JPH0430376B2 - - Google Patents

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Publication number
JPH0430376B2
JPH0430376B2 JP58217611A JP21761183A JPH0430376B2 JP H0430376 B2 JPH0430376 B2 JP H0430376B2 JP 58217611 A JP58217611 A JP 58217611A JP 21761183 A JP21761183 A JP 21761183A JP H0430376 B2 JPH0430376 B2 JP H0430376B2
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Prior art keywords
cellulose
phenyl carbamate
solvent
carbamate
separation
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Expired - Lifetime
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JPS60108751A (en
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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
    • B01J20/281Sorbents 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
    • B01J20/28Solid 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
    • 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
    • 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
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • B01J20/321Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
    • 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
    • B01J20/3268Macromolecular compounds
    • B01J20/3272Polymers obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
    • B01J20/3274Proteins, nucleic acids, polysaccharides, antibodies or antigens
    • 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)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (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】[Detailed description of the invention]

本発明はセルロース誘導体であるセルロースフ
エニルカルバメートを物質の分離剤として使用す
ることに関するものである。分離する物質として
は通常の低分子化合物以外に特に従来直接分離す
ることが非常に困難であつた光学異性体を主な分
離の対象とするものである。 一般にラセミ体と光学活性体は異なつた生理活
性を示すことが多く、例えば、医薬、農薬等の分
野では薬害の防止や単位使用量当りの薬効の向上
のために光学異性体の分離を必要とする場合があ
る。従来光学異性体の分離には優先晶出法やジア
ステレオマー法が行われているが、これらの方法
では分離可能な光学異性体の種類が限られてお
り、また長時間を要する場合が多い。従つてクロ
マト法による簡便な分割法の開発が強く望まれて
いる。 クロマト法による光学異性体の分離の研究は以
前より行なわれている。例えば、セルロースまた
は1部のセルロース誘導体はカラムクロマトグラ
フイー用分離剤として光学分割に用いられてい
る。セルロース誘導体としては結晶系型に属す
る微結晶三酢酸セルロース、カルボキシメチルセ
ルロース等である。しかしながら、これらのセル
ロースまたは1部のセルロース誘導体は分離対象
物の範囲が狭く、分離能力も十分ではない。 本発明者らは鋭意研究の結果、驚くべきことに
セルロースフエニルカルバメートに優れた化合物
分離能と異性体分離能、特に光学異性体分離能が
あることを見いだした。 セルロースフエニルカルバメートが優れた光学
異性体分離能を示す明確な理由は明らかではない
が、セルロースの持つ規則的な不斉性とカルバメ
ート基の水素結合形成能とフエニル基の芳香族性
と剛直性が光学異性体の分離に大きな影響を与え
ているものと考えられる。 本発明のセルロースフエニルカルバメートは数
平均重合度5〜5000であり、好ましくは10〜1000
であり、さらに好ましくは10〜500である。セル
ロースフエニルカルバメートの平均置換度は、下
式で定義する。 平均置換度=1分子当りのフエニルカルバメート基の数
数平均重合度 本発明のセルロースフエニルカルバメートの平
均置換度は1〜3.4、好ましくは1.8〜3.2である。
セルロースフエニルカルバメートの未反応の水酸
基は、本発明のセルロースフエニルカルバメート
の異性体分離能を損なわない範囲でさらにエステ
ル化、カルバメート化、エーテル化を行うことが
できる。 本発明のセルロースフエニルカルバメートの合
成法は通常のイソシアナートとアルコールからウ
レタンを生ずる反応方法が、そのまま適用でき
る。 例えば三級アミン塩基類のルイス塩基、または
スズ化合物等のルイス酸触媒存在下にフエニルイ
ソシアナートとセルロースを反応させることによ
つて得られる。 クロマト用分離剤は粒状であることが好ましい
ことから、セルロースフエニルカルバメートを化
合物の分離剤として用いるには、セルロースフエ
ニルカルバメートを破砕するかビーズ状にするこ
とが好ましい。粒子の大きさは使用するカラムや
プレートの大きさによつて異なるが、1μm〜10
mmであり、好ましくは1μm〜300μmで、粒子は
多孔質であることが好ましい。 さらに分離剤の耐圧能力の向上、溶媒置換によ
る膨潤、収縮の防止、理論段数の向上のために、
セルロースフエニルカルバメートは担体に保持さ
せることが好ましい。適当な担体の大きさは使用
するカラムやプレートの大きさにより変るが、一
般に1μm〜10mmであり、好ましくは1μm〜300μ
mである。担体は多孔質であることが好ましく、
平均孔径は10〓〜100μmであり、好ましくは、
50〓〜50000〓である。セルロースフエニルカル
バメートを保持させる量は担体に対して1〜100
重量%、好ましくは5〜50重量%である。 セルロースフエニルカルバメートを担体に保持
させる方法は化学的方法でも物理的方法でも良
い。物理的方法としては、セルロースフエニルカ
ルバメートを可溶性の溶剤に溶解させ、担体と良
く混合し、減圧又は加温下、気流により溶剤を留
去させる方法や、セルロースフエニルカルバメー
トを可溶性の溶剤に溶解させ、担体と良く混合し
た後該溶剤と相溶性の無い液体中に撹拌、分散せ
しめ、該溶剤を拡散させる方法もある。このよう
にして担体に保持したセルロースフエニルカルバ
メートを結晶化する場合には熱処理などの処理を
行うことができる。また、少量の溶剤を加えてセ
ルロースフエニルカルバメートを一旦膨潤あるい
は溶解せしめ、再び溶剤を留去することにより、
その保持状態、ひいては分離能を変化せしめるこ
とが可能である。 担体としては多孔質有機担体又は多孔質無機担
体があり、好ましくは多孔質無機担体である。多
孔質有機担体として適当なものは、ポリスチレ
ン、ポリアクリルアミド、ポリアクリレート等か
ら成る高分子物質があげられる。多孔質無機担体
として適当なものはシリカ、アルミナ、マグネシ
ア、酸化チタン、ガラス、ケイ酸塩、カオリンの
如き合成若しくは天然の物質があげられ、セルロ
ースフエニルカルバメートとの親和性を良くする
ために表面処理を行つても良い。表面処理の方法
としては有機シラン化合物を用いたシラン化処理
やプラズマ重合による表面処理法等がある。 本発明のセルロースフエニルカルバメートを主
たる構成要素とする分離剤を化合物分離の目的に
使用するには、クロマト法が好適である。クロマ
ト法に使用する際の展開溶媒としては、セルロー
スフエニルカルバメートを溶かす溶媒は使用でき
ないが、セルロースフエニルカルバメートを化学
的方法で担体に結合させた場合や、セルロースフ
エニルカルバメートを架橋した場合には特に制約
はない。 本発明のセルロースフエニルカルバメートを主
たる構成要素とする分離剤は、化合物の分離に有
効で、特に従来分離が非常に困難であつた光学異
性体の分割に有効である。分離の対象となる光学
異性体は不斉中心を持つ化合物や分子不斉な化合
物で、セルロースフエニルカルバメートによつ
て、光学異性体のどちらか一方がより強く保持さ
れるものである。 以下本発明を実施例によつて詳述するが、本発
明はこれらの実施例に限定されるものではない。
尚、実施例中に表わされる用語の定義は以下の通
りである。 容量比(K′)=〔(対掌体の保持時間)−(デツドタ
イム)〕/(デツドタイム) 分離係数(α)=より強く吸着される対掌体の容量比/
より弱く吸着される対掌体の容量比 分離度(Rs)=2×(より強く吸着される対掌体とより
弱く吸着される対掌体の両ピーク間の距離)/両ピーク
のバンド幅の合計 合成例 1 セルロース(メルク社、カラムクロマト用)1
gを乾燥ピリジン50mgに分散させ、これにフエニ
ルイソシアナート8mlを加え撹拌下110℃に保つ
た。16時間後反応物を1のメタノールに注ぎ、
生じた白色の固形物を別し、室温で2時間、60
℃で3時間減圧乾燥した。収量は1.45gであつ
た。 生成物はクロロホルム、塩化メチレン、ジオキ
サン等にほぼ完全に溶解した。赤外およびNMR
スペクトルによりセルロースイトリスフエニルカ
ルバメートであることを確認のうえ、GPCで求
めた重合度は200であつた。 元素分析 測定値 C,60.93%;H,4.68%;N,7.93% 理論値 C,62.42%;H,4.85%;N,8.09% 〔(C27H25N3O8oとして〕 合成例 2 シリカゲル(Lichrospher SI4000、メルク社)
102gを180℃で2時間乾燥後、乾燥ベンゼン600
ml、ピリジン6mlおよび3−アミノプロピルトリ
エトキシシラン20mlの混合物中に分散させ、加熱
還流下で16時間反応させた。反応終了後反応混合
物を2のメタノール中に注ぎ、修飾シリカゲル
を別した。 合成例−1で得たセルローストリスフエニルカ
ルバメート0.76gをジオキサン10mlとエタノール
5mlの混合溶媒に溶解させた。微量の不溶物を除
いたのち、溶液5mlに修飾シリカゲル3.0gを混
合し、減圧下で溶媒を留去した。この担持操作を
さらに2度繰り返し、セルローストリスフエニル
カルバメート担持シリカゲルを調製した。 実施例 1 合成例2で調製した担持シリカゲルを長さ25cm
内径0.46cmのステンレスカラムにスラリー法で充
填した。高速液体クロマトグラフは日本分光工業
(株)製のTRIROTAR−を、検出器には
UVIDEC−およびDIP−181旋光計を用いた。
溶媒には(1)ヘキサン−2−プロパノール(混合重
量比90/10)、(2)ヘキサン−2−プロパノール
(80:20)、(3)ヘキサン−2−プロパノール−ジエ
チルアミン(80:20:0.001)、(4)エタノール−水
(50:50)、(5)エタノール−水(70:30)を用い、
流速はいずれも0.5ml/min、カラム温度は25℃
とした。 種々のラセミ体の分割結果を表1に、種々のア
キラルな化合物の分離結果を表2に示した。 分子量測定 分子量は標準ポリスチレンに対する較正曲線を
用いてGPC法により求めた。GPCカラムは
Shodex A80Mを、溶媒にはテトラヒドロフラン
を使用した。
The present invention relates to the use of cellulose phenyl carbamate, a cellulose derivative, as a material separation agent. The substances to be separated are not only ordinary low-molecular compounds, but also optical isomers, which have traditionally been very difficult to separate directly. In general, racemic forms and optically active forms often exhibit different physiological activities, and for example, in the fields of medicine and agrochemicals, it is necessary to separate optical isomers in order to prevent drug damage and improve drug efficacy per unit amount used. There are cases where Traditionally, the preferential crystallization method and diastereomer method have been used to separate optical isomers, but these methods limit the types of optical isomers that can be separated and often require a long time. . Therefore, there is a strong desire to develop a simple separation method using chromatography. Research on the separation of optical isomers by chromatography has been conducted for some time. For example, cellulose or some cellulose derivatives are used in optical resolution as separation agents for column chromatography. Examples of cellulose derivatives include microcrystalline cellulose triacetate and carboxymethyl cellulose, which belong to crystalline types. However, these celluloses or some cellulose derivatives have a narrow range of targets for separation and do not have sufficient separation ability. As a result of extensive research, the present inventors surprisingly discovered that cellulose phenyl carbamate has excellent compound separation ability and isomer separation ability, particularly optical isomer separation ability. The exact reason why cellulose phenyl carbamate exhibits excellent optical isomer separation is not clear, but it is due to the regular asymmetry of cellulose, the ability of the carbamate group to form hydrogen bonds, and the aromaticity and rigidity of the phenyl group. It is thought that this has a great influence on the separation of optical isomers. The cellulose phenyl carbamate of the present invention has a number average degree of polymerization of 5 to 5,000, preferably 10 to 1,000.
and more preferably 10 to 500. The average degree of substitution of cellulose phenyl carbamate is defined by the following formula. Average degree of substitution = number average degree of polymerization of phenyl carbamate groups per molecule The average degree of substitution of the cellulose phenyl carbamate of the present invention is 1 to 3.4, preferably 1.8 to 3.2.
The unreacted hydroxyl group of the cellulose phenyl carbamate can be further esterified, carbamate-formed, or etherified within a range that does not impair the isomer separation ability of the cellulose phenyl carbamate of the present invention. For the synthesis of cellulose phenyl carbamate of the present invention, a conventional reaction method for producing urethane from isocyanate and alcohol can be applied as is. For example, it can be obtained by reacting phenyl isocyanate and cellulose in the presence of a Lewis base such as a tertiary amine base or a Lewis acid catalyst such as a tin compound. Since the separating agent for chromatography is preferably in the form of particles, in order to use cellulose phenyl carbamate as a separating agent for compounds, it is preferable to crush the cellulose phenyl carbamate or form it into beads. The size of the particles varies depending on the size of the column and plate used, but is between 1 μm and 10 μm.
mm, preferably 1 μm to 300 μm, and the particles are preferably porous. Furthermore, in order to improve the pressure resistance of the separation agent, prevent swelling and shrinkage due to solvent substitution, and increase the number of theoretical plates,
Preferably, cellulose phenyl carbamate is retained on a carrier. The appropriate size of the carrier varies depending on the size of the column or plate used, but is generally 1 μm to 10 mm, preferably 1 μm to 300 μm.
It is m. Preferably, the carrier is porous;
The average pore size is 10〓~100μm, preferably,
50〓~50000〓. The amount of cellulose phenyl carbamate retained is 1 to 100% of the carrier.
% by weight, preferably from 5 to 50% by weight. A method for retaining cellulose phenyl carbamate on a carrier may be a chemical method or a physical method. Physical methods include dissolving cellulose phenyl carbamate in a soluble solvent, mixing well with the carrier, and distilling off the solvent with an air stream under reduced pressure or heating, and dissolving cellulose phenyl carbamate in a soluble solvent. There is also a method in which the solvent is thoroughly mixed with a carrier and then stirred and dispersed in a liquid that is incompatible with the solvent. When the cellulose phenyl carbamate held on the carrier in this manner is crystallized, a treatment such as heat treatment can be performed. In addition, by adding a small amount of solvent to once swell or dissolve cellulose phenyl carbamate, and then distilling off the solvent again,
It is possible to change the retention state and thus the separation power. The carrier may be a porous organic carrier or a porous inorganic carrier, preferably a porous inorganic carrier. Suitable porous organic carriers include polymeric substances such as polystyrene, polyacrylamide, polyacrylate, and the like. Suitable porous inorganic carriers include synthetic or natural materials such as silica, alumina, magnesia, titanium oxide, glass, silicates, and kaolin; You may also process it. Examples of surface treatment methods include silanization using an organic silane compound and surface treatment using plasma polymerization. In order to use the separation agent containing cellulose phenyl carbamate as a main component of the present invention for the purpose of separating compounds, chromatography is suitable. A solvent that dissolves cellulose phenyl carbamate cannot be used as a developing solvent when used in chromatography, but when cellulose phenyl carbamate is bonded to a carrier by a chemical method or when cellulose phenyl carbamate is crosslinked, There are no particular restrictions. The separating agent containing cellulose phenyl carbamate as a main component of the present invention is effective in separating compounds, and is particularly effective in resolving optical isomers, which have conventionally been very difficult to separate. The optical isomers to be separated are compounds with an asymmetric center or molecularly asymmetric compounds, and one of the optical isomers is more strongly retained by cellulose phenyl carbamate. EXAMPLES The present invention will be described in detail below with reference to Examples, but the present invention is not limited to these Examples.
The definitions of terms used in the examples are as follows. Capacity ratio (K') = [(Retention time of enantiomer) - (Dead time)] / (Dead time) Separation coefficient (α) = Capacity ratio of enantiomer that is more strongly adsorbed /
Volumetric resolution of the more weakly adsorbed enantiomer (Rs) = 2 x (distance between both peaks of the more strongly adsorbed enantiomer and weaker adsorbed enantiomer)/bandwidth of both peaks Total synthesis example 1 Cellulose (Merck Co., Ltd., for column chromatography) 1
g was dispersed in 50 mg of dry pyridine, 8 ml of phenyl isocyanate was added thereto, and the temperature was maintained at 110°C with stirring. After 16 hours, the reaction mixture was poured into 1 methanol.
Separate the white solid that forms and store at room temperature for 2 hours at 60°C.
It was dried under reduced pressure at ℃ for 3 hours. The yield was 1.45g. The product was almost completely dissolved in chloroform, methylene chloride, dioxane, etc. Infrared and NMR
The spectrum confirmed that it was cellulose itris phenyl carbamate, and the degree of polymerization determined by GPC was 200. Elemental analysis Measured value C, 60.93%; H, 4.68%; N, 7.93% Theoretical value C, 62.42%; H, 4.85%; N, 8.09% [as (C 27 H 25 N 3 O 8 ) o ] Synthesis example 2 Silica gel (Lichrospher SI4000, Merck & Co.)
After drying 102g at 180℃ for 2 hours, dry benzene 600g
ml, 6 ml of pyridine and 20 ml of 3-aminopropyltriethoxysilane, and reacted under heating under reflux for 16 hours. After the reaction was completed, the reaction mixture was poured into 2 methanol, and the modified silica gel was separated. 0.76 g of cellulose trisphenyl carbamate obtained in Synthesis Example 1 was dissolved in a mixed solvent of 10 ml of dioxane and 5 ml of ethanol. After removing a trace amount of insoluble matter, 3.0 g of modified silica gel was mixed with 5 ml of the solution, and the solvent was distilled off under reduced pressure. This loading operation was repeated twice to prepare cellulose trisphenyl carbamate-supported silica gel. Example 1 The supported silica gel prepared in Synthesis Example 2 was 25 cm long.
A stainless steel column with an inner diameter of 0.46 cm was packed using the slurry method. The high-performance liquid chromatograph is TRIROTAR- manufactured by JASCO Corporation, and the detector is
UVIDEC- and DIP-181 polarimeters were used.
The solvents include (1) hexane-2-propanol (mixing weight ratio 90/10), (2) hexane-2-propanol (80:20), (3) hexane-2-propanol-diethylamine (80:20:0.001). ), (4) ethanol-water (50:50), (5) ethanol-water (70:30),
Flow rate is 0.5ml/min in both cases, column temperature is 25℃
And so. Table 1 shows the resolution results of various racemates, and Table 2 shows the separation results of various achiral compounds. Molecular weight measurement Molecular weight was determined by GPC method using a calibration curve for standard polystyrene. GPC column is
Shodex A80M was used, and tetrahydrofuran was used as the solvent.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 合成例 3 数平均重合度110、アセチル化度2.49のセルロ
ーストリアセテート100gを、1の酢酸に溶解
し、5.2mlの水と5mlの濃硫酸を加え、80℃、3
時間反応させた。反応液を冷却し、過剰のマグネ
シウム水溶液で硫酸を中和した。該溶液を3の
水中に入れて、低分子量化したセルローストリア
セテートを沈殿させた。グラスフイルター(G3)
によつて別、更に1の水に分散後別し、真
空乾燥した。生成物を塩化メチレンに溶解させ、
2−プロパノールに再沈殿する操作を2回繰り返
して精製した後乾燥した。生成物は、IRスペク
トル及びNMRスペクトルよりセルローストリア
セテートであり、蒸気圧浸透圧法より求めた数平
均分子量は7900で、数平均重合度に換算すると27
であつた。蒸気圧浸透圧法は、ペーパープレツシ
ヤーオスモメーターCORONA117を用いて溶媒
にクロロホルム−1%エタノールの混合溶媒を使
用して測定した。 得られた低分子量セルローストリアセテート
10.0gを100mlのピリジンに溶解し、更に8.0mlの
100%水和ヒドラジンを加えた。室温で1時間放
置した後、90〜100℃に加熱した。生成した沈殿
物をグラスフイルターで別後ピリジンで洗浄し
た。得られた生成物は、IRスペクトルよりセル
ロースであることを確認した。 得られた低分子量セルロース5gと若干のピリ
ジンに乾燥ピリジンを100ml加えて分散させ、水
を除くためにベンゼン100mlを加えて、精留管を
通して留去した。残つた低分子量セルロースのピ
リジン懸濁液を60〜70℃に加熱し、撹拌しながら
16.3mlのフエニルイソシアナートを滴下し、100
〜105℃で3時間35分保つた。ピリジン、フエニ
ルイソシアナートを減圧下で留去し、反応物を塩
化メチレン中に入れて溶解させた。副生した塩化
メチレン不溶物をグラスフイルター(G3)にて
別した後、可溶部を2−プロパノールで分別し
た。2−プロパノール不溶の生成物は、5.67g得
られ淡褐色固体であつた。IRスペクトル、NMR
スペクトルより、セルローストリスフエニルカバ
メートであることを確認した。 IRスペクトル:3500cm-1νNH,3300cm-1νNH,1700
cm-1νC=0,1530cm-1νNH, NMRスペクトル:18H Broad singlet centered
at δ 7 7H multiplets δ6.0〜3.0 合成例 4 シリカゲル(Lichrospher SI1000、メルク社
製)を乾燥窒素気流中で2〜10時間120〜150℃に
加熱し、乾燥した。乾燥したシリカゲル20gを無
水ベンゼン100mlに懸濁し、そこに3−アミノプ
ロピルトリメトキシシラン6gを加え、乾燥窒素
気流下加熱還流した。このとき生成するメタノー
ルは系外に除くようにして5〜10時間反応させ
た。反応終了後室温に冷却し、グラスフイルター
で過した。得られた修飾シリカゲルは無水ベン
ゼンで洗つた後、真空中40℃で乾燥した。 アミノプロピルシラン処理したシリカゲル6g
を80℃で1時間減圧乾燥後、50mlの乾燥塩化メチ
レン中に分散させ、さらにトリエチルアミン2
ml、フエニルイソシアナート1mlを加えてよく混
合し、1日放置した。その後1時間40℃に加温し
た。溶媒をデカンテーシヨンし、塩化メチレン、
エタノール、アセトンで洗浄後乾燥した。 合成例1で得られた、セルローストリスフエニ
ルカルバメート0.9gを塩化メチレン4.5mlに溶解
させ、修飾したシリカゲル3.5gと混合し、減圧
下で溶媒を留去した。 実施例 2 合成例4で得られた、セルローストリスフエニ
ルカルバメートを担持したシリカビーズを、長さ
25cm内径0.46cmのステンレスカラムにスラリー法
で充填した。高速液体クロマトグラフは日本分光
工業(株)製のTRIROTARSRを用い、検出器
はUVIDEC−を用いた。流速は0.2ml/minで
溶媒にはヘキサン−2−プロパノール(9:1)
を使用した。種々のラセミ体を分割した結果を表
3に示した。
[Table] Synthesis Example 3 100 g of cellulose triacetate with a number average degree of polymerization of 110 and a degree of acetylation of 2.49 was dissolved in 1 part of acetic acid, 5.2 ml of water and 5 ml of concentrated sulfuric acid were added, and the mixture was heated at 80°C for 30 minutes.
Allowed time to react. The reaction solution was cooled, and the sulfuric acid was neutralized with an excess magnesium aqueous solution. The solution was placed in water in Step 3 to precipitate cellulose triacetate having a lower molecular weight. Glass filter (G3)
After dispersion in water, the mixture was separated and dried under vacuum. Dissolve the product in methylene chloride,
The procedure of reprecipitation in 2-propanol was repeated twice for purification and then drying. The product is cellulose triacetate according to the IR spectrum and NMR spectrum, and the number average molecular weight determined by vapor pressure osmotic pressure method is 7900, which is 27 when converted to number average degree of polymerization.
It was hot. The vapor pressure osmotic pressure method was measured using a paper pressure osmometer CORONA117 using a mixed solvent of chloroform and 1% ethanol as the solvent. Obtained low molecular weight cellulose triacetate
Dissolve 10.0g in 100ml of pyridine, then add 8.0ml of
100% hydrated hydrazine was added. After being left at room temperature for 1 hour, it was heated to 90-100°C. The generated precipitate was separated using a glass filter and then washed with pyridine. The obtained product was confirmed to be cellulose by IR spectrum. 100 ml of dry pyridine was added to 5 g of the obtained low molecular weight cellulose and some pyridine to disperse it, and 100 ml of benzene was added to remove water, which was then distilled off through a rectification tube. The remaining pyridine suspension of low molecular weight cellulose was heated to 60-70°C and stirred.
Drop 16.3 ml of phenyl isocyanate and add 100 ml of phenyl isocyanate.
It was kept at ~105°C for 3 hours and 35 minutes. Pyridine and phenyl isocyanate were distilled off under reduced pressure, and the reaction product was dissolved in methylene chloride. After the by-produced methylene chloride insoluble matter was separated using a glass filter (G3), the soluble portion was fractionated using 2-propanol. 5.67 g of the 2-propanol-insoluble product was obtained as a light brown solid. IR spectrum, NMR
From the spectrum, it was confirmed that it was cellulose trisphenyl carbamate. IR spectrum: 3500cm -1 ν NH , 3300cm -1 ν NH , 1700
cm -1 ν C=0 , 1530cm -1 ν NH , NMR spectrum: 18H Broad singlet centered
at δ 7 7H multiplets δ 6.0 to 3.0 Synthesis Example 4 Silica gel (Lichrospher SI1000, manufactured by Merck & Co.) was heated to 120 to 150° C. for 2 to 10 hours in a stream of dry nitrogen and dried. 20 g of dried silica gel was suspended in 100 ml of anhydrous benzene, 6 g of 3-aminopropyltrimethoxysilane was added thereto, and the mixture was heated to reflux under a stream of dry nitrogen. The reaction was continued for 5 to 10 hours while the methanol produced at this time was removed from the system. After the reaction was completed, the mixture was cooled to room temperature and filtered through a glass filter. The obtained modified silica gel was washed with anhydrous benzene and then dried in vacuo at 40°C. 6g of aminopropylsilane-treated silica gel
After drying under reduced pressure at 80℃ for 1 hour, it was dispersed in 50 ml of dry methylene chloride, and then triethylamine 2
ml and phenyl isocyanate (1 ml) were added, mixed well, and left to stand for one day. Thereafter, the mixture was heated to 40°C for 1 hour. Decant the solvent, methylene chloride,
After washing with ethanol and acetone, it was dried. 0.9 g of cellulose trisphenyl carbamate obtained in Synthesis Example 1 was dissolved in 4.5 ml of methylene chloride, mixed with 3.5 g of modified silica gel, and the solvent was distilled off under reduced pressure. Example 2 The silica beads supporting cellulose trisphenyl carbamate obtained in Synthesis Example 4 were
A 25 cm stainless steel column with an inner diameter of 0.46 cm was packed using the slurry method. The high-performance liquid chromatograph used was TRIROTARSR manufactured by JASCO Corporation, and the detector used was UVIDEC-. The flow rate was 0.2 ml/min, and the solvent was hexane-2-propanol (9:1).
It was used. Table 3 shows the results of resolution of various racemates.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 セルロースフエニルカルバメートを主たる構
成要素とする分離剤。
1. A separation agent whose main component is cellulose phenyl carbamate.
JP58217611A 1983-11-18 1983-11-18 Separating agent Granted JPS60108751A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58217611A JPS60108751A (en) 1983-11-18 1983-11-18 Separating agent

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Application Number Priority Date Filing Date Title
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Publications (2)

Publication Number Publication Date
JPS60108751A JPS60108751A (en) 1985-06-14
JPH0430376B2 true JPH0430376B2 (en) 1992-05-21

Family

ID=16707000

Family Applications (1)

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Country Link
JP (1) JPS60108751A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2579621B2 (en) * 1986-09-01 1997-02-05 ダイセル化学工業 株式会社 Optical resolution method of lignans
JP3190206B2 (en) 1993-06-22 2001-07-23 ダイセル化学工業株式会社 Separating agent for optical isomers and method for producing the same
JPH07260762A (en) * 1994-03-17 1995-10-13 Daicel Chem Ind Ltd Filler for high-speed liquid chromatography and manufacture thereof
JP3746315B2 (en) 1994-07-07 2006-02-15 ダイセル化学工業株式会社 Separating agent
EP0957358B1 (en) * 1995-12-21 2008-01-23 Daicel Chemical Industries, Ltd. Packing material for high-speed liquid chromatography
CN1211322C (en) 2001-04-27 2005-07-20 大赛璐化学工业株式会社 Separating agent composed of polysaccharide derivatives with polycyclic structure
KR100938207B1 (en) 2001-07-06 2010-01-22 다이셀 가가꾸 고교 가부시끼가이샤 Novel separation agent for optical isomer separation and preparation method thereof
WO2011158935A1 (en) * 2010-06-18 2011-12-22 ダイセル化学工業株式会社 Resolving agent for optical isomers
US9562121B2 (en) 2013-02-12 2017-02-07 National University Corporation Kanazawa University Optically active poly(diphenylacetylene) compound, preparation method therefor, and use thereof as optical isomer separating agent

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