Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0764890B2 - Method for producing crosslinked polystyrene derivative having hydroxyl group - Google Patents
[go: Go Back, main page]

JPH0764890B2 - Method for producing crosslinked polystyrene derivative having hydroxyl group - Google Patents

Method for producing crosslinked polystyrene derivative having hydroxyl group

Info

Publication number
JPH0764890B2
JPH0764890B2 JP61134531A JP13453186A JPH0764890B2 JP H0764890 B2 JPH0764890 B2 JP H0764890B2 JP 61134531 A JP61134531 A JP 61134531A JP 13453186 A JP13453186 A JP 13453186A JP H0764890 B2 JPH0764890 B2 JP H0764890B2
Authority
JP
Japan
Prior art keywords
hydroxyl group
group
crosslinked polystyrene
resin
glycidyl
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
Application number
JP61134531A
Other languages
Japanese (ja)
Other versions
JPS62290703A (en
Inventor
弘 垣内
正男 友井
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP61134531A priority Critical patent/JPH0764890B2/en
Publication of JPS62290703A publication Critical patent/JPS62290703A/en
Publication of JPH0764890B2 publication Critical patent/JPH0764890B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は合成吸着剤、クロマト充填剤として有用な水酸
基を有する親水性架橋ポリスチレン誘導体を製造する方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a hydrophilic crosslinked polystyrene derivative having a hydroxyl group, which is useful as a synthetic adsorbent or a chromatographic packing material.

〔従来の技術〕 従来、水溶液中から有機化合物を吸着回収するための合
成吸着剤としては、多孔質架橋ポリスチレンが用いられ
ている。しかし、ポリスチレンは水とのなじみが悪いた
め、カラムへの充填時に、一度アルコール(水)溶液で
充填した後にアルコールを水に置換するという操作を行
なわないと、合成吸着剤が浮いてしまい、カラムとして
使用できないという欠点があつた。このような多孔質架
橋ポリスチレンを親水化して水なじみをよくする工夫と
して、ポリスチレンへの水酸基の導入がある。
[Prior Art] Conventionally, porous cross-linked polystyrene has been used as a synthetic adsorbent for adsorbing and recovering an organic compound from an aqueous solution. However, since polystyrene is not well compatible with water, the synthetic adsorbent will float unless the column is filled with an alcohol (water) solution and then the alcohol is replaced with water. There was a drawback that it could not be used as. As a device for making such a porous cross-linked polystyrene hydrophilic so as to improve water familiarity, there is introduction of a hydroxyl group into polystyrene.

水酸基を持つ架橋ポリスチレンの合成法として、いくつ
かの方法が知られている。例えば、架橋ポリスチレンを
クロルメチルメチルエーテルでクロルメチル化した後、
クロルメチル基を加水分解する方法がある。しかし、架
橋クロルメチル化ポリスチレンのクロルメチル基は加水
分解を受けにくく、水酸化ナトリウム等のアルカリ水を
用いる加水分解では、十分な水酸基の導入が行なえな
い。
Several methods are known as methods for synthesizing crosslinked polystyrene having a hydroxyl group. For example, after chlormethylating crosslinked polystyrene with chloromethyl methyl ether,
There is a method of hydrolyzing the chloromethyl group. However, the chloromethyl group of crosslinked chloromethylated polystyrene is not easily hydrolyzed, and a sufficient amount of hydroxyl groups cannot be introduced by hydrolysis using alkaline water such as sodium hydroxide.

モノマーとしてビニルベンジルエステルを用い、架橋剤
と共重合した後、加水分解することにより、架橋ポリビ
ニルベンジルアルコールを得る方法もあるが、この方法
ではベンゼン環一つに水酸基が一つしか導入できず、架
橋剤として、ジビニルベンゼンを多く用いた多孔質高架
橋ポリビニルベンジルアルコールでは、親水化が不十分
であつた。このようなポリビニルベンジルアルコールに
糖を反応させて親水性を向上させた樹脂も知られている
が、反応工程が長く複雑である。
There is also a method of obtaining a crosslinked polyvinylbenzyl alcohol by using vinylbenzyl ester as a monomer, copolymerizing with a crosslinking agent, and then hydrolyzing it, but in this method, only one hydroxyl group can be introduced into one benzene ring, As a cross-linking agent, porous highly cross-linked polyvinyl benzyl alcohol using a large amount of divinylbenzene was insufficient in hydrophilization. A resin obtained by reacting a polyvinyl benzyl alcohol with a sugar to improve hydrophilicity is also known, but the reaction process is long and complicated.

親水性の合成吸着剤、クロマト充填剤としては、デキス
トラン、セルロース等の多糖類を架橋したものや、架橋
ポリビニルアルコール、架橋ポリハイドロキシエチル
(メタ)アクリレート等の架橋合成高分子及びこれらの
親水性樹脂に、アルキル基やフエニル基を導入した樹脂
が知られている。しかし、これらの樹脂は、樹脂がやわ
らかく耐圧性に問題があつたり、酸、アルカリに不安定
であるという問題点を有する。
Examples of hydrophilic synthetic adsorbents and chromatographic fillers include cross-linked polysaccharides such as dextran and cellulose, cross-linked polyvinyl alcohol, cross-linked polyhydroxyethyl (meth) acrylate and other cross-linked synthetic polymers and hydrophilic resins thereof. A resin in which an alkyl group or a phenyl group is introduced is known. However, these resins have problems that they are soft and have problems in pressure resistance, and that they are unstable to acids and alkalis.

〔発明の目的〕[Object of the Invention]

本発明の目的は、工業的に有利な方法で親水性にすぐれ
た樹脂の製造方法を提供するものである。すなわち、物
理的安定性、化学的安定性にすぐれた架橋ポリスチレン
に、水酸基やポリエチレングリコール基を導入すること
により、親水性樹脂を製造する方法を提供するものであ
る。
An object of the present invention is to provide a method for producing a resin having excellent hydrophilicity by an industrially advantageous method. That is, the present invention provides a method for producing a hydrophilic resin by introducing a hydroxyl group or a polyethylene glycol group into a crosslinked polystyrene excellent in physical stability and chemical stability.

〔発明の構成〕[Structure of Invention]

本発明の親水性樹脂の製造方法は、下記一般式(I)で
表わされるグリシジル基を有するスチレン誘導体を架橋
剤と共重合させた後、得られた共重合体のグリシジル基
を、水、アルコール、ポリエチレングリコール、又は、
ポリプロピレングリコール等の水酸基を有する化合物と
反応させることにより、水酸基を持つ架橋ポリスチレン
誘導体を得る方法である。
The method for producing a hydrophilic resin of the present invention is a method in which a styrene derivative having a glycidyl group represented by the following general formula (I) is copolymerized with a crosslinking agent, and then the glycidyl group of the obtained copolymer is treated with water or alcohol. , Polyethylene glycol, or
It is a method of obtaining a crosslinked polystyrene derivative having a hydroxyl group by reacting with a compound having a hydroxyl group such as polypropylene glycol.

(m及びnは0〜6の数を示し、RはH又はアルキル基
を示す。) 以下、本発明の構成要素を詳細に説明する。
(M and n show the number of 0-6, R shows H or an alkyl group.) Hereinafter, the component of this invention is demonstrated in detail.

本発明で用いられる一般式(I)で表わされるグリシジ
ル基を有するスチレン誘導体としては、ビニルベンジル
グリシジルエーテル、メチルビニルベンジルグリシジル
エーテル、ビニルフエニルブチルグリシジルエーテル、
ビニルベンジルオキシエチルグリシジルエーテル等々が
あげられる。
Examples of the styrene derivative having a glycidyl group represented by the general formula (I) used in the present invention include vinylbenzyl glycidyl ether, methylvinylbenzyl glycidyl ether, vinylphenyl butyl glycidyl ether,
Examples thereof include vinylbenzyloxyethyl glycidyl ether and the like.

架橋剤としては、ジビニルベンゼン、ジビニルトルエ
ン、ジビニルナフタレン、エチレングリコールジメタク
リレート、トリメチロールプロパントリ(メタ)アクリ
レート等々のスチレンと共重合しうる二個以上のビニル
基を有する単量体が用いられる。
As the cross-linking agent, a monomer having two or more vinyl groups capable of copolymerizing with styrene, such as divinylbenzene, divinyltoluene, divinylnaphthalene, ethylene glycol dimethacrylate, and trimethylolpropane tri (meth) acrylate is used.

グリシジル基を有するスチレン誘導体と架橋剤との共重
合は、公知の懸濁重合により行なうことができる。すな
わち、分散安定剤を含む水相中に、モノマー相としてグ
リシジル基を有するエチレン誘導体、架橋剤、重合開始
剤及び必要に応じ多孔質化剤を含む有機相を分散させ、
加熱、重合することによりビーズ状の共重合体を得るこ
とができる。ここで、分散安定剤としては、ゼラチン、
ポリビニルアルコール、カルボキシメチルセルロース等
の高分子化合物や、ケイ酸マグネシウム、硫酸カルシウ
ム等の微粉末無機化合物が0.05〜5%の濃度で用いられ
る。重合開始剤としては、過酸化ベンゾイルに代表され
る過酸化物、アゾビスイソブチロニトリルに代表される
アゾ化合物等々が単量体に対し0.01〜10重量%用いられ
る。多孔質な架橋共重合体を得るためには、モノマー相
に多孔質化剤を加える必要がある。多孔質化剤として
は、ヘプタン、オクタン、デカン、シクロヘキサン等の
(シクロ)アルカン、ヘキサノール、ペンタノール、2
−エチルヘキサノール等のアルコール等々、モノマーは
溶かすが線状ポリマーは溶解しない溶媒(貧溶媒とも言
う)を単独で単量体に対し20〜70%で又は、トルエン、
シクロロエタン等の線状ポリマーも溶解する溶媒(良溶
媒とも言う)と共に単量体に対し40〜200%で用いた
り、ポリスチレン等の線状ポリマーを単独で単量体に対
し2〜40%、又は良溶媒と共に用いたりする。重合反応
は、主に窒素雰囲気下で、50〜90℃で5〜24時間加熱す
ることにより行なわれる。
The copolymerization of the styrene derivative having a glycidyl group and the crosslinking agent can be carried out by a known suspension polymerization. That is, in an aqueous phase containing a dispersion stabilizer, an ethylene derivative having a glycidyl group as a monomer phase, a cross-linking agent, a polymerization initiator and an organic phase containing a porosifying agent as necessary are dispersed,
A bead-shaped copolymer can be obtained by heating and polymerizing. Here, as the dispersion stabilizer, gelatin,
Polymer compounds such as polyvinyl alcohol and carboxymethyl cellulose, and fine powder inorganic compounds such as magnesium silicate and calcium sulfate are used at a concentration of 0.05 to 5%. As the polymerization initiator, a peroxide represented by benzoyl peroxide, an azo compound represented by azobisisobutyronitrile, or the like is used in an amount of 0.01 to 10% by weight based on the monomer. In order to obtain a porous crosslinked copolymer, it is necessary to add a porosifying agent to the monomer phase. Examples of the porosifying agent include (cyclo) alkanes such as heptane, octane, decane, and cyclohexane, hexanol, pentanol, 2
-Ethanol such as alcohol such as ethylhexanol, which dissolves a monomer but does not dissolve a linear polymer (also referred to as a poor solvent), is used at 20 to 70% with respect to the monomer alone, or toluene,
With a solvent that also dissolves linear polymers such as sichloroethane (also called a good solvent), it is used at 40 to 200% with respect to the monomer, or linear polymer such as polystyrene is used at 2 to 40% with respect to the monomer alone. Or used together with a good solvent. The polymerization reaction is carried out mainly by heating at 50 to 90 ° C. for 5 to 24 hours under a nitrogen atmosphere.

得られた共重合体のグリシジル基と反応させる水酸基を
有する化合物としては、メタノール、エタノール、プロ
パノール、ブタノール、エチレングリコール、プロピレ
ングリコール、グリセリン等々の脂肪族アルコール、フ
エノール、カテコール、ピロガロール等々の芳香族アル
コール、ジエチレングリコール、トリエチレングリコー
ル等々のポリエチレングリコール、ジプロピレングリコ
ール、トリプロピレングリコール等のポリプロピレング
リコール及び水が挙げられる。
Examples of the compound having a hydroxyl group that reacts with the glycidyl group of the obtained copolymer include aliphatic alcohols such as methanol, ethanol, propanol, butanol, ethylene glycol, propylene glycol and glycerin, and aromatic alcohols such as phenol, catechol and pyrogallol. , Polyethylene glycol such as diethylene glycol and triethylene glycol, polypropylene glycol such as dipropylene glycol and tripropylene glycol, and water.

これらの水酸基を有する化合物の反応は、溶媒を用いな
くとも行なうことができるが、ジオキサン、エチレンク
ロライド、トルエン等の共重合体を膨潤する溶媒を用い
ると反応が容易になる。また、この反応には、硫酸、塩
酸、三フツ化ホウ素等の酸触媒又は、水酸化ナトリウ
ム、水酸化カリウム等又は、トリエチルアミン等の3級
アミンのごときアルカリ触媒を必要とする。
The reaction of these compounds having a hydroxyl group can be carried out without using a solvent, but the reaction is facilitated by using a solvent which swells the copolymer such as dioxane, ethylene chloride and toluene. Further, this reaction requires an acid catalyst such as sulfuric acid, hydrochloric acid or boron trifluoride, or an alkali catalyst such as sodium hydroxide or potassium hydroxide or a tertiary amine such as triethylamine.

水酸基を有する化合物の種類及びその導入量により、親
水化の程度を任意に変えることができる。グリシジル基
との反応率を最大にするためには、共重合体中のグリシ
ジル基の10倍量以上の水酸基を有する化合物を用いる。
グリシジル基との反応は、50〜90℃で2〜24時間程度行
なう。
The degree of hydrophilization can be arbitrarily changed depending on the type of the compound having a hydroxyl group and the amount of the compound introduced. In order to maximize the reaction rate with the glycidyl group, a compound having 10 times or more hydroxyl groups as compared with the glycidyl group in the copolymer is used.
The reaction with the glycidyl group is carried out at 50 to 90 ° C. for about 2 to 24 hours.

ポリエチレングリコールによる変性等、反応後もグリシ
ジル基の残存がある場合には、1〜20%程度の硫酸を用
いて、50〜80℃で1〜8時間程度加熱して開環反応を行
ない、親水性の架橋ポリスチレン誘導体を得る。
If glycidyl groups remain after the reaction such as modification with polyethylene glycol, use 1 to 20% sulfuric acid to heat the ring at 50 to 80 ° C for 1 to 8 hours to perform the ring opening reaction. A cross-linked polystyrene derivative having a property of being obtained.

〔実施例〕〔Example〕

以下、本発明を実施例により更に詳細に説明する。 Hereinafter, the present invention will be described in more detail with reference to Examples.

実施例1 A:多孔質架橋ポリビニルベンジルグリシジルエーテルの
合成 撹拌装置と窒素導入管、冷却器及び温度計を取り付けた
500mlの四ツ口フラスコに、分散媒として、ポリビニル
ピロリドン2.5gを含む水275mlを入れ、モノマー相とし
て、ビニルベンジルグリシジルエーテル19g、ジビニル
ベンゼン(純度55%)15.4g、4−メチル−2−ペンタ
ノール28g、オクタン7g、アゾビスイソブチロニトリル
0.7gの混合溶液を分散した。窒素雰囲気下で30分間分散
した後、70℃−24時間重合反応を行なつた。
Example 1 A: Synthesis of porous cross-linked polyvinyl benzyl glycidyl ether A stirring device, a nitrogen introducing tube, a condenser and a thermometer were attached.
A 500 ml four-necked flask was charged with 275 ml of water containing 2.5 g of polyvinylpyrrolidone as a dispersion medium, and as a monomer phase, 19 g of vinylbenzyl glycidyl ether, 15.4 g of divinylbenzene (purity 55%), 4-methyl-2-pen. 28g Tanol, 7g Octane, Azobisisobutyronitrile
0.7 g of the mixed solution was dispersed. After dispersing for 30 minutes in a nitrogen atmosphere, a polymerization reaction was carried out at 70 ° C for 24 hours.

得られた共重合体ビーズは、過、熱メタノール洗浄
後、アセトン洗浄を行ない、60℃で減圧乾燥した。収量
は31gであつた。
The copolymer beads thus obtained were washed with excess methanol, hot methanol, washed with acetone, and dried under reduced pressure at 60 ° C. The yield was 31 g.

得られた共重合体ビーズのエポキシ環の含有量を、塩酸
−ジオキサン法により測定したところ、2.5mmol/gであ
つた。
The epoxy ring content of the obtained copolymer beads was measured by the hydrochloric acid-dioxane method and found to be 2.5 mmol / g.

B:多孔質架橋ポリビニルベンジルグリシジルエーテルの
水による変性 撹拌装置、冷却器、温度計を取りつけた三ツ口フラスコ
に、Aで得られた共重合体5.0gとジオキサン100mlを入
れ、アスピレーターを用いて、樹脂から気泡がでなくな
るまで脱気した。その後、5NのH2SO4水溶液500mlを加
え、80℃で24時間反応させた。反応終了後、樹脂を過
し、水で、液が中性になるまで洗浄後、アセトンで洗
浄した。60℃で減圧乾燥後1,2−グリコール基を有する
樹脂5.2gを得た。生成した樹脂のIRスペクトルでは、水
酸基の特性吸収3500cm-1のピークが発現した。
B: Modification of porous cross-linked polyvinyl benzyl glycidyl ether with water Into a three-necked flask equipped with a stirrer, a cooler and a thermometer, 5.0 g of the copolymer obtained in A and 100 ml of dioxane were put, and a resin was added using an aspirator. Degas from until no bubbles left. Then, 500 ml of a 5N H 2 SO 4 aqueous solution was added, and the mixture was reacted at 80 ° C. for 24 hours. After the reaction was completed, the resin was filtered, washed with water until the liquid became neutral, and then washed with acetone. After drying under reduced pressure at 60 ° C, 5.2 g of a resin having a 1,2-glycol group was obtained. In the IR spectrum of the resin produced, a peak at a characteristic absorption of hydroxyl groups of 3500 cm -1 was developed.

グリシジル基の開環反応率は、塩酸・ジオキサン法によ
り、残存エポキシ環の定量を行なうことにより決定し
た。反応率は92%であつた。
The ring-opening reaction rate of the glycidyl group was determined by quantifying the residual epoxy ring by the hydrochloric acid / dioxane method. The reaction rate was 92%.

実施例2 A:多孔質架橋ポリビニルベンジルグリシジルエーテルの
合成 撹拌装置と窒素導入管、冷却器及び温度計を取りつけた
四ツ口フラスコに、分散媒として、ポリビニルアルコー
ル1.5gを含む水300mlを入れ、モノマー相として、ビニ
ルベンジルグリシジルエーテル20g、ジビニルベンゼン
(純度56%)20g、n−ヘプタン15g、2,2′−アゾビス
−2,4−ジメチルバレロニトリル0.2gの混合溶液を分散
した。窒素雰囲気下で30分間分散した後、70℃−8時間
重合反応を行なつた。得られた共重合体ビーズは、
過、水洗後、アセトンで洗浄した後、室温で減圧乾燥し
た。収量は32gであつた。塩酸・ジオキサン法で測定し
たエポキシ環の存在量は、2.1mmol/gであつた。
Example 2 A: Synthesis of porous cross-linked polyvinyl benzyl glycidyl ether In a four-necked flask equipped with a stirrer, a nitrogen inlet tube, a condenser and a thermometer, 300 ml of water containing 1.5 g of polyvinyl alcohol was placed as a dispersion medium, As a monomer phase, a mixed solution of 20 g of vinylbenzyl glycidyl ether, 20 g of divinylbenzene (purity 56%), 15 g of n-heptane and 0.2 g of 2,2'-azobis-2,4-dimethylvaleronitrile was dispersed. After dispersing for 30 minutes in a nitrogen atmosphere, a polymerization reaction was carried out at 70 ° C. for 8 hours. The obtained copolymer beads are
After washing with water, washing with acetone, and drying under reduced pressure at room temperature. The yield was 32 g. The abundance of the epoxy ring measured by the hydrochloric acid / dioxane method was 2.1 mmol / g.

B:多孔質架橋ポリビニルグリシジルエーテルのグリセリ
ンによる変性 撹拌装置、冷却器、温度計を取りつけた三ツ口フラスコ
にAで得られた共重合体5.0g、ジオキサン35ml、グリセ
リン14mlを加え、更に酸触媒として3フツ化ホウ素エチ
ルエーテルコンプレツクス1mlを加え、80℃で6時間反
応させた。樹脂は過後、ジオキサン、水で順次洗浄を
行なつた。
B: Modification of porous cross-linked polyvinyl glycidyl ether with glycerin To a three-necked flask equipped with a stirrer, a cooler, and a thermometer, 5.0 g of the copolymer obtained in A, 35 ml of dioxane, and 14 ml of glycerin were added, and 3 as an acid catalyst 1 ml of boron fluoride ethyl ether complex was added and reacted at 80 ° C. for 6 hours. After the resin passed, it was washed successively with dioxane and water.

このようにして得られた樹脂を60℃で減圧乾燥を行なつ
た後、塩酸・ジオキサン法により残存エポキシ環の定量
を行ない、エポキシ環の反応率を求めたところ、エポキ
シ環の反応率は、89%であつた。また、生成した樹脂の
IRスペクトルでは、水酸基の特性吸収3500cm-1のピーク
が発現した。
After the resin thus obtained was dried under reduced pressure at 60 ° C., the residual epoxy ring was quantified by the hydrochloric acid / dioxane method, and the reaction rate of the epoxy ring was determined. It was 89%. In addition, the generated resin
In the IR spectrum, a peak at a characteristic absorption of hydroxyl groups of 3500 cm -1 was developed.

実施例3 多孔質架橋ポリビニルベンジルグリシジルエ
ーテルのポリエチレングリコールによる変性 実施例2・Aで得られた共重合体ビーズ5.0gを、ポリエ
チレングリコール#300(キシダ化学社製)15gのジオキ
サン45ml溶液を加え、ポリエチレングリコールで変性し
た。反応操作は実施例2・Bと同様にして行なつた。
Example 3 Modification of porous cross-linked polyvinyl benzyl glycidyl ether with polyethylene glycol 5.0 g of the copolymer beads obtained in Example 2A were added with a solution of 15 g of polyethylene glycol # 300 (Kishida Chemical Co., Ltd.) in 45 ml of dioxane, It was modified with polyethylene glycol. The reaction operation was performed in the same manner as in Example 2B.

得られた樹脂の一部をとり、60℃で減圧乾燥後残存エポ
キシ基の量を、塩酸・ジオキサン法により測定しエポキ
シ環の反応率を求めたところ、63%であつた。生成した
樹脂のIRスペクトルでは、水酸基の特性吸収3500cm-1
ピークが確認された。
A part of the obtained resin was dried under reduced pressure at 60 ° C., and the amount of residual epoxy groups was measured by the hydrochloric acid / dioxane method to obtain a reaction rate of epoxy ring, which was 63%. In the IR spectrum of the produced resin, a peak at a characteristic absorption of a hydroxyl group of 3500 cm -1 was confirmed.

残りの樹脂に10%硫酸35mlを加え、60℃−5時間加熱処
理した。処理後の樹脂の一部をとり、60℃で減圧乾燥
後、塩酸・ジオキサン法により残存エポキシ環の量を定
量したところ、6%であつた。
35 ml of 10% sulfuric acid was added to the remaining resin, and the mixture was heated at 60 ° C. for 5 hours. A part of the treated resin was taken, dried under reduced pressure at 60 ° C., and the amount of residual epoxy ring was quantified by the hydrochloric acid / dioxane method.

〔発明の効果〕 本発明によると容易に化学的、物理的安定性にすぐれた
架橋ポリスチレン誘導体が得られるものである。
[Advantages of the Invention] According to the present invention, a crosslinked polystyrene derivative having excellent chemical and physical stability can be easily obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】下記一般式(I)で表わされるグリシジル
基を有するスチレン誘導体を、二個以上のビニル基を有
する単量体と共重合させた後、得られた共重合体のグリ
シジル基を、水酸基を有する化合物で変性することを特
徴とする、水酸基を持つ架橋ポリスチレン誘導体の製造
方法。 (m及びnは0〜6の数を示し、RはH又はアルキル基
を示す)
1. A styrene derivative having a glycidyl group represented by the following general formula (I) is copolymerized with a monomer having two or more vinyl groups, and then the glycidyl group of the obtained copolymer is converted into A method for producing a crosslinked polystyrene derivative having a hydroxyl group, which comprises denaturing with a compound having a hydroxyl group. (M and n are numbers from 0 to 6, and R is H or an alkyl group)
JP61134531A 1986-06-10 1986-06-10 Method for producing crosslinked polystyrene derivative having hydroxyl group Expired - Lifetime JPH0764890B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61134531A JPH0764890B2 (en) 1986-06-10 1986-06-10 Method for producing crosslinked polystyrene derivative having hydroxyl group

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61134531A JPH0764890B2 (en) 1986-06-10 1986-06-10 Method for producing crosslinked polystyrene derivative having hydroxyl group

Publications (2)

Publication Number Publication Date
JPS62290703A JPS62290703A (en) 1987-12-17
JPH0764890B2 true JPH0764890B2 (en) 1995-07-12

Family

ID=15130497

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61134531A Expired - Lifetime JPH0764890B2 (en) 1986-06-10 1986-06-10 Method for producing crosslinked polystyrene derivative having hydroxyl group

Country Status (1)

Country Link
JP (1) JPH0764890B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6911464B2 (en) * 2017-03-31 2021-07-28 昭和電工マテリアルズ株式会社 Separator and column

Also Published As

Publication number Publication date
JPS62290703A (en) 1987-12-17

Similar Documents

Publication Publication Date Title
US5244926A (en) Preparation of ion exchange and adsorbent copolymers
US4052343A (en) Crosslinked, macroreticular poly(dimethylaminoethyl methacrylate) ion-exchange resins and method of preparation by aqueous suspension polymerization using trialkylamine phase extender
US3586646A (en) Cation exchanger with sponge structure
EP2205672B1 (en) Non-ionic porous, small solid resin with chemically bonded crown ether
JP2005510609A5 (en)
AU2002353728A1 (en) Post-modification of a porous support
US4031037A (en) Three-dimensional polymeric gel materials containing phosphoric acid residues capable of dissociation and a method for their preparation
JPH07330827A (en) Polymer carrier Organic tin catalyst
JP3629795B2 (en) Anion exchanger
US2862894A (en) Preparation of anion-exchange resins containing weakly basic and strongly basic functional groups
JPH0764890B2 (en) Method for producing crosslinked polystyrene derivative having hydroxyl group
JP3446274B2 (en) Manufacturing method of separation agent
EP0135292A1 (en) A method of preparing a highly porous resin
JPH0518843B2 (en)
JP4341097B2 (en) Crosslinked polymer particles for anion analysis liquid chromatography, production method thereof and use thereof
JP3232699B2 (en) Porous anion exchange resin and method for producing the same
JP3543476B2 (en) Method for producing crosslinked copolymer
JP3716056B2 (en) Weakly basic anion exchanger
EP0496405A1 (en) Porous resin and process for its production
JPH1028879A (en) Ion exchange resin with improved water washability and method for producing the same
JPH0722711B2 (en) Anion exchange resin and method for producing the same
JP2890481B2 (en) Method for producing hydrophilic crosslinked copolymer particles
JPS5813561B2 (en) Hannosei Epoxide Kioyuusurujiyugoutai Oyobi Sonoseizohou
JPH0667990B2 (en) Crosslinked copolymer and method for producing ion exchange resin using the same as a matrix
JPH0142746B2 (en)

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term