JPS62279805A - Separation membrane using polysulfone containing carboxyl group and its production - Google Patents

Separation membrane using polysulfone containing carboxyl group and its production

Info

Publication number
JPS62279805A
JPS62279805A JP12344486A JP12344486A JPS62279805A JP S62279805 A JPS62279805 A JP S62279805A JP 12344486 A JP12344486 A JP 12344486A JP 12344486 A JP12344486 A JP 12344486A JP S62279805 A JPS62279805 A JP S62279805A
Authority
JP
Japan
Prior art keywords
polysulfone
carboxylic acid
separation membrane
acid group
formulas
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
JP12344486A
Other languages
Japanese (ja)
Inventor
Yoshio Himeshima
姫島 義夫
Masaru Kurihara
優 栗原
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP12344486A priority Critical patent/JPS62279805A/en
Publication of JPS62279805A publication Critical patent/JPS62279805A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/66Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68Polysulfones; Polyethersulfones

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To obtain a separation membrane wherein separation performance is good and amount of fresh water to be produced is not decreased even in the operation of a long time by using polysulfone having carboxyl group in a benzene ring of a principal chain. CONSTITUTION:Acetylated polysulfone is obtained by allowing acetyl chloride to react with polysulfone dissolved in dichloroethane in the presence of Lewis acid such as aluminum chloride. Then acetylated polysulfone is dissolved in methylene chloride and this soln. is stirred together with bromotetrabutylammonium and sodium hypochlorite to perform haloform reaction. After separating an organic phase of the reaction soln., it is reprecipitated by n-hexane or the like to obtain white powdery polysulfone contg. carboxyl group. This compd. and polysulfone are dissolved in dimethylformamide in the prescribed proportion and this soln. is cast on nonwoven fabric such as polyester fiber fixed on a glass plate and this is immersed into pure water and thereby a fiber-reinforced polysulfone membrane is obtained.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〔産業上の利用分野〕 本発明は、液状混合物の成分、特に海水およびカン水を
脱塩して淡水化することができる逆浸透膜や、コロイド
次元の浮遊粒子の分離に使用される限外濾過、精密濾過
膜として有用なカルボン酸基含有ポリスルホン分離膜に
関する。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Industrial Application] The present invention provides a reverse osmosis membrane and a membrane that can desalinate and desalinate components of a liquid mixture, particularly seawater and can water. , relates to a carboxylic acid group-containing polysulfone separation membrane useful as an ultrafiltration or precision filtration membrane used to separate colloidal suspended particles.

〔従来の技術〕[Conventional technology]

従来からポリスルホンおよびスルホン化ポリスルホンは
、逆浸透膜、限外濾過膜、精密濾過膜用素材として有効
であることが知られている。ここでいう膜はポリスルホ
ン又はスルホン化ポリスルホンを適当な溶媒に溶解し、
これをシート状にした後、浴中で凝固するか又は、高分
子支持体上にコーティングし、溶媒を蒸発させることに
よって形成せしめた膜である。このようにして得られた
逆浸透膜、限外濾過膜、精密濾過膜は熱水、加熱スチー
ム、酸、アルカリの他多くの薬品に絶える膜として開発
が進められている。
It has been known that polysulfone and sulfonated polysulfone are effective as materials for reverse osmosis membranes, ultrafiltration membranes, and microfiltration membranes. The membrane here is prepared by dissolving polysulfone or sulfonated polysulfone in a suitable solvent.
A film is formed by forming this into a sheet, coagulating it in a bath, or coating it on a polymeric support and evaporating the solvent. The reverse osmosis membranes, ultrafiltration membranes, and microfiltration membranes thus obtained are being developed as membranes that can withstand hot water, heated steam, acids, alkalis, and many other chemicals.

(発明が解決しようとする問題点〕 従来、ポリスルホン膜は、耐久性の優れた膜でおる事が
知られているが、その分離性能が低い点や、目づまりに
よる造水量の低下が問題であった。
(Problems to be solved by the invention) Conventionally, polysulfone membranes are known to have excellent durability, but they have problems such as low separation performance and a decrease in the amount of water produced due to clogging. there were.

本発明者らは、イオン性基であるカルボン酸基をポリス
ルホン鎖に導入することによってアニオン性物質による
造水量低下を防ぐことを目的として鋭意検討した結果、
カルボン酸基を有するポリスルホン膜は、造水量が低下
する事なく目的物質を分離する事を見い出し本発明に到
達した。
As a result of intensive study by the present inventors with the aim of preventing a decrease in the amount of water produced due to anionic substances by introducing a carboxylic acid group, which is an ionic group, into a polysulfone chain,
The present invention was achieved by discovering that a polysulfone membrane having carboxylic acid groups can separate target substances without reducing the amount of water produced.

(問題点を解決するための手段) 上記目的を達成するため本発明は下記の構成からなる。(Means for solving problems) In order to achieve the above object, the present invention consists of the following configuration.

[(1)  ポリスルホンからなる分離膜において、該
ポリスルホンの主鎖を構成するベンゼン環のいずれかの
位置にカルボン11を有することを特徴とするカルボン
酸基含有ポリスルホン分離膜。
[(1) A polysulfone separation membrane containing a carboxylic acid group, which has carbon 11 at any position of a benzene ring constituting the main chain of the polysulfone.

(2)  カルボン酸基を有するポリスルホン分離膜の
製造方法において、ポリスルホンをアセチル化し、その
後ハロホルム反応によりアセチル基をカルボン酸基に変
換し分離膜とすることを特徴とするカルボン酸基含有ポ
リスルホン分離膜の製造方法。」 本発明により、工業的に生産されているポリスルホンに
イオン性基であるカルボンlの導入が可能となりその結
果長期運転による造水量低下の原因となる目づまり物質
とカルボン酸基含有ポリスルホンとの電子的反発が起こ
り、目づまりによる造水量低下を防ぐことが可能となっ
た。
(2) A method for producing a polysulfone separation membrane containing a carboxylic acid group, which comprises acetylating polysulfone and then converting the acetyl group into a carboxylic acid group through a haloform reaction to obtain a separation membrane. manufacturing method. According to the present invention, it is possible to introduce carboxyl, which is an ionic group, into industrially produced polysulfone, and as a result, the electrons between clogging substances and carboxylic acid group-containing polysulfone, which cause a decrease in the amount of water produced during long-term operation, are enabled. This made it possible to prevent a decrease in the amount of water produced due to clogging.

本発明の一般式[I]、[n]中のR1〜R1B、式[
III]中のR1−R1゜、式[IV]中のR1−R8
のうちカルボン酸基以外の置換基として、水素、低級ア
ルキル基、アミノ基、アミノメチル基、アミノエチル基
、水酸基、ヒドロキシメチル基、ヒドロキシエチル基、
クロロメチル基、クロロエチル基、ブロモメチル基、ブ
ロモエチル基、ヨードメチル基、ヨードエチル基、フッ
素、塩素、臭素、ヨウ素、メトキシ基、エトキシ基、ス
ルホン酸基、カルボキシメチル基、カルボキシエチル基
などが挙げられるが、膜の分離性能を左右する水との親
和性および化合物の安定性から好ましくはスルホン酸基
および水素でおる。
R1 to R1B in the general formula [I] and [n] of the present invention, the formula [
R1-R1° in formula [III], R1-R8 in formula [IV]
Among these, substituents other than carboxylic acid groups include hydrogen, lower alkyl groups, amino groups, aminomethyl groups, aminoethyl groups, hydroxyl groups, hydroxymethyl groups, hydroxyethyl groups,
Examples include chloromethyl group, chloroethyl group, bromomethyl group, bromoethyl group, iodomethyl group, iodoethyl group, fluorine, chlorine, bromine, iodine, methoxy group, ethoxy group, sulfonic acid group, carboxymethyl group, carboxyethyl group, etc. Sulfonic acid groups and hydrogen are preferred from the viewpoint of affinity with water and stability of the compound, which affect the separation performance of the membrane.

式[1]、[n]中のR1−R16、式[I[]中のR
1−R12、式[N]中のR1−R8の中で、水素以外
の置換基であるカルボン酸基は、1繰り返し巾位尚たり
平均0.03〜3個のうちから任意に選ぶことができ、
膜の分離性能を考慮すると0.2〜1個であることが好
ましい。
R1-R16 in formula [1], [n], R in formula [I[]
1-R12, among R1-R8 in formula [N], the carboxylic acid group which is a substituent other than hydrogen can be arbitrarily selected from among 0.03 to 3 on average per repeat width. I can,
Considering the separation performance of the membrane, the number is preferably 0.2 to 1.

本発明においては、ポリスルホンは公知のいかなるもの
でおってもよいが、1例を示すと下記の如きものでおる
In the present invention, the polysulfone may be any known polysulfone, but one example is as follows.

(ただし式[I]、[n]中のR1〜RIB、式[II
I]中のR1〜R1□、式[IV]中のR1−R8のう
ち少なくとも1つはカルボキシル基を示す。)本発明に
おいて分離膜とする技術は、公知のいかなる装膜技術も
使用できる。たとえば、上記のカルボキシル化ホリスル
ホンをジメチルホルムアミドなどの溶媒に溶かしてキャ
スト液とし、これを布帛などの支持体のうえにキャスト
して脱溶媒する方法などである。
(However, R1 to RIB in formula [I], [n], formula [II]
At least one of R1 to R1□ in I] and R1 to R8 in formula [IV] represents a carboxyl group. ) In the present invention, any known membrane coating technology can be used to form a separation membrane. For example, the above-mentioned carboxylated folysulfone is dissolved in a solvent such as dimethylformamide to form a casting liquid, which is then cast onto a support such as a fabric and the solvent is removed.

本発明の式[I]〜[IV]の重合体は、好ましくは第
1段階において、前記一般式[I]、[]I]中のR1
−R16、式[III]中のR1−R12、式[Iυコ
コ中R1−R8が全て水素原子であるポリスルホンに、
フリーデルクラフッ反応によりアセチル基を導入する。
The polymers of formulas [I] to [IV] of the present invention are preferably prepared in the first step by R1
-R16, R1-R12 in formula [III], polysulfone in which R1-R8 in formula [Iυ here are all hydrogen atoms,
An acetyl group is introduced by Friedel-Kraf reaction.

この時用いられる触媒としては各種のルイス酸、例えば
、塩化アルミニウム1、五塩化アンチモン、塩化第二鉄
、塩化第一鉄、四塩化チタン、三フッ化ホウ素、塩化第
二スズ、塩化ビスマス、塩化亜鉛、塩化水銀などが用い
られる仙、フッ化水素、硫酸、ポリリン酸なども用いら
れる。しかし、反応性を考慮すると塩化アルミニウムが
特に好ましいが、塩化第二スズ、塩化亜鉛もよく用いら
れる。)8媒としては、ニトロベンゼン、二硫化炭素、
ジクロロメタン、四塩化炭素、1.2−ジクロロエタン
が用いられるが、溶解性および反応性を考慮すると1.
2−ジクロロエタンが好ましい。第1段階で得られた、
アセチル化ポリスルホンは、第2段階における相間移動
反応によるハロホルム反応を行なう事によってカルボキ
シル基含有ポリスルホンを1qる。相間移動反応の触媒
としては、ヨウ化テトラメチルアンモニウム、臭化テト
ラエチルアンモニウム、塩化プロピルアンモニウム、臭
化71〜57口ピルアンモニウム、硫酸水素テトラブチ
ルアンモニウム、塩化テトラブチルアンモニウム、臭化
テトラブチルアンモニウム、ヨウ化テトラブチルアンモ
ニウム、過塩素酸テトラブチルアンモニウム、臭化テト
ラペンタアンモニウム、臭化テトラヘキサアンモニウム
、臭化テトラヘプタアンモニウム、臭化テトラオクタア
ンモニウムなどのアンモニウム塩が用いられるが、反応
性および取り扱い易さの点から臭化テトラブチルアンモ
ニウムが好ましい。この臭化テトラブチルアンモニウム
は、水相しか溶解しない次亜塩素酸イオンをアセチル化
ポリスルホンが溶解している有殿相へ移動させ、その為
にハロホルム反応を行なう事が可能となる。
Catalysts used at this time include various Lewis acids, such as aluminum 1 chloride, antimony pentachloride, ferric chloride, ferrous chloride, titanium tetrachloride, boron trifluoride, stannic chloride, bismuth chloride, and chloride. Zinc, mercury chloride, etc. are used, and hydrogen fluoride, sulfuric acid, polyphosphoric acid, etc. are also used. However, in consideration of reactivity, aluminum chloride is particularly preferred, but stannic chloride and zinc chloride are also often used. ) As the 8 medium, nitrobenzene, carbon disulfide,
Dichloromethane, carbon tetrachloride, and 1,2-dichloroethane are used, but considering solubility and reactivity, 1.
2-dichloroethane is preferred. obtained in the first stage,
Acetylated polysulfone is converted into 1q of carboxyl group-containing polysulfone by performing haloform reaction by phase transfer reaction in the second step. Catalysts for phase transfer reactions include tetramethylammonium iodide, tetraethylammonium bromide, propylammonium chloride, 71-57 pylammonium bromide, tetrabutylammonium hydrogen sulfate, tetrabutylammonium chloride, tetrabutylammonium bromide, and iodine. Ammonium salts such as tetrabutylammonium chloride, tetrabutylammonium perchlorate, tetrapentaammonium bromide, tetrahexaammonium bromide, tetraheptaammonium bromide, and tetraoctaammonium bromide are used, but they have low reactivity and ease of handling. From this point of view, tetrabutylammonium bromide is preferred. This tetrabutylammonium bromide transfers hypochlorite ions, which are dissolved only in the aqueous phase, to the precipitate phase in which acetylated polysulfone is dissolved, thereby making it possible to carry out the haloform reaction.

具体的な製造方法を以下に示す。A specific manufacturing method is shown below.

本発明の上記式[I]の共重合体は、例えば次の製造方
法に従って製造される。
The copolymer of the above formula [I] of the present invention is produced, for example, according to the following production method.

第1段階     1 第2段階 第1段階:2塩化エタンに溶解したポリスルホンに、塩
化アルミニウム存在下塩化アセ チルを反応させて、式[B]の化合物 を製造する。
1st Step 1 2nd Step 1st Step: Polysulfone dissolved in ethane dichloride is reacted with acetyl chloride in the presence of aluminum chloride to produce a compound of formula [B].

第2段階:式[B]の化合物を塩化メチレンに溶解し、
これを臭化テトラブチルアンモ ニウム水溶液と共に攪拌することによ って、式[C’]の化合物を製造する。
Second step: Dissolving the compound of formula [B] in methylene chloride,
By stirring this with an aqueous tetrabutylammonium bromide solution, a compound of formula [C'] is produced.

本発明で原料化合物として用いるポリスルホンは市販さ
れており(例えば、ユニオン・カーバイト社製の商品名
Udel P−1700)容易に入手することができる
Polysulfone used as a raw material compound in the present invention is commercially available (for example, trade name Udel P-1700 manufactured by Union Carbide Company) and can be easily obtained.

上記した反応プロセスにより、前記式[I]のカルボキ
シル化ポリスルホンはもちろん、その他の共重合体(た
とえば式[■]、式[■]、式[11111]などの共
重合体も製造することができる。
Through the reaction process described above, not only the carboxylated polysulfone of formula [I] but also other copolymers (for example, copolymers of formula [■], formula [■], formula [11111], etc.) can be produced. .

次に、同様の例についての実施例により本発明を更に詳
しく説明する。
The invention will now be explained in more detail by means of similar examples.

〔実施例〕〔Example〕

カルボキシル化ポリスルホンの前駆体であるアセチル化
ポリスルホンは参考例に示す方法によって合成した。
Acetylated polysulfone, which is a precursor of carboxylated polysulfone, was synthesized by the method shown in Reference Example.

参考例1 ■ アセチル化ポリスルホンの合成 窒素気流下、4.30C]の塩化アセチルをジクロロエ
タンに溶解し、更に7.’11CJの塩化アルミニウム
を溶解した。この溶液を、窒素気流下、11、OOg、
ポリスルホン(ユニオン・カーバイト社製の商品名Ud
el P−1700)のジクロロエタン溶液100m1
中に、滴下した。この時の溶液温度は、3℃であった。
Reference Example 1 ■ Synthesis of acetylated polysulfone Under a nitrogen atmosphere, acetyl chloride of 4.30C] was dissolved in dichloroethane, and further 7. '11CJ aluminum chloride was dissolved. This solution was mixed with 11,00 g of nitrogen under a stream of nitrogen.
Polysulfone (trade name Ud manufactured by Union Carbide)
el P-1700) dichloroethane solution 100ml
It dripped inside. The solution temperature at this time was 3°C.

更に4°Cで70分間攪拌した後に、反応溶液を1αの
メタノール中に注いだ、析出した白色沈澱を1戸別し、
更に、45℃/ 2 mmHgの条件下で乾燥を行なっ
た。
After further stirring at 4°C for 70 minutes, the reaction solution was poured into 1α methanol, and the precipitated white precipitate was separated.
Furthermore, drying was performed under the conditions of 45° C./2 mmHg.

収徂=11.52に] ■ 分析結果 赤外吸収:’1680,1582,1250゜1 ’1
45cm−1 核磁気共鳴(CD(43,TMS):δ7,898〜6
.880 (m>、2.511 (S)、1.692 (S)ppm 核磁気共鳴スペクトル分析より、1.38mmol/g
アセチル化されている。
Convergence = 11.52] ■ Analysis result Infrared absorption: '1680, 1582, 1250°1 '1
45cm-1 Nuclear magnetic resonance (CD(43, TMS): δ7,898~6
.. 880 (m>, 2.511 (S), 1.692 (S) ppm From nuclear magnetic resonance spectrum analysis, 1.38 mmol/g
Acetylated.

カルボキシル化ポリスルホンは、実施例1,2で示す方
法によって合成した。
Carboxylated polysulfone was synthesized by the method shown in Examples 1 and 2.

実施例1 アセチル化ポリスルホン1.OOC]を100m1のジ
オキサンに溶解し、そこに市販次亜塩素酸ナトリウム水
溶液(20ml)を滴下し、その後60°Cで3時間加
熱した。反応溶液を酸性にしてから400m1の水中に
沈澱した後、)戸別し、これを再び1001i11のジ
オキサンに溶かした後に20m1の次亜塩素酸ナトリウ
ムを滴下した。60℃で1時間加熱すると2相に分離し
たので有機相を分離した。更に50m1の次亜塩素酸ナ
トリウム水滴液を滴下し、60’Cで1時間加熱したと
ころ、不溶性の化合物が得られたので、溶液を酸性にし
た後に戸別、乾燥した。赤外吸収スペクトルは第1図に
示す。
Example 1 Acetylated polysulfone 1. OOC] was dissolved in 100 ml of dioxane, and a commercially available aqueous sodium hypochlorite solution (20 ml) was added dropwise thereto, followed by heating at 60°C for 3 hours. After the reaction solution was acidified and precipitated in 400 ml of water, it was separated and dissolved again in 1001i11 dioxane, and 20 ml of sodium hypochlorite was added dropwise. When heated at 60° C. for 1 hour, the mixture separated into two phases, and the organic phase was separated. Further, 50 ml of aqueous sodium hypochlorite solution was added dropwise and heated at 60'C for 1 hour. Since an insoluble compound was obtained, the solution was made acidic and then dried from house to house. The infrared absorption spectrum is shown in FIG.

実施例2 200ff113つロフラスコに、次亜塩素酸ナトリウ
ム水溶液3Qml、0.500の臭化テトラブチルアン
モニウムそれに、30m1の塩化メチレンに溶解した0
、50に]のアシル化ポリスルホンを入れ、空温で激し
く澄拌した。反応溶液をビー力に移し、20m1の塩化
メチレンと2Qmlの水を加えた。亜硫酸水素ナトリウ
ムを加えた後に、1NHC0,で水相を酸性にした。有
機相を分離後、n−ヘキサンで再沈澱すると白色粉末が
析出したのでこれを戸別、乾燥した。イオン交換容量は
、1.05meQ/g<1繰り返し単位当たり0.3個
)であった。得られたポリマの赤外吸収スペクトルを第
2図に示す。実施例2で得られたカルボン酸基含有ポリ
スルホン化合物の製膜法を実施例3に示す。
Example 2 In 113 200ff flasks, 3Qml of sodium hypochlorite aqueous solution, 0.500ml of tetrabutylammonium bromide, and 0.5ml of tetrabutylammonium bromide dissolved in 30ml of methylene chloride were added.
, 50] was added, and the mixture was vigorously clarified at air temperature. The reaction solution was transferred to a beaker and 20ml of methylene chloride and 2Qml of water were added. After adding sodium bisulfite, the aqueous phase was made acidic with 1N HCO. After separating the organic phase, it was reprecipitated with n-hexane to precipitate a white powder, which was then dried separately. The ion exchange capacity was 1.05 meQ/g<0.3 molecules per repeating unit). FIG. 2 shows the infrared absorption spectrum of the obtained polymer. Example 3 shows a method for forming a film of the carboxylic acid group-containing polysulfone compound obtained in Example 2.

実施例3 タテ30cm、ヨコ20cmの大きさのポリエステル繊
維からなる不織布をガラス板上に固定し、その上にポリ
スルホン(ユニオン・カーム41〜社製)Udel P
−3500)とカルボン酸基含有ポリスルホン化合物を
6:4(ffli比)の割合で含む16重伍%ジメチル
ホルムアミド(DMF)溶液を250μmの厚みで空温
(20’C)でキャストし、ただちに純水中に浸漬して
5分間放置することによって繊維補強ポリスルホン膜を
作製した。このようにして得られた膜を、温度25°C
1圧力5に9/m2、原水11000pl)ポリエチレ
ングリコール(PEG−100000)水溶液で運転開
始3時間後と21時間後のポリエチレングリコール排除
率と造水量を第1表に示す。
Example 3 A nonwoven fabric made of polyester fibers measuring 30 cm in length and 20 cm in width was fixed on a glass plate, and polysulfone (manufactured by Union Calm 41~) Udel P was placed on top of it.
-3500) and a carboxylic acid group-containing polysulfone compound at a ratio of 6:4 (ffli ratio), a 16% dimethylformamide (DMF) solution was cast to a thickness of 250 μm at air temperature (20'C), and immediately purified. A fiber-reinforced polysulfone membrane was prepared by immersing it in water and leaving it for 5 minutes. The film thus obtained was heated at a temperature of 25°C.
Table 1 shows the polyethylene glycol rejection rate and water generation amount 3 hours and 21 hours after the start of operation using a polyethylene glycol (PEG-100000) aqueous solution (1 pressure 5 to 9/m2, raw water 11000 pl).

比較例 タテ3Qcm、ヨコ20cmの大きさのポリエステル繊
維からなる不織布をガラス板上に固定し、その上にポリ
スルホン(ユニオン・カーバイト社製の商品名Udel
 P−1700)の15@0%ジメチルホルムアミド(
DMF>溶液を200μmの厚みで空温(20’C)で
キャストし、ただちに純水中に浸漬して5分間放置する
ことによって繊維補強ポリスルホン膜を得た。このよう
にして得られたポリスルホン膜を実施例と同様の方法に
よって評価を行なった。その結果を第1表に示す。
Comparative Example A nonwoven fabric made of polyester fibers with a length of 3 Q cm and a width of 20 cm was fixed on a glass plate, and polysulfone (trade name: Udel manufactured by Union Carbide Co., Ltd.) was placed on top of it.
P-1700) in 15@0% dimethylformamide (
A fiber-reinforced polysulfone membrane was obtained by casting the DMF> solution to a thickness of 200 μm at air temperature (20'C), immediately immersing it in pure water, and leaving it for 5 minutes. The polysulfone membrane thus obtained was evaluated in the same manner as in the examples. The results are shown in Table 1.

第1表 第1表において膜性能を示す数字は、 [排除率(%)−造水@(m3/m2・日〉1の形式%
式% (発明の効果〕 本発明により、市販されている化合物を用いてカルボン
酸基含有ポリスルホンを容易に供給することができるよ
うになる。このカルボン酸基含有ポリスルホンは製膜す
ることにより、良好な分離膜性能を示し、運転時間によ
り造水量の低下する事のない膜を製造することができる
Table 1 In Table 1, the numbers indicating membrane performance are as follows:
Formula % (Effect of the invention) According to the present invention, it becomes possible to easily supply a polysulfone containing a carboxylic acid group using a commercially available compound. It is possible to produce a membrane that exhibits excellent separation membrane performance and that does not reduce the amount of water produced due to operating time.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例1のカルボン酸基含有ポリスル
ホンの赤外吸収スペクトルを示す。 第2図は本発明の実施例2のカルボン酸基含有ポリスル
ホンの赤外吸収スペクトルを示す。 特許出願人  東 し 株 式 会 社12図
FIG. 1 shows an infrared absorption spectrum of the carboxylic acid group-containing polysulfone of Example 1 of the present invention. FIG. 2 shows an infrared absorption spectrum of the carboxylic acid group-containing polysulfone of Example 2 of the present invention. Patent applicant Toshi Co., Ltd. Figure 12

Claims (1)

【特許請求の範囲】 (1)ポリスルホンからなる分離膜において、該ポリス
ルホンの主鎖を構成するベンゼン環のいずれかの位置に
カルボン酸基を有することを特徴とするカルボン酸基含
有ポリスルホン分離膜。 (2)ポリスルホンが、下記式[ I ]〜[IV]から選
ばれることを特徴とする特許請求の範囲第(1)項記載
のカルボン酸基含有ポリスルホン分離膜。 ▲数式、化学式、表等があります▼[ I ] ▲数式、化学式、表等があります▼[II] ▲数式、化学式、表等があります▼[III] ▲数式、化学式、表等があります▼[IV] (ただし式[ I ]、[II]中のR_1〜R_1_6、
式[III]中のR_1〜R_1_2、式[IV]中のR_
1〜R_8のうち少なくとも1つはカルボキシル基を示
す。)(3)カルボン酸基が、ポリスルホンの1繰り返
し単位当り0.03〜3個であることを特徴とする特許
請求の範囲第(1)項記載のカルボン酸基含有ポリスル
ホン分離膜。 (4)カルボン酸基が、ポリスルホンの1繰り返し単位
当り0.2〜1個であることを特徴とする特許請求の範
囲第(1)項記載のカルボン酸基含有ポリスルホン分離
膜。 (5)カルボン酸基を有するポリスルホン分離膜の製造
方法において、ポリスルホンをアセチル化し、その後ハ
ロホルム反応によりアセチル基をカルボン酸基に変換し
分離膜とすることを特徴とするカルボン酸基含有ポリス
ルホン分離膜の製造方法。 (6)アセチル化触媒がルイス酸から選ばれることを特
徴とする特許請求の範囲第(5)項記載のカルボン酸基
含有ポリスルホン分離膜の製造方法。 (7)アセチル化触媒が、塩化アルミニウムまたは塩化
第二スズから選ばれることを特徴とする特許請求の範囲
第(5)項記載のカルボン酸基含有ポリスルホン分離膜
の製造方法。 (8)ハロホルム反応が、テトラアルキルアンモニウム
塩を触媒とし、アルカリハイポハライトを相間移動反応
によって反応させることを特徴とする特許請求の範囲第
(5)項記載のカルボン酸基含有ポリスルホン分離膜の
製造方法。
Claims: (1) A polysulfone separation membrane containing a carboxylic acid group, characterized in that the separation membrane is made of polysulfone and has a carboxylic acid group at any position of a benzene ring constituting the main chain of the polysulfone. (2) The carboxylic acid group-containing polysulfone separation membrane according to claim (1), wherein the polysulfone is selected from the following formulas [I] to [IV]. ▲There are mathematical formulas, chemical formulas, tables, etc.▼[I] ▲There are mathematical formulas, chemical formulas, tables, etc.▼[II] ▲There are mathematical formulas, chemical formulas, tables, etc.▼[III] ▲There are mathematical formulas, chemical formulas, tables, etc.▼[ IV] (However, R_1 to R_1_6 in formulas [I] and [II],
R_1 to R_1_2 in formula [III], R_ in formula [IV]
At least one of 1 to R_8 represents a carboxyl group. )(3) The carboxylic acid group-containing polysulfone separation membrane according to claim (1), wherein the number of carboxylic acid groups is 0.03 to 3 per one repeating unit of the polysulfone. (4) The carboxylic acid group-containing polysulfone separation membrane according to claim (1), wherein the number of carboxylic acid groups is 0.2 to 1 per repeating unit of the polysulfone. (5) A method for producing a polysulfone separation membrane having a carboxylic acid group, which comprises acetylating polysulfone and then converting the acetyl group into a carboxylic acid group through a haloform reaction to obtain a separation membrane. manufacturing method. (6) The method for producing a carboxylic acid group-containing polysulfone separation membrane according to claim (5), wherein the acetylation catalyst is selected from Lewis acids. (7) The method for producing a carboxylic acid group-containing polysulfone separation membrane according to claim (5), wherein the acetylation catalyst is selected from aluminum chloride or stannic chloride. (8) The carboxylic acid group-containing polysulfone separation membrane according to claim (5), wherein the haloform reaction is carried out by using a tetraalkylammonium salt as a catalyst and reacting alkali hypohalite by a phase transfer reaction. Production method.
JP12344486A 1986-05-30 1986-05-30 Separation membrane using polysulfone containing carboxyl group and its production Pending JPS62279805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12344486A JPS62279805A (en) 1986-05-30 1986-05-30 Separation membrane using polysulfone containing carboxyl group and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12344486A JPS62279805A (en) 1986-05-30 1986-05-30 Separation membrane using polysulfone containing carboxyl group and its production

Publications (1)

Publication Number Publication Date
JPS62279805A true JPS62279805A (en) 1987-12-04

Family

ID=14860752

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12344486A Pending JPS62279805A (en) 1986-05-30 1986-05-30 Separation membrane using polysulfone containing carboxyl group and its production

Country Status (1)

Country Link
JP (1) JPS62279805A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1099468A3 (en) * 1999-11-10 2002-04-24 DEUTSCHE INSTITUTE FÜR TEXTIL- UND FASERFORSCHUNG STUTTGART Stiftung des öffentlichen Rechts Microporous hydrophilic membrane

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1099468A3 (en) * 1999-11-10 2002-04-24 DEUTSCHE INSTITUTE FÜR TEXTIL- UND FASERFORSCHUNG STUTTGART Stiftung des öffentlichen Rechts Microporous hydrophilic membrane

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