JPH06258203A - Cartridge column for solid phase extraction - Google Patents

Cartridge column for solid phase extraction

Info

Publication number
JPH06258203A
JPH06258203A JP5049170A JP4917093A JPH06258203A JP H06258203 A JPH06258203 A JP H06258203A JP 5049170 A JP5049170 A JP 5049170A JP 4917093 A JP4917093 A JP 4917093A JP H06258203 A JPH06258203 A JP H06258203A
Authority
JP
Japan
Prior art keywords
weight
parts
cross
phase extraction
cartridge column
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
JP5049170A
Other languages
Japanese (ja)
Other versions
JP3274898B2 (en
Inventor
Tetsuya Aoyama
哲也 青山
Osamu Hirai
修 平井
Yoshinori Inoue
嘉則 井上
Hiroki Kumagai
浩樹 熊谷
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.)
Yokogawa Analytical Systems Inc
Showa Denko Materials Co Ltd
Original Assignee
Hitachi Chemical Co Ltd
Yokogawa Analytical Systems 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 Hitachi Chemical Co Ltd, Yokogawa Analytical Systems Inc filed Critical Hitachi Chemical Co Ltd
Priority to JP04917093A priority Critical patent/JP3274898B2/en
Publication of JPH06258203A publication Critical patent/JPH06258203A/en
Application granted granted Critical
Publication of JP3274898B2 publication Critical patent/JP3274898B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sampling And Sample Adjustment (AREA)

Abstract

PURPOSE:To provide excellent recovery by using a cross-linked copolymer particle by means of copolymerization of several kinds of the specific materials. CONSTITUTION:Cross-linked copolymer particles 2 are composed by aqueous suspension copolymerization, in which 20-70 parts by weight of divinylbenzene, 30-80 parts by weight of polyhydric alcohol poly (meta) acrylic ester are used so that they make 100 parts by weight in total and other vinyl group monomers are used if necessary. These compounds are used solely or in combination of two or more, and aqueous suspension copolymerization is carried out under the existence of a polymerization starter. Azo group compounds such as benzoyl peroxide, dichlorobenzoyl peroxide, and the like are available for a polymerization starter. A solid phase extracting cartridge column 4 is made by filling the cross-linked copolymer particles 2 in a resin reservoir 3, in which a resin filter 1 is set, and then sealing the reservoir by a resin filter 1 from the upper side.

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、固相抽出用カートリッ
ジカラムに関する。
FIELD OF THE INVENTION The present invention relates to a solid phase extraction cartridge column.

【0002】[0002]

【従来の技術】従来、液体中からの試料の抽出には、液
−液抽出法が多く用いられてきたが、作業の煩雑さ、溶
媒を多量に使用する等の問題があった。現在では、シリ
カ系及びポリマー系多孔性粒子の合成法の発達にともな
い作業が簡単で溶媒の使用量も少なく多量の試料を処理
することができる固相抽出法が用いられるようになって
きた。固相抽出に用いられる粒子は以下のようなものが
知られている。 (1)シリカゲル又はシリカゲルの表面を化学修飾した
化学結合型シリカゲル (2)スチレン−ジビニルベンゼン共重合体 (3)(メタ)アクリル酸エステル共重合体
2. Description of the Related Art Conventionally, a liquid-liquid extraction method has been often used for extracting a sample from a liquid, but there are problems such as complexity of work and use of a large amount of solvent. Nowadays, along with the development of methods for synthesizing silica-based and polymer-based porous particles, a solid-phase extraction method, which is easy to work with, uses a small amount of solvent, and can process a large amount of sample, has come to be used. The following particles are known to be used for solid phase extraction. (1) Silica gel or chemically bonded silica gel in which the surface of silica gel is chemically modified (2) Styrene-divinylbenzene copolymer (3) (Meth) acrylic acid ester copolymer

【0003】[0003]

【発明が解決しようとする課題】しかし、上記(1)の
化学結合型シリカゲルをゴルフ場農薬や食肉中の残留合
成抗菌剤などを分析する環境分析に用いた場合、シリカ
内に含まれる不純物の影響で一部の試料が分解を起こす
という問題点がある。上記(2)のスチレン−ジビニル
共重合体は、疎水性が強いため水溶液を処理する際の作
業性が悪くなるという問題点がある。上記(3)の(メ
タ)アクリル酸エステル共重合体は、親水性が強いため
試料の回収率が低下するという問題点がある。本発明
は、このような問題点を解決し、回収率に優れた固相抽
出用カートリッジカラムを提供するものである。
However, when the chemically-bonded silica gel of (1) above is used for environmental analysis for analyzing agricultural chemicals on golf courses and residual synthetic antibacterial agents in meat, impurities contained in silica are There is a problem that some samples may be decomposed due to the influence. The styrene-divinyl copolymer of the above (2) has a problem that the workability at the time of treating an aqueous solution is deteriorated because of its strong hydrophobicity. The (meth) acrylic acid ester copolymer of the above (3) has a problem that the recovery rate of the sample is lowered due to its strong hydrophilicity. The present invention solves such problems and provides a solid-phase extraction cartridge column having an excellent recovery rate.

【0004】[0004]

【課題を解決するための手段】本発明は、(a)ジビニ
ルベンゼン20〜70重量部、(b)多価アルコールポ
リ(メタ)アクリル酸エステル30〜80重量部
((a)+(b)=100重量部)及び(c)必要に応
じて用いられる他のビニル系モノマーを共重合した架橋
共重合体粒子を樹脂製のリザーバに充てんした固相抽出
用カートリッジカラムに関する。
The present invention comprises (a) 20 to 70 parts by weight of divinylbenzene, (b) 30 to 80 parts by weight of polyhydric alcohol poly (meth) acrylic acid ester ((a) + (b)). = 100 parts by weight) and (c) a solid-phase extraction cartridge column in which a resin-made reservoir is filled with a cross-linked copolymer particle obtained by copolymerizing another vinyl-based monomer used as necessary.

【0005】本発明に用いられる(a)ジビニルベンゼ
ンは特に純度は限定されないが、純度60重量%以上の
ものを使用することが好ましい。本発明に用いられる
(b)多価アルコールポリ(メタ)アクリル酸エステル
(ここで(メタ)アクリル酸の表記は、アクリル酸及び
メタアクリル酸を意味する)としては、エチレングリコ
ールジアクリレート、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アクリレート、プロピレ
ングリコールジメタクリレート、ポリエチレングリコー
ルジアクリレート、ポリエチレングリコールジメタクリ
レート、ポリプロピレングリコールジアクリレート、ポ
リプロピレングリコールジメタクリレート、グリセリン
のジ又はトリアクリレート、グリセリンのジ又はトリメ
タクリレート、トリメチロールプロパンのジ又はトリア
クリレート、トリメチロールプロパンのジ又はトリメタ
クリレート、テトラメチロールメタンのジ、トリまたは
テトラアクリレート、テトラメチロールメタンのジ、ト
リまたはテトラメタクリレート等が挙げられる。反応性
及び生成した共重合体粒子の膨潤性を考慮すると、エチ
レングリコールジメタクリレートが好ましい。これらの
化合物は、単独又は2種以上を組み合わせて使用するこ
とができる。
The (a) divinylbenzene used in the present invention is not particularly limited in purity, but it is preferable to use one having a purity of 60% by weight or more. The polyhydric alcohol poly (meth) acrylic acid ester (b) used in the present invention (herein, the notation of (meth) acrylic acid means acrylic acid and methacrylic acid) includes ethylene glycol diacrylate and ethylene glycol. Dimethacrylate, propylene glycol diacrylate, propylene glycol dimethacrylate, polyethylene glycol diacrylate, polyethylene glycol dimethacrylate, polypropylene glycol diacrylate, polypropylene glycol dimethacrylate, glycerin di- or triacrylate, glycerin di- or trimethacrylate, trimethylolpropane Di- or triacrylate, trimethylolpropane di- or trimethacrylate, tetramethylolmethane di-, tri- or Tetraacrylate, di tetramethylolmethane, tri- or tetramethacrylate, and the like. Considering reactivity and swelling property of the produced copolymer particles, ethylene glycol dimethacrylate is preferable. These compounds can be used alone or in combination of two or more kinds.

【0006】本発明において、(a)ジビニルベンゼン
と(b)多価アルコールポリ(メタ)アクリル酸エステ
ルは、(a)20〜70重量部、(b)30〜80重量
部で、(a)+(b)=100重量部となる割合で使用
される。(a)ジビニルベンゼンが少な過ぎると共重合
体粒子の親水性が増し溶媒間での膨潤、収縮が大きくな
り回収率も低下し、多過ぎると共重合体粒子の疎水性が
増し回収率にバラツキが生じる。
In the present invention, (a) divinylbenzene and (b) polyhydric alcohol poly (meth) acrylic acid ester are (a) 20 to 70 parts by weight, (b) 30 to 80 parts by weight, and (a) + (B) = 100 parts by weight is used. (A) When the amount of divinylbenzene is too small, the hydrophilicity of the copolymer particles increases, the swelling and contraction between the solvents increase, and the recovery rate decreases. When the amount is too large, the hydrophobicity of the copolymer particles increases and the recovery rate varies. Occurs.

【0007】水性懸濁重合は、重合開始剤の存在下で行
う。重合開始剤としては、過酸化ベンゾイル、過酸化ジ
クロルベンゾイル、過酸化ジクミル、過酸化ジ−第3ブ
チル及び過安息香酸第3ブチル、メチルエチルケトンペ
ルオキシド、メチルシクロヘキサノンペルオキシド等の
有機過酸化物、アゾビスイソブチロニトリル、ジメチル
アゾジイソブチレート等のアゾ系化合物が挙げられる。
これらは単独で又は2種以上を組み合わせて使用するこ
とができる。この使用量は単量体の種類などにより適宜
決められるものであるが、単量体の総量に対して0.1
〜4.0重量%使用されることが好ましい。
The aqueous suspension polymerization is carried out in the presence of a polymerization initiator. Examples of the polymerization initiator include benzoyl peroxide, dichlorobenzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide and tert-butyl perbenzoate, organic peroxides such as methyl ethyl ketone peroxide and methyl cyclohexanone peroxide, and azobis. Examples thereof include azo compounds such as isobutyronitrile and dimethylazodiisobutyrate.
These may be used alone or in combination of two or more. The amount used is appropriately determined depending on the kind of the monomer, etc., but is 0.1% with respect to the total amount of the monomers.
It is preferable to use ˜4.0% by weight.

【0008】水性懸濁重合は、分散剤の存在下で行う。
分散剤としては、例えば、ポリビニルアルコール、アル
キルセルロース、ヒドロキシアルキルセルロース、カル
ボキシアルキルセルロース等の水溶性セルロース誘導
体、ポリアクリル酸ナトリウムなどの高分子保護コロイ
ドが挙げられる。分散剤は水に対して1〜0.001重
量%の範囲で使用されることが好ましい。粒径調節等の
ために必要に応じて分散助剤として陰イオン系界面活性
を重合系に添加したり、単量体や有機溶媒の水への溶解
性を低下させる等のために水溶性無機塩を重合系に添加
することができる。
The aqueous suspension polymerization is carried out in the presence of a dispersant.
Examples of the dispersant include water-soluble cellulose derivatives such as polyvinyl alcohol, alkyl cellulose, hydroxyalkyl cellulose and carboxyalkyl cellulose, and polymeric protective colloids such as sodium polyacrylate. The dispersant is preferably used in the range of 1 to 0.001% by weight with respect to water. If necessary, an anionic surfactant may be added to the polymerization system as a dispersion aid to adjust the particle size, or the solubility of the monomer or organic solvent in water may be reduced to improve the solubility of the water-soluble inorganic substance. Salts can be added to the polymerization system.

【0009】重合時に水と相溶しない有機溶媒を添加す
ることにより生成する共重合体を多孔性にすることがで
きる。本発明で用いられる水と相溶しない有機溶媒は、
25℃で水100gに対しての溶解量が15g以下のも
であり、例えば、トルエン、ジエチルベンゼン、ドデカ
ン、イソアミルアルコール、酢酸エチル、酢酸プロピ
ル、酢酸ブチル、セロソルブアセテート等がある。これ
らの溶媒は、単独又は2種以上を組合せて用いても良
い。これらは単量体の総量に対して0〜300重量%使
用されることが好ましい。
The copolymer produced can be made porous by adding an organic solvent which is incompatible with water during the polymerization. The organic solvent that is incompatible with water used in the present invention,
The amount dissolved in 100 g of water at 25 ° C. is 15 g or less, and examples thereof include toluene, diethylbenzene, dodecane, isoamyl alcohol, ethyl acetate, propyl acetate, butyl acetate, and cellosolve acetate. You may use these solvents individually or in combination of 2 or more types. These are preferably used in an amount of 0 to 300% by weight based on the total amount of monomers.

【0010】重合反応は、通常、70〜90℃の温度範
囲で5〜8時間行われる。以上のようにして得られた粒
径が10〜200μm、好ましくは30〜100μmの
球状共重合体粒子は、必要に応じて分級し、固相抽出用
の架橋共重合体粒子として使用される。樹脂製のリザー
バーは、有機溶媒に不溶性で、架橋共重合体粒子が試料
の濃縮作業中に樹脂製のリザーバーから流れでたりしな
ければよく、その材質、形は特に制限されない。そのよ
うなものとして例えば、ポリプロピレン、ポリエチレン
等の容積1〜500ml、好ましくは5〜50mlの注射器
型シリンジに樹脂性のフィルターがセットされたものを
挙げることができる。架橋共重合体粒子の樹脂製のリザ
ーバーへの充てん量は粒子のかさ密度、試料の濃縮量に
より異なるが、通常、樹脂製のリザーバーの容積8mlに
対して300〜2000mg、好ましくは、400〜10
00mgとなるように充てんする。
The polymerization reaction is usually carried out in the temperature range of 70 to 90 ° C. for 5 to 8 hours. The spherical copolymer particles having a particle size of 10 to 200 μm, preferably 30 to 100 μm, obtained as described above are classified as necessary and used as cross-linked copolymer particles for solid phase extraction. The resin-made reservoir is insoluble in an organic solvent, and the cross-linked copolymer particles need not flow out of the resin-made reservoir during the sample concentration operation, and the material and shape thereof are not particularly limited. Examples of such a material include a syringe type syringe having a volume of 1 to 500 ml, preferably 5 to 50 ml, such as polypropylene or polyethylene, and a resin filter set therein. The filling amount of the crosslinked copolymer particles in the resin reservoir varies depending on the bulk density of the particles and the concentration of the sample, but is usually 300 to 2000 mg, preferably 400 to 10 mg per 8 ml volume of the resin reservoir.
Fill to 00 mg.

【0011】[0011]

【実施例】次に、実施例により本発明を説明する。EXAMPLES Next, the present invention will be described with reference to examples.

【0012】実施例1 純度60重量%のジビニルベンゼン(三共化成株式会社
製)100g、エチレングリコールジメタクリレート1
00g、水に不溶な有機溶媒としての酢酸ブチル200
g、イソアミルアルコール50g及びアゾビスイソブチ
ロニトリル1.0gの混合液を0.2重量%のメチルセ
ルロース水溶液1リットル中に懸濁させホモミキサーを
使用して高速撹拌下(1500rpm)70℃で50分間
撹拌し、粒径を30〜100μmになるように調節し
た。その後、プロペラ撹拌装置に移して撹拌しながら
(200rpm)80℃で6時間反応させて固相抽出用共
重合体粒子を得た。この粒子を濾過して水2リットル、
次いでアセトン2リットルで超音波洗浄し、1時間後濾
過して風乾、真空乾燥を行った(収率は98%であっ
た)。得られた粒子を40〜90μmに分級し、固相抽
出カートリッジカラム用の架橋共重合体粒子とした。図
1に示すように、この架橋共重合体粒子2を樹脂製のフ
ィルター1がセットされた樹脂製(ポリプロピレン製)
のリザーバー3に0.5g充てんし、さらに上から樹脂
製のフィルター1で栓をして固相抽出用カートリッジカ
ラム4とした。この固相抽出用カートリッジカラム4を
用いて以下の手順で農薬の濃縮、回収率の測定を行っ
た。 (1)固相抽出用カートリッジカラム4を図2のように
吸引マニホールド6にセットする。 (2)吸引マニホールド6内に受器のメスフラスコ7を
セットする。 (3)吸引を開始して減圧し、吸引マニホールド6内を
11〜13mmHgに調節する。 (4)5mlのアセトニトリルを試料注入用リザーバー5
に入れ二方コック8を開き吸引する。 (5)続けて、30mlの純水を通液させる。 (6)10ppmに調整された6種類の農薬入標準試料5m
lを200mlのメスフラスコで40倍に希釈することに
より得られた各0.25ppmに調製された6種類の農薬
入りの試料200mlを試料注入用リザーバー5に投入し
て固体抽出用カートリッジカラム4を通液させ各農薬成
分を固体抽出用カートリッジカラム4内の架橋共重合体
粒子2中に濃縮(吸着により)させる。 (7)液が固体抽出用カートリッジカラム4を抜け切っ
た後、二方コック8を閉じ、試料注入用リザーバー5を
取り付けたまま固相抽出用カラム4を隣に移し、の二方
コック10に取り付ける。 (8)試料注入用リザーバー5に5mlのアセトニトリル
を加え、二方コック10を開き濃縮された農薬成分を溶
出させメスフラスコ9に導く(このとき、固相抽出用カ
ートリッジカラム4内の架橋重合体粒子2中に濃縮(吸
着により)されていた農薬が、すべて脱着し溶出す
る)。 (9)濃縮された農薬成分をよく振盪、撹拌後20μl
を高速液体クロマトグラフィー(HPLC)で分離しそ
の面積値を求める。 (10)各10ppmに調製された7種類の農薬入試料
(標準試料)20μlを高速液体クロマトグラフィー
(HPLC)で分離しその面積値を求める。 (11)濃縮成分の面積値/標準試料の面積値で回収率
を求める。 架橋共重合体粒子の濃縮能力(吸着能力又は脱着能力)
が弱いと試料中の農薬が架橋共重合体粒子に吸着されず
又は吸着されたものがスムーズに脱着されず回収率が低
下する。回収率測定の結果を表1に示した。すべての回
収率が85%以上であることから試料の濃縮能力に優れ
ていることが分かった。
Example 1 100 g of divinylbenzene (manufactured by Sankyo Kasei Co., Ltd.) having a purity of 60% by weight, 1 part of ethylene glycol dimethacrylate
00g, butyl acetate 200 as an organic solvent insoluble in water
g, 50 g of isoamyl alcohol and 1.0 g of azobisisobutyronitrile are suspended in 1 liter of a 0.2% by weight aqueous solution of methylcellulose, and stirred at 70 ° C. under high speed stirring (1500 rpm) using a homomixer. After stirring for a minute, the particle size was adjusted to 30 to 100 μm. Then, the mixture was transferred to a propeller stirrer and reacted at 80 ° C. for 6 hours while stirring (200 rpm) to obtain copolymer particles for solid phase extraction. Filter the particles into 2 liters of water,
Then, the mixture was ultrasonically washed with 2 liters of acetone, filtered for 1 hour, air-dried and vacuum-dried (yield was 98%). The obtained particles were classified to 40 to 90 μm to obtain crosslinked copolymer particles for solid phase extraction cartridge column. As shown in FIG. 1, the cross-linked copolymer particles 2 are made of resin (made of polypropylene) in which a resin filter 1 is set.
0.5 g was filled in the reservoir 3 of the above, and the cartridge column 4 for solid-phase extraction was obtained by capping with the resin filter 1 from above. Using this solid-phase extraction cartridge column 4, the pesticide was concentrated and the recovery rate was measured by the following procedure. (1) The solid phase extraction cartridge column 4 is set in the suction manifold 6 as shown in FIG. (2) Set the receiving measuring flask 7 in the suction manifold 6. (3) Start suction and reduce the pressure to adjust the inside of the suction manifold 6 to 11 to 13 mmHg. (4) Reservoir 5 for sample injection with 5 ml of acetonitrile
And open the two-way cock 8 to suck. (5) Continuously, pass 30 ml of pure water. (6) 6m standard sample containing 6 kinds of pesticides adjusted to 10ppm
200 ml of samples containing 6 kinds of pesticides prepared to 0.25 ppm each by diluting 1 to 40 times with a 200 ml volumetric flask is put into the sample injection reservoir 5 to set the solid extraction cartridge column 4. The pesticide components are passed through the liquid and concentrated (by adsorption) into the cross-linked copolymer particles 2 in the solid extraction cartridge column 4. (7) After the liquid has passed through the solid extraction cartridge column 4, the two-way cock 8 is closed, the solid-phase extraction column 4 is moved to the next side while the sample injection reservoir 5 is attached, and the two-way cock 10 is attached. Install. (8) Add 5 ml of acetonitrile to the sample injection reservoir 5 and open the two-way cock 10 to elute the concentrated pesticide components and guide them to the measuring flask 9 (at this time, the cross-linked polymer in the solid phase extraction cartridge column 4). All pesticides that have been concentrated (by adsorption) in particles 2 are desorbed and eluted). (9) 20 μl of the concentrated pesticide ingredients after shaking and stirring
Are separated by high performance liquid chromatography (HPLC) and the area value is determined. (10) 20 μl of 7 kinds of pesticide-containing samples (standard samples) prepared to 10 ppm each are separated by high performance liquid chromatography (HPLC) and the area value is obtained. (11) Obtain the recovery rate by the area value of the concentrated component / the area value of the standard sample. Concentration capacity of cross-linked copolymer particles (adsorption capacity or desorption capacity)
If it is weak, the pesticide in the sample is not adsorbed on the cross-linked copolymer particles, or the adsorbed one is not smoothly desorbed, and the recovery rate is lowered. The results of recovery measurements are shown in Table 1. Since all of the recoveries were 85% or more, it was found that the sample had an excellent concentration ability.

【0013】実施例2 純度60重量%のジビニルベンゼン140g、エチレン
グリコールジメタクリレート60gを用いた以外は、実
施例1と同様な方法で合成、回収率の測定を行い、結果
を表1に示した。回収率は、実施例1と同様に優れてい
た。
Example 2 Synthesis and recovery were measured in the same manner as in Example 1 except that 140 g of divinylbenzene having a purity of 60% by weight and 60 g of ethylene glycol dimethacrylate were used, and the results are shown in Table 1. . The recovery rate was excellent as in Example 1.

【0014】比較例1 純度60重量%のジビニルベンゼン200gを用いた以
外は、実施例1と同様の方法で合成、回収率の測定を行
い、結果を表1に示した。一部の回収率が低く、再現性
にも乏しかった。
Comparative Example 1 Synthesis and recovery were measured in the same manner as in Example 1 except that 200 g of divinylbenzene having a purity of 60% by weight was used, and the results are shown in Table 1. Part of the recovery rate was low and reproducibility was poor.

【0015】比較例2 エチレングリコールジメタクリレート160g、ステア
リルメタクリレート40g及び酢酸ブチル200gを使
用した以外は、実施例1と同様な方法で合成、回収率の
測定を行い、結果を表1に示した。比較例1と同様に一
部の回収率が低く、再現性にも乏しかった。
Comparative Example 2 Synthesis and recovery were measured in the same manner as in Example 1 except that 160 g of ethylene glycol dimethacrylate, 40 g of stearyl methacrylate and 200 g of butyl acetate were used, and the results are shown in Table 1. Similar to Comparative Example 1, a part of the recovery rate was low and the reproducibility was poor.

【表1】 HPLCの測定条件は、 カラム:Excelpak GLF−R27(5mmφ×250m
m) 移動相:アセトニトリル/25mM KH2PO4(pH3.
15) 流量:1.0ml/分 検出器:紫外線吸収検出器 波長:UV220nm 注入量:20μl
[Table 1] The HPLC measurement conditions are as follows: Column: Excelpak GLF-R27 (5 mmφ x 250 m
Mobile phase: acetonitrile / 25 mM KH 2 PO 4 (pH 3.
15) Flow rate: 1.0 ml / min Detector: Ultraviolet absorption detector Wavelength: UV220nm Injection volume: 20 μl

【0016】[0016]

【発明の効果】本発明の固相抽出用カートリッジカラム
はコンパクトであり安価で使い捨てとすることもでき
る。また、吸着性及び脱着性がよく回収率に優れるの
で、農薬、ハロゲン系溶剤等の環境関連化合物の希薄溶
液の試料を作業性よく容易に濃縮でき、濃縮された試料
は各種の分析に好適に用いることができ、各種の分析を
容易に行うことができる。
The solid-phase extraction cartridge column of the present invention is compact, inexpensive, and disposable. In addition, since the adsorption and desorption properties are good and the recovery rate is excellent, samples of dilute solutions of environment-related compounds such as agricultural chemicals and halogenated solvents can be easily concentrated with good workability, and the concentrated samples are suitable for various analyzes. It can be used and various analyzes can be easily performed.

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

【図1】本発明の固相抽出用カートリッジカラムの模式
図。
FIG. 1 is a schematic view of a solid phase extraction cartridge column of the present invention.

【図2】本発明の固相抽出用カートリッジカラムを用い
た試料の濃縮、回収装置の一例を示す模式図。
FIG. 2 is a schematic diagram showing an example of an apparatus for concentrating and recovering a sample using the solid phase extraction cartridge column of the present invention.

【符号の説明】[Explanation of symbols]

1 フィルター 2 架橋共重合体粒子 3 樹脂性のリザーバー 4 固相抽出用カートリッジカラム 5 試料注入用リザーバー 6 吸引マニホールド 7 メスフラスコ 8 二方コック 9 メスフラスコ 10 二方コック 11 三方コック 1 Filter 2 Crosslinked Copolymer Particles 3 Resinous Reservoir 4 Cartridge Column for Solid Phase Extraction 5 Reservoir for Sample Injection 6 Suction Manifold 7 Volumetric Flask 8 Two-way Cock 9 Two-way Flask 10 Two-way Cock 11 Three-way Cock 11

───────────────────────────────────────────────────── フロントページの続き (72)発明者 平井 修 茨城県日立市東町四丁目13番1号 日立化 成工業株式会社茨城研究所内 (72)発明者 井上 嘉則 東京都武蔵野市中町一丁目16番10号 横河 アナリティカルシステムズ株式会社内 (72)発明者 熊谷 浩樹 東京都武蔵野市中町一丁目16番10号 横河 アナリティカルシステムズ株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Osamu Hirai 4-13-1, Higashimachi, Hitachi-shi, Ibaraki Hitachi Chemical Co., Ltd. Ibaraki Research Institute (72) Inventor Yoshinori Inoue 1-16-1, Nakamachi, Musashino-shi, Tokyo No. 10 Yokogawa Analytical Systems Co., Ltd. (72) Inventor Hiroki Kumagai 1-16-10 Nakamachi, Musashino-shi, Tokyo Yokogawa Analytical Systems Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 (a)ジビニルベンゼン20〜70重量
部、(b)多価アルコールポリ(メタ)アクリル酸エス
テル30〜80重量部((a)+(b)=100重量
部)及び(c)必要に応じて用いられる他のビニル系モ
ノマーを水性懸濁共重合した架橋共重合体粒子を樹脂製
のリザーバーに充てんした固相抽出用カートリッジカラ
ム。
1. (a) 20 to 70 parts by weight of divinylbenzene, (b) 30 to 80 parts by weight of a polyhydric alcohol poly (meth) acrylic acid ester ((a) + (b) = 100 parts by weight) and (c). ) A solid-phase extraction cartridge column in which a resin-made reservoir is filled with cross-linked copolymer particles obtained by aqueous suspension-copolymerizing other vinyl-based monomers used as necessary.
JP04917093A 1993-03-10 1993-03-10 Cartridge column for solid phase extraction Expired - Lifetime JP3274898B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04917093A JP3274898B2 (en) 1993-03-10 1993-03-10 Cartridge column for solid phase extraction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04917093A JP3274898B2 (en) 1993-03-10 1993-03-10 Cartridge column for solid phase extraction

Publications (2)

Publication Number Publication Date
JPH06258203A true JPH06258203A (en) 1994-09-16
JP3274898B2 JP3274898B2 (en) 2002-04-15

Family

ID=12823602

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001343378A (en) * 2000-06-02 2001-12-14 Showa Denko Kk Filler for solid-phase extraction and solid-phase extraction method
US6602928B2 (en) * 2000-08-21 2003-08-05 Showa Denko Kabushiki Kaisha Packing material and cartridge for solid phase extraction
JP2009156657A (en) * 2007-12-26 2009-07-16 Japan Organo Co Ltd Automatic solid-phase pretreatment apparatus and solid-phase pretreatment method of sample water
JP2010256225A (en) * 2009-04-27 2010-11-11 Nippon Filcon Co Ltd Sintered-type adsorbent for solid phase extraction, and cartridge
JP4838938B2 (en) * 1998-12-08 2011-12-14 アジレント・テクノロジーズ・インク Modular solid phase extraction plate assembly
US8101073B2 (en) 2004-08-31 2012-01-24 Shinwa Chemical Industries, Ltd. Separating agent for solid-phase extraction
CN106066258A (en) * 2016-06-13 2016-11-02 青岛容广电子技术有限公司 A kind of sampling head for the sampling of stationary source low concentrations of particulates thing

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4838938B2 (en) * 1998-12-08 2011-12-14 アジレント・テクノロジーズ・インク Modular solid phase extraction plate assembly
JP2001343378A (en) * 2000-06-02 2001-12-14 Showa Denko Kk Filler for solid-phase extraction and solid-phase extraction method
US6602928B2 (en) * 2000-08-21 2003-08-05 Showa Denko Kabushiki Kaisha Packing material and cartridge for solid phase extraction
US8101073B2 (en) 2004-08-31 2012-01-24 Shinwa Chemical Industries, Ltd. Separating agent for solid-phase extraction
JP2009156657A (en) * 2007-12-26 2009-07-16 Japan Organo Co Ltd Automatic solid-phase pretreatment apparatus and solid-phase pretreatment method of sample water
JP2010256225A (en) * 2009-04-27 2010-11-11 Nippon Filcon Co Ltd Sintered-type adsorbent for solid phase extraction, and cartridge
CN106066258A (en) * 2016-06-13 2016-11-02 青岛容广电子技术有限公司 A kind of sampling head for the sampling of stationary source low concentrations of particulates thing

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