JP2851417B2 - Orientation separation membrane and method for producing the same - Google Patents
Orientation separation membrane and method for producing the sameInfo
- Publication number
- JP2851417B2 JP2851417B2 JP31039690A JP31039690A JP2851417B2 JP 2851417 B2 JP2851417 B2 JP 2851417B2 JP 31039690 A JP31039690 A JP 31039690A JP 31039690 A JP31039690 A JP 31039690A JP 2851417 B2 JP2851417 B2 JP 2851417B2
- Authority
- JP
- Japan
- Prior art keywords
- separation membrane
- voltage
- membrane
- producing
- same
- 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.)
- Expired - Lifetime
Links
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、各種分離に用いられる精密濾過膜、限外濾
過膜、逆浸透膜等の分離膜に関し、詳しくは特定の方法
により分子鎖が厚さ方向に配向してなる分離膜に関す
る。The present invention relates to a separation membrane such as a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane used for various separations. The present invention relates to a separation membrane oriented in a thickness direction.
逆浸透プロセス等の膜分離に用いられる分離膜には、
耐熱性、機械的強度、耐薬品性等の各種耐性が要求され
ており、すべてを満足するものは未だ得られていない。Separation membranes used for membrane separation such as reverse osmosis processes include
Various resistances such as heat resistance, mechanical strength, and chemical resistance are required, and none of them satisfy all of them.
例えば、複合逆浸透膜は、通常2種の反応体の非混合
性溶液間の界面重合反応によって得られる。微多孔性支
持体の表面でかかる反応を行うことにより、界面重合に
より得られた緻密層は、多孔質支持体の表面に形成され
る。かかる方法で得られた複合膜は、通常優れた選択性
を有するが、しかしその緻密層の厚みが数10μm以上と
なると、透過性能は小さくなりすぎる。超薄膜は、良好
な透過性能を有するが、欠陥を無くするのが難しく、ま
た化学的耐性や機械的耐性に劣るという問題があった。For example, composite reverse osmosis membranes are usually obtained by interfacial polymerization reactions between immiscible solutions of two reactants. By performing such a reaction on the surface of the microporous support, a dense layer obtained by interfacial polymerization is formed on the surface of the porous support. The composite membrane obtained by such a method usually has excellent selectivity, but when the thickness of the dense layer is several tens μm or more, the permeability is too small. Although the ultrathin film has good transmission performance, it has problems that it is difficult to eliminate defects and that it has poor chemical resistance and mechanical resistance.
本発明者らは、前記の問題を解決するために鋭意検討
した結果、分離膜を直流電圧印加状態で界面重合により
製造することにより、分子鎖が配向し、透過性能に優れ
た分離膜が得られることを見い出し、本発明に至ったも
のである。The inventors of the present invention have conducted intensive studies to solve the above-described problems. It has been found that the present invention has been achieved.
即ち本発明は、直流電圧印加状態で、界面重合により
形成されてなる配向分離膜、及び以下の工程からなる配
向分離膜の製造方法を提供する。That is, the present invention provides an alignment separation film formed by interfacial polymerization in a state where a DC voltage is applied, and a method for manufacturing an alignment separation film including the following steps.
(a)2官能性反応体(A)溶液を支持体に塗布する工
程、 (b)塗布された支持体に、その表面と垂直方向に直流
電圧を印加する工程、及び (c)直流電圧印加状態で、塗布された支持体に(A)
と反応する2官能性反応体(B)の溶液を接触させる工
程。(A) applying a bifunctional reactant (A) solution to a support; (b) applying a DC voltage to the coated support in a direction perpendicular to the surface thereof; and (c) applying a DC voltage. In the state, on the coated support (A)
Contacting a solution of a bifunctional reactant (B) that reacts with
本発明において、2官能性の反応体(A)としては、
通常の条件下で重合反応可能である点から、NH基やNH2
基のような反応性基を2つ有するものが好ましく、例え
ばメタフェニレンジアミン、パラフェニレンジアミン、 等のアミン反応体等の一種もしくは複数が挙げられる。
またかかる反応体の溶液としては、水、が好ましく用い
られる。上記溶液には、さらに他の多官能性反応体や、
支持体を濡らすための添加剤(例えば、SLS等のイオン
性界面活性剤、HCl等のハイドロクロリックアシッド、
テトラエチルアミン、ベンゼンスルフォニックアシッド
等)等を添加することもできる。In the present invention, the bifunctional reactant (A) includes:
From the point that the polymerization reaction can be performed under ordinary conditions, NH groups and NH 2
Those having two reactive groups such as a group are preferable, for example, metaphenylenediamine, paraphenylenediamine, And the like, and one or more of such amine reactants.
As the solution of the reactant, water is preferably used. The solution may further contain other polyfunctional reactants,
Additives for wetting the support (for example, ionic surfactants such as SLS, hydrochloric acid such as HCl,
Tetraethylamine, benzenesulfonic acid, etc.) can also be added.
かかる反応体(A)と界面重合させる反応体(B)と
しては、上記反応体(A)と反応して線状ポリマー鎖を
形成する必要がある点から、反応性基を2つ有するもの
が好ましく、かつ後記の溶媒に可能なものが好ましい。
例えば、パラメトキシクロライド、メタメトキシクロラ
イド、 等の一種もしくは複数が用いられる。またかかる反応体
(B)の溶液としては、反応体(A)の溶液と混ざらな
い、例えばベンゼン、DMF、DM Ac、IPソルベント(炭素
数6〜7の脂肪族炭化水素溶剤)等が挙げられる。As the reactant (B) to be interfacially polymerized with the reactant (A), those having two reactive groups are necessary because they need to react with the reactant (A) to form a linear polymer chain. Those which are preferable and which can be used for the solvents described below are preferable.
For example, para methoxy chloride, meta methoxy chloride, One or more of these are used. Examples of the solution of the reactant (B) include, for example, benzene, DMF, DMAc, and IP solvents (aliphatic hydrocarbon solvents having 6 to 7 carbon atoms) which are not mixed with the solution of the reactant (A). .
本発明においては、上記2種の反応体を、直流電圧印
加状態で、支持体上にて界面重合し、その後電圧印加状
態のまま乾燥することにより、本発明の分離膜を得るこ
とができる。また必要に応じて支持体を剥離して分離膜
とすることもできる。In the present invention, the two kinds of reactants are interfacially polymerized on a support under a DC voltage applied state, and then dried under a voltage applied state, whereby the separation membrane of the present invention can be obtained. If necessary, the support may be peeled off to form a separation membrane.
ここで、直流電圧印加条件は、反応体の種類、電極間
の距離、温度、目的とする膜厚等によって異なり、溶媒
の分離、支持体や生成する膜への損傷が生じない限り、
特に限定されない。通常、20〜200℃で、直流電圧数V
〜数KV、好ましくは1〜10KVとする。Here, the DC voltage application condition depends on the type of the reactants, the distance between the electrodes, the temperature, the target film thickness, and the like.
There is no particular limitation. Normally, 20 to 200 ° C, DC voltage several V
To several KV, preferably 1 to 10 KV.
また支持体としては、例えばポリスルホン、ポリイキ
ド、酢酸セルロース等からなる精密濾過膜、限外濾過膜
等が用いられる。As the support, for example, a microfiltration membrane or an ultrafiltration membrane made of polysulfone, polyimide, cellulose acetate or the like is used.
本発明の分離膜は、上記の特定の方法により、緻密層
の分子鎖が電圧印加方向、即ち膜の厚み方向に配向成長
している。In the separation membrane of the present invention, the molecular chains of the dense layer are oriented and grown in the voltage application direction, that is, the thickness direction of the membrane, by the above specific method.
本発明における配向分離膜は、従来の膜に比べて高い
透過性能及び排除性能を有する。The orientation separation film in the present invention has higher permeation performance and rejection performance than the conventional film.
ポリスルホン限外濾過膜に、メタフェニレンジアミン
の0.25%水溶液を塗布した。この塗布された膜を、ステ
ンレス鋼からなる2つの電極間に配置し、室温にて50
V、又は100Vの直流電圧を印加した。次いで、0.1%のパ
ラメトキシクロライドと0.23%のメタメトキシクロライ
ドを含むIPソルベント溶液を、電圧印加状態で、上記膜
に接触させ、30分間保持して、本発明の分離膜を得た。A 0.25% aqueous solution of metaphenylenediamine was applied to the polysulfone ultrafiltration membrane. This coated film was placed between two electrodes made of stainless steel and kept at room temperature for 50 minutes.
V or 100 V DC voltage was applied. Next, an IP solvent solution containing 0.1% of paramethoxy chloride and 0.23% of metamethoxychloride was brought into contact with the above-mentioned membrane in a state where a voltage was applied, and kept for 30 minutes to obtain a separation membrane of the present invention.
かかる分離膜を、1500ppmのNaClを含む塩水を用い
て、pH7、15kgf/cm2の条件下で評価した。その結果を表
に示す。The separation membrane was evaluated under the conditions of pH 7 and 15 kgf / cm 2 using a saline solution containing 1500 ppm of NaCl. The results are shown in the table.
直流電圧を印加しない以外は実施例と同様にして得た
分離膜の評価結果を表に併せて示す。The evaluation results of the separation membrane obtained in the same manner as in the example except that no DC voltage is applied are also shown in the table.
表からわかるように、本発明の分離膜は、排除性能は
変わらないにもかかわらず、透過性能に優れている。As can be seen from the table, the separation membrane of the present invention is excellent in permeation performance despite the same rejection performance.
Claims (2)
されてなる配向分離膜。An orientation separation film formed by interfacial polymerization in a state where a DC voltage is applied.
向分離膜の製造方法。 (a)2官能性反応体(A)溶液を支持体に塗布する工
程、 (b)塗布された支持体に、その表面と垂直方向に直流
電圧を印加する工程、及び (c)直流電圧印加状態で、塗布された支持体に(A)
と反応する2官能性反応体(B)溶液を接触させる工
程。2. The method for producing an orientation separation film according to claim 1, comprising the following steps. (A) applying a bifunctional reactant (A) solution to a support; (b) applying a DC voltage to the coated support in a direction perpendicular to the surface thereof; and (c) applying a DC voltage. In the state, on the coated support (A)
Contacting a bifunctional reactant (B) solution that reacts with
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31039690A JP2851417B2 (en) | 1990-11-15 | 1990-11-15 | Orientation separation membrane and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31039690A JP2851417B2 (en) | 1990-11-15 | 1990-11-15 | Orientation separation membrane and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04180823A JPH04180823A (en) | 1992-06-29 |
JP2851417B2 true JP2851417B2 (en) | 1999-01-27 |
Family
ID=18004761
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31039690A Expired - Lifetime JP2851417B2 (en) | 1990-11-15 | 1990-11-15 | Orientation separation membrane and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2851417B2 (en) |
-
1990
- 1990-11-15 JP JP31039690A patent/JP2851417B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04180823A (en) | 1992-06-29 |
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