JPH06287149A - Separation of distributed benzene isomer and agent for separation process - Google Patents

Separation of distributed benzene isomer and agent for separation process

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Publication number
JPH06287149A
JPH06287149A JP3517891A JP3517891A JPH06287149A JP H06287149 A JPH06287149 A JP H06287149A JP 3517891 A JP3517891 A JP 3517891A JP 3517891 A JP3517891 A JP 3517891A JP H06287149 A JPH06287149 A JP H06287149A
Authority
JP
Japan
Prior art keywords
group
substituted
cyclodextrin
benzene
separation
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
JP3517891A
Other languages
Japanese (ja)
Other versions
JPH0774170B2 (en
Inventor
Isamu Uemasu
勇 上桝
Hideki Takahashi
英樹 高橋
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.)
Ensuiko Sugar Refining Co Ltd
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Ensuiko Sugar Refining Co Ltd
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 Agency of Industrial Science and Technology, Ensuiko Sugar Refining Co Ltd filed Critical Agency of Industrial Science and Technology
Priority to JP3035178A priority Critical patent/JPH0774170B2/en
Priority to US07/703,885 priority patent/US5177302A/en
Priority to EP91109239A priority patent/EP0487818B1/en
Priority to DE69127744T priority patent/DE69127744T2/en
Priority to HU912733A priority patent/HU212635B/en
Publication of JPH06287149A publication Critical patent/JPH06287149A/en
Publication of JPH0774170B2 publication Critical patent/JPH0774170B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To separate a mixture of disubstituted benzene derivatives into constituent components with simple liquid-liquid extraction in high selectivity by using a substituted cyclodextrin as a clathrate-separation agent. CONSTITUTION:A disubstituted benzene derivative mixture is made to contact with a substituted cyclodextrin produced by substituting the hydrogen atom of at least one hydroxyl group of a cyclodextrin with at least one group selected from glucosyl, maltosyl, maltooligosaccharide residue, methyl, hydroxyethyl, hydroxypropyl, sulfonic acid group, alkylenesulfonic acid group and carboxyalkyl (preferably under stirring or shaking at 20-25 deg.C) to form disubstituted benzene derivative clathrate complex of the substituted cyclodextrin according to the clathrate complex forming constant of each isomer and the disubstituted benzene derivative is separated from the clathrate complex. Since the substituted cyclodextrin molecule is not decomposed, it can be recovered and reused. The process is applicable for the separation of mixture containing any combination of three kinds of disubstituted benzene derivatives.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は化学合成原料や溶剤とし
て有用なベンゼン二置換異性体の効果的な分離法及び該
ベンゼン二置換異性体包接分離用薬剤に関する。詳しく
は置換型シクロデキストリンがベンゼン二置換異性体を
その大きさ及び形状に応じて選択的に包接する機能を利
用して、分離用薬剤として用い、これとベンゼン二置換
異性体混合物を接触させ、生成した包接錯体から選択的
に濃縮されたベンゼン二置換異性体を脱離させ回収する
方法並びに該ベンゼン二置換異性体の分離用薬剤に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an effective method for separating benzene di-substituted isomers, which is useful as a raw material for chemical synthesis and as a solvent, and a drug for inclusion and separation of the benzene di-substituted isomers. Specifically, the substituted cyclodextrin is used as a separating agent by utilizing the function of selectively encapsulating a benzene di-substituted isomer according to its size and shape, and contacting this with a benzene di-substituted isomer mixture, The present invention relates to a method for desorbing and collecting a benzene di-substituted isomer selectively concentrated from a generated inclusion complex, and a drug for separating the benzene di-substituted isomer.

【0002】[0002]

【従来の技術】ベンゼン二置換異性体の分離法として
は、沸点の差を利用する蒸留法あるいは融点の差を利用
する晶析法が一般的である。蒸留法においては、ベンゼ
ン二置換化合物の各異性体の沸点が比較的近接している
ため、精密蒸留を繰り返さざるを得ないが、これは時間
がかかるだけでなく、消費エネルギーも大きい。また、
晶析法については特に共晶点の組成がどの位置にあるか
が問題であり、晶析に供する原料の組成が共晶点からな
るべく離れていなければ有効な分離が行えない。
2. Description of the Related Art As a method for separating benzene di-substituted isomers, a distillation method utilizing a difference in boiling point or a crystallization method utilizing a difference in melting point is generally used. In the distillation method, since the boiling points of the isomers of the disubstituted benzene compound are relatively close to each other, precision distillation has to be repeated, but this not only takes time, but also consumes a large amount of energy. Also,
In the crystallization method, the position of the composition of the eutectic point is a problem, and effective separation cannot be performed unless the composition of the raw material used for crystallization is as far as possible from the eutectic point.

【0003】また、ベンゼン二置換異性体の分離はガス
クロマトグラフィーや高速液体クロマトグラフィーによ
っても行われるが、これらは分析が主目的であり、工業
的に多量に取り扱うのには適していない。本発明に関連
のある技術として、シクロデキストリンまたは化学修飾
したシクロデキストリンを分離用薬剤として用いるベン
ゼン化合物異性体の分離は既に特許が申請されている
(例えば特開昭52−42825号公報、「ベンゼン化
合物異性体分離法」)が、包接錯体は沈澱形であり、固液
分離操作が必要である。
Separation of benzene di-substituted isomers is also carried out by gas chromatography or high performance liquid chromatography, but these are mainly used for analysis and are not suitable for industrial handling in large quantities. As a technique related to the present invention, a patent has already been applied for the separation of benzene compound isomers using cyclodextrin or chemically modified cyclodextrin as a separating agent (for example, JP-A-52-42825, "Benzene"). In the compound isomer separation method "), the inclusion complex is in a precipitation form and solid-liquid separation operation is necessary.

【0004】しかし、シクロデキストリン包接錯体の固
体は極めて微細であり、固液分離操作に非常に手間がか
かるため、これが当該分離法実施上の最大の難点となっ
ている。
However, since the solid of the cyclodextrin inclusion complex is extremely fine and the solid-liquid separation operation is very troublesome, this is the greatest difficulty in carrying out the separation method.

【0005】[0005]

【発明が解決しようとする課題】本発明は、溶解度の改
良を意図して製造されている置換型シクロデキストリン
を利用し、ベンゼン二置換異性体を高選択的に分離する
新規で経済的な方法及び該ベンゼン二置換異性体の分離
用薬剤を提供することを目的とするものである。
DISCLOSURE OF THE INVENTION The present invention utilizes a substituted cyclodextrin produced for the purpose of improving solubility, and is a novel and economical method for separating benzene disubstituted isomers with high selectivity. And an agent for separating the benzene di-substituted isomer.

【0006】[0006]

【課題を解決するための手段】本発明によれば、ベンゼ
ン二置換異性体(o-、m-、p-体の3種)の混合物と、シ
クロデキストリンの少なくとも一つの水酸基の水素が、
グルコシル基,マルトシル基,マルトオリゴ糖残渣,メ
チル基,ヒドロキシエチル基,ヒドロキシプロピル基,
スルホン酸基,アルキレンスルホン酸基およびカルボキ
シアルキル基のうちの少なくとも一つで置換された置換
型シクロデキストリンとを接触させることにより、前記
置換型シクロデキストリンのベンゼン二置換異性体包接
錯体をそれぞれの包接錯体生成定数に従って形成させ、
次いで当該包接錯体からベンゼン二置換異性体を脱離す
ることを特徴とするベンゼン二置換異性体を分離する方
法及びシクロデキストリンの少なくとも一つの水酸基の
水素が、グルコシル基,マルトシル基,マルトオリゴ糖
残渣,メチル基,ヒドロキシエチル基,ヒドロキシプロ
ピル基,スルホン酸基,アルキレンスルホン酸基および
カルボキシアルキル基のうちの少なくとも一つで置換さ
れた置換型シクロデキストリンからなるベンゼン二置換
異性体包接分離用薬剤が提供される。
According to the present invention, a mixture of benzene di-substituted isomers (o-, m- and p-forms) and hydrogen of at least one hydroxyl group of cyclodextrin are
Glucosyl group, maltosyl group, maltooligosaccharide residue, methyl group, hydroxyethyl group, hydroxypropyl group,
A benzene di-substituted isomer inclusion complex of the substituted cyclodextrin is obtained by bringing the substituted cyclodextrin substituted with at least one of a sulfonic acid group, an alkylene sulfonic acid group and a carboxyalkyl group into contact with each other. Formed according to the inclusion complex formation constant,
Next, a method for separating a benzene di-substituted isomer from the inclusion complex, the method comprising separating the benzene di-substituted isomer, and hydrogen of at least one hydroxyl group of cyclodextrin is a glucosyl group, maltosyl group, maltooligosaccharide residue Agent for inclusion and separation of benzene di-substituted isomers, which comprises a substituted cyclodextrin substituted with at least one of the following: a methyl group, a hydroxyethyl group, a hydroxypropyl group, a sulfonic acid group, an alkylenesulfonic acid group and a carboxyalkyl group Will be provided.

【0007】以下に本発明を詳細に説明する。本発明で
はベンゼン二置換異性体の分離用薬剤としてシクロデキ
ストリンの少なくとも一つの水酸基の水素が、グルコシ
ル基,マルトシル基,マルトオリゴ糖残基,メチル基,
ヒドロキシエチル基,ヒドロキシプロピル基,スルホン
酸基,アルキレンスルホン酸基およびカルボキシアルキ
ル基のうちの少なくとも一つで置換された置換型シクロ
デキストリンを用いる。ここで、シクロデキストリンと
してはα−,β−およびγ−シクロデキストリンのいず
れであってもよい。
The present invention will be described in detail below. In the present invention, hydrogen of at least one hydroxyl group of cyclodextrin is used as a drug for separating benzene di-substituted isomers, and glucosyl group, maltosyl group, maltooligosaccharide residue, methyl group,
A substituted cyclodextrin substituted with at least one of a hydroxyethyl group, a hydroxypropyl group, a sulfonic acid group, an alkylenesulfonic acid group and a carboxyalkyl group is used. Here, the cyclodextrin may be any of α-, β- and γ-cyclodextrin.

【0008】これらの置換型シクロデキストリンはそれ
自体及びベンゼン二置換異性体の包接錯体の水への溶解
度が他のシクロデキストリンや置換体を用いる場合と比
べて大きいので、例えばスラリー状態にしなくても高濃
度水溶液として扱うことができる。また、包接錯体形成
時に沈澱することがなく固液分離の操作が不要なので、
全体のプロセスが簡単になるという著しい利点がある。
Since these substituted cyclodextrins have a higher solubility in water of the inclusion complex of the disubstituted benzene isomer itself and water than other cyclodextrins or substituted ones, it is not necessary to make them into a slurry state, for example. Can also be treated as a high-concentration aqueous solution. Further, since the inclusion complex does not precipitate during the formation of the inclusion complex and the solid-liquid separation operation is unnecessary,
There is a significant advantage that the whole process is simple.

【0009】本発明で使用する置換型シクロデキストリ
ン、特にグルコシル−シクロデキストリンやマルトシル
−シクロデキストリンによる包接化は、既に食品分野等
に応用されているが、本発明のようにベンゼン二置換異
性体の分離を目的としてこれらの置換型シクロデキスト
リンの包接錯体生成能を利用した例はない。
The inclusion cyclodextrin used in the present invention, especially the inclusion with glucosyl-cyclodextrin or maltosyl-cyclodextrin, has already been applied to the food field and the like. There is no example in which the inclusion complex-forming ability of these substituted cyclodextrins is used for the purpose of separating the.

【0010】本発明においては、これらの置換型シクロ
デキストリンを水に溶解させ、この液にベンゼン二置換
異性体の混合物、例えばキシレン,ジクロロベンゼン,
クロロトルエン,クロロニトロベンゼン,ニトロトルエ
ン,ジニトロベンゼン,ブロモトルエン,クロロベンゾ
トリフルオライド,アミノチオフェノール,ジビニルベ
ンゼン,ビニルトルエン,アミノベンゾトリフルオライ
ド,ビス(トリフルオロメチル)ベンゼン,クロロベン
ジルクロライド,フルオロベンジルクロライド,ブロモ
ニトロベンゼン,フルオロニトロベンゼン,フルオロト
ルエン,フルオロアニリン,フルオロベンゾニトリル等
の異性体混合物を加え、激しくかく拌または振とうす
る。ただし、キシレン異性体を置換型α−シクロデキス
トリンを用いて分離する方法については、既に本発明者
らが特許出願(特願平2−121212)しており、本
発明ではこれを除外する。置換型シクロデキストリンの
濃度は水に対し5〜100重量%であるが、好ましくは
10〜30重量%が適当である。なお、置換基を持たな
いシクロデキストリンやベンゼン二置換異性体包接錯体
の水に対する溶解度が5重量%未満であるような他の置
換型シクロデキストリンの場合は、この包接錯体を形成
させる過程で包接錯体の沈澱物を生成したり、著しく低
濃度での操作を余儀なくされ不都合であるが、本発明に
用いる特定の前記置換型シクロデキストリンでは、この
ような不都合を生じない。
In the present invention, these substituted cyclodextrins are dissolved in water and a mixture of benzene disubstituted isomers such as xylene, dichlorobenzene,
Chlorotoluene, chloronitrobenzene, nitrotoluene, dinitrobenzene, bromotoluene, chlorobenzotrifluoride, aminothiophenol, divinylbenzene, vinyltoluene, aminobenzotrifluoride, bis (trifluoromethyl) benzene, chlorobenzyl chloride, fluorobenzyl chloride, Add an isomer mixture of bromonitrobenzene, fluoronitrobenzene, fluorotoluene, fluoroaniline, fluorobenzonitrile, etc. and vigorously stir or shake. However, the present inventors have already filed a patent application for a method for separating xylene isomers using a substituted α-cyclodextrin (Japanese Patent Application No. 2-121212), and the present invention excludes this. The concentration of the substituted cyclodextrin is 5 to 100% by weight with respect to water, preferably 10 to 30% by weight. In addition, in the case of other substituted cyclodextrins such that the solubility of the cyclodextrin having no substituent or the benzene di-substituted isomer inclusion complex in water is less than 5% by weight, the inclusion complex is formed in the process. The inclusion complex precipitates are generated, and the operation at a remarkably low concentration is forced to be inconvenient, but the specific substituted cyclodextrin used in the present invention does not cause such inconvenience.

【0011】置換型シクロデキストリン溶液とベンゼン
二置換異性体混合物の混合割合は、ベンゼン二置換異性
体のモル数が置換型シクロデキストリンのそれの1〜1
0倍になるようにする。かく拌または振とうはできるだ
け激しく、数秒から数十分間行う。なお、温度は10〜
40℃、好ましくは20〜25℃とする。かく拌または
振とう終了後、適当な方法で油水分離を行う。例えば5
〜10分間遠心分離を行ったり、或は塩を加える等の液
液抽出において油層と水層との分離性の向上に用いられ
る公知の手段を用いることができる。
The mixing ratio of the substituted cyclodextrin solution and the benzene disubstituted isomer mixture is such that the number of moles of the benzene disubstituted isomer is 1 to 1 of that of the substituted cyclodextrin.
Make it 0 times. Stir or shake as vigorously as possible for a few seconds to tens of minutes. The temperature is 10
The temperature is 40 ° C., preferably 20 to 25 ° C. After completion of stirring or shaking, oil-water separation is performed by an appropriate method. Eg 5
A known means used for improving the separability between the oil layer and the aqueous layer in liquid-liquid extraction such as centrifugation for 10 minutes or addition of a salt can be used.

【0012】水層に溶解している包接錯体からベンゼン
二置換異性体を得るためには、シクロデキストリン包接
錯体は60〜70℃以上の水溶液中では解離するという
公知事実に基づき、水層を60℃以上に加熱することに
よって、包接されたベンゼン二置換異性体を解離させ、
水層から分離させるか、或は置換型シクロデキストリン
に包接され難く、水に溶解しにくい比較的低沸点の揮発
性有機溶媒、例えばエチルエーテル,n−ヘキサン等を
用い、常温或は60〜70℃の加温下で、ベンゼン二置
換異性体を有機層に抽出する。この際、水層は透明な置
換型シクロデキストリン水溶液となる。また、ベンゼン
二置換異性体を抽出した有機層から有機溶媒を揮発させ
ると、ベンゼン二置換異性体が得られる。
In order to obtain the benzene disubstituted isomer from the inclusion complex dissolved in the water layer, the cyclodextrin inclusion complex is dissociated in an aqueous solution at 60 to 70 ° C. or higher based on the known fact. Is heated to 60 ° C. or higher to dissociate the included benzene di-substituted isomer,
Use a volatile organic solvent having a relatively low boiling point, such as ethyl ether or n-hexane, which is hard to be separated from the aqueous layer or included in the substituted cyclodextrin and is hardly dissolved in water, at room temperature or 60- The benzene di-substituted isomer is extracted into the organic layer under heating at 70 ° C. At this time, the aqueous layer becomes a transparent substitution type cyclodextrin aqueous solution. Moreover, the benzene di-substituted isomer is obtained by evaporating the organic solvent from the organic layer from which the benzene di-substituted isomer is extracted.

【0013】1回の包接化ではベンゼン二置換異性体の
分離が不十分で、他の成分も混ざっている場合、包接分
離されたベンゼン二置換異性体混合物を原料として、繰
返し置換型シクロデキストリンによる包接化を行うこと
によって目的とするベンゼン二置換異性体の純度を高め
ることができる。
When separation of the benzene di-substituted isomer is insufficient in one inclusion, and other components are also mixed, the inclusion-separated benzene di-substituted isomer mixture is used as a starting material for repeated substitution-type cyclohexane. By performing inclusion with dextrin, the purity of the target disubstituted benzene isomer can be increased.

【0014】なお、以上の全過程において、本発明に用
いる置換型シクロデキストリン分子自体は分解すること
がないので、回収再利用が可能である。
It should be noted that the substituted cyclodextrin molecule used in the present invention itself is not decomposed in the above-mentioned whole process, so that it can be recovered and reused.

【0015】本発明において包接分離用薬剤として用い
る置換型シクロデキストリンは、3種類(o-、m-、p-
体)のベンゼン二置換異性体の組合せ全てを含む混合物
の分離に対して適用し得るものである。
In the present invention, three types of substituted cyclodextrins (o-, m-, p-) are used as agents for inclusion and separation.
It is applicable to separation of a mixture containing all combinations of benzene di-substituted isomers.

【0016】[0016]

【実施例】以下、実施例によって本発明をさらに具体的
に説明する。 実施例1 モノマルトシル−β−シクロデキストリン0.729g
を水5gに溶解し、o−、p−ジクロロベンゼンをそれ
ぞれ65%,35%含む混合物0.735gを加えた。
The present invention will be described in more detail with reference to the following examples. Example 1 0.729 g of monomaltosyl-β-cyclodextrin
Was dissolved in 5 g of water, and 0.735 g of a mixture containing 65% and 35% of o- and p-dichlorobenzene was added.

【0017】25℃で5分間かく拌した後、反応生成物
を3,000rpmで5分間遠心分離にかけてから水層
を取り出し、これとエチルエーテルとを振り混ぜ、エー
テル層からエーテルを揮発させて有機化合物を得た。
After stirring at 25 ° C. for 5 minutes, the reaction product was centrifuged at 3,000 rpm for 5 minutes, the aqueous layer was taken out, and this was shaken with ethyl ether, and ether was volatilized from the ether layer to form an organic layer. The compound was obtained.

【0018】本実施例における成分の組成変化を表1に
示した。これはキャピラリーガスクロマトグラフ法で分
析したもので、表中の数字は各成分の重量百分率を示
す。
Table 1 shows the composition changes of the components in this example. This was analyzed by capillary gas chromatography, and the numbers in the table indicate the weight percentage of each component.

【0019】 [0019]

【0020】実施例2 o−、p−ジクロロベンゼンの含有率をそれぞれ84
%,16%とした以外は実施例1と同様に行った。結果
を表2に示す。
Example 2 The contents of o- and p-dichlorobenzene were 84% respectively.
% And 16% were performed in the same manner as in Example 1. The results are shown in Table 2.

【0021】 [0021]

【0022】実施例3 o−、p−ジクロロベンゼンの含有率をそれぞれ93
%,7%とした以外は実施例1と同様に行った。結果を
表3に示す。
Example 3 The contents of o- and p-dichlorobenzene were 93% respectively.
% And 7%, but the same operation as in Example 1. The results are shown in Table 3.

【0023】 [0023]

【0024】実施例4 モノマルトシル−β−シクロデキストリンの代わりにメ
チル−β−シクロデキストリン0.656gを用いた以
外は実施例1と同様に行った。結果を表4に示す。
Example 4 Example 1 was repeated except that 0.656 g of methyl-β-cyclodextrin was used instead of monomaltosyl-β-cyclodextrin. The results are shown in Table 4.

【0025】 [0025]

【0026】実施例5 モノマルトシル−β−シクロデキストリンの代わりにヒ
ドロキシエチル−β−シクロデキストリン0.722g
を用いた以外は実施例1と同様に行った。結果を表5に
示す。
Example 5 0.722 g of hydroxyethyl-β-cyclodextrin instead of monomaltosyl-β-cyclodextrin
The same procedure as in Example 1 was performed except that was used. The results are shown in Table 5.

【0027】 [0027]

【0028】実施例6 ジクロロベンゼン異性体混合物を、o−、m−、p−体
それぞれ等量含むものとした以外は実施例1と同様に行
った。結果を表6に示す。
Example 6 Example 6 was carried out in the same manner as in Example 1 except that the dichlorobenzene isomer mixture was contained in the o-, m- and p-forms in equal amounts. The results are shown in Table 6.

【0029】 [0029]

【0030】実施例7 モノグルコシル−β−シクロデキストリン1.34gを
水10gに溶解し、市販の特級キシレン3gを加えた。
以下、実施例1と同様に行った。成分の組成変化を表7
に示す。
Example 7 1.34 g of monoglucosyl-β-cyclodextrin was dissolved in 10 g of water, and 3 g of commercial grade xylene was added.
Thereafter, the same procedure as in Example 1 was performed. Table 7 shows the composition changes of the ingredients
Shown in.

【0031】 [0031]

【0032】実施例8 市販の特級キシレンの代わりにエチルベンゼンとo−、
m−、p−キシレン異性体の等量混合物3gを用いた以
外は実施例7と同様に行った。結果を表8に示す。
Example 8 Instead of commercial grade xylene, ethylbenzene and o-,
The procedure of Example 7 was repeated except that 3 g of an equal mixture of m- and p-xylene isomers was used. The results are shown in Table 8.

【0033】 [0033]

【0034】実施例9 市販の特級キシレンの代わりにm−、p−キシレン異性
体の等量混合物3gを用いた以外は実施例7と同様に行
った。結果を表9に示す。
Example 9 Example 7 was repeated except that 3 g of an equal mixture of m- and p-xylene isomers was used in place of the commercially available special grade xylene. The results are shown in Table 9.

【0035】 [0035]

【0036】実施例10 モノマルトシル−β−シクロデキストリン0.729g
を水5gに溶解し、o−、m−、p−ニトロトルエンを
それぞれ63%,4%,33%含む混合物0.686g
を加えた。以下、実施例1と同様に行った。結果を表1
0に示す。
Example 10 0.729 g of monomaltosyl-β-cyclodextrin
Was dissolved in 5 g of water, and 0.686 g of a mixture containing 63%, 4%, and 33% of o-, m-, and p-nitrotoluene, respectively.
Was added. Thereafter, the same procedure as in Example 1 was performed. The results are shown in Table 1.
It shows in 0.

【0037】 [0037]

【0038】実施例11 モノマルトシル−β−シクロデキストリン0.729g
を水5gに溶解し、o−、m−、p−クロロベンゾトリ
フルオライド(CBTF)を等量ずつ含む混合物0.9
05gを加えた。以下、実施例1と同様に行った。結果
を表11に示す。
Example 11 0.729 g of monomaltosyl-β-cyclodextrin
Is dissolved in 5 g of water, and a mixture containing o-, m-, p-chlorobenzotrifluoride (CBTF) in equal amounts 0.9.
05g was added. Thereafter, the same procedure as in Example 1 was performed. The results are shown in Table 11.

【0039】 [0039]

【0040】実施例12 モノマルトシル−β−シクロデキストリン0.729g
を水5gに溶解し、o−、p−クロロベンゾトリフルオ
ライド(CBTF)を等量ずつ含む混合物0.906g
を加えた。以下、実施例1と同様に行った。結果を表1
2に示す。
Example 12 0.729 g of monomaltosyl-β-cyclodextrin
Is dissolved in 5 g of water, and 0.906 g of a mixture containing o- and p-chlorobenzotrifluoride (CBTF) in equal amounts.
Was added. Thereafter, the same procedure as in Example 1 was performed. The results are shown in Table 1.
2 shows.

【0041】 [0041]

【0042】実施例13 モノマルトシル−β−シクロデキストリン0.729g
を水5gに溶解し、o−、p−クロロトルエンを等量ず
つ含む混合物0.633gを加えた。以下、実施例1と
同様に行った。結果を表13に示す。
Example 13 0.729 g of monomaltosyl-β-cyclodextrin
Was dissolved in 5 g of water, and 0.633 g of a mixture containing equal amounts of o- and p-chlorotoluene was added. Thereafter, the same procedure as in Example 1 was performed. The results are shown in Table 13.

【0043】 [0043]

【0044】実施例14 モノグルコシル−α−シクロデキストリン0.584g
を水5gに溶解し、o−、m−、p−ニトロトルエン異
性体の等量混合物0.70gを加えた。以下、実施例1
と同様に行った。結果を表14に示す。
Example 14 0.584 g of monoglucosyl-α-cyclodextrin
Was dissolved in 5 g of water, and 0.70 g of an equal mixture of o-, m- and p-nitrotoluene isomers was added. Hereinafter, Example 1
I went the same way. The results are shown in Table 14.

【0045】 [0045]

【0046】実施例15 モノグルコシル−α−シクロデキストリン0.568g
を水5gに溶解し、o−、p−ジクロロベンゼンをそれ
ぞれ65%,35%含む混合物0.74gを加えた。以
下、実施例1と同様に行った。結果を表15に示す。
Example 15 0.568 g of monoglucosyl-α-cyclodextrin
Was dissolved in 5 g of water, and 0.74 g of a mixture containing 65% and 35% of o- and p-dichlorobenzene was added. Thereafter, the same procedure as in Example 1 was performed. The results are shown in Table 15.

【0047】 [0047]

【0048】[0048]

【発明の効果】本発明によれば、ベンゼン二置換異性体
混合物から各成分を液液抽出の簡便な操作で高選択的に
分離することができる。また、抽出に用いた置換型シク
ロデキストリンを再び抽出に用いることができるので、
低コストでベンゼン二置換異性体を分離することができ
る。
EFFECTS OF THE INVENTION According to the present invention, each component can be highly selectively separated from a benzene disubstituted isomer mixture by a simple operation of liquid-liquid extraction. In addition, since the substituted cyclodextrin used for extraction can be used again for extraction,
The benzene disubstituted isomer can be separated at low cost.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C07C 201/16 7188−4H 205/06 7188−4H (72)発明者 高橋 英樹 神奈川県横浜市鶴見区大黒町13番46号 塩 水港精糖株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical display location C07C 201/16 7188-4H 205/06 7188-4H (72) Inventor Hideki Takahashi Tsurumi, Yokohama-shi, Kanagawa 13-46, Daikokucho, Tokyo

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ベンゼン二置換異性体(o-、m-、p-体の
3種)の混合物と、シクロデキストリンの少なくとも一
つの水酸基の水素が、グルコシル基,マルトシル基,マ
ルトオリゴ糖残基,メチル基,ヒドロキシエチル基,ヒ
ドロキシプロピル基,スルホン酸基,アルキレンスルホ
ン酸基およびカルボキシアルキル基のうちの少なくとも
一つで置換された置換型シクロデキストリンとを接触さ
せることにより、置換型シクロデキストリンのベンゼン
二置換異性体包接錯体をそれぞれの包接錯体生成定数に
従って形成させ、次いで当該包接錯体からベンゼン二置
換異性体を脱離することを特徴とするベンゼン二置換異
性体を分離する方法。
1. A mixture of benzene di-substituted isomers (o-, m-, and p-forms) and hydrogen of at least one hydroxyl group of cyclodextrin is a glucosyl group, a maltosyl group, a maltooligosaccharide residue, Substituted cyclodextrin benzene by contacting with a substituted cyclodextrin substituted with at least one of a methyl group, a hydroxyethyl group, a hydroxypropyl group, a sulfonic acid group, an alkylenesulfonic acid group and a carboxyalkyl group. A method for separating a benzene disubstituted isomer, which comprises forming a disubstituted isomer inclusion complex according to each inclusion complex formation constant and then desorbing the benzene disubstituted isomer from the inclusion complex.
【請求項2】 シクロデキストリンの少なくとも一つの
水酸基の水素が、グルコシル基,マルトシル基,マルト
オリゴ糖残基,メチル基,ヒドロキシエチル基,ヒドロ
キシプロピル基,スルホン酸基,アルキレンスルホン酸
基およびカルボキシアルキル基のうちの少なくとも一つ
で置換された置換型シクロデキストリンからなるベンゼ
ン二置換異性体包接分離用薬剤。
2. The hydrogen of at least one hydroxyl group of cyclodextrin is a glucosyl group, maltosyl group, maltooligosaccharide residue, methyl group, hydroxyethyl group, hydroxypropyl group, sulfonic acid group, alkylene sulfonic acid group and carboxyalkyl group. An agent for inclusion and separation of benzene di-substituted isomers, which comprises a substituted cyclodextrin substituted with at least one of the above.
JP3035178A 1990-11-27 1991-02-05 Method for separating benzene di-substituted isomers and agent for separating the same Expired - Lifetime JPH0774170B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP3035178A JPH0774170B2 (en) 1991-01-18 1991-02-05 Method for separating benzene di-substituted isomers and agent for separating the same
US07/703,885 US5177302A (en) 1990-11-27 1991-05-22 Process for separating isomers of disubstituted benzenes and agents to be used therefor
EP91109239A EP0487818B1 (en) 1990-11-27 1991-06-06 Process for separating isomers of disubstituted benzenes
DE69127744T DE69127744T2 (en) 1990-11-27 1991-06-06 Isomer separation process for disubstituted benzenes
HU912733A HU212635B (en) 1990-11-27 1991-08-16 Process for separating disubstituted benzene isomers

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP1687291 1991-01-18
JP3-16872 1991-01-18
JP3035178A JPH0774170B2 (en) 1991-01-18 1991-02-05 Method for separating benzene di-substituted isomers and agent for separating the same

Publications (2)

Publication Number Publication Date
JPH06287149A true JPH06287149A (en) 1994-10-11
JPH0774170B2 JPH0774170B2 (en) 1995-08-09

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001316301A (en) * 2000-03-03 2001-11-13 Natl Inst Of Advanced Industrial Science & Technology Meti Continuous selective separating method using inclusion complexing agent and equipment for the same
WO2014003000A1 (en) * 2012-06-29 2014-01-03 三菱瓦斯化学株式会社 Method and apparatus for separating alkyl aromatic hydrocarbon

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03184925A (en) * 1989-09-19 1991-08-12 Agency Of Ind Science & Technol Method for separating and purifying xylene isomer and/ or ethylbenzene and chemical for separating clathrate used for the same method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03184925A (en) * 1989-09-19 1991-08-12 Agency Of Ind Science & Technol Method for separating and purifying xylene isomer and/ or ethylbenzene and chemical for separating clathrate used for the same method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001316301A (en) * 2000-03-03 2001-11-13 Natl Inst Of Advanced Industrial Science & Technology Meti Continuous selective separating method using inclusion complexing agent and equipment for the same
JP4493834B2 (en) * 2000-03-03 2010-06-30 独立行政法人産業技術総合研究所 Continuous selective inclusion and separation method and apparatus
WO2014003000A1 (en) * 2012-06-29 2014-01-03 三菱瓦斯化学株式会社 Method and apparatus for separating alkyl aromatic hydrocarbon
KR20150021956A (en) * 2012-06-29 2015-03-03 미쯔비시 가스 케미칼 컴파니, 인코포레이티드 Method and apparatus for separating alkyl aromatic hydrocarbon
JPWO2014003000A1 (en) * 2012-06-29 2016-06-02 三菱瓦斯化学株式会社 Method and apparatus for separating alkyl aromatic hydrocarbons
US9896397B2 (en) 2012-06-29 2018-02-20 Mitsubishi Gas Chemical Company, Inc. Method and apparatus for separating alkyl aromatic hydrocarbon
US10207967B2 (en) 2012-06-29 2019-02-19 Mitsubishi Gas Chemical Company, Inc. Method and apparatus for separating alkyl aromatic hydrocarbon

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