WO2010079605A1 - Process for producing high-purity 1-benzyl-3-aminopyrrolidine - Google Patents

Process for producing high-purity 1-benzyl-3-aminopyrrolidine Download PDF

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WO2010079605A1
WO2010079605A1 PCT/JP2009/050167 JP2009050167W WO2010079605A1 WO 2010079605 A1 WO2010079605 A1 WO 2010079605A1 JP 2009050167 W JP2009050167 W JP 2009050167W WO 2010079605 A1 WO2010079605 A1 WO 2010079605A1
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benzyl
aminopyrrolidine
water
tartaric acid
purity
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PCT/JP2009/050167
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French (fr)
Japanese (ja)
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年弘 藤野
龍治 小川
健一 酒井
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東レ・ファインケミカル株式会社
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Priority to JP2010545664A priority Critical patent/JP5397706B2/en
Priority to PCT/JP2009/050167 priority patent/WO2010079605A1/en
Publication of WO2010079605A1 publication Critical patent/WO2010079605A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D207/00Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D207/02Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D207/04Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members
    • C07D207/10Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D207/14Nitrogen atoms not forming part of a nitro radical

Definitions

  • the present invention relates to a method for purifying 1-benzyl-3-aminopyrrolidine having low chemical purity in which impurities are mixed.
  • a salt is formed from a mixture of (R) -1-benzyl-3-aminopyrrolidine represented by the formula (S) -1-benzyl-3-aminopyrrolidine and a mixture of L-tartaric acid and D-tartaric acid and mixed with water. And a method for producing high-purity 1-benzyl-3-aminopyrrolidine characterized by crystallization in a mixed solvent of an organic solvent and water.
  • high chemical purity 1-benzyl-3-aminopyrrolidine can be obtained in high yield from low chemical purity 1-benzyl-3-aminopyrrolidine by a simple industrially feasible method.
  • the chemical purity is low because it contains many impurities such as 4-amino-1-benzylpiperidine represented by Such impurities are difficult to remove because their properties are similar to racemic 1-benzyl-3-aminopyrrolidine, and from low chemical purity racemic 1-benzyl-3-aminopyrrolidine to high chemical purity racemic 1-benzyl.
  • impurities such as 4-amino-1-benzylpiperidine represented by Such impurities are difficult to remove because their properties are similar to racemic 1-benzyl-3-aminopyrrolidine, and from low chemical purity racemic 1-benzyl-3-aminopyrrolidine to high chemical purity racemic 1-benzyl.
  • a high purification yield cannot be achieved in the operation for removing impurities. Therefore, it was necessary to develop a purification method for obtaining high-purity racemic 1-benzyl-3-aminopyrrolidine in high yield.
  • Example 4 The same operation as in Example 2 was carried out except that the amount of methanol used was changed to 11.4 g and the amount of water used was changed to 4.1 g to obtain 6.4 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. .
  • the content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.3%, and the crystallization yield was 87%.
  • moisture content was 14.2%.
  • 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.8%.
  • Example 10 The same operation as in Example 5 was carried out except that methanol was changed to acetonitrile, to obtain 6.1 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid.
  • the content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.7%, and the crystallization yield was 83%.
  • the water content was 13.7%.
  • 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well.
  • the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%.
  • the cake was taken out and dried under vacuum to obtain 4.8 g of a racemic 1-benzyl-3-aminopyrrolidine and succinic acid salt.
  • the content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 60.3%, and the crystallization yield was 86%.
  • 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well.
  • Comparative Example 8 The same operation as in Example 2 was performed except that methanol was not used and the amount of water used was changed to 15.5 g, to obtain 4.6 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid.
  • the content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.9%, and the crystallization yield was 62%.
  • moisture content was 13.3%.
  • 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well.
  • the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine was 100.0% (note that toluene was excluded).
  • the mixture was cooled to about 3 ° C. over 30 minutes, and further stirred at 0 to 5 ° C. for 2 hours.
  • the slurry was filtered, and the cake was washed with 5 ml of 50% aqueous methanol solution.
  • the cake was taken out and vacuum-dried to obtain 3.2 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt.
  • the content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 47.0%, and the crystallization yield was 44%.
  • the water content was 13.8%.

Abstract

An industrially practicable purification method is provided by which 1-benzyl-3-aminopyrrolidine having a high chemical purity can be produced in a high yield. A salt is formed from tartaric acid and low-chemical-purity 1-benzyl-3-aminopyrrolidine containing impurities. The salt is crystallized from a mixed solvent comprising water and an organic solvent miscible with water to thereby produce high-purity 1-benzyl-3-aminopyrrolidine.

Description

高純度1-ベンジル-3-アミノピロリジンの製造方法Method for producing high-purity 1-benzyl-3-aminopyrrolidine
 本発明は、不純物が混入している化学純度の低い1-ベンジル-3-アミノピロリジンの精製方法に関する。 The present invention relates to a method for purifying 1-benzyl-3-aminopyrrolidine having low chemical purity in which impurities are mixed.
 従来、1-ベンジル-3-アミノピロリジンを精製する方法として、例えば低い光学純度の光学活性1-ベンジル-3-アミノピロリジンを非光学活性な酸の塩とし、溶媒中で晶析させて光学純度を向上させる方法(特許文献1)が知られている。また、ラセミ1-ベンジル-3-アミノピロリジンを光学分割して必要とする光学活性な1-ベンジル-3-アミノピロリジンの塩を取得する方法として、光学活性な酒石酸を用いる方法(特許文献2)や光学活性なアミノ酸誘導体を用いる方法(特許文献3)が知られている。しかし、不純物が混入した化学純度の低い1-ベンジル-3-アミノピロリジンから高い化学純度の1-ベンジル-3-アミノピロリジンを高い収率で製造するための精製方法は知られていない。 Conventionally, as a method for purifying 1-benzyl-3-aminopyrrolidine, for example, optically active 1-benzyl-3-aminopyrrolidine having a low optical purity is converted into a salt of a non-optically active acid and crystallized in a solvent to obtain an optical purity. There is known a method (Patent Document 1) for improving the above. Further, as a method for obtaining the optically active 1-benzyl-3-aminopyrrolidine salt required by optical resolution of racemic 1-benzyl-3-aminopyrrolidine, a method using optically active tartaric acid (Patent Document 2) And a method using an optically active amino acid derivative (Patent Document 3) is known. However, there is no known purification method for producing high chemical purity 1-benzyl-3-aminopyrrolidine in a high yield from low chemical purity 1-benzyl-3-aminopyrrolidine mixed with impurities.
 1-ベンジル-3-アミノピロリジンは、医薬品の中間体として重要な光学活性1-ベンジル-3-アミノピロリジンを製造するための原料として有用である。また、1-ベンジル-3-アミノピロリジンを貴金属触媒下に接触還元して3-アミノピロリジンとし、次いで光学活性な酸を用いて光学分割して製造される医薬品の中間体として重要な光学活性3-アミノピロリジンを製造するための原料としても有用である。ここで、1-ベンジル-3-アミノピロリジンや3-アミノピロリジンを光学活性な酸を用いて光学分割して光学活性な1-ベンジル-3-アミノピロリジンや光学活性な3-アミノピロリジンを製造するに際して不純物が混入した原料を使用すると、目的とする光学活性体も化学純度が低いものしか得られず、また光学分割プロセスにおける収率低下の原因にもなる。また、1-ベンジル-3-アミノピロリジンを貴金属触媒の存在下に接触還元するに際して、不純物を多く含んだ純度の低い1-ベンジル-3-アミノピロリジンを使用すると、含まれる不純物が触媒を被毒して反応を阻害することもある。従って、医薬品の中間体として重要な光学活性1-ベンジル-3-アミノピロリジンや光学活性3-アミノピロリジン等をより安価に製造するために、高い収率で高い化学純度の1-ベンジル-3-アミノピロリジンを製造する方法の開発が望まれていた。
国際公開第03/082815号パンフレット 特許第2995704号公報 特開平9-124595号公報
1-Benzyl-3-aminopyrrolidine is useful as a raw material for producing optically active 1-benzyl-3-aminopyrrolidine which is important as an intermediate for pharmaceuticals. Further, catalytic activity of 1-benzyl-3-aminopyrrolidine in the presence of a noble metal catalyst to give 3-aminopyrrolidine, followed by optical resolution using an optically active acid is an important optical activity 3 -It is also useful as a raw material for producing aminopyrrolidine. Here, 1-benzyl-3-aminopyrrolidine or 3-aminopyrrolidine is optically resolved using an optically active acid to produce optically active 1-benzyl-3-aminopyrrolidine or optically active 3-aminopyrrolidine. At this time, when a raw material mixed with impurities is used, only the target optically active substance having a low chemical purity can be obtained, and this can cause a decrease in yield in the optical resolution process. In addition, when 1-benzyl-3-aminopyrrolidine is catalytically reduced in the presence of a noble metal catalyst and 1-benzyl-3-aminopyrrolidine having a low purity and containing a large amount of impurities is used, the impurities contained in the catalyst poison the catalyst. In some cases, the reaction may be inhibited. Therefore, in order to produce optically active 1-benzyl-3-aminopyrrolidine and optically active 3-aminopyrrolidine, which are important as intermediates for pharmaceuticals, at a lower cost, 1-benzyl-3- with high yield and high chemical purity. Development of a method for producing aminopyrrolidine has been desired.
International Publication No. 03/082815 Pamphlet Japanese Patent No. 2995704 JP-A-9-124595
 本発明の目的は、不純物が混入している化学純度の低いラセミ1-ベンジル-3-アミノピロリジンをはじめとする1-ベンジル-3-アミノピロリジンの(R)-体と(S)-体の混合物から、高い収率で高い化学純度の1-ベンジル-3-アミノピロリジンを製造することにある。 The object of the present invention is to provide (R) -form and (S) -form of 1-benzyl-3-aminopyrrolidine including low-purity racemic 1-benzyl-3-aminopyrrolidine mixed with impurities. The object is to produce 1-benzyl-3-aminopyrrolidine with high yield and high chemical purity from the mixture.
 本発明者らは高い化学純度の1-ベンジル-3-アミノピロリジンの製造方法を鋭意検討した結果、ラセミ1-ベンジル-3-アミノピロリジンとラセミ酒石酸から塩を形成し、水と混和する有機溶媒と水の混合溶媒中で晶析することによって高い化学純度のラセミ1-ベンジル-3-アミノピロリジンが高い収率で製造でき、またこれを片方の光学異性体がもう一方の光学異性体よりも多くなった(R)-体と(S)--体の混合物においても適用できることを見いだした。 As a result of intensive studies on a method for producing 1-benzyl-3-aminopyrrolidine having high chemical purity, the present inventors have formed an organic solvent that forms a salt from racemic 1-benzyl-3-aminopyrrolidine and racemic tartaric acid and is miscible with water. High-purity racemic 1-benzyl-3-aminopyrrolidine can be produced in high yield by crystallization in a mixed solvent of water and water, and one optical isomer is more than the other optical isomer. It was found that the present invention can also be applied to a mixture of (R) -form and (S)-form which have increased.
 すなわち、本発明は、不純物が混入している化学純度の低い式(1) That is, the present invention has a low chemical purity formula (1) in which impurities are mixed.
Figure JPOXMLDOC01-appb-C000002
Figure JPOXMLDOC01-appb-C000002
で表される(R)-1-ベンジル-3-アミノピロリジンと(S)-1-ベンジル-3-アミノピロリジンの混合物とL-酒石酸とD-酒石酸の混合物から塩を形成し、水と混和する有機溶媒と水の混合溶媒中で晶析することを特徴とする、高純度1-ベンジル-3-アミノピロリジンの製造方法である。 A salt is formed from a mixture of (R) -1-benzyl-3-aminopyrrolidine represented by the formula (S) -1-benzyl-3-aminopyrrolidine and a mixture of L-tartaric acid and D-tartaric acid and mixed with water. And a method for producing high-purity 1-benzyl-3-aminopyrrolidine characterized by crystallization in a mixed solvent of an organic solvent and water.
 本発明によれば、工業的に実施可能な簡便な方法で、低い化学純度の1-ベンジル-3-アミノピロリジンから高い化学純度の1-ベンジル-3-アミノピロリジンが高い収率で取得できる。 According to the present invention, high chemical purity 1-benzyl-3-aminopyrrolidine can be obtained in high yield from low chemical purity 1-benzyl-3-aminopyrrolidine by a simple industrially feasible method.
 本発明を具体的に述べる。 The present invention will be specifically described.
 尚、本発明における「高い収率」とは収率が70%以上のことであり、「高い化学純度」とは化学純度が99.0%以上のことである。従って、「高い収率で高い化学純度の1-ベンジル-3-アミノピロリジンを製造する方法」とは化学純度が99.0%以上の1-ベンジル-3-アミノピロリジンを原料に含まれる1-ベンジル-3-アミノピロリジンに対して70%以上の収率で製造する方法のことである。 In the present invention, “high yield” means that the yield is 70% or more, and “high chemical purity” means that the chemical purity is 99.0% or more. Therefore, “a method for producing 1-benzyl-3-aminopyrrolidine having a high yield and high chemical purity” means that 1-benzyl-3-aminopyrrolidine having a chemical purity of 99.0% or more is contained in the raw material. It is a method of producing with a yield of 70% or more based on benzyl-3-aminopyrrolidine.
 本発明において使用できる原料の1-ベンジル-3-アミノピロリジンは、不斉点が存在しない物質を出発物質として立体選択的な反応条件を設定しないで合成されたラセミ1-ベンジル-3-アミノピロリジン、光学活性1-ベンジル-3-アミノピロリジンをラセミ化したラセミ1-ベンジル-3-アミノピロリジン、製造の過程において片方の光学異性体がもう一方の光学異性体よりも多くなった(R)-体と(S)-体の混合物等であり、その製造方法は特に限定されない。 The starting material 1-benzyl-3-aminopyrrolidine that can be used in the present invention is a racemic 1-benzyl-3-aminopyrrolidine synthesized without a stereoselective reaction condition starting from a substance having no asymmetric point. Racemic 1-benzyl-3-aminopyrrolidine racemized from optically active 1-benzyl-3-aminopyrrolidine, one optical isomer in the process of production was more than the other optical isomer (R)- And the production method thereof is not particularly limited.
 本発明で用いる1-ベンジル-3-アミノピロリジンは、その製造方法により種々の不純物を含有している。例えば、ラセミ1-ベンジル-3-アミノピロリジンは、Journal of Chemical Engineering of Chinese Universities No.4 Vol.17 Aug. 438-441(2003)に記載の方法で製造することができる。 1-Benzyl-3-aminopyrrolidine used in the present invention contains various impurities depending on the production method. For example, racemic 1-benzyl-3-aminopyrrolidine is available from Journal of Chemical Engineering of China Universities No. 4 Vol. 17 Aug. 438-441 (2003).
Figure JPOXMLDOC01-appb-C000003
Figure JPOXMLDOC01-appb-C000003
上記において、R1、R2,R3はアルキル基を表し、好ましくは炭素数1~4のアルキル基、さらに好ましくはメチル基、エチル基である。baseは塩基を表し、好ましくはナトリウムメトキシド、ナトリウムエトキシド、ナトリウムt-ブトキシド、カリウムメトキシド、カリウムエトキシド、カリウムt-ブトキシドであり、さらに好ましくはナトリウムメトキシド、ナトリウムエトキシドである。Acidは酸を表し、好ましくは鉱酸であり、さらに好ましくは塩酸である。
しかし、このような方法で製造したラセミ1-ベンジル-3-アミノピロリジンは、ベンジルアミンや式(2)
In the above, R1, R2, and R3 each represents an alkyl group, preferably an alkyl group having 1 to 4 carbon atoms, more preferably a methyl group or an ethyl group. base represents a base, preferably sodium methoxide, sodium ethoxide, sodium t-butoxide, potassium methoxide, potassium ethoxide, potassium t-butoxide, and more preferably sodium methoxide or sodium ethoxide. Acid represents an acid, preferably a mineral acid, and more preferably hydrochloric acid.
However, racemic 1-benzyl-3-aminopyrrolidine produced by such a method is benzylamine or formula (2)
Figure JPOXMLDOC01-appb-C000004
Figure JPOXMLDOC01-appb-C000004
で表される4-アミノ-1-ベンジルピペリジン等の不純物を多く含んでいるためその化学純度は低い。このような不純物はその性質がラセミ1-ベンジル-3-アミノピロリジンと類似しているために除去が難しく、低い化学純度のラセミ1-ベンジル-3-アミノピロリジンから高い化学純度のラセミ1-ベンジル-3-アミノピロリジンを得ようとすると、不純物を除去するための操作において高い精製収率は達成できない。従って、高い化学純度のラセミ1-ベンジル-3-アミノピロリジンを高い収率で取得する精製方法を開発する必要があった。 The chemical purity is low because it contains many impurities such as 4-amino-1-benzylpiperidine represented by Such impurities are difficult to remove because their properties are similar to racemic 1-benzyl-3-aminopyrrolidine, and from low chemical purity racemic 1-benzyl-3-aminopyrrolidine to high chemical purity racemic 1-benzyl. When trying to obtain -3-aminopyrrolidine, a high purification yield cannot be achieved in the operation for removing impurities. Therefore, it was necessary to develop a purification method for obtaining high-purity racemic 1-benzyl-3-aminopyrrolidine in high yield.
 本発明者らは、化学純度の低い1-ベンジル-3-アミノピロリジンの精製方法を鋭意検討した結果、1-ベンジル-3-アミノピロリジンと酒石酸から塩を形成し、水と混和する有機溶媒と水の混合溶媒中で晶析する方法を開発するに至った。本発明によれば、高い化学純度の1-ベンジル-3-アミノピロリジンと酒石酸の塩が3水和物として取得できるので、一般的な方法で処理することによって高い化学純度の1-ベンジル-3-アミノピロリジンを製造することができる。 As a result of intensive studies on a method for purifying 1-benzyl-3-aminopyrrolidine having a low chemical purity, the present inventors have found that an organic solvent that forms a salt from 1-benzyl-3-aminopyrrolidine and tartaric acid and is miscible with water A method for crystallization in a mixed solvent of water has been developed. According to the present invention, since a salt of 1-benzyl-3-aminopyrrolidine having high chemical purity and tartaric acid can be obtained as a trihydrate, 1-benzyl-3 having high chemical purity can be obtained by treating it by a general method. Aminopyrrolidine can be produced.
 本発明で使用する酒石酸としては一般に市販されているラセミ酒石酸や市販のL-酒石酸とD-酒石酸を混合したものを使用することができる。その使用量は、収率良く高純度1-ベンジル-3-アミノピロリジンを得るという観点から、原料中に含まれる1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルが好ましい。原料の1-ベンジル-3-アミノピロリジンに含まれる塩基性の不純物が多い場合には、それら不純物を中和する分の酒石酸を増量することで高い精製収率が達成できる。例えば、ラセミ1-ベンジル-3-アミノピロリジンを原料として使用する場合には、1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルのラセミ酒石酸が存在する系で晶析することによって高い精製収率が達成できる。また、その製造の過程において片方の光学異性体がもう一方の光学異性体よりも多くなった1-ベンジル-3-アミノピロリジンを原料として使用する場合には、そこに含まれる(R)-1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルのD-酒石酸と(S)-1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルのL-酒石酸が存在する系で晶析することによって高い精製収率が達成できる。 As tartaric acid used in the present invention, commercially available racemic tartaric acid or a mixture of commercially available L-tartaric acid and D-tartaric acid can be used. From the viewpoint of obtaining high-purity 1-benzyl-3-aminopyrrolidine with high yield, the amount used is 0.95-1.15 times moles relative to 1-benzyl-3-aminopyrrolidine contained in the raw material. preferable. If the starting material 1-benzyl-3-aminopyrrolidine contains many basic impurities, a high purification yield can be achieved by increasing the amount of tartaric acid to neutralize these impurities. For example, when racemic 1-benzyl-3-aminopyrrolidine is used as a raw material, crystallization is performed in a system in which 0.95 to 1.15 times moles of racemic tartaric acid are present relative to 1-benzyl-3-aminopyrrolidine. By doing so, a high purification yield can be achieved. Further, when 1-benzyl-3-aminopyrrolidine in which one optical isomer is larger than the other optical isomer is used as a raw material in the production process, it is contained in (R) -1 0.95 to 1.15 times moles of D-tartaric acid with respect to benzyl-3-aminopyrrolidine and 0.95 to 1.15 times moles of L with respect to (S) -1-benzyl-3-aminopyrrolidine A high purification yield can be achieved by crystallization in a system in which tartaric acid is present.
 本発明で使用する水と混和する有機溶媒は、特に限定されないが、メタノール、エタノール、n-プロパノール、2-プロパノール、テトラヒドロフラン、アセトニトリル、アセトン、および/または、これらから選ばれる一種または二種以上の混合液が好ましく使用することができる。その使用量は、精製収率や生産性等を考えた場合に、原料のラセミ1-ベンジル-3-アミノピロリジンに対して0.8~3.5重量倍が好ましい。 The organic solvent miscible with water used in the present invention is not particularly limited, but methanol, ethanol, n-propanol, 2-propanol, tetrahydrofuran, acetonitrile, acetone, and / or one or more selected from these A mixed solution can be preferably used. The amount used is preferably 0.8 to 3.5 times the weight of the raw material racemic 1-benzyl-3-aminopyrrolidine in view of purification yield, productivity and the like.
 本発明では水の存在は不可欠である。本発明に従って晶析をおこなうと、水と混和する有機溶媒と水の混合溶媒への溶解度が小さい(R)-1-ベンジル-3-アミノピロリジンとD-酒石酸の塩の3水和物と(S)-1-ベンジル-3-アミノピロリジンとL-酒石酸の塩の3水和物が析出する。一方、(R)-1-ベンジル-3-アミノピロリジンとL-酒石酸の塩や(S)-1-ベンジル-3-アミノピロリジンとD-酒石酸の塩は水和物を形成せず、水と混和する有機溶媒と水の混合溶媒への溶解度が高いために析出し難い。本発明で使用する水の量は、上記3水和物が効率よく生成するという観点から原料に含まれる1-ベンジル-3-アミノピロリジンに対して好ましくは8倍モル以上であり、更に好ましくは9倍モル以上である。これより少ないと、1-ベンジル-3-アミノピロリジンと酒石酸の塩の3水和物が析出しにくくなり、大幅に収率が低下するので好ましくない。使用量の上限は特に限定されないが、精製収率や生産性等を考えた場合に、原料の1-ベンジル-3-アミノピロリジンに対して3重量倍程度である。 In the present invention, the presence of water is indispensable. When crystallization is carried out according to the present invention, (R) -1-benzyl-3-aminopyrrolidine and D-tartaric acid salt trihydrate, which has a low solubility in an organic solvent miscible with water and a mixed solvent of water, S) -1-benzyl-3-aminopyrrolidine and L-tartaric acid salt trihydrate are precipitated. On the other hand, the salt of (R) -1-benzyl-3-aminopyrrolidine and L-tartaric acid or the salt of (S) -1-benzyl-3-aminopyrrolidine and D-tartaric acid does not form a hydrate, Precipitation is difficult because of the high solubility of the organic solvent and water in the mixed solvent. The amount of water used in the present invention is preferably 8 times mol or more with respect to 1-benzyl-3-aminopyrrolidine contained in the raw material from the viewpoint of efficiently producing the trihydrate, and more preferably It is 9 times mole or more. If it is less than this, it is difficult to precipitate the trihydrate of 1-benzyl-3-aminopyrrolidine and tartaric acid salt, which is not preferable because the yield is greatly reduced. The upper limit of the amount used is not particularly limited, but is about 3 times the weight of 1-benzyl-3-aminopyrrolidine as a raw material in view of purification yield and productivity.
 本発明においては、1-ベンジル-3-アミノピロリジンの(R)-体と(S)-体の混合物と酒石酸のD-体とL-体の混合物を用いて上記混合溶媒中で塩の水和物を形成させることにより、混合溶媒中で析出しやすい(R)-1-ベンジル-3-アミノピロリジンとD-酒石酸の塩の3水和物と(S)-1-ベンジル-3-アミノピロリジンとL-酒石酸の塩の3水和物が析出していくため、平衡状態にいたることなく高収率で高化学純度化することができるのである。 In the present invention, salt water is used in the above mixed solvent using a mixture of (R) -form and (S) -form of 1-benzyl-3-aminopyrrolidine and a mixture of D-form and L-form of tartaric acid. (R) -1-benzyl-3-aminopyrrolidine and D-tartaric acid trihydrate and (S) -1-benzyl-3-amino which are easily precipitated in a mixed solvent by forming a solvate Since the trihydrate of the salt of pyrrolidine and L-tartaric acid precipitates, it can be highly purified with high yield without reaching an equilibrium state.
 1-ベンジル-3-アミノピロリジンと酒石酸の塩を形成する方法や形成された塩を水と混和する有機溶媒と水の混合溶媒中から析出させる方法としては特に限定されないが、例えば水、水と混合する有機溶媒、ラセミ酒石酸、1-ベンジル-3-アミノピロリジンの順に晶析装置に仕込み、混合物を加熱して均一溶液としたのち、適当な温度で種晶((R)-1-ベンジル-3-アミノピロリジン・D-酒石酸塩の3水和物と(S)-1-ベンジル-3-アミノピロリジン・L-酒石酸塩の3水和物)を加えてから冷却する方法が採用できる。種晶を加える時機は、水と混和する有機溶媒と水の混合比率やその使用量によって異なるが、おおよそ20~40℃の範囲である。析出した結晶を濾別する温度は特に限定されないが、高い収率で塩を得るためにはその温度は低い方が好ましく、通常は0~20℃である。 A method for forming a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid and a method for precipitating the formed salt from a mixed solvent of an organic solvent mixed with water and water are not particularly limited. The organic solvent to be mixed, racemic tartaric acid, and 1-benzyl-3-aminopyrrolidine were charged into the crystallizer in this order, and the mixture was heated to obtain a homogeneous solution, and then seed crystals ((R) -1-benzyl- A method of cooling after adding 3-aminopyrrolidine · D-tartrate trihydrate and (S) -1-benzyl-3-aminopyrrolidine · L-tartrate trihydrate) can be employed. The timing for adding the seed crystals varies depending on the mixing ratio of the organic solvent mixed with water and water and the amount of water used, but is in the range of approximately 20 to 40 ° C. The temperature at which the precipitated crystals are separated by filtration is not particularly limited, but in order to obtain a salt with a high yield, the temperature is preferably low and is usually 0 to 20 ° C.
 かくして得られた1-ベンジル-3-アミノピロリジンと酒石酸の塩の3水和物から1-ベンジル-3-アミノピロリジンの単離は、一般的な方法に従って実施できる。例えば、塩を水とトルエン中で撹拌しながら水酸化ナトリウムの水溶液を添加して塩基性とし、分液して得たトルエン層を濃縮することによって1-ベンジル-3-アミノピロリジが取得できる。 Isolation of 1-benzyl-3-aminopyrrolidine from the trihydrate of 1-benzyl-3-aminopyrrolidine and tartaric acid salt thus obtained can be carried out according to a general method. For example, 1-benzyl-3-aminopyrrolidi can be obtained by adding a sodium hydroxide aqueous solution while stirring the salt in water and toluene to make it basic, and concentrating the toluene layer obtained by liquid separation.
 以下、実施例により本発明を更に詳細に説明するが、本発明はこれらに限定されるものではない。尚、以下の実施例や比較例における1-ベンジル-3-アミノピロリジンの含有率は高速液体クロマトグラフィーを用いて決定し、化学純度はガスクロマトグラフィーを用いて決定した。
<1-ベンジル-3-アミノピロリジンの含有率(HPLC)>
カラム:Mightysil RP-18GP(関東化学)4.6mmφ×150mm
移動相:2.5mM ドデシル硫酸ナトリウム水溶液(pH2.2、リン酸使用)630mlとアセトニトリル370mlの混合液
カラムオーブン温度:40℃
検出器:UV 205nm
内部標準物質:2,4-ジクロロアニリン
<1-ベンジル-3-アミノピロリジンの化学純度(GC)>
カラム:NEUTRA BOND-1(ジーエルサイエンス)0.25mmI.D.×60m、0.4μm
カラムオーブン温度:70℃(15分)-20℃/分→270℃(20分)
注入口:200℃
検出器:200℃
キャリヤーガス:ヘリウム 全流量52ml/分
スプリット比:19
 参考例
 撹拌機、温度計を装着した容量1Lのフラスコに、ベンジルアミン53.6g(0.50モル)とメタノール26.8gを仕込んだ。撹拌しながら、この混合液にアクリル酸メチル43.1g(0.50モル)を2時間かけて添加した。このとき反応液の温度を約50℃に保った。添加終了後、更に同温度で2時間撹拌を続けた。この反応液にトリエチルアミン64.0g(0.63モル)を添加したのち、クロロ酢酸メチル68.6g(0.63モル)を2時間かけて添加した。添加終了後、約70℃加熱して4時間撹拌を続けた。この反応液を室温まで冷却し、トルエン216gと水130gを加えて撹拌した。靜置後、水層を抜き出し、残ったトルエン層を減圧下に濃縮して濃縮液178gを得た。この濃縮液にメタノール73gを加えて希釈し、20から25℃で28%ナトリウムメトキシドのメタノール溶液122.7g(0.64モル)を3時間かけて仕込み、更に同温度で3時間撹拌を続けた。
EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to these. In the following Examples and Comparative Examples, the content of 1-benzyl-3-aminopyrrolidine was determined using high performance liquid chromatography, and the chemical purity was determined using gas chromatography.
<Content of 1-benzyl-3-aminopyrrolidine (HPLC)>
Column: Mightysil RP-18GP (Kanto Chemical) 4.6 mmφ × 150 mm
Mobile phase: 2.5 mM sodium dodecyl sulfate aqueous solution (pH 2.2, using phosphoric acid) 630 ml and acetonitrile 370 ml mixed liquid Column oven temperature: 40 ° C.
Detector: UV 205nm
Internal standard: 2,4-dichloroaniline <chemical purity of 1-benzyl-3-aminopyrrolidine (GC)>
Column: NEUTRA BOND-1 (GL Science) 0.25 mmI. D. × 60m, 0.4μm
Column oven temperature: 70 ° C (15 minutes)-20 ° C / minute → 270 ° C (20 minutes)
Inlet: 200 ° C
Detector: 200 ° C
Carrier gas: Helium Total flow rate 52 ml / min Split ratio: 19
Reference Example 53.6 g (0.50 mol) of benzylamine and 26.8 g of methanol were charged into a 1 L flask equipped with a stirrer and a thermometer. While stirring, 43.1 g (0.50 mol) of methyl acrylate was added to the mixed solution over 2 hours. At this time, the temperature of the reaction solution was kept at about 50 ° C. After completion of the addition, stirring was further continued at the same temperature for 2 hours. After adding 64.0 g (0.63 mol) of triethylamine to the reaction solution, 68.6 g (0.63 mol) of methyl chloroacetate was added over 2 hours. After completion of the addition, the mixture was heated at about 70 ° C. and stirred for 4 hours. The reaction solution was cooled to room temperature, and 216 g of toluene and 130 g of water were added and stirred. After laying, the aqueous layer was extracted, and the remaining toluene layer was concentrated under reduced pressure to obtain 178 g of a concentrated solution. This concentrated liquid was diluted with 73 g of methanol, charged with 122.7 g (0.64 mol) of 28% sodium methoxide in methanol at 20 to 25 ° C. over 3 hours, and further stirred at the same temperature for 3 hours. It was.
 この反応液に水167gと35%塩酸167g(1.6モル)の混合液を約1時間かけて加え、約75℃で7時間撹拌した。反応液を減圧下に濃縮して、479gの濃縮液を得た。20から40℃で、pHが約12になるまで48%水酸化ナトリウム水溶液を加えた。トルエン118gを加えて撹拌したのち、水層を抜き出した。残ったトルエン層を減圧下に濃縮して濃縮液110gを得た。濃縮液中には1-ベンジル-3-ピロリジノンが58.2%含まれていた。 A mixed solution of 167 g of water and 167 g (1.6 mol) of 35% hydrochloric acid was added to this reaction solution over about 1 hour, and the mixture was stirred at about 75 ° C. for 7 hours. The reaction solution was concentrated under reduced pressure to obtain 479 g of a concentrated solution. At 20-40 ° C., 48% aqueous sodium hydroxide was added until the pH was about 12. 118 g of toluene was added and stirred, and then the aqueous layer was extracted. The remaining toluene layer was concentrated under reduced pressure to obtain a concentrated solution 110 g. The concentrate contained 58.2% of 1-benzyl-3-pyrrolidinone.
 撹拌機、温度計を装着した容量500mlのフラスコに、水220g、硫酸ヒドロキシルアミン31.4gを仕込んだ。この溶液を約25℃に保ちながら、1-ベンジル-3-ピロリジノンを含む濃縮液を1時間かけて添加した。靜置したのちに分液してトルエン層を除いた。残った水層に、pHが約12になるまで48%水酸化ナトリウム水溶液を約2時間かけて添加した。このとき内液の温度を約25℃に保った。析出した結晶を濾別して、104.8gのウェットケークを得た。ウェットケークには1-ベンジル-3-ピロリジノンオキシムが55.7%含まれていた。 In a 500 ml flask equipped with a stirrer and a thermometer, 220 g of water and 31.4 g of hydroxylamine sulfate were charged. While maintaining this solution at about 25 ° C., a concentrated solution containing 1-benzyl-3-pyrrolidinone was added over 1 hour. After placing the solution, the solution was separated to remove the toluene layer. A 48% sodium hydroxide aqueous solution was added to the remaining aqueous layer over about 2 hours until the pH reached about 12. At this time, the temperature of the internal liquid was kept at about 25 ° C. The precipitated crystals were separated by filtration to obtain 104.8 g of wet cake. The wet cake contained 55.7% 1-benzyl-3-pyrrolidinone oxime.
 容量1Lのオートクレーブに1-ベンジル-3-ピロリジノンオキシムを含むウェットケーク全量、メタノール235g、28%アンモニア水54g、およびラネーニッケル触媒15gを仕込んだ。水素ガスで約0.5MPaに加圧しながら、約50℃で2時間撹拌した。反応終了後、触媒を濾別し、濾過液を減圧下に濃縮して濃縮液57.0gを得た。濃縮液には1-ベンジル-3-アミノピロリジンが84.4%含まれていた。1-ベンジル-3-アミノピロリジンの収率は出発原料であるベンジルアミンに対して54.6モル%であった。濃縮液をガスクロマトグラフィーで分析したところ、その組成は、1-ベンジル-3-アミノピロリジン94.7%、ベンジルアミン0.6%、その他4.7%であった。濃縮液を1規定塩酸で中和滴定したところ、その中に含まれる塩基性の成分は、10.0meq./gであった。  A 1 L autoclave was charged with a total amount of wet cake containing 1-benzyl-3-pyrrolidinone oxime, 235 g of methanol, 54 g of 28% ammonia water, and 15 g of Raney nickel catalyst. The mixture was stirred at about 50 ° C. for 2 hours while being pressurized to about 0.5 MPa with hydrogen gas. After completion of the reaction, the catalyst was filtered off, and the filtrate was concentrated under reduced pressure to obtain 57.0 g of a concentrated solution. The concentrate contained 84.4% of 1-benzyl-3-aminopyrrolidine. The yield of 1-benzyl-3-aminopyrrolidine was 54.6 mol% based on the starting material benzylamine. The concentrated liquid was analyzed by gas chromatography. The composition was 94.7% 1-benzyl-3-aminopyrrolidine, 0.6% benzylamine, and 4.7% other. The concentrated solution was neutralized and titrated with 1N hydrochloric acid, and the basic component contained therein was 10.0 meq. / G. *
 実施例1
 撹拌機、温度計を装着した容量300mlのフラスコに、参考例で取得したラセミ1-ベンジル-3-アミノピロリジンを含む濃縮液39.9g、エタノール42g、水42g、およびDL-酒石酸30.0gを仕込んだ。撹拌しながら、約55℃に加熱して固形物を溶解したのち、約33℃まで冷却した。そこに(R)-1-ベンジル-3-アミノピロリジンとD-酒石酸の塩の3水和物と(S)-1-ベンジル-3-アミノピロリジンとL-酒石酸の塩の3水和物の混合物(以下、種晶と略称する)を約0.1g添加し、30~35℃に保って1時間撹拌した。次いで、2時間かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを、遠心濾過器を使用して濾過し、ケークに50%エタノール水溶液25gを噴霧して洗浄した。ケークを取り出し、真空乾燥して1-ベンジル-3-アミノピロリジンと酒石酸の塩68.7gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.6%であり、晶析収率は95%であった。また、塩の中の水分は14.3%であった。この塩の全量に水74gとトルエン74gを加え、撹拌しながらpHが約12になるまで48%水酸化ナトリウム水溶液を加えた。分液して得たトルエン層を約80℃に加熱し、圧力が約1.3kPaでトルエンが留出しなくなるまで濃縮した。濃縮液量は31.4gであった。ガスクロマトグラフィーで分析したところ、その組成は、1-ベンジル-3-アミノピロリジン99.1%、トルエン0.9%、その他0.1%であった。
Example 1
Into a 300 ml flask equipped with a stirrer and a thermometer, 39.9 g of the concentrated solution containing racemic 1-benzyl-3-aminopyrrolidine obtained in the Reference Example, 42 g of ethanol, 42 g of water, and 30.0 g of DL-tartaric acid were added. Prepared. While stirring, the mixture was heated to about 55 ° C. to dissolve the solid, and then cooled to about 33 ° C. There are (R) -1-benzyl-3-aminopyrrolidine and D-tartaric acid salt trihydrate and (S) -1-benzyl-3-aminopyrrolidine and L-tartaric acid salt trihydrate. About 0.1 g of the mixture (hereinafter abbreviated as seed crystal) was added, and the mixture was kept at 30 to 35 ° C. and stirred for 1 hour. Subsequently, the mixture was cooled to about 3 ° C. over 2 hours, and further stirred at 0 to 5 ° C. for 2 hours. The slurry was filtered using a centrifugal filter, and the cake was washed by spraying 25 g of 50% aqueous ethanol. The cake was taken out and vacuum-dried to obtain 68.7 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.6%, and the crystallization yield was 95%. The water content in the salt was 14.3%. 74 g of water and 74 g of toluene were added to the total amount of this salt, and a 48% aqueous sodium hydroxide solution was added until the pH reached about 12 while stirring. The toluene layer obtained by the liquid separation was heated to about 80 ° C., and concentrated until the toluene was not distilled at a pressure of about 1.3 kPa. The amount of the concentrated liquid was 31.4 g. Analysis by gas chromatography revealed that the composition was 99.1% 1-benzyl-3-aminopyrrolidine, 0.9% toluene, and 0.1% other.
 実施例2
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、メタノール13.4g、水2.8g、およびDL-酒石酸3.1gを仕込んだ。撹拌しながら、約55℃に加熱して固形物を溶解したのち、約30℃まで冷却した。そこに種晶を約20mg添加し、20~30℃に保って1時間撹拌した。次いで、30分かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを濾過し、ケークに50%メタノール水溶液5mlを振りかけて洗浄した。ケークを取り出し、真空乾燥して1-ベンジル-3-アミノピロリジンと酒石酸の塩5.8gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.8%であり、晶析収率は79%であった。また、水分は13.3%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.8%であった。
Example 2
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, methanol 13.4 g, water 2.8 g, and DL -Charged 3.1 g of tartaric acid. While stirring, the mixture was heated to about 55 ° C. to dissolve the solid, and then cooled to about 30 ° C. About 20 mg of seed crystals were added thereto, and the mixture was stirred for 1 hour while maintaining at 20 to 30 ° C. Subsequently, the mixture was cooled to about 3 ° C. over 30 minutes, and further stirred at 0 to 5 ° C. for 2 hours. The slurry was filtered, and the cake was washed with 5 ml of 50% aqueous methanol solution. The cake was taken out and vacuum-dried to obtain 5.8 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.8%, and the crystallization yield was 79%. Moreover, the water | moisture content was 13.3%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.8%.
 実施例3
 水の使用量を3.2gに変えた以外は実施例2と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.0gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.6%であり、晶析収率は82%であった。また、水分は13.7%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.7%であった。
Example 3
The same operation as in Example 2 was carried out except that the amount of water used was changed to 3.2 g to obtain 6.0 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.6%, and the crystallization yield was 82%. The water content was 13.7%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.7%.
 実施例4
 メタノールの使用量を11.4g、水の使用量を4.1gに変えた以外は実施例2と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.4gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.3%であり、晶析収率は87%であった。また、水分は14.2%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.8%であった。
Example 4
The same operation as in Example 2 was carried out except that the amount of methanol used was changed to 11.4 g and the amount of water used was changed to 4.1 g to obtain 6.4 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. . The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.3%, and the crystallization yield was 87%. Moreover, the water | moisture content was 14.2%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.8%.
 実施例5
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、メタノール7.2g、水8.4g、およびDL-酒石酸3.1gを仕込んだ。撹拌しながら、約55℃に加熱して固形物を溶解したのち、約30℃まで冷却した。そこに種晶を約20mg添加し、20~30℃に保って1時間撹拌した。次いで、30分かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを濾過し、ケークに50%メタノール水溶液5mlを振りかけて洗浄した。ケークを取り出し、真空乾燥して1-ベンジル-3-アミノピロリジンと酒石酸の塩6.3gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.7%であり、晶析収率は86%であった。また、水分は13.6%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.6%であった。
Example 5
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, methanol 7.2 g, water 8.4 g, and DL -Charged 3.1 g of tartaric acid. While stirring, the mixture was heated to about 55 ° C. to dissolve the solid, and then cooled to about 30 ° C. About 20 mg of seed crystals were added thereto, and the mixture was stirred for 1 hour while maintaining at 20 to 30 ° C. Subsequently, the mixture was cooled to about 3 ° C. over 30 minutes, and further stirred at 0 to 5 ° C. for 2 hours. The slurry was filtered, and the cake was washed with 5 ml of 50% aqueous methanol solution. The cake was taken out and vacuum-dried to obtain 6.3 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.7%, and the crystallization yield was 86%. The water content was 13.6%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.6%.
 実施例6
 メタノールの使用量を4.4g、水使用量を11.1gに変えた以外は実施例2と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.2gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.7%であり、晶析収率は85%であった。また、水分は13.5%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.9%であった。
Example 6
The same operation as in Example 2 was carried out except that the amount of methanol used was changed to 4.4 g and the amount of water used was changed to 11.1 g to obtain 6.2 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.7%, and the crystallization yield was 85%. The water content was 13.5%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%.
 実施例7
 DL-酒石酸の使用量を2.8gに変えた以外は実施例5と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩5.2gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は47.2%であり、晶析収率は71%であった。また、水分は12.5%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.6%であった。
Example 7
The same operation as in Example 5 was carried out except that the amount of DL-tartaric acid was changed to 2.8 g to obtain 5.2 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 47.2%, and the crystallization yield was 71%. The water content was 12.5%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.6%.
 実施例8
 DL-酒石酸の使用量を3.4gに変えた以外は実施例5と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.3gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は47.1%であり、晶析収率は87%であった。また、水分は12.7%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.9%であった。
Example 8
Except that the amount of DL-tartaric acid used was changed to 3.4 g, the same operation as in Example 5 was performed to obtain 6.3 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 47.1%, and the crystallization yield was 87%. The water content was 12.7%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%.
 実施例9
 メタノールをアセトンに変えた以外は実施例5と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.6gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.5%であり、晶析収率は89%であった。また、水分は13.7%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.8%であった。
Example 9
The same operation as in Example 5 was carried out except that methanol was changed to acetone to obtain 6.6 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.5%, and the crystallization yield was 89%. The water content was 13.7%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.8%.
 実施例10
 メタノールをアセトニトリルに変えた以外は実施例5と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.1gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.7%であり、晶析収率は83%であった。また、水分は13.7%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.9%であった。
Example 10
The same operation as in Example 5 was carried out except that methanol was changed to acetonitrile, to obtain 6.1 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.7%, and the crystallization yield was 83%. The water content was 13.7%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%.
 実施例11
 メタノールをテトラヒドロフランに変えた以外は実施例5と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩6.4gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.8%であり、晶析収率は88%であった。また、水分は13.8%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.9%であった。
実施例12
 市販の、光学純度が99.0%e.e.以上、化学純度が99.0%以上、1-ベンジル-3-アミノピロリジンの含有率が99.4%の光学活性(R)-1-ベンジル-3-アミノピロリジン1.0g、市販の1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン2.8g、メタノール11.4g、水4.1g、DL-酒石酸2.2g、およびD-酒石酸0.8gを仕込んだ。撹拌しながら、約55℃に加熱して固形物を溶解したのち、約30℃まで冷却した。そこに種晶を約20mg添加し、20~30℃に保って1時間撹拌した。次いで、30分かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを濾過し、ケークに50%メタノール水溶液5mlを振りかけて洗浄した。ケークを取り出し、真空乾燥して1-ベンジル-3-アミノピロリジンと酒石酸の塩6.6gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は47.9%であり、晶析収率は92%であった。また、水分は11.3%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.8%であった。
Example 11
The same operation as in Example 5 was carried out except that methanol was changed to tetrahydrofuran to obtain 6.4 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.8%, and the crystallization yield was 88%. The water content was 13.8%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%.
Example 12
A commercially available optical purity of 99.0% e.e. e. As described above, 1.0 g of optically active (R) -1-benzyl-3-aminopyrrolidine having a chemical purity of 99.0% or more and a 19.4-benzyl-3-aminopyrrolidine content of 99.4%, The content of benzyl-3-aminopyrrolidine was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine, 4-amino- 1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 2.8 g, methanol 11.4 g, water 4.1 g, DL-tartaric acid 2.2 g, And 0.8 g of D-tartaric acid were charged. While stirring, the mixture was heated to about 55 ° C. to dissolve the solid, and then cooled to about 30 ° C. About 20 mg of seed crystals were added thereto, and the mixture was stirred for 1 hour while maintaining at 20 to 30 ° C. Subsequently, the mixture was cooled to about 3 ° C. over 30 minutes, and further stirred at 0 to 5 ° C. for 2 hours. The slurry was filtered, and the cake was washed with 5 ml of 50% aqueous methanol solution. The cake was taken out and vacuum-dried to obtain 6.6 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 47.9%, and the crystallization yield was 92%. Moreover, the water | moisture content was 11.3%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.8%.
 比較例1
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン20.1g、メタノール130g、水14.2g、および98%硫酸10.2gを仕込んだ。撹拌しながら、約60℃に加熱し、そこにラセミ1-ベンジル-3-アミノピロリジンと硫酸の塩(1水和物)を約50mg添加した。スラリーを50~60℃に保って0.5時間撹拌したのち、1時間かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを濾過し、ケークにメタノール10mlを振りかけて洗浄した。ケークを取り出し、真空乾燥してラセミ1-ベンジル-3-アミノピロリジンと硫酸の塩26.3gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は59.9%であり、晶析収率は89%であった。また、水分は6.1%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析した組成は、1-ベンジル-3-アミノピロリジン98.2%、ベンジルアミン0.4%、4-アミノ-1-ベンジルピペリジン1.4%であった(但し、トルエンは除いて計算した)。
Comparative Example 1
The content of commercially available 1-benzyl-3-aminopyrrolidine is 87.6%, and the composition analyzed by gas chromatography is 91.8% of 1-benzyl-3-aminopyrrolidine, 2.3% of benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 20.1 g, methanol 130 g, water 14.2 g, and 98% sulfuric acid 10.2 g was charged. While stirring, the mixture was heated to about 60 ° C., and about 50 mg of racemic 1-benzyl-3-aminopyrrolidine and sulfuric acid salt (monohydrate) was added thereto. The slurry was kept at 50-60 ° C. and stirred for 0.5 hour, then cooled to about 3 ° C. over 1 hour, and further stirred at 0-5 ° C. for 2 hours. The slurry was filtered, and the cake was washed with 10 ml of methanol. The cake was taken out and vacuum-dried to obtain 26.3 g of racemic 1-benzyl-3-aminopyrrolidine and sulfuric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 59.9%, and the crystallization yield was 89%. Moreover, the water | moisture content was 6.1%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. The composition of the toluene layer analyzed by gas chromatography was 98.2% 1-benzyl-3-aminopyrrolidine, 0.4% benzylamine, and 1.4% 4-amino-1-benzylpiperidine (provided that Calculated excluding toluene).
 比較例2
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン20.0g、エタノール120g、および35%塩酸21.7gを仕込んだ。撹拌しながら、約60℃に加熱して溶解した。溶液を冷却して約23℃とし、そこにラセミ1-ベンジル-3-アミノピロリジンの2塩酸塩を約50mg添加した。スラリーを20~25℃に保って5時間撹拌した。スラリーを濾過し、ケークにエタノール7mlを振りかけて洗浄した。ケークを取り出し、真空乾燥してラセミ1-ベンジル-3-アミノピロリジンと塩酸の塩11.8gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は69.9%であり、晶析収率は47%であった。また。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析した組成は、1-ベンジル-3-アミノピロリジン99.0%、ベンジルアミン0.1%、4-アミノ-1-ベンジルピペリジン0.9%であった(但し、トルエンは除いて計算した)。
Comparative Example 2
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. , 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 20.0 g, ethanol 120 g, and 35% hydrochloric acid 21.7 g It is. While stirring, it was heated to about 60 ° C. to dissolve. The solution was cooled to about 23 ° C., and about 50 mg of racemic 1-benzyl-3-aminopyrrolidine dihydrochloride was added thereto. The slurry was kept at 20-25 ° C. and stirred for 5 hours. The slurry was filtered and washed by sprinkling 7 ml of ethanol on the cake. The cake was taken out and dried under vacuum to obtain 11.8 g of racemic 1-benzyl-3-aminopyrrolidine and hydrochloric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 69.9%, and the crystallization yield was 47%. Also. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. The composition of the toluene layer analyzed by gas chromatography was as follows: 1-benzyl-3-aminopyrrolidine 99.0%, benzylamine 0.1%, 4-amino-1-benzylpiperidine 0.9% (however, Calculated excluding toluene).
 比較例3
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン20.2g、水21.1g、および35%塩酸21.9gを混合したのち約80℃に加熱し、圧力約4.7kPaで水が留出しなくなるまで濃縮した。濃縮液にエタノール100gを加えたのち約80℃に加熱し、再度圧力約4.7kPaで留出しなくなるまで濃縮した。濃縮液にエタノール96gを加え、約20℃まで冷却したのちラセミ1-ベンジル-3-アミノピロリジンの2塩酸塩50mgを添加した。スラリーを1時間かけて約3℃まで冷却し、更に0~5℃で1時間撹拌を続けた。スラリーを濾過し、ケークにエタノール10mlを振りかけて洗浄した。ケークを取り出し、真空乾燥してラセミ1-ベンジル-3-アミノピロリジンと塩酸の塩21.7gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は68.9%であり、晶析収率は85%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析した組成は、1-ベンジル-3-アミノピロリジン98.1%、ベンジルアミン0.3%、4-アミノ-1-ベンジルピペリジン1.5%であった(但し、トルエンは除いて計算した)。
Comparative Example 3
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 20.2 g, water 21.1 g, and 35% hydrochloric acid 21.9 g After mixing, the mixture was heated to about 80 ° C. and concentrated at a pressure of about 4.7 kPa until no water distilled off. After adding 100 g of ethanol to the concentrate, the mixture was heated to about 80 ° C. and concentrated again at a pressure of about 4.7 kPa until no distillation occurred. After adding 96 g of ethanol to the concentrated liquid and cooling to about 20 ° C., 50 mg of racemic 1-benzyl-3-aminopyrrolidine dihydrochloride was added. The slurry was cooled to about 3 ° C. over 1 hour and further stirred at 0-5 ° C. for 1 hour. The slurry was filtered, and the cake was washed with 10 ml of ethanol. The cake was taken out and vacuum-dried to obtain 21.7 g of racemic 1-benzyl-3-aminopyrrolidine and hydrochloric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 68.9%, and the crystallization yield was 85%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. The composition of the toluene layer analyzed by gas chromatography was 98.1% 1-benzyl-3-aminopyrrolidine, 0.3% benzylamine, and 1.5% 4-amino-1-benzylpiperidine (provided that Calculated excluding toluene).
 比較例4
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、エタノール18.0g、およびコハク酸2.4gを仕込んだ。撹拌しながら、20~25℃に保って5時間撹拌した。スラリーを濾過し、ケークにエタノール5mlを振りかけて洗浄した。ケークを取り出し、真空乾燥してラセミ1-ベンジル-3-アミノピロリジンとコハク酸の塩4.8gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は60.3%であり、晶析収率は86%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析した組成は、1-ベンジル-3-アミノピロリジン96.9%、ベンジルアミン0.3%、4-アミノ-1-ベンジルピペリジン2.8%であった(但し、トルエンは除いて計算した)。
Comparative Example 4
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, ethanol 18.0 g, and succinic acid 2.4 g Prepared. While stirring, the mixture was kept at 20 to 25 ° C. and stirred for 5 hours. The slurry was filtered and washed by sprinkling 5 ml of ethanol on the cake. The cake was taken out and dried under vacuum to obtain 4.8 g of a racemic 1-benzyl-3-aminopyrrolidine and succinic acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 60.3%, and the crystallization yield was 86%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. The composition of the toluene layer analyzed by gas chromatography was 96.9% 1-benzyl-3-aminopyrrolidine, 0.3% benzylamine, and 2.8% 4-amino-1-benzylpiperidine (however, Calculated excluding toluene).
 比較例5
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、エタノール18.0g、およびDL-リンゴ酸2.7gを仕込んだ。撹拌しながら、0~5℃に保って12時間撹拌した。析出した結晶は性状の悪い凝集物であり、濾過することができなかった。
Comparative Example 5
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, ethanol 18.0 g, and DL-malic acid 2. 7g was charged. While stirring, the mixture was kept at 0 to 5 ° C. and stirred for 12 hours. The precipitated crystals were aggregates with poor properties and could not be filtered.
 比較例6
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、エタノール8.9g、およびマレイン酸2.4gを仕込んだ。撹拌しながら、0~5℃に保って12時間撹拌したが結晶は析出しなかった。
Comparative Example 6
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, ethanol 8.9 g, and maleic acid 2.4 g. Prepared. While stirring, the mixture was kept at 0-5 ° C. for 12 hours, but no crystals were precipitated.
 比較例7
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、エタノール9.1g、および酢酸2.4gを仕込んだ。撹拌しながら、0~5℃に保って12時間撹拌したが結晶は析出しなかった。
Comparative Example 7
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low-purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, ethanol 9.1 g, and acetic acid 2.4 g It is. While stirring, the mixture was kept at 0-5 ° C. for 12 hours, but no crystals were precipitated.
 比較例8
 メタノールを使用せず、水の使用量を15.5gに変えた以外は実施例2と同じ操作をおこなって、1-ベンジル-3-アミノピロリジンと酒石酸の塩4.6gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は46.9%であり、晶析収率は62%であった。また、水分は13.3%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、1-ベンジル-3-アミノピロリジンの化学純度は100.0%であった(但し、トルエンは除いて計算した)。
Comparative Example 8
The same operation as in Example 2 was performed except that methanol was not used and the amount of water used was changed to 15.5 g, to obtain 4.6 g of a salt of 1-benzyl-3-aminopyrrolidine and tartaric acid. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 46.9%, and the crystallization yield was 62%. Moreover, the water | moisture content was 13.3%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine was 100.0% (note that toluene was excluded).
 比較例9
 市販の、1-ベンジル-3-アミノピロリジンの含有率が87.6%であり、ガスクロマトグラフィーで分析した組成が、1-ベンジル-3-アミノピロリジン91.8%、ベンジルアミン2.3%、4-アミノ-1-ベンジルピペリジン3.8%、その他成分2.1%である純度の低いラセミ1-ベンジル-3-アミノピロリジン3.9g、メタノール7.2、水8.4g、およびD-酒石酸3.1gを仕込んだ。撹拌しながら、約55℃に加熱して固形物を溶解したのち、約30℃まで冷却した。そこに種晶を約20mg添加し、20~30℃に保って1時間撹拌した。次いで、30分かけて約3℃まで冷却し、更に0~5℃で2時間撹拌を続けた。スラリーを濾過し、ケークに50%メタノール水溶液5mlを振りかけて洗浄した。ケークを取り出し、真空乾燥して1-ベンジル-3-アミノピロリジンと酒石酸の塩3.2gを取得した。取得した塩の中の1-ベンジル-3-アミノピロリジンの含有率は47.0%であり、晶析収率は44%であった。また、水分は13.8%であった。容量20mlの蓋付きサンプル瓶に、取得した塩1g、水1g、トルエン1g、および48%水酸化ナトリウム水溶液0.6gを採取して良く振り混ぜた。トルエン層をガスクロマトグラフィーで分析したところ、トルエンを除いて計算した1-ベンジル-3-アミノピロリジンの化学純度は99.9%であった。取得した塩の中の1-ベンジル-3-アミノピロリジンは(R)-体であり、その光学純度は97.0%e.e.であった。
Comparative Example 9
The commercially available 1-benzyl-3-aminopyrrolidine content was 87.6%, and the composition analyzed by gas chromatography was 91.8% 1-benzyl-3-aminopyrrolidine, 2.3% benzylamine. 4-amino-1-benzylpiperidine 3.8%, other components 2.1% low purity racemic 1-benzyl-3-aminopyrrolidine 3.9 g, methanol 7.2, water 8.4 g, and D -Charged 3.1 g of tartaric acid. While stirring, the mixture was heated to about 55 ° C. to dissolve the solid, and then cooled to about 30 ° C. About 20 mg of seed crystals were added thereto, and the mixture was stirred for 1 hour while maintaining at 20 to 30 ° C. Subsequently, the mixture was cooled to about 3 ° C. over 30 minutes, and further stirred at 0 to 5 ° C. for 2 hours. The slurry was filtered, and the cake was washed with 5 ml of 50% aqueous methanol solution. The cake was taken out and vacuum-dried to obtain 3.2 g of 1-benzyl-3-aminopyrrolidine and tartaric acid salt. The content of 1-benzyl-3-aminopyrrolidine in the obtained salt was 47.0%, and the crystallization yield was 44%. The water content was 13.8%. In a sample bottle with a capacity of 20 ml, 1 g of the obtained salt, 1 g of water, 1 g of toluene, and 0.6 g of 48% aqueous sodium hydroxide solution were collected and shaken well. When the toluene layer was analyzed by gas chromatography, the chemical purity of 1-benzyl-3-aminopyrrolidine calculated by removing toluene was 99.9%. 1-Benzyl-3-aminopyrrolidine in the obtained salt is the (R) -form, and its optical purity is 97.0% e.e. e. Met.

Claims (5)

  1. 不純物が混入している化学純度の低い式(1)
    Figure JPOXMLDOC01-appb-C000001
    で表される(R)-1-ベンジル-3-アミノピロリジンと(S)-1-ベンジル-3-アミノピロリジンの混合物とL-酒石酸とD-酒石酸の混合物から塩を形成し、水と混和する有機溶媒と水の混合溶媒中で晶析することを特徴とする高純度1-ベンジル-3-アミノピロリジンの製造方法。
    Formula (1) with low chemical purity that contains impurities
    Figure JPOXMLDOC01-appb-C000001
    A salt is formed from a mixture of (R) -1-benzyl-3-aminopyrrolidine represented by the formula (S) -1-benzyl-3-aminopyrrolidine and a mixture of L-tartaric acid and D-tartaric acid and mixed with water. A method for producing high-purity 1-benzyl-3-aminopyrrolidine characterized by crystallization in a mixed solvent of an organic solvent and water.
  2. (R)-1-ベンジル-3-アミノピロリジンと(S)-1-ベンジル-3-アミノピロリジンの混合物がラセミ1-ベンジル-3-アミノピロリジンであり、L-酒石酸とD-酒石酸の混合物がラセミ酒石酸である請求項1記載の高純度1-ベンジル-3-アミノピロリジンの製造方法。 The mixture of (R) -1-benzyl-3-aminopyrrolidine and (S) -1-benzyl-3-aminopyrrolidine is racemic 1-benzyl-3-aminopyrrolidine, and the mixture of L-tartaric acid and D-tartaric acid is The process for producing high purity 1-benzyl-3-aminopyrrolidine according to claim 1, which is racemic tartaric acid.
  3. (R)-1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルのD-酒石酸と、(S)-1-ベンジル-3-アミノピロリジンに対して0.95~1.15倍モルのL-酒石酸が存在する系で晶析する請求項1記載の高純度1-ベンジル-3-アミノピロリジンの製造方法。 0.95 to 1.15 moles of D-tartaric acid relative to (R) -1-benzyl-3-aminopyrrolidine and 0.95 to 1 relative to (S) -1-benzyl-3-aminopyrrolidine 2. The process for producing high-purity 1-benzyl-3-aminopyrrolidine according to claim 1, wherein the crystallization is carried out in a system containing 15-fold moles of L-tartaric acid.
  4. 1-ベンジル-3-アミノピロリジンに含まれる不純物が塩基性化合物である請求項1記載の高純度1-ベンジル-3-アミノピロリジンの製造方法。 The method for producing high-purity 1-benzyl-3-aminopyrrolidine according to claim 1, wherein the impurity contained in 1-benzyl-3-aminopyrrolidine is a basic compound.
  5. 水と混和する有機溶媒が、メタノール、エタノール、n-プロパノール、2-プロパノール、テトラヒドロフラン、アセトニトリル、アセトン、および/または、これらから選ばれる一種または二種以上の混合液である請求項1記載の高純度1-ベンジル-3-アミノピロリジンの製造方法。 2. The organic solvent miscible with water is methanol, ethanol, n-propanol, 2-propanol, tetrahydrofuran, acetonitrile, acetone, and / or one or a mixture of two or more selected from these. A method for producing 1-benzyl-3-aminopyrrolidine having a purity.
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