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JPH0314499B2 - - Google Patents
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JPH0314499B2 - - Google Patents

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Publication number
JPH0314499B2
JPH0314499B2 JP56122300A JP12230081A JPH0314499B2 JP H0314499 B2 JPH0314499 B2 JP H0314499B2 JP 56122300 A JP56122300 A JP 56122300A JP 12230081 A JP12230081 A JP 12230081A JP H0314499 B2 JPH0314499 B2 JP H0314499B2
Authority
JP
Japan
Prior art keywords
resin
general formula
group
structural unit
anion exchange
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
JP56122300A
Other languages
Japanese (ja)
Other versions
JPS5824354A (en
Inventor
Koji Itagaki
Yoshio Umezawa
Akihiro Shimura
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 Industries Ltd
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 Industries Ltd filed Critical Mitsubishi Chemical Industries Ltd
Priority to JP56122300A priority Critical patent/JPS5824354A/en
Publication of JPS5824354A publication Critical patent/JPS5824354A/en
Publication of JPH0314499B2 publication Critical patent/JPH0314499B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は親水性の弱塩基性陰イオン交換樹脂に
関するものである。 特に本発明は、使用時における体積変化の小さ
い弱塩基性の陰イオン交換樹脂に関するものであ
る。 弱塩基性陰イオン交換樹脂としては、ビニルベ
ンジルアミン、N−アミノアルキルアクリルアミ
ド、ビニルピリジン、アミノアルコールの(メ
タ)アクリル酸エステル等の架橋共重合体や、ポ
リエチレンイミン、アミノアルキルセルロース、
アミノアルキルデキストラン等の架橋物が良く知
られている。しかし、これらの弱塩基性陰イオン
交換樹脂は、一般に水溶液中で著るしく膨潤した
り、遊離塩基形と負荷形との体積変化が大きいと
いう欠点を有している。 本発明は、下記一般式(1)及び下記一般式(2)で示
される構造単位を有し、多価アルコールのポリア
クリル酸エステルおよびポリメタクリル酸エステ
ルから選ばれた架橋剤により架橋されてなる架橋
共重合体であつて、架橋剤の含有量が20(重量)
%以上80(重量)%以下であり、イオン交換容量
が0.1〜3meq/grである親水性の弱塩基性陰イ
オン交換樹脂を提供するものである。 (式中R1は水素原子またはメチル基を示し、R2
及びR3は水素原子または置換基を有していても
よいアルキル基を示す。) (式中、R1は水素原子またはメチル基を示す。) 本発明に係る弱塩基性の陰イオン交換樹脂は適
度の硬さを有しており、使用時における体積変化
が少ないので、高速液体クロマトグラフイーの充
填剤として特に好適である。 本発明に係る弱塩基性陰イオン交換樹脂につい
て詳細に説明すると、このものは、陰イオン交換
能を与える前記一般式(1)で示される構造単位と、
親水性を与える一般式(2)で示される構造単位を有
し、更に多価アルコールのポリアクリル酸エステ
ルおよびポリメタクリル酸エステルから選ばれる
架橋剤による架橋構造を有するものである。 多価アルコールのポリアクリル酸エステルまた
はポリメタクリル酸エステルとしては、通常、エ
チレングリコールジメタクリレート、ジエチレン
グリコールジメタクリレート、トリエチレングリ
コールジメタクリレート、テトラエチレングリコ
ールジメタクリレート、プロピレングリコールジ
メタクリレート、ジプロピレングリコールジメタ
クリレート、トリプロピ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クリ
レート、ペンタエリスリトールテトラメタクリレ
ート、1、3−ブチレングリコールジメタクリレ
ートおよびこれらに対応するアクリレートが、単
独でまたは混合して用いられる。好ましくはエチ
レングリコールのジアクリレートまたはジメタク
リレートが用いられる。これらの架橋剤は樹脂中
の20(重量)%以上80(重量)%以下を占めるべき
である。特に好ましくは、樹脂の30〜60(重量)
%を占める。樹脂中に占める架橋剤の比率が小さ
過ぎると樹脂の膨潤性が大きくなり、高速液体ク
ロマトグラフイーの充填剤その他の用途に不適当
となる。逆に架橋剤の比率が大きくなり過ぎる
と、前記一般式(1)で示される構造単位の減少によ
る交換容量の低下または前記一般式(2)で示される
構造単位の減少による親水性の低下をもたらす。 前記一般式(1)で示される構造単位としては、
R2及びR3が、両方又は一方が水素原子、アルキ
ル基、ヒドロキシ基置換アルキル基、置換されて
いてもよいアミノ基置換アルキル基であるものが
挙げられ、具体的には式中の
The present invention relates to a hydrophilic weakly basic anion exchange resin. In particular, the present invention relates to a weakly basic anion exchange resin that exhibits small volume changes during use. Examples of weakly basic anion exchange resins include crosslinked copolymers such as vinylbenzylamine, N-aminoalkylacrylamide, vinylpyridine, and (meth)acrylic acid esters of aminoalcohols, polyethyleneimine, aminoalkylcellulose,
Crosslinked products such as aminoalkyl dextran are well known. However, these weakly basic anion exchange resins generally have the disadvantage that they swell significantly in aqueous solutions and have a large volume change between the free base form and the loaded form. The present invention has a structural unit represented by the following general formula (1) and the following general formula (2), and is crosslinked with a crosslinking agent selected from polyacrylic esters and polymethacrylic esters of polyhydric alcohols. A crosslinked copolymer with a crosslinking agent content of 20 (by weight)
% to 80% (by weight) and has an ion exchange capacity of 0.1 to 3 meq/gr. (In the formula, R 1 represents a hydrogen atom or a methyl group, and R 2
and R 3 represents a hydrogen atom or an alkyl group which may have a substituent. ) (In the formula, R 1 represents a hydrogen atom or a methyl group.) The weakly basic anion exchange resin according to the present invention has appropriate hardness and has little volume change during use, so it can be used as a high-speed liquid. It is particularly suitable as a packing material for chromatography. To explain in detail the weakly basic anion exchange resin according to the present invention, this resin has a structural unit represented by the general formula (1) that provides anion exchange ability,
It has a structural unit represented by the general formula (2) that provides hydrophilicity, and further has a crosslinked structure using a crosslinking agent selected from polyacrylic esters and polymethacrylic esters of polyhydric alcohols. Polyacrylic esters or polymethacrylic esters of polyhydric alcohols usually include ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, triethylene glycol dimethacrylate, tetraethylene glycol dimethacrylate, propylene glycol dimethacrylate, dipropylene glycol dimethacrylate, Tripropylene glycol dimethacrylate, trimethylolpropane trimethacrylate, pentaerythritol tetramethacrylate, 1,3-butylene glycol dimethacrylate and their corresponding acrylates are used alone or in mixtures. Preferably, diacrylate or dimethacrylate of ethylene glycol is used. These crosslinking agents should account for at least 20% (by weight) and at most 80% (by weight) of the resin. Particularly preferably 30 to 60 (by weight) of the resin
%. If the proportion of the crosslinking agent in the resin is too small, the resin will have a large swelling property, making it unsuitable for use as a filler for high performance liquid chromatography or other uses. On the other hand, if the ratio of the crosslinking agent becomes too large, the exchange capacity will decrease due to a decrease in the structural units represented by the general formula (1), or the hydrophilicity will decrease due to a decrease in the structural units represented by the general formula (2). bring. The structural unit represented by the general formula (1) is as follows:
Examples include those in which both or one of R 2 and R 3 is a hydrogen atom, an alkyl group, a hydroxy group-substituted alkyl group, an optionally substituted amino group-substituted alkyl group, and specifically, in the formula

【式】構造とし て、アミノ基、メチルアミノ基、ジメチルアミノ
基、エチルアミノ基、ジエチルアミノ基、プロピ
ルアミノ基、ジプロピルアミノ基、β−ヒドロキ
シエチルアミノ基、ビス(β−ヒドロキシエチ
ル)アミノ基、β−アミノエチルアミノ基、β−
エチルアミノエチルアミノ基、β−(β−エチル
アミノエチル)アミノエチルアミノ基などの基を
有する構造単位である。 また、前記一般式(1)の構造単位は樹脂のイオン
交換容量が0.1〜3meq/gとなる量で樹脂中に存
在させる。イオン交換容量が0.1meq/gより小
さいとイオン交換樹脂としての実用性に乏しい。
一方、イオン交換容量が3meq/gより大きくな
ると、遊離塩基形と負荷形との間の樹脂の体積変
化が大きくなり、実用上種々の障害をもたらす。 本発明に係る樹脂の好適なイオン交換容量は
0.3〜2meq/gである。前記一般式(2)で示される
構造単位は、(前記一般式(2)で示される構造単位
+前記一般式(1)で示される構造単位)の合計モル
数に対する前記一般式(2)で示される構造単位のモ
ル数が30〜98%を占めるような量で樹脂中に存在
させるのが好ましい。前記一般式(2)で示される構
造単位の量が少ないと樹脂の親水性が低下する。 本発明に係る樹脂は上記の架橋剤部分、前記一
般式(1)で示される構造単位部分および前記一般式
(2)で示される構造単位部分から本質的に成つてい
るが、所望ならばアクリル酸またはメタクリル酸
のメチルエステルやエチルエステルから由来する
構造単位を含んでいてもよい。 本発明に係る樹脂は、架橋剤とアクリル酸また
はメタクリル酸のグリシジルエステルとを共重合
させて架橋共重合体とし、次いでこれにアミンを
反応させてグリシジルエステルの一部を3−アミ
ノ−2−ヒドロキシプロピルエステルに変化させ
たのち、グリシジルエステルのエポキシ環を水と
反応させて開環させることにより容易に製造する
ことができる。 重合反応は公知の任意の方法で行ない得るが、
通常は適当な分散安定剤を存在させた水性媒体中
で懸濁重合方式で行ない、粒状の共重合体を得る
のが好ましい。分散安定剤としては、通常、ゼラ
チン、ポリアクリル酸ソーダ、カルボキシメチル
セルロース、ポリビニルアルコール等が用いられ
る。また、水性媒体中には塩類を溶解させて重合
反応原料の水性媒体中への溶解を防止するのが好
ましい。塩としては、塩化ナトリウム、塩化カル
シウム、硫酸ナトリウム、炭酸ナトリウム等が用
いられる。重合反応は一般に適当な重合開始剤を
用いて行なわれる。重合開始剤としては、一般に
過酸化ベンゾイル、t−ブチルハイドロパーオキ
サイド、アゾビスイソブチロニトリル、ジメチル
アゾビス(メチルバレート)、アゾビス(α、α
−ジメチルバレロニトリル)等の有機過酸化物や
有機アゾビス化合物等が用いられる。これらの重
合開始剤は、通常、反応原料の0.01〜5(重量)
%となるような量で使用される。 重合反応は通常、撹拌下に50〜90℃で6〜20時
間で完了する。また、この重合反応に際して多孔
質の架橋共重合体を生成させると、多孔質の親水
性でかつ弱塩基性の陰イオン交換樹脂を得ること
ができる。多孔質の架橋共重合体の製法は公知で
あり、通常は、(1)反応原料中に、これに均一に混
和するが、生成する架橋共重合体に対しては親和
性の少ない溶媒を存在させて重合する方法、(2)反
応原料中にポリスチレンのような線状重合体を存
在させて重合し、生成した架橋共重合体から該線
状重合体を抽出除去する方法、(3)反応原料中にポ
リスチレンのような線状重合体とトルエン、酢酸
エチル、ジメチルホルムアミドのような生成する
架橋共重合体に親和性を有する溶媒を存在させて
重合し、生成した架橋共重合体から該線状重合体
を抽出除去する方法のいずれかが用いられる。 架橋共重合体とアミンとの反応は、(3)式に対応
する1級または2級アミンを水、メタノール、ジ
オキサン、トルエン等の溶媒に溶解し、これに架
橋共重合体を懸濁させて、40〜100℃で3〜10時
間反応させればよい。エポキシ環のアミノ化の程
度は、反応条件を選択することにより容易に調節
することができる。 エポキシ環の開環反応は、上記によりアミノ化
した架橋共重合体を、硫酸か燐酸を含む水中に懸
濁させ、30〜100℃で5〜20時間保持すればよい。 本発明に係る弱塩基性陰イオン交換樹脂は、そ
の内部にグリセリンモノエステル構造を含んでい
るので親水性に富んでいる。また、架橋剤を含め
て全体が脂肪族成分で構成されていて芳香族成分
を含まないので、蛋白質その他の種々の有機物に
対する疎水結合に起因する物理的吸着が少ない。
さらに本発明に係る弱塩基性陰イオン交換樹脂
は、遊離塩基形と負荷形との間における体積変化
が少なく、かつ硬くてカラムに充填したときに圧
力損失が少ない。従つて本発明に係る弱塩基性の
陰イオン交換樹脂はクロマトグラフイー、特に高
速液体クロマトグラフイーの充填剤として有用で
ある。 以下に実施例により本発明をさらに具体的に説
明するが、本発明はその要旨を超えない限り、以
下の実施例に限定されるものではない。 なお、本明細書におけるイオン交換樹脂の交換
容量、膨潤度およびC/OH体積比は以下のよ
うにして測定した。 交換容量および膨潤度 水酸化ナトリウム水溶液で再生したのち脱塩水
で十分に水洗したOH形樹脂を10mlのメスシリン
ダーに入れ、底部を軽くたたきながら正確に10ml
秤取する。この樹脂を遠心分離機で350Gで5分
間脱水したのち、その重量(a1g)を精秤する。 次いで、この樹脂を0.2規定の塩酸水溶液200ml
中に入れ、室温で24時間振盪する。この塩酸水溶
液の20mlを0.1規定の水酸化ナトリウム水溶液で
滴定する。 別に、上記と同様にして正確に10mlの樹脂を秤
取し、上記と同様にして脱水したのちその重量
(a2g)を精秤する。次いで、この樹脂を60℃、
10mmHgの真空乾燥器中で24時間乾燥したのち、
再び重量(Cg)を精秤する。 膨潤度=10/C(ml/g) 交換容量=(ho−h)×0.1×f×200/20/a1
×C/a2(meq/g) ここに、h及びhoは、それぞれ樹脂を投入す
る前及び投入した後の、滴定に要した水酸化ナト
リウムの量(ml)、fは水酸化ナトリウムのフア
クターである。 Cl/OH体積比 樹脂を水酸化ナトリウム水溶液で再生し、水洗
したのち、1規定塩酸でC形とし、脱塩水で十
分に水洗する。この樹脂を10mlのメスシリンダー
に入れ、底部を軽くたたきながら正確に10ml秤取
する。この樹脂を1規定水酸化ナトリウム水溶液
でOH形にしたのち脱塩水で十分に水洗する。10
mlのメスシリンダーを用いて底部を軽くたたきな
がら樹脂の体積(dml)を測定する。 C/OH体績比=10/d 実施例 1 グリシジルメタクリレート210g、エチレング
リコールジメタクリレート90g、トルエン300g
および2,2′−アゾビス−2,4−ジメチルバレ
ロニトリル3gの混合物を、イオン交換水2100ml
にポリビニルアルコール21gと塩化ナトリウム
168gを溶解した溶液に加え、高速で撹拌しなが
ら70℃で8時間懸濁重合させた。反応物を冷却し
たのち生成した共重合体粒子を取し、水洗し
た。次いでこの共重合体を、トルエン1125mlと水
375mlとの混合液中に入れ、室温で3時間撹拌し
たのち過した。更に、この共重合体を1.5の
メタノールに投入して撹拌することを2回反復し
たのち、80℃で8時間乾燥した。以上の操作を経
た粒子を篩分して、粒径50〜100μの共重合体粒
子258gを得た。この共重合体粒子50gをメタノ
ール250ml中に入れ、撹拌しながらこれに8%の
ジメチルアミンを含むメタノール溶液25mlを加
え、引続き60℃で6時間反応させた。反応物を
取し、イオン交換水で洗浄した。 次に、これを10%硫酸水溶液250ml中に入れ、
撹拌しながら90℃で5時間保持した。冷却後、反
応物を取し、水洗した。 次いでこれをカラムに詰め、2規定の水酸化ナ
トリウム水溶液250mlを2時間かけて流し、次い
で脱塩水1000mlを流して水洗した。このようにし
て得た陰イオン交換樹脂の交換容量は0.23meq/
g、膨潤度は3.37ml/g、C/OH体積比は
1.01であつた。 実施例 2 実施例1で得られた共重合体粒子50gをメタノ
ール250ml中に入れ、撹拌しながらこれにジエチ
ルアミン18gを加え、引続き60℃で6時間反応さ
せた。以下、実施例1と全く同様にして陰イオン
交換樹脂を得た。 このようにして得た陰イオン交換樹脂の交換容
量は1.79meq/g、膨潤度は3.31ml/g、C/
OH体積比は1.05であつた。 実施例 3 実施例1で得られた共重合体粒子25gをメチノ
ール250ml中に入れ、撹拌しながらこれにジエタ
ノールアミン25mlを加え、引続いて60℃で6時間
反応させた。以下、実施例1と全く同様にして陰
イオン交換樹脂を得た。 このようにして得た陰イオン交換樹脂は交換容
量1.68meq/g、膨潤度3.30ml/g、C/OH
体積比1.04であつた。
[Formula] Structure: amino group, methylamino group, dimethylamino group, ethylamino group, diethylamino group, propylamino group, dipropylamino group, β-hydroxyethylamino group, bis(β-hydroxyethyl)amino group, β-aminoethylamino group, β-
It is a structural unit having a group such as an ethylaminoethylamino group or a β-(β-ethylaminoethyl)aminoethylamino group. Further, the structural unit of the general formula (1) is present in the resin in an amount such that the ion exchange capacity of the resin is 0.1 to 3 meq/g. If the ion exchange capacity is less than 0.1 meq/g, the resin is not practical as an ion exchange resin.
On the other hand, when the ion exchange capacity is greater than 3 meq/g, the volume change of the resin between the free base form and the loaded form becomes large, causing various practical problems. The preferred ion exchange capacity of the resin according to the present invention is
It is 0.3 to 2meq/g. The structural unit represented by the general formula (2) is expressed by the general formula (2) relative to the total number of moles of (the structural unit represented by the general formula (2) + the structural unit represented by the general formula (1)). Preferably, it is present in the resin in an amount such that the number of moles of the indicated structural unit accounts for 30 to 98%. When the amount of the structural unit represented by the general formula (2) is small, the hydrophilicity of the resin decreases. The resin according to the present invention includes the above-mentioned crosslinking agent part, the structural unit part represented by the above general formula (1), and the above-mentioned general formula (1).
Although it essentially consists of the structural unit moiety shown in (2), it may also contain a structural unit derived from methyl ester or ethyl ester of acrylic acid or methacrylic acid, if desired. The resin according to the present invention is produced by copolymerizing a crosslinking agent and a glycidyl ester of acrylic acid or methacrylic acid to form a crosslinked copolymer, and then reacting this with an amine to convert a portion of the glycidyl ester into 3-amino-2- It can be easily produced by converting the glycidyl ester into a hydroxypropyl ester and then reacting the epoxy ring of the glycidyl ester with water to open the ring. The polymerization reaction can be carried out by any known method, but
Usually, it is preferable to carry out suspension polymerization in an aqueous medium in the presence of a suitable dispersion stabilizer to obtain a granular copolymer. As the dispersion stabilizer, gelatin, sodium polyacrylate, carboxymethyl cellulose, polyvinyl alcohol, etc. are usually used. Further, it is preferable to dissolve salts in the aqueous medium to prevent the polymerization reaction raw material from dissolving in the aqueous medium. As the salt, sodium chloride, calcium chloride, sodium sulfate, sodium carbonate, etc. are used. The polymerization reaction is generally carried out using a suitable polymerization initiator. As a polymerization initiator, generally benzoyl peroxide, t-butyl hydroperoxide, azobisisobutyronitrile, dimethylazobis(methyl barate), azobis(α, α
-dimethylvaleronitrile), organic azobis compounds, etc. are used. These polymerization initiators usually account for 0.01 to 5 (by weight) of the reaction raw materials.
It is used in an amount such that %. The polymerization reaction is usually completed in 6 to 20 hours at 50 to 90°C under stirring. Furthermore, if a porous crosslinked copolymer is produced during this polymerization reaction, a porous, hydrophilic and weakly basic anion exchange resin can be obtained. Methods for producing porous crosslinked copolymers are well known, and usually include (1) the presence of a solvent in the reaction raw material that is homogeneously mixed therein but has little affinity for the crosslinked copolymer to be produced; (2) A method in which a linear polymer such as polystyrene is polymerized in the presence of a reaction raw material, and the linear polymer is extracted and removed from the resulting crosslinked copolymer; (3) A method in which the linear polymer is extracted and removed from the crosslinked copolymer produced. Linear polymers such as polystyrene are polymerized in the presence of a solvent that has an affinity for the resulting cross-linked copolymer, such as toluene, ethyl acetate, or dimethylformamide, and the resulting cross-linked copolymer is then polymerized. Any method of extracting and removing the polymer may be used. The reaction between the crosslinked copolymer and the amine can be carried out by dissolving the primary or secondary amine corresponding to formula (3) in a solvent such as water, methanol, dioxane, or toluene, and suspending the crosslinked copolymer in this. , the reaction may be carried out at 40 to 100°C for 3 to 10 hours. The degree of amination of the epoxy ring can be easily controlled by selecting reaction conditions. The ring-opening reaction of the epoxy ring can be carried out by suspending the aminated crosslinked copolymer in water containing sulfuric acid or phosphoric acid and holding the suspension at 30 to 100°C for 5 to 20 hours. The weakly basic anion exchange resin according to the present invention contains a glycerin monoester structure therein and is therefore highly hydrophilic. Furthermore, since the entire composition including the crosslinking agent is composed of aliphatic components and does not contain aromatic components, there is little physical adsorption of proteins and other various organic substances due to hydrophobic bonds.
Furthermore, the weakly basic anion exchange resin according to the present invention exhibits little volume change between the free base form and the loaded form, and is hard and causes little pressure loss when packed in a column. Therefore, the weakly basic anion exchange resin according to the present invention is useful as a packing material for chromatography, especially high performance liquid chromatography. EXAMPLES The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited to the following Examples unless it exceeds the gist thereof. In addition, the exchange capacity, swelling degree, and C/OH volume ratio of the ion exchange resin in this specification were measured as follows. Exchange capacity and swelling degree: Pour the OH type resin, which has been regenerated with an aqueous sodium hydroxide solution and thoroughly washed with demineralized water, into a 10 ml measuring cylinder, and tap the bottom to accurately collect 10 ml.
Weigh out. This resin was dehydrated using a centrifuge at 350G for 5 minutes, and then its weight (a 1 g) was accurately weighed. Next, add this resin to 200ml of 0.2N hydrochloric acid aqueous solution.
Shake at room temperature for 24 hours. Titrate 20 ml of this aqueous hydrochloric acid solution with a 0.1N aqueous sodium hydroxide solution. Separately, accurately weigh out 10 ml of resin in the same manner as above, dehydrate it in the same manner as above, and then accurately weigh its weight (a 2 g). Next, this resin was heated to 60℃,
After drying for 24 hours in a vacuum dryer at 10 mmHg,
Accurately weigh the weight (Cg) again. Swelling degree = 10/C (ml/g) Exchange capacity = (ho-h) x 0.1 x f x 200/20/a 1
×C/a 2 (meq/g) where h and ho are the amount of sodium hydroxide required for titration (ml) before and after adding the resin, respectively, and f is the factor of sodium hydroxide. It is. Cl/OH volume ratio After regenerating the resin with an aqueous sodium hydroxide solution and washing it with water, convert it to form C with 1N hydrochloric acid and thoroughly washing it with demineralized water. Pour this resin into a 10ml graduated cylinder and tap the bottom to accurately measure out 10ml. This resin is converted into OH form with a 1N aqueous sodium hydroxide solution, and then thoroughly washed with demineralized water. Ten
Measure the volume (dml) of the resin by tapping the bottom using a ml graduated cylinder. C/OH performance ratio = 10/d Example 1 Glycidyl methacrylate 210g, ethylene glycol dimethacrylate 90g, toluene 300g
and 3 g of 2,2'-azobis-2,4-dimethylvaleronitrile in 2100 ml of ion-exchanged water.
21g of polyvinyl alcohol and sodium chloride
It was added to a solution in which 168 g was dissolved, and suspension polymerization was carried out at 70° C. for 8 hours while stirring at high speed. After cooling the reaction product, the produced copolymer particles were collected and washed with water. Next, add this copolymer to 1125 ml of toluene and water.
The mixture was stirred at room temperature for 3 hours, and then filtered. Furthermore, this copolymer was poured into 1.5 methanol and stirred twice, and then dried at 80° C. for 8 hours. The particles subjected to the above operations were sieved to obtain 258 g of copolymer particles having a particle size of 50 to 100 μm. 50 g of the copolymer particles were placed in 250 ml of methanol, and 25 ml of a methanol solution containing 8% dimethylamine was added thereto with stirring, followed by reaction at 60° C. for 6 hours. The reaction product was taken and washed with ion-exchanged water. Next, put this in 250ml of 10% sulfuric acid aqueous solution,
The temperature was maintained at 90° C. for 5 hours while stirring. After cooling, the reaction product was taken and washed with water. Next, this was packed in a column, and 250 ml of a 2N aqueous sodium hydroxide solution was poured over 2 hours, followed by 1000 ml of demineralized water for washing. The exchange capacity of the anion exchange resin thus obtained was 0.23meq/
g, swelling degree is 3.37ml/g, C/OH volume ratio is
It was 1.01. Example 2 50 g of the copolymer particles obtained in Example 1 were placed in 250 ml of methanol, and 18 g of diethylamine was added thereto with stirring, followed by reaction at 60° C. for 6 hours. Thereafter, an anion exchange resin was obtained in exactly the same manner as in Example 1. The exchange capacity of the anion exchange resin thus obtained was 1.79 meq/g, the degree of swelling was 3.31 ml/g, and the C/
The OH volume ratio was 1.05. Example 3 25 g of the copolymer particles obtained in Example 1 were placed in 250 ml of methanol, and 25 ml of diethanolamine was added thereto with stirring, followed by reaction at 60° C. for 6 hours. Thereafter, an anion exchange resin was obtained in exactly the same manner as in Example 1. The anion exchange resin thus obtained had an exchange capacity of 1.68 meq/g, a swelling degree of 3.30 ml/g, and a C/OH
The volume ratio was 1.04.

Claims (1)

【特許請求の範囲】 1 下記一般式(1)及び下記一般式(2)で示される構
造単位を有し、多価アルコールのポリアクリル酸
エステルおよびポリメタクリル酸エステルから選
ばれた架橋剤により架橋されてなる架橋共重合体
であつて、架橋剤の含有が20(重量)%以上80(重
量)%以下であり、イオン交換容量が0.1〜
3meq/grである親水性の弱塩基性陰イオン交
換樹脂。 (式中R1は水素原子またはメチル基を示し、R2
及びR3は水素原子または置換基を有していても
よいアルキル基を示す。) (式中、R1は水素原子またはメチル基を示す。)
[Claims] 1. It has a structural unit represented by the following general formula (1) and the following general formula (2), and is crosslinked with a crosslinking agent selected from polyacrylic esters and polymethacrylic esters of polyhydric alcohols. is a crosslinked copolymer made of a polyester resin, the content of a crosslinking agent is 20% (by weight) or more and 80% (by weight) or less, and the ion exchange capacity is 0.1 to 0.1%.
Hydrophilic, weakly basic anion exchange resin with 3meq/gr. (In the formula, R 1 represents a hydrogen atom or a methyl group, and R 2
and R 3 represents a hydrogen atom or an alkyl group which may have a substituent. ) (In the formula, R 1 represents a hydrogen atom or a methyl group.)
JP56122300A 1981-08-04 1981-08-04 Hydrophilic and weakly basic anion exchange resin Granted JPS5824354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56122300A JPS5824354A (en) 1981-08-04 1981-08-04 Hydrophilic and weakly basic anion exchange resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56122300A JPS5824354A (en) 1981-08-04 1981-08-04 Hydrophilic and weakly basic anion exchange resin

Publications (2)

Publication Number Publication Date
JPS5824354A JPS5824354A (en) 1983-02-14
JPH0314499B2 true JPH0314499B2 (en) 1991-02-26

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Family Applications (1)

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JP56122300A Granted JPS5824354A (en) 1981-08-04 1981-08-04 Hydrophilic and weakly basic anion exchange resin

Country Status (1)

Country Link
JP (1) JPS5824354A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109666179A (en) * 2018-12-27 2019-04-23 安徽三星树脂科技有限公司 A kind of macroreticular weakly base acrylic acid series exchanger resin and preparation method thereof

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60169427A (en) * 1984-02-15 1985-09-02 Mitsubishi Chem Ind Ltd Method of separation of protein
JP2767251B2 (en) * 1988-04-01 1998-06-18 三菱化学株式会社 Composite separating agent and method for producing the same
JP2595004B2 (en) * 1988-01-20 1997-03-26 オルガノ株式会社 Enzyme-immobilizing carrier, its enzyme-immobilizing method and enzyme desorbing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109666179A (en) * 2018-12-27 2019-04-23 安徽三星树脂科技有限公司 A kind of macroreticular weakly base acrylic acid series exchanger resin and preparation method thereof

Also Published As

Publication number Publication date
JPS5824354A (en) 1983-02-14

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