratio (F / C) of the fluorine atom and carbon atom in said (A) perfluorocarbon is 1.5 or more. 前記(B)酸素含有物質が、酸素、オゾン、二酸化炭素、水、一酸化窒素、二酸化窒素、二酸化硫黄および三酸化硫黄からなる群から選択される1種以上である請求項1〜3のいずれか一項に記載の分離膜の製造方法。 (B) the oxygen-containing substance, either oxygen, ozone, carbon dioxide, water, nitrogen monoxide, nitrogen dioxide, according to claim 1 to 3 in which at least one selected from the group consisting of sulfur dioxide and sulfur trioxide A method for producing the separation membrane according to claim 1 . 前記(A)パーフルオロカーボンが、テトラフルオロエチレンまたはヘキサフルオロプロピレンであり、前記(B)酸素含有物質が酸素である請求項1〜のいずれか一項に記載の分離膜の製造方法。 The method for manufacturing a separation membrane according to any one of claims 1 to 4 , wherein the (A) perfluorocarbon is tetrafluoroethylene or hexafluoropropylene, and the (B) oxygen-containing substance is oxygen. 前記雰囲気中に存在する酸素原子の原子数とフッ素原子の原子数の比(O/F比)が0.05〜100である、請求項1〜5のいずれか一項に記載の分離膜の製造方法。The separation membrane according to any one of claims 1 to 5, wherein the ratio of the number of oxygen atoms and the number of fluorine atoms (O / F ratio) present in the atmosphere is 0.05 to 100. Production method. 前記雰囲気中における(A)パーフルオロカーボンおよび(B)酸素含有物質の含有割合の合計が50モル%以上である、請求項1〜6のいずれか一項に記載の分離膜の製造方法。The manufacturing method of the separation membrane as described in any one of Claims 1-6 whose sum total of the content rate of (A) perfluorocarbon in the said atmosphere and (B) oxygen-containing substance is 50 mol% or more. 前記多孔質膜の孔径が0.01〜5μmである、請求項1〜7のいずれか一項に記載の分離膜の製造方法。The manufacturing method of the separation membrane as described in any one of Claims 1-7 whose pore diameter of the said porous membrane is 0.01-5 micrometers. 前記多孔質膜の材質が、ポリオレフィン、ポリスルホン、ポリエーテルスルホン、ポリカーボネート、ポリアミド、ポリイミド、ポリアクリロニトリル、ポリビニルアルコール、酢酸セルロース、ポリテトラフルオロエチレン、エチレンテトラフルオロエチレン共重合体、ポリクロロトリフルオロエチレン、またはポリフッ化ビニリデンである、請求項1〜8のいずれか一項に記載の分離膜の製造方法。The material of the porous membrane is polyolefin, polysulfone, polyethersulfone, polycarbonate, polyamide, polyimide, polyacrylonitrile, polyvinyl alcohol, cellulose acetate, polytetrafluoroethylene, ethylenetetrafluoroethylene copolymer, polychlorotrifluoroethylene, Or the manufacturing method of the separation membrane as described in any one of Claims 1-8 which is a polyvinylidene fluoride. 請求項1〜9のいずれか一項に記載の方法で製造される、水処理用分離膜。The separation membrane for water treatment manufactured by the method as described in any one of Claims 1-9.
JP2006239964A 2006-09-05 2006-09-05 Separation membrane manufacturing method and separation membrane for water treatment Expired - Fee Related JP5082347B2 (en)

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CN106574166B (en) 2014-07-30 2018-10-02 三菱综合材料株式会社 Surface covering material, coated film and hydrophilic oil repellent material
WO2016017754A1 (en) 2014-07-30 2016-02-04 三菱マテリアル株式会社 Filter medium, method for producing filter medium, water treatment module, and water treatment device
WO2016017686A1 (en) 2014-07-30 2016-02-04 三菱マテリアル株式会社 Hydrophilic oil repellent agent and method for manufacturing same, and surface covering material, coating film, resin composition, oil-water separation filter medium, and porous body
JP6461573B2 (en) 2014-07-30 2019-01-30 三菱マテリアル株式会社 Oil / water separator / collector
JP6384843B2 (en) * 2017-08-21 2018-09-05 国立大学法人弘前大学 Fluorine-containing nanocomposite particles and method for producing the same, coating agent containing the same, oil-water separation membrane, and resin composition

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JPS6099326A (en) * 1983-11-04 1985-06-03 Agency Of Ind Science & Technol Separation film for gas
JPS6223401A (en) * 1985-07-22 1987-01-31 Nok Corp Ultrafiltration membrane
AU7135087A (en) * 1986-04-11 1987-10-15 Applied Membrane Technology Inc. Preparation of a hydrophilic microfiltration membrane by means of plasma treatment
JPH0761434B2 (en) * 1988-03-18 1995-07-05 セントラル硝子株式会社 Material permeable membrane
US5073175A (en) * 1988-08-09 1991-12-17 Air Products And Chemicals, Inc. Fluorooxidized polymeric membranes for gas separation and process for preparing them
JP2926869B2 (en) * 1990-04-20 1999-07-28 エヌオーケー株式会社 Hollow fiber surface treatment method for hollow fiber module
JPH05329342A (en) * 1992-05-29 1993-12-14 Dainippon Ink & Chem Inc Production of polymeric separation membrane

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