JPH04256439A - Pyrogen adsorbent - Google Patents

Pyrogen adsorbent

Info

Publication number
JPH04256439A
JPH04256439A JP3103229A JP10322991A JPH04256439A JP H04256439 A JPH04256439 A JP H04256439A JP 3103229 A JP3103229 A JP 3103229A JP 10322991 A JP10322991 A JP 10322991A JP H04256439 A JPH04256439 A JP H04256439A
Authority
JP
Japan
Prior art keywords
glycidyl methacrylate
beads
molecular weight
pyrogen
polymer beads
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
JP3103229A
Other languages
Japanese (ja)
Inventor
Kiyoshi Hidachi
日達 清
Kohei Okawa
大川 浩平
Shiro Fujikake
藤掛 史朗
Noboru Iida
昇 飯田
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals 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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP3103229A priority Critical patent/JPH04256439A/en
Publication of JPH04256439A publication Critical patent/JPH04256439A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To remove a pyrogen, that is, a substance which causes pyrexia by adsorption when allowed to enter a living body by injection, artificial dialysis or other method. CONSTITUTION:The pore diameter of porous polymer beads contg. glycidyl methacrylate as a constituent is controlled to >=50,000 (expressed in terms of the mol.wt. of dextran) and polyethyleneimine is bonded to the epoxy group of the glycidyl methacrylate.

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、注射、人口透析等によ
り生体内に投与または溶出混入された場合に発熱を誘発
する物質、即ち発熱物質(パイロジェン)の除去に有効
な吸着剤に関する。さらに詳しくは、注射液、輸液、透
析液等に混入している発熱物質の吸着除去剤に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorbent effective for removing a pyrogen, a substance that induces heat generation when administered or eluted into a living body by injection, artificial dialysis, etc. More specifically, the present invention relates to an adsorption/removal agent for pyrogens contained in injection solutions, infusions, dialysates, and the like.

【0002】0002

【従来の技術】現在発熱物質として問題になっているの
は、大腸菌等のグラム陰性細菌の細胞壁由来のリポポリ
サッカライド(LPS)であることがわかっている。発
熱物質の除去に関しては種々の研究がなされており、活
性炭、イオン交換樹脂、各種分離膜による除去が試みら
れいるが未だ実用の域には達していない。即ち、これら
の吸着剤ではパイロジェンの選択性が低く、また吸着除
去量も満足のいく値は得られていない。さらに吸着剤合
成過程の不純物溶出の問題もあって実際に用いることは
できないのが現状である。
BACKGROUND OF THE INVENTION It has been found that lipopolysaccharide (LPS), which is derived from the cell walls of Gram-negative bacteria such as Escherichia coli, is currently a problematic pyrogen. Various studies have been conducted regarding the removal of pyrogens, and attempts have been made to remove them using activated carbon, ion exchange resins, and various separation membranes, but they have not yet reached the level of practical use. That is, these adsorbents have low selectivity for pyrogen, and a satisfactory amount of adsorption and removal cannot be obtained. Furthermore, there is also the problem of impurity elution during the adsorbent synthesis process, so it is currently impossible to actually use it.

【0003】0003

【発明が解決しようとする課題】本発明はパイロジエン
の選択性が高く、その吸着量及び吸着速度の大きい吸着
剤を得ることを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to obtain an adsorbent which has high selectivity for pyrodiene and has a high adsorption amount and speed.

【0004】0004

【課題を解決するための手段】本発明者らは、従来より
LPSの燐酸基がアミノ基と相互作用すること、アミノ
基のうちでも一級アミノ基型がアニオン性物質との相互
作用が最も弱く、LPSに対する選択性が高いこと、ま
たアミノ基が疎水性基の末端に結合している場合、また
は疎水性担体にアミノ基が結合している場合、LPSの
燐酸基及び疎水基がともに相互作用して高度な選択性と
吸着能力をもたらすことを見いだし、この知見に基ずき
本発明を完成するに至った。
[Means for Solving the Problem] The present inventors have conventionally discovered that the phosphoric acid group of LPS interacts with the amino group, and that among the amino groups, the primary amino group type has the weakest interaction with anionic substances. , the selectivity for LPS is high, and when the amino group is bonded to the end of the hydrophobic group or when the amino group is bonded to the hydrophobic carrier, both the phosphoric acid group and the hydrophobic group of LPS interact. It was discovered that high selectivity and adsorption ability can be achieved by using this method, and based on this knowledge, the present invention was completed.

【0005】即ち本発明はグリシジルメタクリレートを
構成成分として含有してなる多孔質ポリマービーズのエ
ポキシ基にポリエチレンイミンを結合してなる発熱物質
吸着剤を提供するものである。なお、グリシジルメタク
リレートを構成成分として含有してなる多孔質ポリマー
ビーズの細孔径がデキストランの分子量換算で5万以上
であることが好ましい。
That is, the present invention provides a pyrogen adsorbent made by bonding polyethyleneimine to the epoxy groups of porous polymer beads containing glycidyl methacrylate as a constituent component. Note that it is preferable that the pore diameter of the porous polymer beads containing glycidyl methacrylate as a constituent component is 50,000 or more in terms of the molecular weight of dextran.

【0006】本発明におけるグリシジルメタクリレート
を構成成分として含有してなる多孔質ポリマービーズは
例えば、グリシジルメタクリレートまたはこれと相溶性
のある他のモノマー、例えばアクリル酸、アクリル酸メ
チル、メタクリル酸、メタクリル酸メチル、メタクリル
酸ヒドロキシエチル等のアクリル系モノマー、スチレン
、p−メチルスチレン、α−メチルスチレン等のスチレ
ン系モノマー、ジビニルベンゼン、メチレンビスアクリ
ルアミド、等の二官能性モノマーを、任意の割合で混合
し、これに非重合性でかつ、これらのモノマーと反応し
ない溶媒、例えば、ペンタン、ヘキサン、オクタン、イ
ソオクタン等の脂肪族炭化水素、ベンゼン、トルエン、
エチルベンゼン、キシレン等の芳香族炭化水素、ヘキサ
ノール、オクタノール、ドデカノール等の脂肪族アルコ
ール、ベンジルアルコール等の芳香族アルコール、等の
うち一種または二種以上の混合物を適当量添加し重合を
おこなった後、該溶媒を抽出等の既知の方法により除去
し得られる多孔質ビーズである。これらの溶媒は、種類
、組合せ、添加量を適当に選ぶことにより、細孔径がデ
キストランの分子量換算で、102 〜107の範囲で
任意に制御できる。
Porous polymer beads containing glycidyl methacrylate as a constituent in the present invention include, for example, glycidyl methacrylate or other monomers compatible therewith, such as acrylic acid, methyl acrylate, methacrylic acid, and methyl methacrylate. , acrylic monomers such as hydroxyethyl methacrylate, styrene monomers such as styrene, p-methylstyrene, and α-methylstyrene, and difunctional monomers such as divinylbenzene and methylenebisacrylamide are mixed in any proportion, In addition, solvents that are non-polymerizable and do not react with these monomers, such as aliphatic hydrocarbons such as pentane, hexane, octane, and isooctane, benzene, toluene,
After polymerization by adding an appropriate amount of one or a mixture of two or more of aromatic hydrocarbons such as ethylbenzene and xylene, aliphatic alcohols such as hexanol, octanol, and dodecanol, and aromatic alcohols such as benzyl alcohol, These are porous beads obtained by removing the solvent by a known method such as extraction. By appropriately selecting the type, combination, and amount of these solvents added, the pore diameter can be arbitrarily controlled within the range of 102 to 107 in terms of the molecular weight of dextran.

【0007】また、重合の際、必要に応じて適当な、開
始剤、または、触媒、例えばベンゾイルパーオキサイド
、アゾビスイソブチルニトリル等を使用することもでき
る。得られる多孔質ビーズは、エポキシ基を含有してい
るがその含有率は、好ましくは、0.01meq/g以
上、更に好ましくは0.1meq/g以上である。これ
らモノマー溶液を分散させる分散媒は、モノマー溶液を
安定に分散させるものであればどんな物でもよく、界面
活性剤、無機塩、水溶性高分子等のうち任意の組合せが
可能である。界面活性剤等の種類、添加量、撹拌分散の
速度等の条件を適当に組み合わせることにより、1μm
〜数mmまで任意の粒子径のビーズが得られる。多孔質
ビーズの孔径はデキストラン標準分子量物質によるゲル
パーミエーションクロマトグラフィー(GPC)によっ
て評価できる。
[0007] Further, during the polymerization, an appropriate initiator or catalyst such as benzoyl peroxide, azobisisobutylnitrile, etc. may be used as necessary. The resulting porous beads contain epoxy groups, and the content thereof is preferably 0.01 meq/g or more, more preferably 0.1 meq/g or more. The dispersion medium for dispersing these monomer solutions may be any material as long as it can stably disperse the monomer solution, and any combination of surfactants, inorganic salts, water-soluble polymers, etc. can be used. By appropriately combining conditions such as the type of surfactant, amount added, speed of stirring and dispersion, etc.
Beads of arbitrary particle size up to several mm can be obtained. The pore size of porous beads can be evaluated by gel permeation chromatography (GPC) using dextran standard molecular weight substances.

【0008】すなわち、グリシジルメタクリレートを構
成成分として含有してなる多孔質ポリマービーズを適当
な方法でふるい分け、液体クロマトグラフィー用のステ
ンレスカラムに充填する。孔径評価用のビーズは100
μm以下のものでも、できるだけ均一サイズが好ましい
。ステンレスカラムのサイズは、通常市販されている(
例えば日本精密(株)社製4.6mmφ*150mm)
カラムで充分である。GPC測定を行う標準分子量物質
は、できるだけ該ポリマービーズとの相互作用が無いも
のが好ましく、デキストラン標準分子量物質(シグマケ
ミカル社製)が適当である。その他の標準分子量物質、
例えば球状タンパク質、ポリエチレングリコール等は、
必ずしも分子量の順番に溶出しなかったり、吸着されて
しまうことがあり適当でない。測定方法は、標準分子量
デキストランを用いた通常の水系GPC測定でよい。即
ち、蒸留水を溶離液として、液体クロマトグラフィー装
置により種々の分子量のデキストランの溶出容量を測定
するものである。
That is, porous polymer beads containing glycidyl methacrylate as a constituent are sieved by an appropriate method and packed into a stainless steel column for liquid chromatography. Beads for pore size evaluation are 100
Even if it is less than μm, it is preferable that the size is as uniform as possible. Stainless steel column sizes are usually commercially available (
For example, 4.6mmφ*150mm manufactured by Nippon Seimitsu Co., Ltd.)
A column is sufficient. The standard molecular weight substance used for GPC measurement is preferably one that has as little interaction as possible with the polymer beads, and dextran standard molecular weight substance (manufactured by Sigma Chemical Co., Ltd.) is suitable. Other standard molecular weight substances,
For example, globular proteins, polyethylene glycol, etc.
This is not appropriate because it may not necessarily elute in the order of molecular weight or may be adsorbed. The measurement method may be normal aqueous GPC measurement using standard molecular weight dextran. That is, the elution capacity of dextran of various molecular weights is measured using a liquid chromatography device using distilled water as an eluent.

【0009】グリシジルメタクリレートを構成成分とし
て含有してなる多孔質ポリマービーズは、発熱物質吸着
剤に用いる場合デキストランの分子量にして5万以上、
好ましくは10万以上の範囲に排除限界分子量を持つも
のがよい。本発明におけるポリエチレンイミンは特にそ
の分子量に制限はないが、好ましくは500以上、更に
好ましくは2000以上100万以下である。
When the porous polymer beads containing glycidyl methacrylate as a constituent component are used as a pyrogen adsorbent, the molecular weight of dextran is 50,000 or more.
Preferably, it has an exclusion limit molecular weight in the range of 100,000 or more. The molecular weight of polyethyleneimine in the present invention is not particularly limited, but is preferably 500 or more, more preferably 2,000 or more and 1,000,000 or less.

【0010】ポリエチレンイミングをグリシジルメタク
リレートを構成成分として含有してなる多孔質ポリマー
ビーズに結合させる方法は、該ポリマービーズを水中に
分散しポリエリレンイミンを添加して加熱することで得
られる。またこのとき必要に応じて苛性ソーダあるいは
トリエチルアミン等の塩基性物質の存在下で反応を行う
[0010] A method for bonding polyethylene imine to porous polymer beads containing glycidyl methacrylate as a constituent is obtained by dispersing the polymer beads in water, adding polyerylene imine, and heating. At this time, the reaction is carried out in the presence of a basic substance such as caustic soda or triethylamine, if necessary.

【0011】[0011]

【作用】本発明により、注射液、透析液、輸液、培養薬
品等に含まれる発熱物質の吸着技術が確立された。その
メカニズムは明かではないが、吸着剤の有する一級アミ
ノ基及びそれに結合している疎水基、疎水性担体によっ
てLPSが選択的に吸着され、さらに吸着剤の細孔径の
制御により吸着表面の増大と、他の共存タンパク質等の
吸着表面への拡散を制御できるものと考えられる。
[Operation] According to the present invention, a technology for adsorbing pyrogens contained in injection solutions, dialysates, infusions, culture chemicals, etc. has been established. Although the mechanism is not clear, LPS is selectively adsorbed by the primary amino group of the adsorbent, the hydrophobic group bonded to it, and the hydrophobic carrier, and the adsorption surface is increased by controlling the pore size of the adsorbent. It is thought that the diffusion of other coexisting proteins to the adsorbed surface can be controlled.

【0012】0012

【発明の効果】本発明の発熱物質吸着剤は、(1)発熱
物質以外の塩類、アミノ酸、有用タンパク質を吸着する
ことなく選択性が高い(2)発熱物質の吸着量及び吸着
速度が大きいなどの優れた効果を奏する。
Effects of the Invention The pyrogen adsorbent of the present invention has (1) high selectivity without adsorbing salts, amino acids, and useful proteins other than pyrogens, and (2) high pyrogen adsorption amount and adsorption rate. It has excellent effects.

【0013】[0013]

【実施例】以下実施例にしたがって、本発明をさらに詳
しく説明するが、本発明は、これら実施例に限られるも
のではない。なお発熱物質の定量測定は生化学工業社(
株式会社)製エンドトキシン定量試薬キットによるリム
ルス発色テストを行った。 製造例1 グリシジルメタクレート14.3g、ジビニルベンゼン
13.0g、ジエチルベンゼン50mlに、過酸化ベン
ゾイル0.3gを加え均一によく撹拌し、1%部分鹸化
ポリビニルアルコール水溶液300ml中に撹拌分散し
、70℃16時間重合反応を行う。反応終了後、ビーズ
を濾過し、温水で充分洗浄して、完全にポリビニルアル
コールを除去する。更に50℃メタノールでジエチルベ
ンゼン及び未反応モノマーを完全に抽出除去する。得ら
れたポリマービーズを乾燥して、塩酸ジメチルフォルム
アミド法によりエポキシ基の含有率を測定すると、3m
mol/gであった。このビーズ5gを蒸留水100m
l中に浸漬し、平均分子量6000のポリエチレンイミ
ン2gを加え、更にトリエチルアミン0.1gを加えて
80℃で8時間加熱する。反応したビーズを濾過して6
0℃の温水で充分洗浄する。このようにして得られたビ
ーズを30mmol燐酸緩衝液及び1mol食塩水で洗
浄し更にエンドトキシンフリーな蒸留水で塩類を完全に
除去する。このビーズを分級して、37〜74μmのも
のを取り出し、ステンレスラカムに充填して、GPC測
定を行った。その結果、このビーズの排除限界分子量は
、約40万であった。
EXAMPLES The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited to these Examples. The quantitative measurement of pyrogens was conducted by Seikagaku Kogyo Co., Ltd. (
A limulus color development test was conducted using an endotoxin quantitative reagent kit manufactured by Co., Ltd.). Production Example 1 Add 0.3 g of benzoyl peroxide to 14.3 g of glycidyl methacrylate, 13.0 g of divinylbenzene, and 50 ml of diethylbenzene, stir well and uniformly, stir and disperse in 300 ml of a 1% partially saponified polyvinyl alcohol aqueous solution, and stir and disperse at 70°C. The polymerization reaction is carried out for 16 hours. After the reaction is complete, the beads are filtered and thoroughly washed with warm water to completely remove polyvinyl alcohol. Furthermore, diethylbenzene and unreacted monomers are completely extracted and removed with methanol at 50°C. When the obtained polymer beads were dried and the content of epoxy groups was measured by the hydrochloric acid dimethylformamide method, it was found that 3 m
It was mol/g. 5g of these beads in 100ml of distilled water
2 g of polyethyleneimine having an average molecular weight of 6,000 was added, and further 0.1 g of triethylamine was added, and the mixture was heated at 80° C. for 8 hours. Filter the reacted beads and
Wash thoroughly with warm water at 0°C. The beads thus obtained are washed with 30 mmol phosphate buffer and 1 mol saline, and the salts are completely removed with endotoxin-free distilled water. The beads were classified and beads having a diameter of 37 to 74 μm were taken out and filled in a stainless steel rack, and GPC measurement was performed. As a result, the exclusion limit molecular weight of these beads was approximately 400,000.

【0014】製造例2 製造例1において、平均分子量10万のポリエチレンイ
ミン2gを加えた他は製造例1と同様にして製造した。 このビーズを分級して、37〜74μmのものを取り出
し、ステンレスカラムに充填して、GPC測定を行った
。その結果、このビーズの排除限界分子量は、約20万
であった。
Production Example 2 Production was carried out in the same manner as in Production Example 1 except that 2 g of polyethyleneimine having an average molecular weight of 100,000 was added. The beads were classified and beads having a diameter of 37 to 74 μm were taken out, filled in a stainless steel column, and subjected to GPC measurement. As a result, the exclusion limit molecular weight of these beads was approximately 200,000.

【0015】実施例1 製造例1及び2で得られた吸着剤それぞれ1gを、ステ
ンレスカラム(内径4.5mm、長さ150mm)に充
填し1mol食塩水150mlを0.5ml/minで
通液したのち発熱物質の含まれない蒸留水で完全に食塩
を洗浄する、その後大腸菌由来のエンドトキシン(生化
学工業社(株)製LPSコントロールE、coli  
055−B5)1ng/mlに調製した蒸留水250m
lを、流速0.5ml/minで通液しカラム出口より
捕集した蒸留水中に含まれるエンドトキシンを定量した
Example 1 1 g of each of the adsorbents obtained in Production Examples 1 and 2 was packed into a stainless steel column (inner diameter 4.5 mm, length 150 mm), and 150 ml of 1 mol saline solution was passed through the column at a rate of 0.5 ml/min. After that, the salt was completely washed away with pyrogen-free distilled water, and then the endotoxin derived from Escherichia coli (LPS Control E, manufactured by Seikagaku Kogyo Co., Ltd.) was removed.
055-B5) 250ml of distilled water adjusted to 1ng/ml
1 was passed through the column at a flow rate of 0.5 ml/min, and the endotoxin contained in the distilled water collected from the column outlet was quantified.

【0016】実施例2 L−イソロイシン、L−ロイシン、L−リジン、L−メ
チオニン、L−フェニルアラニン、L−スレオニン、L
−バリン、L−トリプトファンそれぞれ0.1g/1を
含む蒸留水を大腸菌由来のエンドトキシン(生化学工業
社(株)製LPSコントロール  E、coli  0
55−B5)で1ng/mlに調製した溶液100ml
中に製造例1及び2で得られた吸着剤それぞれ1gを、
分散し撹拌しながら室温で8時間吸着させる。吸着処理
した上澄み液のエンドトキシン濃度及びアミノ酸濃度を
測定してエンドトキシン吸着率及びアミノ酸の回収率を
算出した。アミノ酸分析は、日本分光株式会社製アミノ
酸分析装置を用いた。
Example 2 L-isoleucine, L-leucine, L-lysine, L-methionine, L-phenylalanine, L-threonine, L
- Distilled water containing 0.1 g/1 each of valine and L-tryptophan was added to Escherichia coli-derived endotoxin (LPS control manufactured by Seikagaku Corporation) E. coli 0
100 ml of a solution prepared to 1 ng/ml with 55-B5)
1 g of each of the adsorbents obtained in Production Examples 1 and 2 was placed inside.
Disperse and adsorb at room temperature for 8 hours with stirring. The endotoxin concentration and amino acid concentration of the adsorbed supernatant were measured, and the endotoxin adsorption rate and amino acid recovery rate were calculated. For amino acid analysis, an amino acid analyzer manufactured by JASCO Corporation was used.

【0017】[0017]

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】  グリシジルメタクリレートを構成成分
として含有してなる多孔質ポリマービーズのエポキシ基
にポリエチレンイミンを結合してなる発熱物質吸着剤。
1. A pyrogen adsorbent comprising polyethyleneimine bonded to the epoxy groups of porous polymer beads containing glycidyl methacrylate as a constituent component.
【請求項2】  グリシジルメタクリレートを構成成分
として含有してなる多孔質ポリマービーズの細孔径がデ
キストランの分子量換算で5万以上である請求項1記載
の発熱物質吸着剤。
2. The pyrogen adsorbent according to claim 1, wherein the porous polymer beads containing glycidyl methacrylate as a constituent have a pore diameter of 50,000 or more in terms of the molecular weight of dextran.
JP3103229A 1991-02-06 1991-02-06 Pyrogen adsorbent Pending JPH04256439A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3103229A JPH04256439A (en) 1991-02-06 1991-02-06 Pyrogen adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3103229A JPH04256439A (en) 1991-02-06 1991-02-06 Pyrogen adsorbent

Publications (1)

Publication Number Publication Date
JPH04256439A true JPH04256439A (en) 1992-09-11

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JP3103229A Pending JPH04256439A (en) 1991-02-06 1991-02-06 Pyrogen adsorbent

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020225964A1 (en) * 2019-05-09 2020-11-12 昭和電工マテリアルズ株式会社 Adsorbent particles, method for producing adsorbent particles, base material particles, filling column and method for recovering rare earth element

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020225964A1 (en) * 2019-05-09 2020-11-12 昭和電工マテリアルズ株式会社 Adsorbent particles, method for producing adsorbent particles, base material particles, filling column and method for recovering rare earth element
CN113840652A (en) * 2019-05-09 2021-12-24 昭和电工材料株式会社 Adsorbent particle, method for producing adsorbent particle, substrate particle, packed column, and method for recovering rare earth element

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