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JPH0339047B2 - - Google Patents
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JPH0339047B2 - - Google Patents

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Publication number
JPH0339047B2
JPH0339047B2 JP58048000A JP4800083A JPH0339047B2 JP H0339047 B2 JPH0339047 B2 JP H0339047B2 JP 58048000 A JP58048000 A JP 58048000A JP 4800083 A JP4800083 A JP 4800083A JP H0339047 B2 JPH0339047 B2 JP H0339047B2
Authority
JP
Japan
Prior art keywords
silica gel
amino acids
optically active
hours
group
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP58048000A
Other languages
Japanese (ja)
Other versions
JPS59173756A (en
Inventor
Noryuki Watanabe
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.)
Tosoh Corp
Original Assignee
Tosoh 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 Tosoh Corp filed Critical Tosoh Corp
Priority to JP58048000A priority Critical patent/JPS59173756A/en
Publication of JPS59173756A publication Critical patent/JPS59173756A/en
Publication of JPH0339047B2 publication Critical patent/JPH0339047B2/ja
Granted legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28061Surface area, e.g. B.E.T specific surface area being in the range 100-500 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
    • B01J20/28004Sorbent size or size distribution, e.g. particle size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28016Particle form
    • B01J20/28019Spherical, ellipsoidal or cylindrical
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28078Pore diameter
    • B01J20/28083Pore diameter being in the range 2-50 nm, i.e. mesopores
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/281Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B01J20/286Phases chemically bonded to a substrate, e.g. to silica or to polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/281Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B01J20/29Chiral phases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3204Inorganic carriers, supports or substrates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3214Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B01J20/3217Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
    • B01J20/3219Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond involving a particular spacer or linking group, e.g. for attaching an active group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3257Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3257Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such
    • B01J20/3259Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such comprising at least two different types of heteroatoms selected from nitrogen, oxygen or sulfur with at least one silicon atom
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3257Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such
    • B01J20/3263Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such comprising a cyclic structure containing at least one of the heteroatoms nitrogen, oxygen or sulfur, e.g. an heterocyclic or heteroaromatic structure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/50Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/54Sorbents specially adapted for analytical or investigative chromatography

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Nanotechnology (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 本発明は、光学異性体の分離を可能とする液体
クロマトグラフイー用充てん剤に関するものであ
る。さらに詳しくは、水溶液系でのゲル浸透クロ
マトグラフイーに使用されている親水性のゲルに
光学活性アミノ酸を固定化し、アミノ酸等の光学
異性体などの分離ができる液体クロマトグラフイ
ー用充てん剤に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a packing material for liquid chromatography that enables separation of optical isomers. More specifically, it relates to a packing material for liquid chromatography that immobilizes optically active amino acids on a hydrophilic gel used in gel permeation chromatography in an aqueous solution system and is capable of separating optical isomers of amino acids, etc. It is.

従来、光学異性体の液体クロマトグラフイーに
よる分離法として、配位子交換クロマトグラフイ
ーが利用され、その充てん剤としてイオン交換樹
脂,逆相クロマトグラフイー用オクタデシルシラ
ン、化学結合型シリカゲル等が利用されている。
Conventionally, ligand exchange chromatography has been used as a method for separating optical isomers by liquid chromatography, and ion exchange resins, octadecylsilane for reversed-phase chromatography, chemically bonded silica gel, etc. are used as packing materials. has been done.

しかし、上記の方法では光学活性アミノ酸を溶
離液自身に添加しておく必要があり、分離法とし
ては煩雑であり、かつ、高価な方法となる。
However, in the above method, it is necessary to add the optically active amino acid to the eluent itself, making the separation method complicated and expensive.

したがつて、光学活性物質を充てん剤自身に化
学結合させ、より簡易に分離する方法が考えられ
るが、充てん剤がスチレンゲルのような非極性の
場合、配位子交換以外の吸着性が水溶液系溶離液
では認められ、ピークのひろがり(理論段数の低
下),分析時間の長期化等、特に芳香族系の試料
では好ましくない現象が発生するため、新しい分
離法が望まれている。
Therefore, it may be possible to chemically bond the optically active substance to the packing material itself for easier separation, but if the packing material is non-polar like styrene gel, the adsorption properties other than ligand exchange will be lower than that of the aqueous solution. A new separation method is desired, as undesirable phenomena occur especially with aromatic samples, such as broadening of peaks (reduction in the number of theoretical plates) and prolongation of analysis time.

本発明者は、上記問題に鑑み鋭意研究の結果、
吸着性の比較的少ないシリカゲルに光学活性アミ
ノ酸を固定化し、アミノ酸等の光学異性体の分離
に適する充てん剤を見い出し本発明を完成した。
As a result of intensive research in view of the above problems, the present inventor has found that
We have completed the present invention by immobilizing optically active amino acids on silica gel, which has relatively low adsorption properties, and found a packing material suitable for separating optical isomers such as amino acids.

すなわち、本発明はシリカゲル細孔表面を通常
の方法でアミノプロピル化し、活性化N−アシル
を導入できる試薬を作用させてアミノ酸を固定化
し、アミノ酸等の光学異性体の分離に適する液体
クロマトグラフイー用充てん剤を提供するもので
ある。
That is, the present invention is a liquid chromatography system suitable for separating optical isomers such as amino acids by aminopropylating the silica gel pore surface using a conventional method and immobilizing amino acids by applying a reagent capable of introducing activated N-acyl. The present invention provides fillers for use in

以下本発明を詳細に説明する。 The present invention will be explained in detail below.

本発明は、アミノ基を有するシランカツプリン
グ剤を用いてアミノプロピル化が行なわれたアミ
ノプロピル化シリカゲルを有機溶媒中において活
性N−アシルを導入できる試薬と保護基を有する
光学活性アミノ酸を反応させた反応液に加えるこ
とによつてアミノ酸がシリカゲル細孔表面に0.3
〜0.5m mol/g固定化された多孔性球状で、
平均粒子径1〜50μ、好ましくは5〜40μ、平均
孔径10Å〜500Å、好ましくは50〜300Å、表面積
100〜500m2/g、好ましくは200〜350m2/gを有
し、かつ、機械的強度が300Kg/cm2以上である充
てん剤である。
The present invention involves reacting aminopropylated silica gel, which has been aminopropylated using a silane coupling agent having an amino group, with a reagent capable of introducing active N-acyl and an optically active amino acid having a protecting group in an organic solvent. By adding amino acids to the silica gel pore surface, 0.3
~0.5m mol/g immobilized porous sphere,
Average particle size 1-50μ, preferably 5-40μ, average pore size 10-500A, preferably 50-300A, surface area
The filler has an area of 100 to 500 m 2 /g, preferably 200 to 350 m 2 /g, and a mechanical strength of 300 Kg/cm 2 or more.

平均粒子径が1μ未満では分離効率の優れたカ
ラムが得られるが、カラムへの充てんが難かし
く、逆に粒子径が50μを越えるとカラムへの充て
んが容易で試料負荷量も多いが、分離効率が悪く
なるため好ましくない。平均孔径が10Å未満では
有効表面積が小さくなり、また500Åを越えると
機械的強度が弱くなるため好ましくない。
When the average particle size is less than 1μ, a column with excellent separation efficiency can be obtained, but it is difficult to fill the column.On the other hand, when the particle size exceeds 50μ, it is easy to fill the column and the sample load is large, but separation is difficult. This is not preferable because it reduces efficiency. If the average pore diameter is less than 10 Å, the effective surface area becomes small, and if it exceeds 500 Å, the mechanical strength becomes weak, which is not preferable.

本発明においてアミノプロピル化シリカゲルを
得る方法は、通常のアミノプロピル化反応を用い
ることができる。すなわち、多孔性球状で、平均
粒子径1〜50μ,平均孔径10〜500Å,表面積100
〜500cm2/gのシリカゲルを芳香族系有機溶媒中
で温度80〜150℃において反応時間15〜48時間ア
ミノ基を有するシランカツプリング剤と反応させ
てアミノプロピル化シリカゲルを得るものであ
る。
In the present invention, an ordinary aminopropylation reaction can be used to obtain the aminopropylated silica gel. That is, it is porous and spherical, with an average particle diameter of 1 to 50 μ, an average pore diameter of 10 to 500 Å, and a surface area of 100
An aminopropylated silica gel is obtained by reacting ~500 cm 2 /g of silica gel with a silane coupling agent having an amino group in an aromatic organic solvent at a temperature of 80 to 150°C for a reaction time of 15 to 48 hours.

芳香族系有機溶媒としては、ベンゼン,トルエ
ン,キシレン,メチルベンゼン,シクロヘキサン
などを挙げることができるが、特にトルエンが好
ましい。
Examples of the aromatic organic solvent include benzene, toluene, xylene, methylbenzene, and cyclohexane, with toluene being particularly preferred.

アミノ基を有するシランカツプリング剤として
は、3−アミノ−プロピルトリエトキシシラン,
N−(2−アミノエチル)−3−アミノプロピルメ
チルジメトキシシラン,N−(2−アミノエチル)
−γ−アミノプロピルトリメトキシシランなどを
挙げることができるが、特に3−アミノ−プロピ
ルトリエトキシシランが好ましい。
Examples of the silane coupling agent having an amino group include 3-amino-propyltriethoxysilane,
N-(2-aminoethyl)-3-aminopropylmethyldimethoxysilane, N-(2-aminoethyl)
Examples include -γ-aminopropyltrimethoxysilane, and 3-amino-propyltriethoxysilane is particularly preferred.

次に、保護基を有する光学活性アミノ酸と活性
化N−アシルを導入できる試薬と反応させ、そこ
へ上記のアミノプロピル化シリカゲルを加えて光
学活性アミノ酸を固定化するものである。
Next, the optically active amino acid having a protecting group is reacted with a reagent capable of introducing activated N-acyl, and the above aminopropylated silica gel is added thereto to immobilize the optically active amino acid.

保護基を有する光学活性アミノ酸としては、光
学活性アミノ酸の失活を防ぐために、ブチルオキ
シカルボニル(以下、Boc.という)基,トシル
基,ベンジル基,カルボベンダキシ基を有するヒ
スチジン,フエニルアラニン,トリプトフアン等
が挙げることができるが、特にBoc.ヒスチジ
ン・トシレートが好ましい。
Optically active amino acids having a protecting group include histidine, phenylalanine, phenylalanine, and butyloxycarbonyl (hereinafter referred to as Boc.) group, tosyl group, benzyl group, and carbobendoxy group, in order to prevent deactivation of the optically active amino acid. Examples include tryptophan, but Boc. histidine tosylate is particularly preferred.

活性化N−アシルを導入できる試薬としては、
1,1′−カルボニルジイミダゾール,N−アセチ
ルイミダゾール,無水コハク酸を挙げることがで
きるが、特に、1,1′−カルボニルジイミダゾー
ルが好ましい。
Reagents that can introduce activated N-acyl include:
Examples include 1,1'-carbonyldiimidazole, N-acetylimidazole, and succinic anhydride, with 1,1'-carbonyldiimidazole being particularly preferred.

保護基を有する光学活性アミノ酸と活性化N−
アシルを導入できる試薬の反応は、0℃以下、有
機溶媒の存在下、保護基を有する光学活性アミノ
酸と活性化N−アシルを導入できる試薬を混合す
る任意の態様をとることができるが、特に、有機
溶媒に保護基を有する光学活性アミノ酸を溶解
し、撹拌しながら活性化N−アシルを導入できる
試薬を加え、反応容器を氷冷し、二酸化炭素の発
生が止むまで撹拌し続けることにより均一反応溶
液を得ることが好ましい。
Optically active amino acids with protecting groups and activated N-
The reaction with a reagent capable of introducing an acyl can take any form in which an optically active amino acid having a protecting group and a reagent capable of introducing an activated N-acyl are mixed at 0°C or lower in the presence of an organic solvent, but in particular, , by dissolving an optically active amino acid with a protecting group in an organic solvent, adding a reagent capable of introducing activated N-acyl with stirring, cooling the reaction vessel with ice, and continuing to stir until carbon dioxide generation stops, resulting in a uniform solution. Preferably, a reaction solution is obtained.

この反応に用いる活性化N−アシルを導入でき
る試薬の量は、アミノプロピル化シリカゲルに対
してモル比で1〜4倍、好ましくは2〜3倍の量
が望ましい。モル比が1倍未満では、固定化され
るアミノ酸量が少なくなり、4倍を越えると固定
化されるアミノ酸量は変らなく経済的でなく好ま
しくない。
The amount of the reagent capable of introducing activated N-acyl used in this reaction is preferably 1 to 4 times, preferably 2 to 3 times, in molar ratio to the aminopropylated silica gel. If the molar ratio is less than 1 time, the amount of amino acids immobilized will decrease, and if the molar ratio exceeds 4 times, the amount of amino acids immobilized will remain the same, which is unfavorable and uneconomical.

上記操作により得られた均一反応溶液に、上記
のアミノプロピル化シリカゲルを加え、10〜40
℃、好ましくは20〜25℃で、15時間以上、好まし
くは20〜30時間撹拌することにより、シリカゲル
細孔表面に、保護基を有するアミノ酸を固定化す
るものである。
Add the above aminopropylated silica gel to the homogeneous reaction solution obtained by the above operation, and
C, preferably 20 to 25 C, for 15 hours or more, preferably 20 to 30 hours, to immobilize the amino acid having a protecting group on the surface of the silica gel pores.

温度が10℃未満では固定化が急激に進み、シリ
カゲルの細孔表面を覆う恐れがあるため好ましく
ない。また、撹拌時間が15時間未満では十分な固
定化ができないため好ましくない。保護基を有す
るアミノ酸の固定化量は、ケルダール窒素分析お
よび重量変化によつて決定することができる。
If the temperature is lower than 10°C, immobilization will proceed rapidly and the pore surfaces of the silica gel may be covered, which is not preferable. Further, if the stirring time is less than 15 hours, sufficient immobilization cannot be achieved, which is not preferable. The amount of immobilized amino acid having a protecting group can be determined by Kjeldahl nitrogen analysis and weight change.

最後に保護基の除去、例えばBoc.基の除去は、
トリフルオロ酢酸処理によつて行なう。すなわ
ち、蒸留,乾燥したジクロロメタン中のトリフル
オロ酢酸30wt%溶液中に、Boc.アミノ酸を固定
化したシリカゲルを加え、室温にて1時間反応さ
せ、Boc.アミノ酸のBoc.基を除去するものであ
る。各保護基の除去は、その反応前後の赤外線吸
収スペクトルの吸収帯変化により簡単に確認する
ことができる。
Finally, removal of the protecting group, e.g. removal of the Boc.
This is carried out by treatment with trifluoroacetic acid. That is, silica gel immobilized with Boc. amino acids is added to a 30 wt% solution of trifluoroacetic acid in dichloromethane that has been distilled and dried, and the Boc. group of the Boc. amino acids is removed by reacting at room temperature for 1 hour. . Removal of each protecting group can be easily confirmed by the change in absorption band of the infrared absorption spectrum before and after the reaction.

以上の方法により得られた本発明の充てん剤
は、従来の光学活性アミノ酸のシリカゲルへの固
定化により得られた充てん剤と比較して多重のア
ミノ酸をシリカゲルへの固定化が可能であるた
め、各種アミノ酸光学異性体を良好に分離するこ
とができる。
The filler of the present invention obtained by the above method can immobilize multiple amino acids on silica gel compared to conventional fillers obtained by immobilizing optically active amino acids on silica gel. Various amino acid optical isomers can be separated well.

以下、本発明を実施例により説明する。 Hereinafter, the present invention will be explained by examples.

実施例 1〜6 粒径10μ,孔径100Å,表面積350m2/gのシリ
カゲル5gを無水トルエン70ml中、90℃,24時
間、3−アミノ−プロピルトリエトキシシラン5
gと反応させてアミノプロピル化シリカゲルを合
成した。
Examples 1 to 6 5 g of silica gel with a particle size of 10 μ, a pore size of 100 Å, and a surface area of 350 m 2 /g was mixed with 3-amino-propyltriethoxysilane 5 in 70 ml of anhydrous toluene at 90° C. for 24 hours.
Aminopropylated silica gel was synthesized by reacting with g.

次に乾燥したジメチルホルムアミド(以下、
DMFという)70mlにBoc.ヒスチジン・トシレー
ト10gを溶かし、撹拌しながら1,1′−カルボニ
ルジイミダゾール(以下、CDIという)3.2gを
加える。反応容器を氷冷し、二酸化炭素の発生が
止むまで撹拌を続ける。その後、先に合成したア
ミノプロピル化シリカゲルを反応物に加え、室温
で24時間撹拌した。その時のCDIの添加量は、ア
ミノプロピル化シリカゲルにアミノ基の量の2倍
のモル数である。ここでアミノプロピル化シリカ
ゲルのアミノ酸プロピル化度は、2m mole/
gであつた。
Next, dry dimethylformamide (hereinafter referred to as
Dissolve 10 g of Boc. histidine tosylate in 70 ml of DMF, and add 3.2 g of 1,1'-carbonyldiimidazole (hereinafter referred to as CDI) while stirring. Cool the reaction vessel with ice and continue stirring until the evolution of carbon dioxide stops. Thereafter, the previously synthesized aminopropylated silica gel was added to the reaction mixture, and the mixture was stirred at room temperature for 24 hours. The amount of CDI added at this time is twice the number of moles as the amount of amino groups in the aminopropylated silica gel. Here, the degree of amino acid propylation of the aminopropylated silica gel is 2 mmole/
It was hot at g.

このように合成したゲルをDMF,メタノール,
ジクロルメタンで順次完全に洗う。アミノシリカ
ゲルへのBoc.ヒスチジン・トシレートの固定化
量は、ケルダール窒素分析により、0.36m
mole/gと求められた。この値は、重量変化に
よつて求めた値と完全に一致した。
The gel synthesized in this way was mixed with DMF, methanol,
Wash thoroughly sequentially with dichloromethane. The amount of Boc. histidine tosylate immobilized on amino silica gel was determined to be 0.36 m by Kjeldahl nitrogen analysis.
It was calculated as mole/g. This value completely matched the value determined by weight change.

Boc.基の除去は、トリフルオロ酢酸処理*によ
つて行ない、トシレルト基の除去は、ヒドロキシ
ベンゾトリアゾール処理**にて行なつた。各保護
基の除去は、その前後の赤外線吸収スペクトルす
なわち、Boc.基1700cm-1,トシル基1420〜1330cm
-1の吸収帯の吸収変化により確認した。
The Boc. group was removed by trifluoroacetic acid treatment * , and the tosylerto group was removed by hydroxybenzotriazole treatment ** . The infrared absorption spectra before and after the removal of each protecting group are as follows: Boc. group at 1700 cm -1 , Tosyl group at 1420-1330 cm
This was confirmed by the absorption change in the -1 absorption band.

固定化したシリカゲルは、2mmφ,100mmのス
テンレスカラムにテトラブロムエタン,メタノー
ル,四塩化炭素からなる平衡スラリーとして充て
んした。充てん後にCu2+イオンの負荷を行なつ
た。
The immobilized silica gel was filled into a 2 mmφ, 100 mm stainless steel column as an equilibrium slurry consisting of tetrabromoethane, methanol, and carbon tetrachloride. After filling, Cu 2+ ions were loaded.

実施例1〜6として第1図〜6図に、下記の測
定条件でのトリプトフアン、フエニルアラニン,
チロシン,バリン,ドーパミン,マンデル酸のL
一体,D一体の分割されたクロマトグラムを示
す。
As Examples 1 to 6, tryptophan, phenylalanine,
Tyrosine, valine, dopamine, mandelic acid L
The divided chromatograms of D and D are shown.

装 置高速液体クロマトグラフ (東洋曹達工業株式会社製 商品名、
HLC803D) カラム ステンレス製2mmφ,100mm 溶離液 1/15Mリン酸緩衡液(PH4.6)+
10-4MCu2+ 流 速 1.0ml/min 検出器 紫外,210nm *トリフルオロ酢酸処理 蒸留,乾燥したジクロロメタン100mlにトリフ
ルオロ酢酸30%を入れ、室温で1時間反応させ
てBoc.アミノ酸のBoc.基をとる。
Equipment High performance liquid chromatograph (manufactured by Toyo Soda Kogyo Co., Ltd., product name,
HLC803D) Column Stainless steel 2mmφ, 100mm Eluent 1/15M phosphoric acid buffer (PH4.6) +
10 -4 MCu 2+ Flow rate 1.0ml/min Detector Ultraviolet, 210nm *Trifluoroacetic acid treatment Add 30% trifluoroacetic acid to 100ml of distilled and dried dichloromethane and react at room temperature for 1 hour to obtain Boc. Take the base.

**ヒドロキシベンゾトリアゾール処理 THF100ml中でヒドロキシベンゾトリアゾール
0.5gを少過剰加え、室温で2時間反応させる。
2時間後、イソブチレンの発生が終了し、反応
は終了する。
**Hydroxybenzotriazole treatment Hydroxybenzotriazole in 100ml THF
Add a slight excess of 0.5 g and react at room temperature for 2 hours.
After 2 hours, the generation of isobutylene has ceased and the reaction is complete.

比較例 ピリジン175ml中、17.5mlの3−トリエトキシ
シリルプロピルアミンに7.5gのL−プロリンを
加える。混合物を室温で15時間撹拌し、5時間無
水の状態で還流した。そして、15時間、0℃の状
態に保つ。未反応のL−プロリンをフイルターで
除き、溶液を70℃,17mmHg下蒸発させる。乾燥
したベンゼンを加えて、まだ溶液中に残つている
L−プロリンを再結晶化させることにより除く。
続いて60℃にて溶液を真空乾燥することによつて
15gのN−〔3−(トリエトキシシリル−プロピ
ル)〕−L−プロリンアミドが得られた。
Comparative Example 7.5 g of L-proline is added to 17.5 ml of 3-triethoxysilylpropylamine in 175 ml of pyridine. The mixture was stirred at room temperature for 15 hours and refluxed for 5 hours under dry conditions. Then, keep it at 0°C for 15 hours. Unreacted L-proline was removed with a filter, and the solution was evaporated at 70°C under 17 mmHg. Dry benzene is added to remove any L-proline still in solution by recrystallization.
By subsequently vacuum drying the solution at 60°C
15 g of N-[3-(triethoxysilyl-propyl)]-L-prolinamide were obtained.

乾燥したトルエン70ml中に5gのシリカゲルを
加え、再蒸留によつて吸着水を除く。再蒸留温度
が109℃に達した時、15mlのトルエンに2.5mgのN
−〔3−(トリエトキシシリル−プロピル)〕−L−
プロリンアミドの溶解した溶液を加える。混合溶
液を無水の状態で8時間還流した。こうして得ら
れた化学結合シリカゲルをトルエン,エタノー
ル,水,エタノール,トルエンの順に、そして最
後にジエチルエーテルで洗浄する。化学結合シリ
カゲルを真空中、60℃で8時間乾燥する。
Add 5 g of silica gel to 70 ml of dry toluene and remove the adsorbed water by redistillation. When redistillation temperature reached 109℃, 2.5mg N in 15ml toluene
-[3-(triethoxysilyl-propyl)]-L-
Add the dissolved solution of prolinamide. The mixed solution was refluxed under anhydrous conditions for 8 hours. The chemically bonded silica gel thus obtained is washed with toluene, ethanol, water, ethanol, toluene in this order, and finally with diethyl ether. The chemically bonded silica gel is dried in vacuum at 60°C for 8 hours.

こうして得られたL−プロリンの結合した固定
相を四塩化炭素を溶媒としたスラリーで、25cm,
4.8mm IDのステンレスカラムに通常の方法でエ
タノールを用いてパツキングする。パツキング
後、0.02M硫酸銅溶液をカラムに流す。
The L-proline-bonded stationary phase obtained in this way was mixed with a slurry using carbon tetrachloride as a solvent, and
Pack a 4.8mm ID stainless steel column using ethanol in the usual way. After packing, 0.02M copper sulfate solution is applied to the column.

L−プロリン1mole当り0.7moleのCu()イ
オンが固定されて平衡に達した。
Equilibrium was reached with 0.7 mole of Cu() ions fixed per 1 mole of L-proline.

こうして得られたカラムをHPLC装置に接続
し、下記の測定条件でトリプトフアン,フエニル
アラニンおよびチロシンのそれぞれのD−体,L
−体のクロマトグラムを第7図〜9図に示す。
The column thus obtained was connected to an HPLC device, and the D-form, L-form and L-form of tryptophan, phenylalanine and tyrosine were measured under the following measurement conditions.
The chromatograms of the -body are shown in Figures 7-9.

装 置高速液体クロマトグラフ (スペクトラ・フイジツクス社製商品名、
SP8000) カラム ステンレス製4.8mmID,250mm 溶離液 H2O−CH3CN(47:53)−0.15M
NH4Cl 流 速 1.0ml/min 検出器 紫外,210nm
Equipment High performance liquid chromatograph (trade name manufactured by Spectra Physics, Inc.,
SP8000) Column Stainless steel 4.8mm ID, 250mm Eluent H 2 O−CH 3 CN (47:53) −0.15M
NH 4 Cl flow rate 1.0ml/min Detector Ultraviolet, 210nm

【図面の簡単な説明】[Brief explanation of the drawing]

第1図〜第6図は、本発明の充てん剤を用いて
得られたトリプトフアン,フエニルアラニン,チ
ロシン,バリン,ドーパミンおよびマンデル酸の
L−体,D−体が分割されたクロマトグラムであ
る。第7図〜第9図は、従来のシリカゲルに光学
活性アミノ酸を固定化した充てん剤を用いて得ら
れたトリプトフアン,フエニルアラニンおよびチ
ロシンのL−体,D−体が分割されたクロマトグ
ラムである。 1 各種アミノ酸およびマンデル酸のL−体 2 各種アミノ酸およびマンデル酸のD−体
Figures 1 to 6 are chromatograms in which the L-form and D-form of tryptophan, phenylalanine, tyrosine, valine, dopamine, and mandelic acid obtained using the packing material of the present invention are separated. . Figures 7 to 9 are chromatograms in which the L-form and D-form of tryptophan, phenylalanine, and tyrosine were separated using a conventional packing material in which optically active amino acids were immobilized on silica gel. be. 1 L-form of various amino acids and mandelic acid 2 D-form of various amino acids and mandelic acid

Claims (1)

【特許請求の範囲】[Claims] 1 シリカゲル細孔表面にヒスチジンを固定化し
たことにより得られたことを特徴とする光学異性
体分離用充てん剤。
1. A packing material for separating optical isomers, which is obtained by immobilizing histidine on the surface of silica gel pores.
JP58048000A 1983-03-24 1983-03-24 Packing material for separating optical isomer Granted JPS59173756A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58048000A JPS59173756A (en) 1983-03-24 1983-03-24 Packing material for separating optical isomer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58048000A JPS59173756A (en) 1983-03-24 1983-03-24 Packing material for separating optical isomer

Publications (2)

Publication Number Publication Date
JPS59173756A JPS59173756A (en) 1984-10-01
JPH0339047B2 true JPH0339047B2 (en) 1991-06-12

Family

ID=12791041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58048000A Granted JPS59173756A (en) 1983-03-24 1983-03-24 Packing material for separating optical isomer

Country Status (1)

Country Link
JP (1) JPS59173756A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6110771A (en) * 1984-05-22 1986-01-18 Daicel Chem Ind Ltd Separation agent
JPS6177760A (en) * 1984-09-26 1986-04-21 Daicel Chem Ind Ltd Separating agent
JPH0627093B2 (en) * 1984-10-05 1994-04-13 ダイセル化学工業株式会社 Separation method
CH663728A5 (en) * 1985-06-10 1988-01-15 Battelle Memorial Institute PROCESS FOR THE PURIFICATION OF BIOACTIVE SUBSTANCES BY BIOSPECIFIC ADSORPTION.

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
ANGEWANDTE CHEMIE INTERNATIONAL EDITION IN ENGLISH=1982 *

Also Published As

Publication number Publication date
JPS59173756A (en) 1984-10-01

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