JPH07171389A - Manufacture of separating agent - Google Patents

Manufacture of separating agent

Info

Publication number
JPH07171389A
JPH07171389A JP32224793A JP32224793A JPH07171389A JP H07171389 A JPH07171389 A JP H07171389A JP 32224793 A JP32224793 A JP 32224793A JP 32224793 A JP32224793 A JP 32224793A JP H07171389 A JPH07171389 A JP H07171389A
Authority
JP
Japan
Prior art keywords
carrier
group
separating agent
vinyl monomer
meth
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.)
Granted
Application number
JP32224793A
Other languages
Japanese (ja)
Other versions
JP3446274B2 (en
Inventor
Hideaki Kiba
秀明 木庭
Tadashi Adachi
正 足立
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 JP32224793A priority Critical patent/JP3446274B2/en
Publication of JPH07171389A publication Critical patent/JPH07171389A/en
Application granted granted Critical
Publication of JP3446274B2 publication Critical patent/JP3446274B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Graft Or Block Polymers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Polymerisation Methods In General (AREA)

Abstract

PURPOSE:To provide a separating agent especially suitable for liquid-phase chromatography by adding methacryloyl isocyanate, etc., to a carrier having an active hydrogen group on the surface and then copolymerizing the carrier with a polymerizable vinyl monomer. CONSTITUTION:A carrier made of silica gel, polystyrene, etc., having an active hydrogen group e.g. hydroxyl group, carboxyl group, etc., on the surface is used as a carrier for liquid-phase chromatography. Addition reaction of the carrier with a compound, e.g. methacryloyl isocyanate having the formula I or the formula II (R1 is hydrogen or methyl group; n is 1-2 integer) is carried out. Further, the resulting addition reaction product is copolymerized with a copolymerizable vinyl monomer e.g. acrylic acid, acrylamide, etc. Consequently, a polymer part can be introduced into the surface of the carrier and thus a separating agent by which pressure loss is kept from changing and which is suitable for liquid-phase chromatography is provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、分離剤の製造方法に関
し、詳しくは液体クロマトグラフィー用充填剤として好
適に用いられる分離剤の製造方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing a separating agent, and more particularly to a method for producing a separating agent which is preferably used as a packing material for liquid chromatography.

【0002】[0002]

【従来の技術】液体クロマトグラフィー用充填剤に用い
られる担体としては、シリカゲル、ヒドロキシアパタイ
ト等の無機系担体や、デキストラン、セルロース、キト
サン等の天然高分子系担体およびポリスチレン、ポリ
(メタ)アクリル酸エステル等の合成高分子系担体が知
られている。これらの担体はそのままでも、いくつかの
疎水クロマトグラフィー、逆相クロマトグラフィー等の
分離モードでは使用が可能な場合もあるが、近年の技術
の進歩に伴い、それ以外の多様な分離モードでの使用も
可能とするために、これらの担体に各種官能基を付与す
る技術が重要となっている。
2. Description of the Related Art Carriers used as packing materials for liquid chromatography include inorganic carriers such as silica gel and hydroxyapatite, natural polymer carriers such as dextran, cellulose and chitosan, polystyrene and poly (meth) acrylic acid. Synthetic polymer carriers such as esters are known. Although these carriers may be used in some separation modes such as hydrophobic chromatography and reverse phase chromatography even if they are used as they are, they can be used in various other separation modes with the progress of technology in recent years. In order to make it possible, it is important to provide a technique for imparting various functional groups to these carriers.

【0003】上記の担体のうち、例えばシリカゲルであ
れば、シリカゲルのシラノール基に対して各種官能基を
有するシランカップリング剤を反応させたり、必要とあ
れば更に官能基導入を行うこともできる。また、有機系
担体であれば、各種化学反応による官能基導入が可能で
あり、合成高分子系担体であれば合成時に官能基を有す
る化合物を原料として使用することによる官能基導入も
可能である。
Among the above carriers, for example, in the case of silica gel, it is possible to react a silanol group of silica gel with a silane coupling agent having various functional groups and, if necessary, further introduce a functional group. Further, if it is an organic carrier, it is possible to introduce a functional group by various chemical reactions, and if it is a synthetic polymer carrier, it is also possible to introduce a functional group by using a compound having a functional group as a raw material during synthesis. .

【0004】しかし、これらの方法では、官能基化が不
十分な場合には、分離性の低下や担体に分離対象物の非
特異吸着が生じたりする現象が起きることがある。ま
た、特に有機系担体においては、官能基化すると機械的
強度が低下する等の問題があった。これらの問題を解決
するために、担体表面にのみ官能基を高密度に導入する
方法が各種検討されてきた。例えば、特開平1−217
035号公報には、グリシジルモノビニルエステルまた
はグリシジルモノビニルエーテルと多価アルコールのポ
リビニルエステルの共重合体、またはグリシジルモノビ
ニルエステルもしくはグリシジルモノビニルエーテルと
多価アルコールのポリビニルエーテルの共重合体のグリ
シジル基を加水分解させた後にオキシラン環を有するア
ルキルハライドを反応させ、これにオキシラン環を有す
る化合物をグラフト重合させる方法が開示されている。
しかし、この方法ではオキシラン環のグラフト重合物に
よる親水化は達成できるが、更に各種官能基を導入する
ことは難しい。
However, in these methods, when functionalization is insufficient, phenomena such as deterioration of separability and nonspecific adsorption of an object to be separated on a carrier may occur. Further, particularly in the organic carrier, there is a problem that the functional strength is lowered when it is functionalized. In order to solve these problems, various methods for introducing a high density of functional groups only on the surface of the carrier have been studied. For example, JP-A 1-217
No. 035 discloses that a glycidyl group of a glycidyl monovinyl ester or a copolymer of glycidyl monovinyl ether and a polyvinyl ester of a polyhydric alcohol, or a glycidyl monovinyl ester or a copolymer of a glycidyl monovinyl ether and a polyvinyl ether of a polyhydric alcohol is hydrolyzed. After the reaction, an alkyl halide having an oxirane ring is reacted, and a compound having an oxirane ring is graft-polymerized thereto.
However, this method can achieve hydrophilicity with a graft polymer of the oxirane ring, but it is difficult to introduce further various functional groups.

【0005】また、特開平1−310744号公報に
は、ヒドロキシル基を有する支持体を基材とし、その表
面が共有結合した重合度2〜100のポリマーで被覆さ
れている分離剤が開示されている。このポリマーはいわ
ゆる「触手状(tentacle−type)」に結合
しているため、分離剤周辺の環境変化によりその広がり
が大幅に変化する。このことは液体クロマトグラフィー
においては圧力損失が変化する原因となり好ましくな
い。
Further, JP-A-1-310744 discloses a separating agent having a support having a hydroxyl group as a base material, the surface of which is coated with a covalently bonded polymer having a degree of polymerization of 2 to 100. There is. Since this polymer is bound in a so-called "tentacle-type", the spread of the polymer is significantly changed by the environmental change around the separating agent. This is not preferable because it causes a change in pressure loss in liquid chromatography.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記の問題
点を解決した、特に液体クロマトグラフィーに適した分
離剤を提供することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a separating agent which solves the above problems and is particularly suitable for liquid chromatography.

【0007】[0007]

【課題を解決するための手段】本発明は、活性水素基を
表面に有する担体(A)に、下記一般式(I)または一
般式(II)で表される化合物(B)を付加反応させ、次
いでこの付加反応物と重合性ビニル単量体(C)とを共
重合させることにより、該担体(A)の表面に高分子部
分を導入してなる分離剤が、上記の問題点に対して極め
て有効であることを見いだし、本発明に到達した。
In the present invention, a carrier (A) having an active hydrogen group on its surface is subjected to an addition reaction with a compound (B) represented by the following general formula (I) or general formula (II). Then, a separating agent obtained by introducing a polymer portion onto the surface of the carrier (A) by copolymerizing the addition reaction product and the polymerizable vinyl monomer (C) is used to solve the above problems. Therefore, the present invention has been reached, and the present invention has been reached.

【0008】[0008]

【化2】 [Chemical 2]

【0009】(式中、R1 は水素またはメチル基を示
し、nは1〜2の整数を示す) 本発明で用いられる担体(A)は、その表面に活性水素
基を有するものであれば、その組成および多孔性の有無
等には何等限定を受けるものではない。本発明方法で得
られた分離剤を液体クロマトグラフィー用充填剤に用い
る場合には、シリカゲル、ヒドロキシアパタイト等の無
機系担体や、デキストラン、セルロース、キトサン等の
天然高分子系担体およびポリスチレン、ポリ(メタ)ア
クリル酸エステル等の架橋合成高分子の表面に活性水素
基を導入した合成高分子系担体が好ましい。
(In the formula, R 1 represents hydrogen or a methyl group, and n represents an integer of 1 to 2) The carrier (A) used in the present invention has an active hydrogen group on its surface. The composition and the presence or absence of porosity are not particularly limited. When the separating agent obtained by the method of the present invention is used as a packing material for liquid chromatography, silica gel, an inorganic carrier such as hydroxyapatite, a natural polymer carrier such as dextran, cellulose, chitosan and polystyrene, poly ( A synthetic polymer carrier in which an active hydrogen group is introduced on the surface of a crosslinked synthetic polymer such as (meth) acrylic acid ester is preferable.

【0010】また、担体(A)の表面に存在する活性水
素基としては、ヒドロキシル基、カルボキシル基、メル
カプト基、アミノ基およびシラノール基等が挙げられ、
その官能基量は担体1g当たり1×10-5〜1×10-2
モルが好ましい。担体(A)がこれらの活性水素基を有
していない場合には、化学反応により導入すればよい。
無機系担体への活性水素基の導入例としては、エポキシ
基含有シリカゲル(例えばウォーターズプロテインパッ
クアフィニティ:ミリポア社製品)等のエポキシ基を弱
酸性条件にて加水分解して、ヒドロキシル基を導入する
例が挙げられる。また、合成高分子系担体への導入例と
しては、スチレン−ジビニルベンゼン−アクリロニトリ
ル共重合体のニトリル基をアルカリ条件にて加水分解し
てカルボキシル基を導入する例や、グリシジルメタクリ
レート−エチレングリコールジメタクリレート共重合体
のグリシジル基を酸性条件にて加水分解してヒドロキシ
ル基を導入する例等が挙げられる。
Examples of the active hydrogen group existing on the surface of the carrier (A) include a hydroxyl group, a carboxyl group, a mercapto group, an amino group and a silanol group.
The amount of the functional group is 1 × 10 −5 to 1 × 10 −2 per 1 g of the carrier.
Molar is preferred. When the carrier (A) does not have these active hydrogen groups, it may be introduced by a chemical reaction.
As an example of introducing an active hydrogen group into an inorganic carrier, an example of introducing a hydroxyl group by hydrolyzing an epoxy group such as silica gel containing an epoxy group (for example, Waters Protein Pack Affinity: Millipore product) under weakly acidic conditions Is mentioned. In addition, examples of introduction into a synthetic polymer carrier include an example in which a nitrile group of a styrene-divinylbenzene-acrylonitrile copolymer is hydrolyzed under alkaline conditions to introduce a carboxyl group, and glycidyl methacrylate-ethylene glycol dimethacrylate. Examples thereof include introducing a hydroxyl group by hydrolyzing the glycidyl group of the copolymer under acidic conditions.

【0011】前記一般式(I)または一般式(II)で表
される化合物(B)としては、アクリロイルイソシアネ
ート、メタクリロイルイソシアネート、イソシアネート
メチル(メタ)アクリレート、イソシアネートエチル
(メタ)アクリレートが挙げられるが、担体(A)に対
する付加反応における反応性の点から、アクリロイルイ
ソシアネートまたはメタクリロイルイソシアネートが好
ましい。
Examples of the compound (B) represented by the general formula (I) or the general formula (II) include acryloyl isocyanate, methacryloyl isocyanate, isocyanate methyl (meth) acrylate and isocyanate ethyl (meth) acrylate. From the viewpoint of reactivity in the addition reaction to the carrier (A), acryloyl isocyanate or methacryloyl isocyanate is preferable.

【0012】担体(A)に化合物(B)を付加反応させ
るには、一般的には溶媒中で両者を反応させる。溶媒と
しては、酢酸エチル、酢酸ブチル等の酢酸エステル類、
トルエン等の芳香族炭化水素類およびヘキサン、シクロ
ヘキサン等の脂肪族炭化水素類等が挙げられる。また、
付加反応の際に使用される触媒としては、ジブチルチン
ジラウレート等の有機錫化合物、トリエチルアミン等の
第三級アミン等が挙げられる。但し、化合物(B)とし
てアクリロイルイソシアネートまたはメタクリロイルイ
ソシアネートを用いる場合は無触媒での反応が可能であ
り、触媒を使用する場合よりも好ましい。
In order to carry out the addition reaction of the compound (B) to the carrier (A), they are generally reacted in a solvent. As the solvent, acetic acid esters such as ethyl acetate and butyl acetate,
Examples thereof include aromatic hydrocarbons such as toluene and aliphatic hydrocarbons such as hexane and cyclohexane. Also,
Examples of the catalyst used in the addition reaction include organic tin compounds such as dibutyltin dilaurate and tertiary amines such as triethylamine. However, when acryloyl isocyanate or methacryloyl isocyanate is used as the compound (B), the reaction can be performed without a catalyst, which is preferable to the case where a catalyst is used.

【0013】さらに反応温度は0〜70℃で行うのが好
ましく、反応時間は1分〜12時間の範囲が好ましい。
担体(A)に対して付加反応させる化合物(B)の量に
ついては、使用量で担体(A)に対して0.05〜40
重量%、好ましくは0.1〜30重量%である。この量
が少なすぎると、この付加反応生成物と重合性ビニル単
量体(C)とを共重合させる場合に、少量の(C)しか
共重合させ得ない。また多すぎる場合には、(C)の共
重合量とのバランスに不都合が生じて好ましくない。
The reaction temperature is preferably 0 to 70 ° C., and the reaction time is preferably 1 minute to 12 hours.
The amount of the compound (B) to be added to the carrier (A) is 0.05 to 40 with respect to the carrier (A) in the amount used.
%, Preferably 0.1 to 30% by weight. If this amount is too small, only a small amount of (C) can be copolymerized when the addition reaction product and the polymerizable vinyl monomer (C) are copolymerized. On the other hand, if the amount is too large, the balance with the copolymerization amount of (C) may be unfavorable.

【0014】担体(A)と化合物(B)との付加反応物
に、重合性ビニル単量体(C)を共重合させる方法とし
ては、ラジカル重合法、イオン重合法、熱重合法、紫外
線照射法等が用いられるが、なかでもラジカル重合法が
好ましい。この場合に用いられる重合開始剤としては、
2,2′−アゾビスイソブチロニトリル、2,2′−ア
ゾビス(2,4−ジメチルバレロニトリル)、4,4−
アゾビス(4−シアノペンタン酸)等のアゾ系重合開始
剤、t−ブチルヒドロペルオキシド、ジ−t−ブチルペ
ルオキシド、ベンゾイルペルオキシド、ジ−イソプロピ
ルペルオキシジカーボネート、t−ブチルペルオキシイ
ソブチレート及び過酸化水素、過硫酸カリウム、過硫酸
アンモニウム等の過酸化物系重合開始剤またはこれらに
アミン、重亜硫酸ナトリウム等の還元剤を添加した系等
を挙げることが出来る。
As the method for copolymerizing the polymerizable vinyl monomer (C) with the addition reaction product of the carrier (A) and the compound (B), there are radical polymerization method, ionic polymerization method, thermal polymerization method and ultraviolet irradiation. Although the method etc. are used, the radical polymerization method is preferable. As the polymerization initiator used in this case,
2,2'-azobisisobutyronitrile, 2,2'-azobis (2,4-dimethylvaleronitrile), 4,4-
Azo-based polymerization initiators such as azobis (4-cyanopentanoic acid), t-butyl hydroperoxide, di-t-butyl peroxide, benzoyl peroxide, di-isopropyl peroxydicarbonate, t-butyl peroxyisobutyrate and hydrogen peroxide. Examples thereof include peroxide type polymerization initiators such as potassium persulfate and ammonium persulfate, and systems in which a reducing agent such as amine and sodium bisulfite is added to these.

【0015】重合性ビニル単量体(C)としては、(メ
タ)アクリル酸、イタコン酸、マレイン酸等の不飽和カ
ルボン酸類;(メタ)アクリル酸メチル、(メタ)アク
リル酸エチル、(メタ)アクリル酸ブチル、(メタ)ア
クリル酸ステアリル等の(メタ)アクリル酸アルキルエ
ステル、(メタ)アクリル酸ヒドロキシエチル、(メ
タ)アクリル酸ヒドロキシプロピル、(メタ)アクリル
酸フェニル、(メタ)アクリル酸3−クロロ−2−ヒド
ロキシプロピル、(メタ)アクリル酸2−クロロエチ
ル、(メタ)アクリル酸グリシジル、(メタ)アクリル
酸ジメチルアミノエチル、(メタ)アクリル酸ジエチル
アミノエチル、(メタ)アクリル酸テトラヒドロフルフ
リル等の(メタ)アクリル酸エステル類;
As the polymerizable vinyl monomer (C), unsaturated carboxylic acids such as (meth) acrylic acid, itaconic acid and maleic acid; methyl (meth) acrylate, ethyl (meth) acrylate, (meth) Butyl acrylate, alkyl (meth) acrylates such as stearyl (meth) acrylate, hydroxyethyl (meth) acrylate, hydroxypropyl (meth) acrylate, phenyl (meth) acrylate, (meth) acrylic acid 3- Chloro-2-hydroxypropyl, 2-chloroethyl (meth) acrylate, glycidyl (meth) acrylate, dimethylaminoethyl (meth) acrylate, diethylaminoethyl (meth) acrylate, tetrahydrofurfuryl (meth) acrylate, etc. (Meth) acrylic acid esters;

【0016】(メタ)アクリルアミド、N,N−ジメチ
ル(メタ)アクリルアミド、N,N−ジメチルアミノプ
ロピル(メタ)アクリルアミド、2−アクリルアミド−
2−メチルプロパンスルホン酸等の(メタ)アクリルア
ミド誘導体;スチレン、メチルスチレン、α−メチルス
チレン、クロロスチレン、クロロメチルスチレン等のス
チレン及びそのアルキルまたはハロゲン置換体;酢酸ビ
ニル、プロピオン酸ビニル等のビニルエステル類;メチ
ルビニルエーテル、エチルビニルエーテル、ブチルビニ
ルエーテル、オクタデシルビニルエーテル等のビニルエ
ーテル類;
(Meth) acrylamide, N, N-dimethyl (meth) acrylamide, N, N-dimethylaminopropyl (meth) acrylamide, 2-acrylamide-
(Meth) acrylamide derivatives such as 2-methylpropanesulfonic acid; styrenes such as styrene, methylstyrene, α-methylstyrene, chlorostyrene and chloromethylstyrene and alkyl or halogen substituted products thereof; vinyl such as vinyl acetate and vinyl propionate Esters; Vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, butyl vinyl ether and octadecyl vinyl ether;

【0017】アリルアルコール及びそのエステルまたは
エーテル類;アリルアミン、ジアリルアミン等のアリル
アミン誘導体;N−ビニルホルムアミド、N−ビニルア
セトアミド等のビニルアミン誘導体;(メタ)アクリロ
ニトリル、アクロレイン、ビニルスルホン酸ナトリウ
ム、ァリルスルホン酸ナトリウム、p−スチレンスルホ
ン酸ナトリウム、ビニルピリジン、ビニルピロリドンそ
の他のビニル化合物;
Allyl alcohol and its esters or ethers; allylamine derivatives such as allylamine and diallylamine; vinylamine derivatives such as N-vinylformamide and N-vinylacetamide; (meth) acrylonitrile, acrolein, sodium vinylsulfonate, sodium allylsulfonate, p-sodium styrenesulfonate, vinylpyridine, vinylpyrrolidone and other vinyl compounds;

【0018】等が挙げられる。これらの重合性ビニル単
量体は単独でも二種類以上の混合においても用いること
が出来る。これらの単量体を使用した場合は単量体自身
の官能基の特性により、共重合後、そのまま分離剤とし
て使用できる場合と、共重合後、単量体の官能基を他の
官能基と置換したり、加水分解等によって他の官能基に
変換する等の方法により分離剤として使用する場合があ
る。
And the like. These polymerizable vinyl monomers can be used alone or in a mixture of two or more kinds. When these monomers are used, depending on the characteristics of the functional group of the monomer itself, after the copolymerization, it can be used as a separating agent as it is, and after the copolymerization, the functional group of the monomer is different from other functional groups. It may be used as a separating agent by a method such as substitution or conversion to another functional group by hydrolysis or the like.

【0019】特に液体クロマトグラフィー用充填剤の場
合には、例えばイオン性解離基を有する重合性ビニル単
量体を用いることによりイオン交換クロマトグラフィー
用充填剤を、C4 ,C8 ,C18等のC4 以上のアルキル
基を有する重合性ビニル単量体を用いることにより逆相
クロマトグラフィー用充填剤を、C4 以下の低分子アル
キル基やフェニル基を有する重合性ビニル単量体を用い
ることにより疎水クロマトグラフィー用充填剤を、光学
活性基を有する重合性ビニル単量体を用いることにより
光学分割クロマトグラフィー用充填剤を、また水酸基等
の親水性官能基を有する重合性ビニル単量体を用いるこ
とにより水系サイズ排除クロマトグラフィー用充填剤を
それぞれ製造し得る。
Particularly in the case of a packing material for liquid chromatography, for example, by using a polymerizable vinyl monomer having an ionic dissociative group, the packing material for ion exchange chromatography can be prepared as C 4 , C 8 , C 18, etc. The use of a polymerizable vinyl monomer having a C 4 or higher alkyl group as a filler for reverse phase chromatography, and the use of a polymerizable vinyl monomer having a C 4 or lower low molecular weight alkyl group or a phenyl group By using a packing material for hydrophobic chromatography, a packing material for optical resolution chromatography by using a polymerizable vinyl monomer having an optically active group, and a polymerizable vinyl monomer having a hydrophilic functional group such as a hydroxyl group. Each of them can be used to produce a packing material for water-based size exclusion chromatography.

【0020】担体(A)と化合物(B)との付加反応
物、より特定的には(B)由来の不飽和二重結合と重合
性ビニル単量体(C)との共重合反応は、重合性ビニル
単量体(C)を含む溶媒中にて行われ、反応温度につい
ては0〜100℃、反応時間については30分〜24時
間の範囲にて行われる。
The addition reaction product of the carrier (A) and the compound (B), more specifically, the copolymerization reaction of the unsaturated double bond derived from (B) and the polymerizable vinyl monomer (C), The reaction is carried out in a solvent containing the polymerizable vinyl monomer (C) at a reaction temperature of 0 to 100 ° C. and a reaction time of 30 minutes to 24 hours.

【0021】担体(A)と化合物(B)との付加反応物
と共重合させる重合性ビニル単量体(C)の量は、付加
反応物に対して使用量で1〜50重量%、好ましくは2
〜40重量%である。この量が少なすぎると、得られる
分離剤の表面に導入される(C)由来の高分子部分がそ
の表面を充分に被覆することが出来ず、また多すぎる場
合には、表面被覆層が必要以上に厚くなることによる分
離性能の低下等の問題が生じる。
The amount of the polymerizable vinyl monomer (C) copolymerized with the addition reaction product of the carrier (A) and the compound (B) is 1 to 50% by weight based on the addition reaction product, preferably Is 2
-40% by weight. If this amount is too small, the polymer portion derived from (C) introduced on the surface of the resulting separating agent cannot sufficiently cover the surface, and if it is too large, a surface coating layer is required. As the thickness increases, problems such as deterioration of separation performance occur.

【0022】[0022]

【実施例】以下、本発明を実施例により更に具体的に説
明するが、本発明はこれら実施例に限定されるものでは
ない。
EXAMPLES The present invention will now be described in more detail with reference to examples, but the present invention is not limited to these examples.

【0023】参考例1(活性水素基を表面に有する担体
の合成) 撹拌器、コンデンサーおよび温度計を備えた反応器中に
メタクリル酸グリシジルとエチレングリコールジメタク
リレートの重量比を70.4:29.6として共重合に
より製造された球状多孔質共重合体粒子(平均粒子径
4.52μm、比表面積44.2m2 /g、最頻度半径
29.8nm)5重量部を入れ、10重量%硫酸水溶液
50重量部を加え、50℃にて5時間加熱することによ
り、メタクリル酸グリシジル由来のエポキシ基を加水分
解して水酸基に転換した。反応終了後、粒子を脱塩水に
て充分に洗浄し、乾燥した。
Reference Example 1 (Synthesis of Carrier Having Active Hydrogen Group on Surface) In a reactor equipped with a stirrer, a condenser and a thermometer, the weight ratio of glycidyl methacrylate to ethylene glycol dimethacrylate was 70.4: 29. 6 spherical spherical copolymer particles (average particle size 4.52 μm, specific surface area 44.2 m 2 / g, most frequent radius 29.8 nm) produced by copolymerization as 6 were added, and 10% by weight sulfuric acid aqueous solution was added. By adding 50 parts by weight and heating at 50 ° C. for 5 hours, the epoxy group derived from glycidyl methacrylate was hydrolyzed and converted into a hydroxyl group. After completion of the reaction, the particles were thoroughly washed with demineralized water and dried.

【0024】実施例1 攪拌器、コンデンサー、温度計及び窒素ガス導入管を備
えた反応器中に、上記参考例1によって得られた粒子5
重量部を入れ、酢酸エチル45重量部を加えて粒子を分
散させた。反応器を窒素ガスで置換した後に、メタクリ
ロイルイソシアネート1重量部を添加し、窒素雰囲気下
にて撹拌しつつ、25℃にて1時間付加反応を行った。
Example 1 Particles 5 obtained in Reference Example 1 above were placed in a reactor equipped with a stirrer, condenser, thermometer and nitrogen gas inlet tube.
Part by weight was added, and 45 parts by weight of ethyl acetate was added to disperse the particles. After replacing the reactor with nitrogen gas, 1 part by weight of methacryloyl isocyanate was added, and the addition reaction was carried out at 25 ° C. for 1 hour while stirring under a nitrogen atmosphere.

【0025】反応終了後、上記の付加反応により得られ
た粒子をメタノールおよびアセトンにて充分に洗浄し
た。次いでこの粒子を、撹拌器、コンデンサー、温度計
及び窒素ガス導入管を備えた反応器中に入れ、N,N−
ジメチルアミノプロピルメタクリルアミド2重量部、1
N−塩酸11.8重量部、脱塩水35.2重量部を加え
た。反応器を窒素ガスで置換した後に過硫酸カリウム
3.2重量%水溶液を1重量部添加し、窒素雰囲気下に
て70℃に加熱して6時間重合を行い、分離剤とした。
After completion of the reaction, the particles obtained by the above addition reaction were thoroughly washed with methanol and acetone. Then, the particles were put into a reactor equipped with a stirrer, a condenser, a thermometer and a nitrogen gas introducing tube, and N, N
Dimethylaminopropyl methacrylamide 2 parts by weight, 1
11.8 parts by weight of N-hydrochloric acid and 35.2 parts by weight of demineralized water were added. After replacing the reactor with nitrogen gas, 1 part by weight of a 3.2% by weight aqueous solution of potassium persulfate was added, and the mixture was heated to 70 ° C. in a nitrogen atmosphere and polymerized for 6 hours to obtain a separating agent.

【0026】得られた分離剤のN,N−ジメチルアミノ
プロピルメタクリルアミド由来のアニオン交換容量を滴
定法により測定したところ0.20meq/gであっ
た。このようにして得られた分離剤を内径8.0mm、
長さ100mmのガラスカラムに充填し、蛋白質吸脱着
容量の測定を行った。
The anion exchange capacity of the obtained separating agent derived from N, N-dimethylaminopropylmethacrylamide was measured by a titration method and found to be 0.20 meq / g. The separating agent thus obtained had an inner diameter of 8.0 mm,
It was packed in a glass column having a length of 100 mm and the protein adsorption / desorption capacity was measured.

【0027】[0027]

【表1】測定条件: 測定装置:LC−6Aシステム(島津製作所製) 吸着液:14mMトリスヒドロキシメチルアミノメタン
・塩酸緩衝液(pH8.0) 脱着液:14mMトリスヒドロキシメチルアミノメタン
・塩酸緩衝液(pH8.0)+0.5M塩化ナトリウム 流速:1.0ml/min 検出:UV280nm 温度:25℃ 試料:牛血清アルブミン(シグマ社製)
[Table 1] Measurement conditions: Measurement device: LC-6A system (manufactured by Shimadzu Corporation) Adsorption liquid: 14 mM trishydroxymethylaminomethane / hydrochloric acid buffer solution (pH 8.0) Desorption liquid: 14 mM trishydroxymethylaminomethane / hydrochloric acid buffer solution (PH 8.0) +0.5 M sodium chloride Flow rate: 1.0 ml / min Detection: UV280 nm Temperature: 25 ° C. Sample: Bovine serum albumin (manufactured by Sigma)

【0028】上記の条件にて吸着液を通液し、吸着液中
に溶解した試料(牛血清アルブミン)をカラムに注入
し、吸着させた。飽和吸着後、吸着されずに溶出する牛
血清アルブミンをUV280nmの吸光度で定量するこ
とによりカラムに吸着された牛血清アルブミン量を求め
たところ、分離剤1mlあたりの牛血清アルブミン吸着
容量は47.4mgであった。次に、脱着液を通液する
ことによりカラムに吸着した牛血清アルブミンを溶離さ
せた。回収した牛血清アルブミン量をUV280nmの
吸光度より求めたところ、分離剤1mlあたりの脱着容
量は47.3mgであり、吸着容量に対する回収率は9
9.8%であった。
Under the above conditions, the adsorbent was passed through, and the sample (bovine serum albumin) dissolved in the adsorbent was injected into the column for adsorption. After saturated adsorption, the amount of bovine serum albumin adsorbed on the column was determined by quantifying the bovine serum albumin that was not adsorbed and was eluted by the absorbance at UV 280 nm. Met. Next, the desorption solution was passed through to elute the bovine serum albumin adsorbed on the column. When the amount of bovine serum albumin recovered was determined from the absorbance at UV280 nm, the desorption capacity per ml of the separating agent was 47.3 mg, and the recovery rate for the adsorption capacity was 9%.
It was 9.8%.

【0029】比較例1 撹拌器、コンデンサーおよび温度計を備えた反応器中
に、参考例1によって得られた粒子5重量部を入れ、5
N−NaOH水溶液24重量部を加え、室温において超
音波分散下で30分間撹拌した。次いで、51%β−ジ
エチルアミノエチルクロリド塩酸塩水溶液29.4重量
部を加え、50℃にて6時間反応することによりジエチ
ルアミノエチル基を導入して分離剤(比較例1)とし
た。得られた分離剤のジエチルアミノエチル基由来のア
ニオン交換容量を滴定法により測定したところ0.56
meq/gであった。
Comparative Example 1 5 parts by weight of the particles obtained in Reference Example 1 were placed in a reactor equipped with a stirrer, a condenser and a thermometer.
24 parts by weight of N-NaOH aqueous solution was added, and the mixture was stirred at room temperature for 30 minutes under ultrasonic dispersion. Then, 29.4 parts by weight of 51% β-diethylaminoethyl chloride hydrochloride aqueous solution was added, and the mixture was reacted at 50 ° C. for 6 hours to introduce a diethylaminoethyl group to obtain a separating agent (Comparative Example 1). The anion exchange capacity derived from the diethylaminoethyl group of the obtained separating agent was measured by a titration method to be 0.56.
It was meq / g.

【0030】この分離剤について実施例1と同様にして
牛血清アルブミンの吸脱着容量測定を行ったところ、分
離剤1mlあたりの牛血清アルブミン吸着容量は70m
gであったが、1mlあたりの脱着容量は36mg、回
収率は51.4%であり、牛血清アルブミンの粒子への
非特異吸着の程度が高いことがわかった。
The adsorption / desorption capacity of bovine serum albumin was measured for this separating agent in the same manner as in Example 1. The adsorbing capacity of bovine serum albumin per ml of the separating agent was 70 m.
Although the amount was g, the desorption capacity per ml was 36 mg, and the recovery rate was 51.4%, indicating that the degree of nonspecific adsorption of bovine serum albumin to particles was high.

【0031】[0031]

【発明の効果】本発明により得られる分離剤は、その表
面に重合性ビニル単量体(C)由来の高分子部分が共有
結合により高密度に導入されており、重合性ビニル単量
体(C)由来の官能基または重合性ビニル単量体(C)
由来の高分子部分に対して導入される官能基により各種
の分離モードにおいて好適な分離性能を与える。また、
重合性ビニル単量体(C)由来の高分子部分が、担体表
面に付加された化合物(B)由来の複数個の重合性不飽
和二重結合と共有結合することにより担体表面を層状に
被覆する点において、特開平1−310744号公報記
載の分離剤とは異なるものである。この構造は担体自身
の性質による分離性の低下や担体に対する分離対象物の
非特異吸着等の問題を解消し、特に有機系担体において
は担体全体の官能基化による機械的強度の低下を招くこ
とがない。更に液体クロマトグラフィー用充填剤に用い
る場合には、溶離液組成の変化による圧力損失の変化も
最小限に抑えることができ、高速液体クロマトグラフィ
ーにおいて特に好適に用いることが可能である。
INDUSTRIAL APPLICABILITY The separating agent obtained by the present invention has a polymer moiety derived from the polymerizable vinyl monomer (C) introduced into the surface of the polymerizable vinyl monomer (C) at a high density by a covalent bond. C) -derived functional group or polymerizable vinyl monomer (C)
The functional group introduced into the derived polymer portion provides suitable separation performance in various separation modes. Also,
The polymeric portion derived from the polymerizable vinyl monomer (C) is covalently bonded to a plurality of polymerizable unsaturated double bonds derived from the compound (B) added to the surface of the carrier to coat the surface of the carrier in a layered manner. This is different from the separating agent described in JP-A No. 1-310744. This structure solves problems such as deterioration of separability due to the properties of the carrier itself and non-specific adsorption of the separation target on the carrier, and in particular, in organic carriers, the functionalization of the entire carrier causes a decrease in mechanical strength. There is no. Furthermore, when it is used as a packing material for liquid chromatography, it is possible to minimize changes in pressure loss due to changes in the composition of the eluent, and it is possible to use it particularly preferably in high performance liquid chromatography.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08F 292/00 MPZ 7308−4J // C08F 20/58 MNG ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location C08F 292/00 MPZ 7308-4J // C08F 20/58 MNG

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 活性水素基を表面に有する担体(A)
に、下記一般式(I)または一般式(II)で表される化
合物(B)を付加反応させ、次いでこの付加反応物と重
合性ビニル単量体(C)とを共重合させることにより、
該担体(A)の表面に高分子部分を導入することを特徴
とする分離剤の製造方法。 【化1】 (式中、R1 は水素またはメチル基を示し、nは1〜2
の整数を示す)
1. A carrier (A) having an active hydrogen group on its surface.
Is subjected to an addition reaction with a compound (B) represented by the following general formula (I) or general formula (II), and then the addition reaction product and a polymerizable vinyl monomer (C) are copolymerized,
A method for producing a separating agent, which comprises introducing a polymer portion into the surface of the carrier (A). [Chemical 1] (In the formula, R 1 represents hydrogen or a methyl group, and n is 1 to 2
Represents an integer)
【請求項2】 化合物(B)がメタクリロイルイソシア
ネートである請求項1記載の分離剤の製造方法。
2. The method for producing a separating agent according to claim 1, wherein the compound (B) is methacryloyl isocyanate.
JP32224793A 1993-12-21 1993-12-21 Manufacturing method of separation agent Expired - Fee Related JP3446274B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32224793A JP3446274B2 (en) 1993-12-21 1993-12-21 Manufacturing method of separation agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32224793A JP3446274B2 (en) 1993-12-21 1993-12-21 Manufacturing method of separation agent

Publications (2)

Publication Number Publication Date
JPH07171389A true JPH07171389A (en) 1995-07-11
JP3446274B2 JP3446274B2 (en) 2003-09-16

Family

ID=18141549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32224793A Expired - Fee Related JP3446274B2 (en) 1993-12-21 1993-12-21 Manufacturing method of separation agent

Country Status (1)

Country Link
JP (1) JP3446274B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11180996A (en) * 1997-12-16 1999-07-06 Mitsubishi Chemical Corp Separation of lipoprotein and its determination
JP2005510609A (en) * 2001-11-26 2005-04-21 アメルシャム・バイオサイエンシーズ・アクチボラグ Post-modification of porous support
JP2005510593A (en) * 2001-11-26 2005-04-21 アメルシャム・バイオサイエンシーズ・アクチボラグ Post-modification of porous support
US7022744B2 (en) 2002-04-11 2006-04-04 Mitsubishi Chemical Corporation Ion exchanger for lipoproteins separation and lipoproteins separation method using the same
CN1320018C (en) * 2003-02-27 2007-06-06 爱克工业株式会社 Monomer containing colloidal silica, solidified resin composition and resin solidified article thereof
KR100838001B1 (en) * 2005-08-26 2008-06-13 제이에스알 가부시끼가이샤 Polymer, Radiation Sensitive Resin Composition and Spacer for Liquid Crystal Display Element
JP2012032390A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Methods for producing enhanced chromatography medium and using the same
JP2012032392A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Grafting method for improving chromatography medium performance
JP2012032391A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Methods for producing enhanced chromatography medium and using the same

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11180996A (en) * 1997-12-16 1999-07-06 Mitsubishi Chemical Corp Separation of lipoprotein and its determination
JP2005510609A (en) * 2001-11-26 2005-04-21 アメルシャム・バイオサイエンシーズ・アクチボラグ Post-modification of porous support
JP2005510593A (en) * 2001-11-26 2005-04-21 アメルシャム・バイオサイエンシーズ・アクチボラグ Post-modification of porous support
US7022744B2 (en) 2002-04-11 2006-04-04 Mitsubishi Chemical Corporation Ion exchanger for lipoproteins separation and lipoproteins separation method using the same
CN1320018C (en) * 2003-02-27 2007-06-06 爱克工业株式会社 Monomer containing colloidal silica, solidified resin composition and resin solidified article thereof
KR100838001B1 (en) * 2005-08-26 2008-06-13 제이에스알 가부시끼가이샤 Polymer, Radiation Sensitive Resin Composition and Spacer for Liquid Crystal Display Element
JP2012032390A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Methods for producing enhanced chromatography medium and using the same
JP2012032392A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Grafting method for improving chromatography medium performance
JP2012032391A (en) * 2010-07-28 2012-02-16 Rohm & Haas Co Methods for producing enhanced chromatography medium and using the same

Also Published As

Publication number Publication date
JP3446274B2 (en) 2003-09-16

Similar Documents

Publication Publication Date Title
US5114577A (en) Composite separating agent
US5656707A (en) Highly cross-linked polymeric supports
US4772635A (en) Bead-shaped crosslinked copolymers containing epoxide groups and basic amino groups, a process for their preparation and their use
JP5250985B2 (en) New filler for packed bed and its use
KR101297282B1 (en) Novel packing material with excellent hydrophilicity and process for producing the same
CA1255827A (en) Polysaccharide supports
AU2001285152B2 (en) Functionalized polymeric media for separation of analytes
JPS6216133B2 (en)
JP2005510609A5 (en)
JPH0198606A (en) Polymer particle and preparation thereof
JP2896571B2 (en) Composite separating agent and method for producing the same
JPS5858026B2 (en) Packing material for chromatography and its manufacturing method
JP3446274B2 (en) Manufacturing method of separation agent
Turková [6] Immobilization of enzymes on hydroxyalkyl methacrylate gel
JP2005510593A5 (en)
US6746608B2 (en) Use of adsorbent polymer particles in DNA separation
US5667692A (en) Method and supports for gel permeation chromatography
JP3259532B2 (en) Separating agent and method for producing the same
EP0129295A2 (en) An ion exchanger
CN114213581A (en) Preparation method of hydrophilic polyacrylate crosslinked microspheres
JP3740958B2 (en) Modification method of solid surface
JPS6392627A (en) Hydrophilic porous particle
JPH09255730A (en) Production of cross-linked copolymer
JPH08510327A (en) Method and support for gel permeation chromatography
JP3424255B2 (en) Method for producing packing material for liquid chromatography

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 5

Free format text: PAYMENT UNTIL: 20080704

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080704

Year of fee payment: 5

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090704

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090704

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 7

Free format text: PAYMENT UNTIL: 20100704

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100704

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110704

Year of fee payment: 8

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120704

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20130704

LAPS Cancellation because of no payment of annual fees