JP2005068067A - Method for purifying 5,5-dimethylpyrroline-n-oxide - Google Patents

Method for purifying 5,5-dimethylpyrroline-n-oxide Download PDF

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JP2005068067A
JP2005068067A JP2003299459A JP2003299459A JP2005068067A JP 2005068067 A JP2005068067 A JP 2005068067A JP 2003299459 A JP2003299459 A JP 2003299459A JP 2003299459 A JP2003299459 A JP 2003299459A JP 2005068067 A JP2005068067 A JP 2005068067A
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dmpo
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Osamu Ito
治 伊東
Masaaki Aoyama
正明 青山
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Yamagata Public Interest Foundation for Development of Industry
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a purification method for efficiently highly purifying 5,5-dimethylpyrroline-N-oxide (DMPO) usable as a spin trapping agent for an electron spin resonance technique (ESR) by carrying out a series of operations at a temperature not higher than room temperature to reduce the effects of heat. <P>SOLUTION: The method for purifying the DMPO comprises a step for dissolving a crude DMPO in an organic solvent at ≤35°C, and a step for recrystallizing the DMPO at ≤6°C from the obtained solution. The solvent is ethyl acetate, a mixed solvent of the ethyl acetate, or the like, and the amount of the used solvent is 1-3 times as much as that of the crude DMPO. As a result, a colorless columnar crystal is obtained. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本願発明は、不純物を含む粗5,5−ジメチルピロリン−N−オキサイド(以下、5,5−ジメチルピロリン−N−オキサイドをDMPOという)からDMPOを精製する方法に関する。   The present invention relates to a method for purifying DMPO from crude 5,5-dimethylpyrroline-N-oxide containing impurities (hereinafter, 5,5-dimethylpyrroline-N-oxide is referred to as DMPO).

生体内でさまざまな生理活性を示す物質として、フリーラジカルが知られている。フリーラジカルは、虚血性疾患、消化器疾患、癌、神経変性を伴う脳神経疾患、炎症、薬物による臓器障害など数多くの疾患と関係していることから、医学、薬学、生物学の分野で注目され、研究が進められている。   Free radicals are known as substances that exhibit various physiological activities in vivo. Free radicals are related to many diseases such as ischemic diseases, digestive diseases, cancer, cranial nerve diseases with neurodegeneration, inflammation, and organ damage caused by drugs. Research is ongoing.

このようなフリーラジカルの検出法として、分子内不対電子を直接検出する電子スピン共鳴法(ESR)がある。しかし、フリーラジカルは通常寿命が極めて短く、ESR法を用いても生理条件下で直接検出することは困難である。そのため、その短寿命フリーラジカルをラジカル補足剤(スピントラップ剤)を用いて化学的に補足し、安定なラジカル体(スピンアダクト)として検出するスピントラップ法が一般的に用いられている。このスピントラップ剤の一種としてDMPOが用いられており、ヒドロキシラジカル、スーパーオキシド等の分析に多く使われている。   As a method for detecting such free radicals, there is an electron spin resonance method (ESR) that directly detects unpaired electrons in the molecule. However, free radicals usually have a very short life and are difficult to detect directly under physiological conditions using the ESR method. For this reason, a spin trap method is generally used in which the short-lived free radical is chemically captured using a radical scavenger (spin trap agent) and detected as a stable radical (spin adduct). DMPO is used as a kind of spin trapping agent and is often used for analysis of hydroxy radicals, superoxides, and the like.

ところで、ESR法は高感度の分析法であるため、高純度のDMPOを使用しないと不純物由来のESRスペクトルを示し、目的とするフリーラジカルの計測に支障をきたしてしまう。そこで、高純度のDMPOを得るために、粗DMPOを減圧蒸留や精密蒸留によって精製することが行われている。   By the way, since the ESR method is a high-sensitivity analysis method, if high-purity DMPO is not used, an ESR spectrum derived from impurities is shown, which hinders measurement of the intended free radical. Therefore, in order to obtain high-purity DMPO, crude DMPO is purified by vacuum distillation or precision distillation.

DMPOの精製方法として、特許文献1には、粗DMPO水溶液を無極性有機溶媒を用いて洗浄してから有極性有機溶剤を用いて抽出し、蒸留精製することを特徴とする精製方法が開示されている(特許文献1)。また、特許文献2には、粗DMPOの精製において酸化過程を含むことを特徴とする精製方法が開示されている(特許文献2)。   As a DMPO purification method, Patent Document 1 discloses a purification method characterized in that a crude DMPO aqueous solution is washed with a nonpolar organic solvent, extracted with a polar organic solvent, and purified by distillation. (Patent Document 1). Patent Document 2 discloses a purification method characterized by including an oxidation process in the purification of crude DMPO (Patent Document 2).

特開平1−153675号公報Japanese Patent Laid-Open No. 1-153675 特開平1−305061号公報Japanese Patent Laid-Open No. 1-305061

しかし、これらの方法を用いても完全に不純物を取り除くことは困難である。また、高純度品が得られるとしても、得られるのは全体から比するとごく少量であったり、繰り返し蒸留を行うことが必要であったりと、精製効率的が悪い。さらに、DMPOは熱に対して安定な化合物ではないため、蒸留を行う場合、可能な限り高真空状態にして外部から加える温度を下げる必要がある。   However, it is difficult to completely remove impurities using these methods. Further, even if a high-purity product is obtained, the purification efficiency is poor because the amount obtained is very small compared to the whole or it is necessary to repeatedly perform distillation. Furthermore, since DMPO is not a heat-stable compound, when performing distillation, it is necessary to reduce the temperature applied from outside by setting the vacuum as high as possible.

さらに、DMPO水溶液に活性炭を添加することで不純物を吸着させた後に濾過して分析に用いる手法もあるが、正確な濃度が分からなくなるために定量分析に用いるには不向きである。   Furthermore, there is a method of adding activated carbon to a DMPO aqueous solution to adsorb impurities and then using it for analysis, but it is not suitable for use in quantitative analysis because the exact concentration is unknown.

一方、物質を精製する方法として、再結晶化する方法が知られている。再結晶化は、通常、加熱した溶液に精製したい物質を含む組成物を飽和状態になるまで溶解し、その後その飽和溶液を冷却することにより、結晶を析出させる方法である。しかしながら、DMPOは低融点有機化合物(融点:25℃)であり、通常室温では油状物であるため、再結晶化は困難と考えられていた。   On the other hand, a recrystallization method is known as a method for purifying a substance. Recrystallization is usually a method of precipitating crystals by dissolving a composition containing a substance to be purified in a heated solution until saturated, and then cooling the saturated solution. However, DMPO is a low-melting-point organic compound (melting point: 25 ° C.), and is usually an oily substance at room temperature. Therefore, recrystallization has been considered difficult.

上記課題を鑑みたうえで、本願発明は一連の操作を室温以下で行うことにより、熱による影響を少なくし、DMPOを効率よく高純度化する精製方法を提供することを目的とした。また、高純度のDMPOを含有する試薬を提供することによって、より精度の高いフリーラジカル計測等を可能にすることも目的とした。   In view of the above problems, an object of the present invention is to provide a purification method for efficiently purifying DMPO by reducing the influence of heat by performing a series of operations at room temperature or lower. Another object of the present invention is to provide a highly accurate free radical measurement by providing a reagent containing high-purity DMPO.

上記課題を解決するため、鋭意検討した結果、再結晶化の手法を特定の温度以下で行うことにより、上記課題を解決しうることを見出した。すなわち、DMPOを常温若しくは常温より冷却した溶媒に溶解させた後、特定の温度以下に冷却して再結晶化させることにより、効率よく高純度のDMPOが得られることを見いだした。   As a result of intensive studies to solve the above problems, it has been found that the above problems can be solved by performing the recrystallization method at a specific temperature or lower. That is, it has been found that DMPO is dissolved in a normal temperature or a solvent cooled from normal temperature, and then cooled to a specific temperature or lower and recrystallized to efficiently obtain high-purity DMPO.

具体的には、(1)粗5,5−ジメチルピロリン−N−オキサイドを35℃以下の温度で有機溶媒に溶解する工程と、得られた溶液からDMPOを6℃以下の温度で再結晶化する工程を含むことを特徴とする5,5−ジメチルピロリン−N−オキサイドの精製方法;および、(2)上記(1)において、前記溶液に固体状の5,5−ジメチルピロリン−N−オキサイドを添加する工程をさらに含むことを特徴とするDMPOの精製方法を採用した。   Specifically, (1) a step of dissolving crude 5,5-dimethylpyrroline-N-oxide in an organic solvent at a temperature of 35 ° C. or lower, and recrystallizing DMPO from the resulting solution at a temperature of 6 ° C. or lower. A process for purifying 5,5-dimethylpyrroline-N-oxide; and (2) in the above (1), a solid 5,5-dimethylpyrroline-N-oxide in the solution A DMPO purification method characterized by further comprising the step of adding

本願発明の精製方法を採用することにより、簡便な手順で高純度のDMPOを取得することが可能となった。特に、本願発明の精製方法は、繰り返し行うことで更なるDMPOの高純度化を可能にするだけではなく、残った粗DMPOを容易に効率良く回収できる利点を併せ持っている。さらに、DMPOの高純度化はより精度の高いフリーラジカル計測等への助けとなり、高純度品の製造効率が上がることにより製造コストを下げることも可能になる。   By employing the purification method of the present invention, it has become possible to obtain highly pure DMPO by a simple procedure. In particular, the purification method of the present invention not only makes it possible to further purify DMPO by repeating the process, but also has the advantage of easily and efficiently recovering the remaining crude DMPO. Furthermore, the high purity of DMPO helps to more accurate measurement of free radicals and the like, and the manufacturing cost can be reduced by increasing the manufacturing efficiency of high purity products.

発明の実施の形態BEST MODE FOR CARRYING OUT THE INVENTION

本願発明で言う粗DMPOとは、DMPOがそのほとんどを占める組成物をいう。例えば、公知の合成方法(例えば、E.G,Janzen, L.T.Jandrisits, R.V.Shetty, D.L.Haire, J.W.Hilborn, Synthesis and purification of 5,5-Dimethyl-1-pyrroline-N-oxide for biological applications, Chem. Biol., Interactions, 70, 167-172 (1989) に記載される方法)により得られたDMPOをクロマトグラフィー等によってさらに精製したもの等を挙げることができる。また、この場合の溶媒等は除去しておく方が好ましい。さらに、再結晶前に簡単な減圧蒸留を行い着色成分を取り除くことでより再結晶に適した粗DMPOが得られる。   The crude DMPO referred to in the present invention refers to a composition in which DMPO accounts for most. For example, a known synthesis method (for example, EG, Janzen, LTJandrisits, RVShetty, DLHaire, JWHilborn, Synthesis and purification of 5,5-Dimethyl-1-pyrroline-N-oxide for biological applications, Chem. Biol. , Interactions, 70, 167-172 (1989)), and DMPO obtained by further purification by chromatography or the like. In this case, it is preferable to remove the solvent and the like. Furthermore, crude DMPO more suitable for recrystallization can be obtained by performing simple vacuum distillation before recrystallization to remove the colored components.

本願発明で採用する有機溶媒としては、DMPOを溶解し再結晶化させるものを広く採用することができる。また、本願発明では、低い温度で再結晶化を試みるので、以下の要件を満たすことが好ましい。(1)溶媒の凝固点が再結晶温度より低いこと、好ましくは−40℃以下、より好ましくは、−70℃以下の融点を有する有機溶媒が好ましい。(2)室温と冷却した状態のDMPOの溶解度の差が大きい溶媒であること。具体的には酢酸エチル、酢酸エチル・n−ヘキサン混合溶媒、ジエチルエーテル、アセトン、エタノール等を用いることができる。好ましくは、酢酸エチル、酢酸エチル・n−ヘキサン混合溶媒を用いることができる。使用する溶媒の量は制限されないが、粗DMPOの体積に対して、好ましくは1〜3倍量とする。   As the organic solvent used in the present invention, those which dissolve and recrystallize DMPO can be widely used. Moreover, in this invention, since recrystallization is tried at low temperature, it is preferable to satisfy the following requirements. (1) An organic solvent having a freezing point lower than the recrystallization temperature, preferably −40 ° C. or lower, more preferably −70 ° C. or lower is preferable. (2) A solvent having a large difference in solubility between DMPO in a cooled state and at room temperature. Specifically, ethyl acetate, ethyl acetate / n-hexane mixed solvent, diethyl ether, acetone, ethanol or the like can be used. Preferably, a mixed solvent of ethyl acetate and ethyl acetate / n-hexane can be used. The amount of the solvent used is not limited, but is preferably 1 to 3 times the volume of the crude DMPO.

有機溶媒への粗DMPOの溶解は、通常は室温で行う。例えば、0〜35℃の温度範囲内、好ましくは4〜25℃の温度範囲内で溶解を行う。溶解時には、攪拌や振とうを行ってもよい。また溶解時には、粗DMPOの溶解状況を観察しながら、必要最低限の溶媒を徐々に添加しながら粗DMPOを溶解させることが好ましい。粗DMPOを溶解させた後は、溶解温度以上に温度を上げることなく次の工程に進むことが好ましい。   Dissolution of the crude DMPO in the organic solvent is usually performed at room temperature. For example, dissolution is performed within a temperature range of 0 to 35 ° C, preferably within a temperature range of 4 to 25 ° C. At the time of dissolution, stirring and shaking may be performed. Further, at the time of dissolution, it is preferable to dissolve the crude DMPO while gradually adding the minimum necessary solvent while observing the dissolution state of the crude DMPO. After dissolving the crude DMPO, it is preferable to proceed to the next step without raising the temperature above the melting temperature.

粗DMPOの溶液を再結晶化する際の冷却温度は、DMPOが再結晶化する温度であれば、特に定めるものではない。この条件を満たす温度は、6℃以下、より好ましくは、0℃以下、最も好ましくは、−5℃以下である。このような手段を採用すると、DMPOが熱によって影響を受けるのをより効果的に防止しつつ、精製することが可能になる。   The cooling temperature for recrystallizing the crude DMPO solution is not particularly limited as long as the DMPO is recrystallized. The temperature that satisfies this condition is 6 ° C. or less, more preferably 0 ° C. or less, and most preferably −5 ° C. or less. By adopting such means, it becomes possible to purify while preventing the DMPO from being affected by heat more effectively.

冷却時には、必要に応じて、固体状のDMPOを添加してもよい。固体状のDMPOは、DMPOの再結晶化を促進するための核としての役割を果たすものである。従って、添加する固体状のDMPOは微粒子状であることが好ましい。DMPO微粒子は、上記粗DMPOを溶解する溶媒の冷却時又は冷却中に添加する。このDMPO微粒子は、その形状、大きさ等を含め、本願発明の目的を達成する限り広く公知のものを採用できる。従って、DMPO微粒子は特定の形状に限定されない。   During cooling, solid DMPO may be added as necessary. Solid DMPO plays a role as a nucleus for promoting recrystallization of DMPO. Therefore, the solid DMPO to be added is preferably in the form of fine particles. The DMPO fine particles are added during or during cooling of the solvent that dissolves the crude DMPO. As the DMPO fine particles, widely known ones can be adopted as long as the object of the present invention is achieved, including the shape and size thereof. Therefore, the DMPO fine particles are not limited to a specific shape.

DMPOは冷却することにより、柱状や針状等の結晶として得られる。得られた結晶は、グラスフィルターを用いた吸引濾過やデカンテーションにより取り出し、デシケーターにて吸引減圧すること等により有機溶媒を完全に除去する。上記作業はコールドルームのような低温条件下で行うことが望ましい。
有機溶媒への粗DMPOの溶解から結晶の取得までの一連の作業は、遮光下、不活性ガス雰囲気下で行うことが望ましい。また、一連の作業をすべてコールドルームのような低温条件下で行うことも望ましい。
DMPO is obtained in the form of a columnar or acicular crystal by cooling. The obtained crystal is taken out by suction filtration or decantation using a glass filter, and the organic solvent is completely removed by suction and pressure reduction with a desiccator. It is desirable to perform the above operation under a low temperature condition such as a cold room.
It is desirable to perform a series of operations from dissolution of crude DMPO in an organic solvent to acquisition of crystals in an inert gas atmosphere under light shielding. It is also desirable to perform a series of operations under low temperature conditions such as a cold room.

結晶化せずに有機溶媒中に残った残留物は、溶媒を減圧下留去することにより回収することができる。本願発明の精製方法ではDMPOの化学変化を極力抑えることができるため、このとき回収される残留物の中には再結晶化しなかったDMPOが含まれている。したがって、残留物に対して本願発明の精製方法や公知の精製方法を適用することによって、純度が高いDMPOをさらに回収することが可能である。このため、本願発明の精製方法によれば、合成によって得られた粗DMPOに含まれる高価なDMPOを分解させずに効率よく利用しうる。   The residue remaining in the organic solvent without crystallization can be recovered by distilling off the solvent under reduced pressure. Since the chemical change of DMPO can be suppressed as much as possible in the purification method of the present invention, DMPO that has not been recrystallized is contained in the residue recovered at this time. Therefore, DMPO with high purity can be further recovered by applying the purification method of the present invention or a known purification method to the residue. For this reason, according to the purification method of the present invention, expensive DMPO contained in crude DMPO obtained by synthesis can be efficiently used without being decomposed.

本願発明の精製方法によれば、純度が高いDMPOを効率よく取得することができる。また、本願発明の精製方法を実施するために必要とされる試薬や設備は、従来のDMPO精製法に比べて低コストで用意することができる。このため、本願発明の精製方法を利用すれば、高純度のDMPOを簡便かつ安価に取得することができる点で産業上の利用可能性が高い。   According to the purification method of the present invention, DMPO having high purity can be efficiently obtained. In addition, the reagents and equipment required for carrying out the purification method of the present invention can be prepared at a lower cost than the conventional DMPO purification method. For this reason, if the refining method of the present invention is used, industrial applicability is high in that high-purity DMPO can be obtained easily and inexpensively.

本願発明の精製方法により精製したDMPOは、様々な試薬として効果的に利用することができる。本願発明の精製方法により精製したDMPOを用いた試薬は、DMPOの正確な濃度を認識することが容易であるので、特に定量分析用試薬として好ましく用いられる。例えば、フリーラジカル計測用の試薬として用いれば、より精度の高い定量分析が可能になる。また本願発明の精製方法により精製したDMPOは、DMPOを出発物質とする合成反応にも効果的に用いることができる。   DMPO purified by the purification method of the present invention can be effectively used as various reagents. Since the reagent using DMPO purified by the purification method of the present invention can easily recognize the exact concentration of DMPO, it is particularly preferably used as a reagent for quantitative analysis. For example, if it is used as a reagent for measuring free radicals, quantitative analysis with higher accuracy becomes possible. DMPO purified by the purification method of the present invention can also be used effectively in a synthesis reaction using DMPO as a starting material.

以下に実施例を記載して本発明の特徴をさらに具体的に説明する。以下の実施例に示す材料、使用量、割合、処理内容、処理手順等は、本発明の趣旨を逸脱しない限り適宜変更することができる。したがって、本発明の範囲は以下に示す具体例により限定的に解釈されるべきものではない。   The features of the present invention will be described more specifically with reference to the following examples. The materials, amounts used, ratios, processing details, processing procedures, and the like shown in the following examples can be changed as appropriate without departing from the spirit of the present invention. Therefore, the scope of the present invention should not be construed as being limited by the specific examples shown below.

(実施例)
1.粗DMPOの合成
1) 4−メチル−4−ニトロペンタン−1−アールの合成
窒素雰囲気下、2−ニトロプロパン(211.5g)に7%ナトリウムメトキシドメタノール溶液(250mL)を攪拌しながら−10℃〜−15℃に保つように滴下した。次いでをアクロレイン(21.0g)と2−ニトロプロパン(49.1g)の混合溶液を攪拌しながら−10℃〜−15℃に保つように滴下した。滴下終了後、更に30分間攪拌し、反応溶液を室温に戻した。次いで濃塩酸を加えることにより反応溶液を酸性とした後、吸引濾過し、濾液をエバポレートした。残留物をエーテル抽出、無水硫酸マグネシウムで乾燥した。減圧下溶媒を留去した後、減圧蒸留(沸点90〜93℃/6mmHg)にて目的物を得た(38.4g,82%)。
(Example)
1. Synthesis of crude DMPO 1) Synthesis of 4-methyl-4-nitropentan-1-al -10 with stirring a 7% sodium methoxide methanol solution (250 mL) in 2-nitropropane (211.5 g) under nitrogen atmosphere C. to -15.degree. C. was added dropwise. Then, a mixed solution of acrolein (21.0 g) and 2-nitropropane (49.1 g) was added dropwise so as to keep the temperature at −10 ° C. to −15 ° C. with stirring. After completion of the dropwise addition, the mixture was further stirred for 30 minutes, and the reaction solution was returned to room temperature. Then, the reaction solution was acidified by adding concentrated hydrochloric acid, filtered with suction, and the filtrate was evaporated. The residue was extracted with ether and dried over anhydrous magnesium sulfate. After evaporating the solvent under reduced pressure, the desired product was obtained (38.4 g, 82%) by distillation under reduced pressure (boiling point 90-93 ° C./6 mmHg).

2) 2−(3−メチル−3−ニトロブチル)−1,3−ジオキソランの合成
4−メチル−4−ニトロペンタン−1−アール(32.7g)及びエチレングリコール(16.0g)を350mLの脱水ベンゼンに溶解し、更にp−トルエンスルホン酸(0.5g)を加え、水を除きながら7時間加熱還流した。放冷後、飽和炭酸水素ナトリウム水溶液及び水で反応溶液を洗浄した後、無水硫酸マグネシウムで乾燥した。減圧下溶媒を留去した後、減圧蒸留(沸点85〜90℃/4mmHg)にて目的物を得た(31.3g,74%)。
2) Synthesis of 2- (3-methyl-3-nitrobutyl) -1,3-dioxolane 350 mL of 4-methyl-4-nitropentane-1-al (32.7 g) and ethylene glycol (16.0 g) were dehydrated It melt | dissolved in benzene, p-toluenesulfonic acid (0.5g) was added, and it heated and refluxed for 7 hours, removing water. After allowing to cool, the reaction solution was washed with a saturated aqueous sodium hydrogen carbonate solution and water, and then dried over anhydrous magnesium sulfate. After the solvent was distilled off under reduced pressure, the desired product was obtained (31.3 g, 74%) by distillation under reduced pressure (boiling point 85-90 ° C./4 mmHg).

3) 5,5−ジメチルピロリン−N−オキサイド(DMPO)の合成
2−(3−メチル−3−ニトロブチル)−1,3−ジオキソラン(7.0g)の5%塩化アンモニウム水溶液(42mL)の混合溶液を窒素雰囲気下、遮光、攪拌し10℃〜15℃に保つように塩酸で表面を洗浄活性化した亜鉛粉末(9.8g)を加えた。更に30分間攪拌した後、吸引濾過、60℃の温水で洗浄した後、濾液を濃塩酸にて酸性とし、12時間放置した。次いで溶液を40分間70℃に加熱、放冷後に炭酸ナトリウムにてアルカリ性とし、減圧下溶媒を留去、クロロホルム抽出した。無水硫酸マグネシウムで乾燥した後、減圧下溶媒を留去した。シリカゲルカラムクロマトグラフィー(クロロホルム:メタノール=20:1)により精製し、減圧下溶媒を留去することにより目的物を得た(3.5g,84%)。
3) Synthesis of 5,5-dimethylpyrroline-N-oxide (DMPO) Mixing 5% aqueous ammonium chloride solution (42 mL) of 2- (3-methyl-3-nitrobutyl) -1,3-dioxolane (7.0 g) Zinc powder (9.8 g) whose surface was washed and activated with hydrochloric acid so as to keep the solution light-shielded and stirred under nitrogen atmosphere and kept at 10 ° C. to 15 ° C. was added. After further stirring for 30 minutes, suction filtration and washing with hot water at 60 ° C., the filtrate was acidified with concentrated hydrochloric acid and allowed to stand for 12 hours. The solution was then heated to 70 ° C. for 40 minutes, allowed to cool and then made alkaline with sodium carbonate, and the solvent was distilled off under reduced pressure and extracted with chloroform. After drying over anhydrous magnesium sulfate, the solvent was distilled off under reduced pressure. The product was purified by silica gel column chromatography (chloroform: methanol = 20: 1), and the solvent was distilled off under reduced pressure to obtain the desired product (3.5 g, 84%).

2.DMPOの再結晶
5gの上記粗DMPOを、25℃で2.5mLの酢酸エチルに溶解した。さらに、2.5mlのn−ヘキサンを加え、−12℃の冷凍庫内に静置した。この冷却されたDMPO溶液に、固体状のDMPOを微量加え、更に冷凍庫内に静置した。固体状のDMPOが核となることで結晶化が始まった。そして、結晶の成長が止まった段階で、デカンテーションにて結晶と溶液を分け、結晶はデシケーターにて吸引減圧することにより有機溶媒を完全に除去した。得られた結晶は無色柱状結晶(2.5g)であった。溶液側は溶媒を減圧下留去することにより粗DMPOの回収を行った。
2. Recrystallization of DMPO 5 g of the crude DMPO was dissolved in 2.5 mL of ethyl acetate at 25 ° C. Furthermore, 2.5 ml of n-hexane was added, and the mixture was allowed to stand in a -12 ° C freezer. A small amount of solid DMPO was added to the cooled DMPO solution, and the solution was allowed to stand in a freezer. Crystallization started when solid DMPO became a nucleus. Then, when the crystal growth stopped, the crystal and the solution were separated by decantation, and the organic solvent was completely removed by sucking and reducing the pressure of the crystal with a desiccator. The obtained crystals were colorless columnar crystals (2.5 g). On the solution side, the crude DMPO was recovered by distilling off the solvent under reduced pressure.

3.不純物由来ESR信号の測定:
上記1の再結晶前の粗DMPO及び上記2の再結晶により得られたDMPOをそれぞれ超純水にて20倍希釈した。この溶液をフラットセル(ラボテック製)に吸引し、ESRスペクトルを計測した(日本電子製、品番:JES−FR80)。その結果を図1に示す。それぞれのESRスペクトルに存在する両端の信号はESR計測において基準として用いているマンガンマーカー由来の信号である。ここで、(a)は上記1の粗DMPOのESRスペクトルを、(b)は上記2の再結晶により得られたDMPOのESRスペクトルを、それぞれ示している。ここで、(a)では多量の不純物由来のESR信号が存在しているが、(b)では不純物が無くなっているのが認められた。この結果から本願発明の方法を用いたDMPOの精製法が有効であることが確認された。
3. Measurement of impurity-derived ESR signal:
The crude DMPO before recrystallization 1 and DMPO obtained by recrystallization 2 were each diluted 20 times with ultrapure water. This solution was sucked into a flat cell (manufactured by Labotech) and an ESR spectrum was measured (manufactured by JEOL Ltd., product number: JES-FR80). The result is shown in FIG. The signals at both ends present in each ESR spectrum are signals derived from manganese markers used as a reference in ESR measurement. Here, (a) shows the ESR spectrum of the crude DMPO of 1 above, and (b) shows the ESR spectrum of DMPO obtained by the recrystallization of 2 above. Here, in (a), a large amount of impurity-derived ESR signal exists, but in (b), it was recognized that the impurity was lost. From this result, it was confirmed that the DMPO purification method using the method of the present invention was effective.

精製前のDMPOのESRスペクトル(a)と精製後のDMPOのESRスペクトル(b)を示す。The ESR spectrum (a) of DMPO before purification and the ESR spectrum (b) of DMPO after purification are shown.

Claims (2)

粗5,5−ジメチルピロリン−N−オキサイドを35℃以下の温度で有機溶媒に溶解する工程と、得られた溶液からDMPOを6℃以下の温度で再結晶化する工程を含むことを特徴とする5,5−ジメチルピロリン−N−オキサイドの精製方法。 A step of dissolving crude 5,5-dimethylpyrroline-N-oxide in an organic solvent at a temperature of 35 ° C. or lower, and a step of recrystallizing DMPO from the resulting solution at a temperature of 6 ° C. or lower. To purify 5,5-dimethylpyrroline-N-oxide. 前記溶液に固体状の5,5−ジメチルピロリン−N−オキサイドを添加する工程をさらに含むことを特徴とする請求項1に記載の精製方法。

The purification method according to claim 1, further comprising a step of adding solid 5,5-dimethylpyrroline-N-oxide to the solution.

JP2003299459A 2003-08-25 2003-08-25 Method for purifying 5,5-dimethylpyrroline-n-oxide Pending JP2005068067A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01153675A (en) * 1987-12-10 1989-06-15 Mitsui Toatsu Chem Inc Purification of 5,5-dimethylpyrroline-n-oxide
JPH01305061A (en) * 1988-06-03 1989-12-08 Mitsui Toatsu Chem Inc Method for purifying 5,5-dimethylpyproline-n-oxide
JPH0859465A (en) * 1994-08-15 1996-03-05 Yamagata Pref Gov Technopolis Zaidan Spin trapping agent
JPH1045748A (en) * 1996-08-08 1998-02-17 Kuraray Co Ltd Purification of 3-bromothiophene

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01153675A (en) * 1987-12-10 1989-06-15 Mitsui Toatsu Chem Inc Purification of 5,5-dimethylpyrroline-n-oxide
JPH01305061A (en) * 1988-06-03 1989-12-08 Mitsui Toatsu Chem Inc Method for purifying 5,5-dimethylpyproline-n-oxide
JPH0859465A (en) * 1994-08-15 1996-03-05 Yamagata Pref Gov Technopolis Zaidan Spin trapping agent
JPH1045748A (en) * 1996-08-08 1998-02-17 Kuraray Co Ltd Purification of 3-bromothiophene

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