JP2005213477A - Chelate resin and method for producing the same - Google Patents

Chelate resin and method for producing the same Download PDF

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JP2005213477A
JP2005213477A JP2004025449A JP2004025449A JP2005213477A JP 2005213477 A JP2005213477 A JP 2005213477A JP 2004025449 A JP2004025449 A JP 2004025449A JP 2004025449 A JP2004025449 A JP 2004025449A JP 2005213477 A JP2005213477 A JP 2005213477A
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chelate resin
polyamine
carrier
iminoethyl
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JP4605432B2 (en
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Michio Butsugan
道男 佛願
Hiroyuki Kawada
博之 河田
Tetsuya Aoyama
哲也 青山
Yugo Kumagai
雄五 熊谷
Yoshinori Inoue
嘉則 井上
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Resonac Corp
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Hitachi Chemical Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a chelate resin having a large catching amount of a metal, especially selecting/concentrating copper ion in a good efficiency, and a method for producing the chelate resin easily and at a low cost. <P>SOLUTION: This chelate resin obtained by reacting a halogenated acetic acid with a polyamine-containing polymer introduced on a cross-linked carrier is characterized in that the polyamine-containing polymer is a chelate resin of a poly(iminoethyl)amine expressed by general formula (1): H<SB>2</SB>N(C<SB>2</SB>H<SB>4</SB>NH)<SB>n</SB>H [wherein, (n) is a positive integer], the cross-linked carrier contains an epoxy or a halogen group and the modification with ammonia is performed before or after the introduction of a halogenated acetic acid into the poly(iminoethyl)amine, and a method for producing the same is also provided. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は有害金属、特に銅イオンを効率良く選択、濃縮できるキレート樹脂及びその製造方法に関する。該キレート樹脂は、金属イオンの吸着量が多くかつ、脱着速度が速いので、廃液処理用の他分析用前処理剤,クロマトグラフィ担体等にも用いることが出来る。   The present invention relates to a chelate resin capable of efficiently selecting and concentrating harmful metals, particularly copper ions, and a method for producing the same. Since the chelate resin has a large amount of adsorption of metal ions and has a high desorption rate, it can be used for a pretreatment agent for analysis, a chromatographic carrier and the like for waste liquid treatment.

キレート樹脂とは、2つ以上の官能基を有し,キレート結合により特定のイオンを選択的吸着する。キレート結合にあずかる官能基の組み合わせが(N,O)の場合を例にとると、一般的には、クロロメチル化したスチレンとジビニルベンゼンとの共重合体を処理してイミノジ酢酸型,イミノジプロピオン酸型が作製される。ナトリウムイオン,カルシウムイオン,マグネシウムイオン等が多量に存在し、普通のイオン交換だと実用上使用できない廃水中の重金属の選択除去に用いられる(化学大辞典) (1296の化学商品)。担体に導入する イミノジ酢酸(IDA),イミノプロピオン酸等のイミノジカルボン酸は、金属の選択性も小さく、吸着量が十分でない等の課題がある。従って,従来のイミノジ酢酸(IDA)型は、マトリックスの多い試料中の金属を濃縮する目的としては必ずしもベストではない。
また、銅等とキレ−ト化率の高いアミノトリ酢酸(NTA),エチレンジアミンテトラ酢酸等は、試薬が高価で実用化できないという問題もあった。
A chelate resin has two or more functional groups and selectively adsorbs specific ions through chelate bonds. For example, when the combination of functional groups involved in a chelate bond is (N, O), generally, a copolymer of chloromethylated styrene and divinylbenzene is treated to give an iminodiacetic acid type or iminodiamine. A propionic acid form is created. Sodium ion, calcium ion, magnesium ion, etc. are present in large quantities, and they are used for selective removal of heavy metals in wastewater that cannot be used practically by ordinary ion exchange (Chemical Dictionary) (1296 chemical products). Iminodicarboxylic acids such as iminodiacetic acid (IDA) and iminopropionic acid to be introduced into the carrier have problems such as low metal selectivity and insufficient adsorption. Therefore, the conventional iminodiacetic acid (IDA) type is not always the best for the purpose of concentrating metals in a sample with a lot of matrix.
Further, aminotriacetic acid (NTA), ethylenediaminetetraacetic acid and the like, which have a high chelating rate with copper and the like, have a problem that the reagents are expensive and cannot be put into practical use.

特開昭53−1087号公報Japanese Patent Laid-Open No. 53-1087

本発明者らは,アミノトリ酢酸(NTA),エチレンジアミンテトラ酢酸等の高価なイミノジカルボン酸等の試薬を用いず、ポリアミン含有ポリマに安価なハロゲン化酢酸を反応させることにより、金属の吸着性が高いキレート樹脂ができることを見出した。   The present inventors do not use expensive reagents such as aminotriacetic acid (NTA) and ethylenediaminetetraacetic acid, but have a high metal adsorptivity by reacting an inexpensive halogenated acetic acid with a polyamine-containing polymer. It was found that a chelate resin can be formed.

本発明は以下の発明に関する。
<1> 架橋担体に導入されるポリアミン含有ポリマにハロゲン化酢酸を反応させてなるキレート樹脂。
<2> 架橋担体に導入されるポリアミン含有ポリマが、下記一般式(1)のポリ(イミノエチル)アミンである<1>記載のキレート樹脂。

Figure 2005213477
但し、nは正の整数を表す。
<3> 上記一般式(1)のポリ(イミノエチル)アミンが、n=1,2,3であるエチレンジアミン,ジエチレントリアミン,トリエチレンテトラアミンである<2>記載のキレート樹脂。
<4> 架橋担体に導入されるポリアミン含有ポリマが、下記一般式(2)の分岐型ポリ(イミノエチル)アミンである<1>記載のキレート樹脂。
Figure 2005213477
但し、x,yは正の整数を表す。
<5> 架橋担体がエポキシまたはハロゲン基含有するもので、ポリ(イミノエチル)アミンにハロゲン化酢酸導入前、または後に、アンモニアによる変性を行うことを特徴とする<1>〜<4>のいずれかに記載のキレート樹脂。
<6> 上記<5>に記載のキレート樹脂の製造法。 The present invention relates to the following inventions.
<1> A chelate resin obtained by reacting a halogenated acetic acid with a polyamine-containing polymer introduced into a crosslinking carrier.
<2> The chelate resin according to <1>, wherein the polyamine-containing polymer introduced into the crosslinking carrier is a poly (iminoethyl) amine represented by the following general formula (1).
Figure 2005213477
However, n represents a positive integer.
<3> The chelate resin according to <2>, wherein the poly (iminoethyl) amine of the general formula (1) is ethylenediamine, diethylenetriamine, or triethylenetetraamine where n = 1,2,3.
<4> The chelate resin according to <1>, wherein the polyamine-containing polymer introduced into the crosslinked carrier is a branched poly (iminoethyl) amine represented by the following general formula (2).
Figure 2005213477
However, x and y represent a positive integer.
<5> Any one of <1> to <4>, wherein the crosslinking carrier contains an epoxy or a halogen group, and the poly (iminoethyl) amine is modified with ammonia before or after the introduction of halogenated acetic acid. The chelating resin described in 1.
<6> The method for producing a chelate resin according to <5> above.

本発明のキレート樹脂を用いれば、金属の補足量が大きく,特に銅イオンを効率良く選択、濃縮できる。また、本特許記載の製造法に従えば、容易に該キレート樹脂が製造できる。   If the chelate resin of the present invention is used, a large amount of metal is captured, and particularly copper ions can be efficiently selected and concentrated. Further, according to the production method described in this patent, the chelate resin can be easily produced.

以下、本発明の実施形態を詳細に説明する。
本発明は、ポリアミン含有ポリマ(例:式(3))にハロゲン化酢酸を反応させてできるキレート樹脂及びその製造方法に関するものであり、詳しくは、ポリ(イミノエチル)アミン等の担体のポリアミン鎖をハロゲン化酢酸等でカルボキシメチル化し、ポリアミン−ポリカルボン酸型キレート樹脂を合成するものである。該キレート樹脂は、イミノジ酢酸の様な、単一なキレート基を導入したものではないので、以下に示す式(4)〜(6)様な官能基が混在するものである。
Hereinafter, embodiments of the present invention will be described in detail.
The present invention relates to a chelate resin obtained by reacting a halogenated acetic acid with a polyamine-containing polymer (eg, formula (3)) and a method for producing the same. Specifically, a polyamine chain of a carrier such as poly (iminoethyl) amine is used. It carboxymethylates with halogenated acetic acid or the like to synthesize a polyamine-polycarboxylic acid type chelate resin. Since the chelate resin is not the one having a single chelate group introduced like iminodiacetic acid, it has a mixture of functional groups represented by the following formulas (4) to (6).

Figure 2005213477
Figure 2005213477

ポリアミン含有ポリマは,ハロゲン化酢酸が反応できるものであれば特に限定しないが、液体試料(廃液)等から、キレート樹脂を取り出す等の作業を考えると実用上、架橋担体に、ポリアミンが導入されたものが好ましい。   The polyamine-containing polymer is not particularly limited as long as it can react with halogenated acetic acid. However, in consideration of operations such as taking out a chelate resin from a liquid sample (waste liquid) or the like, in practice, polyamine is introduced into the cross-linked carrier. Those are preferred.

架橋担体としては、多孔性ポリスチレンの誘導体,多孔性ポリエステルその誘導体,多孔性ポリビニルアルコールの誘導体等が挙げられるが、ポリアミン導入が容易に出きる様に、ハロゲン基含有のポリクロロメチルスチレン,エポキシ基含有のポリグリシジルメタクリレート等が好ましい。   Examples of the cross-linking carrier include porous polystyrene derivatives, porous polyester derivatives thereof, porous polyvinyl alcohol derivatives, etc., but halogen group-containing polychloromethylstyrene, epoxy group so that polyamine can be easily introduced. Containing polyglycidyl methacrylate is preferred.

担体の合成方法は、特に限定しないが例えば、クロロメチルスチレン,グリシジルメタクリレート等を特許文献1記載の方法に準じて水性懸濁重合させて行うことができる。なお、クロロメチルスチレン,グリシジルメタクリレート等のアミノ基と反応する基を含有モノマーは、10〜90重量%用いる必要がある。少なすぎると、ポリアミン導入量が少なくなり、金属補足量が減る。多すぎると、架橋担体の強度が弱くなり、廃液等で膨潤し、操作が困難となるとともにポリアミン架橋を生じる。   The method for synthesizing the carrier is not particularly limited, and for example, chloromethylstyrene, glycidyl methacrylate and the like can be subjected to aqueous suspension polymerization according to the method described in Patent Document 1. In addition, it is necessary to use 10 to 90% by weight of a monomer containing a group that reacts with an amino group such as chloromethylstyrene or glycidyl methacrylate. If the amount is too small, the amount of polyamine introduced is reduced and the amount of metal supplement is reduced. When the amount is too large, the strength of the cross-linking carrier becomes weak, and it swells with waste liquid or the like, which makes operation difficult and causes polyamine cross-linking.

ハロゲン基,エポキシ基含有ポリマを合成した場合は、ポリアミノ化後及びハロゲン化酢酸導入後に、ハロゲン基,エポキシ基が残り、試料中のマトリックス(有機物質)と反応してしまう可能性があるので、必要に応じて、ハロゲン化酢酸導入前後に、アンモニア水で、ポリアミノ化変性することが好ましい。   When synthesizing halogen group and epoxy group-containing polymers, after polyamination and introduction of halogenated acetic acid, halogen groups and epoxy groups may remain and react with the matrix (organic substance) in the sample. If necessary, it is preferable to perform polyamination modification with aqueous ammonia before and after the introduction of halogenated acetic acid.

架橋担体に導入するポリアミンとしては、アミン含有ポリマであれば良いが、特に前記一般式(1)に示すエチレンジアミン,ジエチレントリアミン,トリエチレンテトラアミン等,前記一般式(2)に示す分岐ポリ(イミノエチル)アミンが望ましい。ポリ(イミノエチル)アミンは、分子鎖が長いと吸着量は増すが、分子鎖が巻くため、脱着が不充分になり、分離剤やクロマトグラフィや、等の用途では不利となる。   The polyamine introduced into the cross-linking carrier may be an amine-containing polymer, but in particular, the branched poly (iminoethyl) represented by the general formula (2) such as ethylenediamine, diethylenetriamine, triethylenetetraamine, etc. represented by the general formula (1). Amines are desirable. Poly (iminoethyl) amine increases the amount of adsorption when the molecular chain is long. However, since the molecular chain is wound, desorption becomes insufficient, which is disadvantageous for uses such as a separating agent and chromatography.

作製した(イミノエチルアミン)を導入した担体(ポリアミン含有ポリマ)に、ハロゲン化酢酸でカルボキシメチル化することにより、キレート樹脂が作製できる。ハロゲン化酢酸としては、クロロ酢酸,ブロモ酢酸等が挙げられる。   A chelate resin can be produced by carboxymethylating the produced carrier (polyamine-containing polymer) into which (iminoethylamine) has been introduced with halogenated acetic acid. Examples of the halogenated acetic acid include chloroacetic acid and bromoacetic acid.

ハロゲン化酢酸は、すべてのアミンに導入する必要はなく、反応状態により、前記式(4)〜(6)等のキレート基が混在する。完全にカルボキシメチル化ができなくともイミノエチレン鎖のスペーサとなり,銅との親和性がアップし、銅の補足量をます。また、酸性下では、プロトネ-ションで排除効果が起き、金属イオン,脱着を容易にすることになる。   Halogenated acetic acid does not need to be introduced into all amines, and chelate groups such as the above formulas (4) to (6) are mixed depending on the reaction state. Even if it cannot be completely carboxymethylated, it becomes a spacer of the iminoethylene chain, increasing its affinity with copper, and supplementing copper. In addition, under acidic conditions, the elimination effect occurs in the protonation, which facilitates metal ions and desorption.

以下実施例により本発明を説明する。
実施例1
The following examples illustrate the invention.
Example 1

(a)架橋担体の製造
グリシジルメタクリレート100g、テトラメチロールメタントリメタクリレート100g、酢酸ブチル180g、イソアミルアルコール120g及びアゾビスイソブチロニトリル0.7gの混合物にイオン交換水1000ml、1%ポリビニルアルコール水溶液200mlを加え、攪拌しながら水酸化ナトリウム水溶液を用いてpH7〜8に調整した。その後、70℃で6時間重合反応を行った。反応物を冷却した後、生成した共重合体粒子を濾取し、メタノール及び水で順次洗浄した。次いで、一日風乾し、さらに80℃の真空乾燥機に入れて6時間乾燥した。乾燥粒子を分級して40〜50μmの多孔性架橋重合体粒子30gを得た。
(b)ポリアミノ化反応
メタノール20g,イオン交換水80gにジエチレンテトラアミン15gを溶解し、(1)で得られた重合体粒子(架橋担体)10gを加え、60℃で5時間反応させた。反応物を濾過し、イオン交換水で洗浄した。この反応物をさらに、0.28%アンモニア水溶液100mlに入れ、30℃で5時間反応させ、残存エポキシ基をアミノ開環した。その後、イオン交換水で洗浄して、ポリアミノ化担体(ポリアミン)を得た。
(c)カルボキシメチル化
1M NaOH水溶液100mlにクロロ酢酸ナトリウム14gを溶解し、(b)で得られたポリアミノ化担体(ポリアミン)を全量入れ、40℃で5時間反応させ、反応物を濾過しイオン交換水、メタノールで洗浄し、キレート樹脂を得た。
(d)評価
カートリッジに、作製したキレート樹脂0.25gを充填し、アセトニトリル,10mM硝酸,0.05M酢酸アンモニウム,イオン交換水でコンディショニング後、0.5 M硫酸銅4 mL負荷し、余剰分の硫酸銅を10mM硝酸,イオン交換水で洗い、1 M硝酸6 mLで溶出し、吸光光度計で銅補足量を測定(測定波長:805 nm,参照セル:水)した。補足量は、250μmol/gであった。
実施例2
(a) Manufacture of a cross-linking carrier A mixture of 100 g of glycidyl methacrylate, 100 g of tetramethylolmethane trimethacrylate, 180 g of butyl acetate, 120 g of isoamyl alcohol and 0.7 g of azobisisobutyronitrile was mixed with 1000 ml of ion-exchanged water and 200 ml of 1% aqueous polyvinyl alcohol solution. In addition, the pH was adjusted to 7-8 using an aqueous sodium hydroxide solution with stirring. Thereafter, a polymerization reaction was carried out at 70 ° C. for 6 hours. After cooling the reaction product, the produced copolymer particles were collected by filtration and washed successively with methanol and water. Subsequently, it was air-dried for one day and further put into a vacuum dryer at 80 ° C. for 6 hours. The dried particles were classified to obtain 30 g of porous crosslinked polymer particles of 40 to 50 μm.
(b) Polyamination reaction 15 g of diethylenetetraamine was dissolved in 20 g of methanol and 80 g of ion-exchanged water, and 10 g of the polymer particles (crosslinked carrier) obtained in (1) were added and reacted at 60 ° C. for 5 hours. The reaction was filtered and washed with ion exchange water. This reaction product was further added to 100 ml of 0.28% aqueous ammonia solution and reacted at 30 ° C. for 5 hours to open the remaining epoxy group with amino ring. Thereafter, it was washed with ion-exchanged water to obtain a polyaminated carrier (polyamine).
(c) Carboxymethylation
Dissolve 14 g of sodium chloroacetate in 100 ml of 1M NaOH aqueous solution, add the whole amount of polyaminated carrier (polyamine) obtained in (b), react at 40 ° C for 5 hours, filter the reaction product, wash with ion-exchanged water and methanol Thus, a chelate resin was obtained.
(d) Evaluation The cartridge was filled with 0.25 g of the prepared chelate resin, conditioned with acetonitrile, 10 mM nitric acid, 0.05 M ammonium acetate and ion-exchanged water, loaded with 4 mL of 0.5 M copper sulfate, and 10 mM of excess copper sulfate. It was washed with nitric acid and ion-exchanged water, eluted with 6 mL of 1 M nitric acid, and the amount of copper supplemented was measured with an absorptiometer (measurement wavelength: 805 nm, reference cell: water). The supplemental amount was 250 μmol / g.
Example 2

(a)架橋担体の製造
クロロメチルスチレン100g、ジビニルベンゼン100g、酢酸ブチル180g、トルエン120g及びアゾビスイソブチロニトリル0.7gの混合物にイオン交換水1000ml、1%ポリビニルアルコール水溶液200mlを加え、攪拌しながら水酸化ナトリウム水溶液を用いてpH7〜8に調整した。その後、70℃で6時間重合反応を行った。反応物を冷却した後、生成した共重合体粒子を濾取し、メタノール及び水で順次洗浄した。次いで、一日風乾し、さらに80℃の真空乾燥機に入れて6時間乾燥した。乾燥粒子を分級して40〜50μmの多孔性架橋重合体粒子30gを得た。
(b)ポリアミノ化反応
メタノール20g,イオン交換水80gにテトラエチレンジアミン15gを溶解し、(1)で得られた重合体粒子(架橋担体)10gを加え、60℃で5時間反応させた。反応物を濾過し、イオン交換水で洗浄した。この反応物をさらに、0.28%アンモニア水溶液100mlに入れ、30℃で5時間反応させ、残存エポキシ基をアミノ開環した。その後、反応物を濾過し、イオン交換水で洗浄して、ポリアミノ化担体(ポリアミン)樹脂を得た。
(c)カルボキシメチル化
1M NaOH水溶液100mlにクロロ酢酸ナトリウム14gを溶解し、(b)で得られたポリアミノ化担体(ポリアミン)樹脂を全量入れ、40℃で5時間反応させ、反応物を濾過しイオン交換水、メタノールで洗浄して、キレート樹脂を得た。
(d)評価
実施例1(d)の評価方法に従い、銅補足量を求めたところ、180μmol/gであった。
比較例1
(a) Production of cross-linked carrier To a mixture of 100 g of chloromethylstyrene, 100 g of divinylbenzene, 180 g of butyl acetate, 120 g of toluene and 0.7 g of azobisisobutyronitrile, add 1000 ml of ion-exchanged water and 200 ml of 1% polyvinyl alcohol aqueous solution, and stir. The pH was adjusted to 7 to 8 using an aqueous sodium hydroxide solution. Thereafter, a polymerization reaction was carried out at 70 ° C. for 6 hours. After cooling the reaction product, the produced copolymer particles were collected by filtration and washed successively with methanol and water. Subsequently, it was air-dried for one day and further put into a vacuum dryer at 80 ° C. for 6 hours. The dried particles were classified to obtain 30 g of porous crosslinked polymer particles of 40 to 50 μm.
(b) Polyamination reaction 15 g of tetraethylenediamine was dissolved in 20 g of methanol and 80 g of ion-exchanged water, and 10 g of the polymer particles (crosslinked carrier) obtained in (1) were added and reacted at 60 ° C. for 5 hours. The reaction was filtered and washed with ion exchange water. This reaction product was further added to 100 ml of 0.28% aqueous ammonia solution and reacted at 30 ° C. for 5 hours to open the remaining epoxy group with amino ring. Thereafter, the reaction product was filtered and washed with ion exchange water to obtain a polyaminated carrier (polyamine) resin.
(c) Carboxymethylation
Dissolve 14 g of sodium chloroacetate in 100 ml of 1M NaOH aqueous solution, add the whole amount of polyaminated carrier (polyamine) resin obtained in (b), react at 40 ° C for 5 hours, filter the reaction product with ion-exchanged water and methanol. Washing gave a chelate resin.
(d) Evaluation According to the evaluation method of Example 1 (d), the amount of copper supplement was determined and found to be 180 μmol / g.
Comparative Example 1

実施例1(a)で作製した担体10gを、イミノジ酢酸ナトリウム6gを0.5M水酸化ナトリウム水溶液100mlに入れ、60℃で5時間反応した。反応物を濾過しイオン交換水で洗浄した。この反応物をさらに、0.01N硫酸水溶液100mlに入れ、40℃で5時間反応させ、残存エポキシ基を開環した。その後、反応物を濾過し、イオン交換水で洗浄して、イミノジ酢酸型キレート樹脂を得た。実施例1(d)の評価方法に従い、銅補足量を求めたところ、80μmol/gであった。   10 g of the carrier prepared in Example 1 (a) was placed in 100 ml of 0.5 M aqueous sodium hydroxide solution and 6 g of sodium iminodiacetate, and reacted at 60 ° C. for 5 hours. The reaction was filtered and washed with ion exchange water. This reaction product was further placed in 100 ml of 0.01N aqueous sulfuric acid solution and reacted at 40 ° C. for 5 hours to open the remaining epoxy groups. Thereafter, the reaction product was filtered and washed with ion-exchanged water to obtain an iminodiacetic acid type chelate resin. According to the evaluation method of Example 1 (d), the amount of copper supplement was determined to be 80 μmol / g.

以上のように、実施例1及び2の銅補足量は、比較例1の銅補足量よりも高いことがわかった。

As described above, it was found that the copper supplements of Examples 1 and 2 were higher than the copper supplement of Comparative Example 1.

Claims (6)

架橋担体に導入されるポリアミン含有ポリマにハロゲン化酢酸を反応させてなるキレート樹脂。 A chelate resin obtained by reacting a halogenated acetic acid with a polyamine-containing polymer introduced into a crosslinking carrier. 架橋担体に導入されるポリアミン含有ポリマが、下記一般式(1)のポリ(イミノエチル)アミンである請求項1記載のキレート樹脂。
Figure 2005213477
但し、nは正の整数を表す。
The chelate resin according to claim 1, wherein the polyamine-containing polymer introduced into the cross-linking carrier is a poly (iminoethyl) amine represented by the following general formula (1).
Figure 2005213477
However, n represents a positive integer.
上記一般式(1)のポリ(イミノエチル)アミンが、n=1,2,3であるエチレンジアミン,ジエチレントリアミン,トリエチレンテトラアミンである請求項2記載のキレート樹脂。 The chelate resin according to claim 2, wherein the poly (iminoethyl) amine of the general formula (1) is ethylenediamine, diethylenetriamine or triethylenetetraamine in which n = 1,2,3. 架橋担体に導入されるポリアミン含有ポリマが、下記一般式(2)の分岐型ポリ(イミノエチル)アミンである請求項1記載のキレート樹脂。
Figure 2005213477
但し、x,yは正の整数を表す。
The chelate resin according to claim 1, wherein the polyamine-containing polymer introduced into the cross-linking carrier is a branched poly (iminoethyl) amine represented by the following general formula (2).
Figure 2005213477
However, x and y represent a positive integer.
架橋担体がエポキシまたはハロゲン基含有するもので、ポリ(イミノエチル)アミンにハロゲン化酢酸導入前、または後に、アンモニアによる変性を行うことを特徴とする請求項1〜4のいずれかの項に記載のキレート樹脂。 The crosslinking carrier according to any one of claims 1 to 4, wherein the crosslinking carrier contains an epoxy or halogen group, and the poly (iminoethyl) amine is modified with ammonia before or after introduction of the halogenated acetic acid. Chelate resin. 請求項5に記載のキレート樹脂の製造法。

A method for producing the chelate resin according to claim 5.

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WO2010098257A1 (en) * 2009-02-27 2010-09-02 日本フイルコン株式会社 Chelating resin
WO2010122954A1 (en) 2009-04-23 2010-10-28 日本フイルコン株式会社 Metal adsorbent containing chelating polymer
JP2010254841A (en) * 2009-04-27 2010-11-11 Nippon Filcon Co Ltd Metal-adsorptive sintered porous body and method for producing the same
WO2013111891A1 (en) 2012-01-27 2013-08-01 日本フイルコン株式会社 Polymer adsorbent
WO2013121863A1 (en) 2012-02-14 2013-08-22 日本フイルコン株式会社 Metal-adsorbing gel and adsorbent supporting metal-adsorbing gel
JP2013194339A (en) * 2012-03-21 2013-09-30 Chubu Kiresuto Kk Chelate-forming fiber, method for producing the same, metal ion capturing method using the fiber and metal chelate fiber
CN116063733A (en) * 2023-02-20 2023-05-05 苏州赛分科技股份有限公司 TED-based high-tolerance metal chelating reagent affinity filler and preparation method and application thereof

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JPS54135890A (en) * 1978-03-24 1979-10-22 Sumitomo Chem Co Ltd Preparation of chelate resin

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JP2010194509A (en) * 2009-02-27 2010-09-09 Nippon Filcon Co Ltd Chelate resin
US20150065617A1 (en) * 2009-04-23 2015-03-05 Nippon Filcon Co., Limited Adsorbent containing chelating polymer
JP2010253359A (en) * 2009-04-23 2010-11-11 Nippon Filcon Co Ltd Metal adsorbent containing chelating polymer compound
US20120132852A1 (en) * 2009-04-23 2012-05-31 Yoshinori Inoue Metal adsorbent containing chelating polymer
WO2010122954A1 (en) 2009-04-23 2010-10-28 日本フイルコン株式会社 Metal adsorbent containing chelating polymer
US9174194B2 (en) * 2009-04-23 2015-11-03 Nippon Filcon Co., Limited Adsorbent containing chelating polymer
US9199219B2 (en) * 2009-04-23 2015-12-01 Nippon Filcon Co., Limited Metal adsorbent containing chelating polymer
JP2010254841A (en) * 2009-04-27 2010-11-11 Nippon Filcon Co Ltd Metal-adsorptive sintered porous body and method for producing the same
WO2013111891A1 (en) 2012-01-27 2013-08-01 日本フイルコン株式会社 Polymer adsorbent
WO2013121863A1 (en) 2012-02-14 2013-08-22 日本フイルコン株式会社 Metal-adsorbing gel and adsorbent supporting metal-adsorbing gel
US9592489B2 (en) 2012-02-14 2017-03-14 Nippon Filcon Co., Limited Metal-adsorbing gel and adsorbent supporting metal-adsorbing gel
JP2013194339A (en) * 2012-03-21 2013-09-30 Chubu Kiresuto Kk Chelate-forming fiber, method for producing the same, metal ion capturing method using the fiber and metal chelate fiber
CN116063733A (en) * 2023-02-20 2023-05-05 苏州赛分科技股份有限公司 TED-based high-tolerance metal chelating reagent affinity filler and preparation method and application thereof

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