JPS5936668A - Preparation of piperazine derivative - Google Patents

Preparation of piperazine derivative

Info

Publication number
JPS5936668A
JPS5936668A JP14598882A JP14598882A JPS5936668A JP S5936668 A JPS5936668 A JP S5936668A JP 14598882 A JP14598882 A JP 14598882A JP 14598882 A JP14598882 A JP 14598882A JP S5936668 A JPS5936668 A JP S5936668A
Authority
JP
Japan
Prior art keywords
temperature
aqueous phase
reaction
crystals
carried out
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.)
Pending
Application number
JP14598882A
Other languages
Japanese (ja)
Inventor
Mitsuhiko Tamura
田村 光彦
Haruo Katsumata
勝俣 晴雄
Tsutomu Yonekura
米倉 務
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.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP14598882A priority Critical patent/JPS5936668A/en
Publication of JPS5936668A publication Critical patent/JPS5936668A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prepare the titled compound, economically, by reacting the piperazinocarbonyl chloride corresponding to the objective compound with a glycine derivative under specific condition, separating the reaction liquid into two phases, and precipitating the compound from the aqueous phase with an acid, wherein said processes are carried out at specific reaction temperature and acid precipitation temperature. CONSTITUTION:4-Ethyl-2,3-dioxopiperazinocarbonyl chloride is made to react with p-hydroxyphenyl glycine in the presence of a base in a mixture of an organic solvent and water at relatively low temperature, i.e. -10-+15 deg.C, preferably -5-+10 deg.C. The reaction mixture if separated into the aqueous phase and the oily phase, and the recovered aqueous phase is made acidic to precipitate the piperazine derivative of formula at 15-80 deg.C, preferably 20-60 deg.C. The objective derivative is useful as an intermediate of antibiotic substance, and is obtained as flowable crystals extremely suitable for the operations such as filtration, washing, etc.

Description

【発明の詳細な説明】 本発明はピペラジン誘導体の製造法に関するものであり
、詳しくは下記構造式 で示されるピペラジン誘導体の製造法に関する亀のであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a piperazine derivative, and more particularly to a method for producing a piperazine derivative represented by the following structural formula.

前足構造式のピペラジン誘導体は例えば、抗生物質の中
間体として有用なものであり、通常、ダーエチルーコ、
3−ジオキソピペラジノカルボニルクロリド(以下、F
!DPOと略称する)とp−ヒドロキシフェニルグリシ
y(以下、HPGと略称する)とを塩基の存在下、有機
溶媒及び水との混合物中で反応させ、次いで、得られた
混合物を水相と油相とに分液し、回収された水相を酸析
することにより製造される。(例えば、特公昭j!−1
.t?’F号公報参照)この方法ではKDPOとHPG
との反応の際に、温度をあまり高くすると目的とするピ
ペラジン誘導体を収率よく得ることができないので、通
常、反応系内を一10〜/!′Cと比較的低温に保持し
て反応を行なうことが望ましい。しかしながら、このよ
うに低温で反応を行なった場合には、引き続く反応混合
物の分液工程及び酸析工程も反応温度と同程度の低温で
実施されることとなるが。
Piperazine derivatives with the forepaw structural formula are useful, for example, as intermediates for antibiotics, and are usually
3-dioxopiperazinocarbonyl chloride (hereinafter referred to as F
! (abbreviated as DPO) and p-hydroxyphenylglycyl (hereinafter abbreviated as HPG) are reacted in a mixture of an organic solvent and water in the presence of a base, and then the resulting mixture is mixed into an aqueous phase and an oil phase. It is produced by separating the aqueous phase into two phases and precipitating the recovered aqueous phase with acid. (For example, Tokuko Shoj!-1
.. T? (Refer to Publication No. F) In this method, KDPO and HPG
If the temperature is too high during the reaction, the desired piperazine derivative cannot be obtained in good yield. It is desirable to carry out the reaction with 'C at a relatively low temperature. However, when the reaction is carried out at such a low temperature, the subsequent liquid separation step and acid precipitation step for the reaction mixture are also carried out at a low temperature comparable to the reaction temperature.

酸析を−10−/j℃の温度範囲で実施した場合には、
得られる目的化合物の結晶がサラサラとならず、油状物
が凝固した様なガム状物となる傾向がある。このように
、ガム状物が生成した場合には、結晶の攪拌及びr過・
洗浄などの操作に著しい困難をきたす。
When acid precipitation is carried out in the temperature range of -10-/j℃,
The crystals of the target compound obtained do not become smooth and tend to form a gummy substance that looks like a solidified oil. In this way, if a gum-like substance is formed, stir the crystals and filtrate.
This makes cleaning and other operations extremely difficult.

本発明者等は上記実情に鑑み、FiDPOとHPGとの
反応を一10〜15℃の温度で行なった場合に、酸析工
程でサラサラの良好な結晶を回収する方法につき種々検
討した結果、酸析をある特定の温度で行なうことによ゛
り本発明の目的が達成されることを見い出し本発明を完
成した。
In view of the above-mentioned circumstances, the present inventors have conducted various studies on methods for recovering smooth crystals in the acid precipitation step when the reaction between FiDPO and HPG is carried out at a temperature of -10 to 15°C. The present invention was completed based on the discovery that the object of the present invention can be achieved by conducting the analysis at a specific temperature.

すなわち、本発明の要旨は、IDPOとHPGとを塩基
の存在下、有機溶媒及び水との混合物中にて反応させ、
次いで、水相と油相とを分離し、得られる水相から酸性
下に結晶を析出させることにより前足構造式のピペラジ
ン誘導体を製造する方法において、反応を−io℃〜/
j℃未満の温度で行ない、しかも、結晶の析出を7!r
−ざ0℃の温度で行なうことを特徴とするピペラジン誘
導体の製造法に存する。
That is, the gist of the present invention is to react IDPO and HPG in the presence of a base in a mixture with an organic solvent and water,
Next, in a method for producing a piperazine derivative having a forefoot structural formula by separating an aqueous phase and an oil phase and precipitating crystals from the resulting aqueous phase under acidic conditions, the reaction is carried out at -io℃~/
It is carried out at a temperature of less than J℃, and the precipitation of crystals is 7! r
- A method for producing a piperazine derivative, characterized in that the process is carried out at a temperature of 0°C.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明はKDPOとHPGとを塩基の存在下で反応させ
るものであるが、原料として用いるF!DPOは通常、
/−エチル−コツ3−ジオキソピペラジンを第3級アミ
ンの存在下、トリメチルクロロシランと反応させ、次い
で、得られた生成物をホスゲンと反応させることにより
容易に得ることができる。一方、HPGは通常の市阪品
を用いることができる。BDPO,!:HPGの使用量
は通常、]1fDPO1モルに対し、0.7〜7.3モ
ルのHPGが使用される。
In the present invention, KDPO and HPG are reacted in the presence of a base, and F! DPOs are usually
/-Ethyl-cotton 3-dioxopiperazine can be easily obtained by reacting with trimethylchlorosilane in the presence of a tertiary amine and then reacting the resulting product with phosgene. On the other hand, for HPG, a normal Ichisaka product can be used. BDPO,! :The amount of HPG used is usually 0.7 to 7.3 mol per 1 mol of 1fDPO.

1npcとHP()の反応により塩化水素が副生するが
、本発明ではこの塩化水素を中和するため、塩基の存在
下で反応が行なわれる。この塩基の種類としては、通常
、アルカリ金属の水酸化物、炭酸塩、重炭酸塩又はトリ
エチルアミン、N−メチルピペリジン、ジエチルアミン
などの有機塩基が挙げられる。塩基の使用量は通常、反
応系内のpHが7〜//に保持されるように用いられる
The reaction between 1npc and HP() produces hydrogen chloride as a by-product, but in the present invention, the reaction is carried out in the presence of a base in order to neutralize this hydrogen chloride. The type of base typically includes alkali metal hydroxides, carbonates, bicarbonates or organic bases such as triethylamine, N-methylpiperidine, diethylamine, and the like. The amount of base used is usually such that the pH within the reaction system is maintained at 7 to 1/2.

本発明の反応は水性媒体中で実施され、水性媒体の使用
量は通常、EDPOとHPGの混合物に対して、λ〜I
O重量倍である。しかし、本発明の反応の場合、原料の
mnpcは有機溶媒の溶液として用いられるので、反応
は有機溶媒−水の混合物中にて実施されることとなる。
The reaction of the present invention is carried out in an aqueous medium, and the amount of aqueous medium used is usually between λ and I for the mixture of EDPO and HPG.
O weight times. However, in the case of the reaction of the present invention, mnpc as a raw material is used as a solution in an organic solvent, so the reaction is carried out in a mixture of organic solvent and water.

この際の有機溶媒の割合は通常、水に対して、O,S−
一重量倍の範囲である。原料1rDpaを溶解する有機
溶媒としては、通常、二塩化エチレン、塩化メチレン、
トルエン、酢酸エチルなどの水不溶性の有機溶媒である
In this case, the ratio of organic solvent to water is usually O, S-
It is in the range of 1 times the weight. The organic solvent for dissolving the raw material 1rDpa usually includes ethylene dichloride, methylene chloride,
Water-insoluble organic solvents such as toluene and ethyl acetate.

反応温度は一り0℃〜/&’C未満、好ましく 5− は−5〜10℃であり、この温度があまり高い場合には
、PDPOとHPGとの反応が良好に進行せず、目的と
するピペラジン誘導体を収率よく得ることはできず、ま
た、あまり低い場合には、水性媒体が凍結するので好ま
しくない。
The reaction temperature is 0°C to less than 10°C, preferably -5 to 10°C; if this temperature is too high, the reaction between PDPO and HPG will not proceed well and the objective will not be achieved. It is not possible to obtain a piperazine derivative with a high yield, and if the yield is too low, the aqueous medium will freeze, which is not preferable.

反応時間は前記温度において、/〜5時間程度である。The reaction time is about 5 hours at the above temperature.

上述の反応は回分式又は連続式で実施できるが、例えば
、回分式にて実施する場合には、例えば、反応器に所定
量のHPGを懸濁させた水媒体を仕込み、これを一定温
度に保持し、攪拌下、1!IDPOの有機溶媒溶液とア
ルカリとを滴下することにより実施することができる。
The above reaction can be carried out batchwise or continuously. For example, when carrying out batchwise, for example, an aqueous medium in which a predetermined amount of HPG is suspended is charged into a reactor, and the aqueous medium is heated to a constant temperature. Hold and stir, 1! This can be carried out by dropping a solution of IDPO in an organic solvent and an alkali.

反応後の混合物は目的とするピペラジン誘導体のアルカ
リ塩を溶解する水相と有機溶媒よりなる油相からなって
いるので、通常の分液法により水相と油相とを分離し、
そして、水相を酸析することにより目的化合物の結晶を
回収する。
The mixture after the reaction consists of an aqueous phase in which the alkali salt of the desired piperazine derivative is dissolved and an oil phase consisting of an organic solvent.
Then, crystals of the target compound are recovered by acid precipitation of the aqueous phase.

酸析に用いる酸としては、通常、塩酸、硫酸、硝酸など
の鉱酸が挙げられ、その使用量は通常、 6− 系内のpHが2以下となるまで添加される。この酸析で
は酸の添加により、すぐに結晶が析出しないので、通常
、酸の添加後、/−&時間の熟成が必要であり、この熟
成により結晶が次第に析出するのである。
The acid used for acid precipitation usually includes mineral acids such as hydrochloric acid, sulfuric acid, and nitric acid, and the amount used is usually added until the pH in the system becomes 2 or less. In this acid precipitation, crystals do not precipitate immediately due to the addition of acid, so it is usually necessary to ripen for /-& hours after addition of acid, and crystals gradually precipitate due to this ripening.

本発明においては、結晶が析出するときの温度を13〜
go℃、好ましくは20〜AO℃に保持することを必須
の要件とするものである。
In the present invention, the temperature at which crystals precipitate is set at 13 to
It is an essential requirement to maintain the temperature at goC, preferably 20 to AOC.

この温度が前記温度範囲よりも低い場合には、油状物が
凝固した様なガム状物が生成し、また、前記温度範囲よ
りも高い場合には、目的とするピペラジン誘導体の水へ
の溶解度が大きくなり結晶の回収率が低下するので好ま
しくない。上記温度範囲で結晶の析出を行なう時は、0
〜10℃という低温で実施する場合とほとんど同一の回
収率で結晶を取得することができる。
If this temperature is lower than the above temperature range, a gummy substance like solidified oil will be produced, and if it is higher than the above temperature range, the solubility of the desired piperazine derivative in water will be reduced. This is not preferable because the crystal size increases and the recovery rate of crystals decreases. When crystal precipitation is performed in the above temperature range, 0
Crystals can be obtained with almost the same recovery as when carried out at lower temperatures of ~10°C.

酸析後の混合物は常法に従って、結晶な濾過し分離した
のち、結晶を必要に応じて水洗し、次いで、乾燥するこ
とにより回収することができる。
The mixture after acid precipitation can be recovered by filtering and separating the crystals according to a conventional method, washing the crystals with water as necessary, and then drying.

 7一 本発明ではKDPOとHPGとを一70〜/S℃未満と
比較的低温で反応させ、しかも、結晶の析出温度を/、
!;−gO℃と反応温度よりも高めて行なうことにより
、酸性下で析出する結晶がガム状にならず、サラサラと
した良好な結晶を得ることができるので、本発明は工業
的に濾過・洗浄等の操作上、極めて好ましい方法である
71 In the present invention, KDPO and HPG are reacted at a relatively low temperature of -70 to less than /S °C, and the crystal precipitation temperature is /,
! By conducting the reaction at -gO°C higher than the reaction temperature, the crystals that precipitate under acidic conditions do not become gummy and good smooth crystals can be obtained. This is an extremely preferable method in terms of operations.

次に、本発明を実施例により更に詳細に説明するが、本
発明はその要旨を越えない限り以下の実施例に限定され
るものではない。
Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to the following Examples unless the gist thereof is exceeded.

実施例1〜3及び比較例/〜コ 攪拌機及び温度調節器を有する反応器に、HP a 1
ttr、2f (/モ/l/)を含有する水/r004
及びトリエチルアミン2Ai、3 f!−を仕込み、系
内の温度をθ℃に調節し、次いで、これに、同温度でK
DPO20I1./、 y−(1モル)を含有する二塩
化エチレン100θd及びトリエチルアミン−〇&、!
 fを反応系内のpi(をデ、3に保持しながら、攪拌
下、2時間かけて滴下し、更に、7時 8− 間攪拌を続は反応を行なった。反応混合物は次いで、静
置し水相と油相とを分液した。
Examples 1 to 3 and Comparative Examples
Water containing ttr, 2f (/mo/l/)/r004
and triethylamine 2Ai, 3 f! -, adjust the temperature in the system to θ℃, and then add K at the same temperature.
DPO20I1. /, y-(1 mol) of ethylene dichloride 100θd and triethylamine-〇&,!
f was added dropwise to the reaction system over 2 hours with stirring while maintaining the pi in the reaction system at 3, and the reaction was continued with further stirring for 7 to 8 hours. Then, the aqueous phase and oil phase were separated.

上述のようにして得た水相を温度調節器を有する攪拌容
器に移し、第1表に示す温度に調節したのち、月〕塩酸
、23ざIを攪拌下、徐々に加え系内のpHをl以下と
し、更に、3時間保持することにより酸析を行なった。
The aqueous phase obtained as described above was transferred to a stirring vessel equipped with a temperature controller, and the temperature was adjusted to the temperature shown in Table 1. Hydrochloric acid, 23% I, was gradually added under stirring to adjust the pH in the system. Acid precipitation was carried out by holding the solution for 3 hours.

この酸析により析出した前足構造式のピペラジン誘導体
の結晶の状轢を観察し、第1表に示す結果を得た。
The state of the crystals of the piperazine derivative having the forefoot structural formula precipitated by this acid precipitation was observed, and the results shown in Table 1 were obtained.

第1表  9− グラスフィルターによりP週・洗浄し、目的生成物の結
晶を回収したが、比較例1〜コで得られた酸析混合物は
全体が一塊となったガム状物でありグラスフィルターに
かけることができなかったので、デカンテーションによ
り母液ヲパージし、目的生成物の結晶を回収した。ガム
状′物についてはそのまま洗浄することができず事前に
繁雑な粉砕処理が必要であった。これらの結晶につき、
目的生成物の回収率を測定したところ、それぞれ、はぼ
同様であり差異はなかった。
Table 1 9 - Crystals of the desired product were collected by washing with a glass filter for P weeks, but the acid precipitation mixture obtained in Comparative Examples 1 to 1 was a gummy substance that was completely lumped into a glass filter. The mother liquor was purged by decantation, and crystals of the desired product were collected. Gum-like substances cannot be washed as they are, and require a complicated crushing process in advance. For these crystals,
When the recovery rates of the target products were measured, they were almost the same and there was no difference.

出 願 人  三菱化成工業株式会社 代 理 人  弁理士 長谷用  − (ほか1名) 1 10−Sender: Mitsubishi Chemical Industries, Ltd. Representative Patent Attorney Hase - (1 other person) 1 10-

Claims (1)

【特許請求の範囲】[Claims] +11 41−エチルーー、3−ジオキソピペラジノカ
ルボニルクロリドとp−ヒドロキシフェニルグリシンと
を塩基の存在下、有機溶媒及び水との混合物中にて反応
させ、次いで、水相と油相とを分離し、得られる水相か
ら酸性下に結晶を析出させることによ抄、下記構造式で
示されるピペラジン誘導体を製造する方法において、反
応を−lθ℃〜/j℃未満の温度で行ない、しかも、結
晶の析出を13〜10℃の温度で行なうことを特徴とす
るピペラジン誘導体の製造法。
+11 41-Ethyl-3-dioxopiperazinocarbonyl chloride and p-hydroxyphenylglycine are reacted in the presence of a base in a mixture of an organic solvent and water, and then the aqueous phase and oil phase are separated. In a method for producing a piperazine derivative represented by the following structural formula by precipitating crystals from the resulting aqueous phase under acidic conditions, the reaction is carried out at a temperature of -lθ°C to less than /j°C, and the crystals are precipitated under acidic conditions. A method for producing a piperazine derivative, characterized in that the precipitation is carried out at a temperature of 13 to 10°C.
JP14598882A 1982-08-23 1982-08-23 Preparation of piperazine derivative Pending JPS5936668A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14598882A JPS5936668A (en) 1982-08-23 1982-08-23 Preparation of piperazine derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14598882A JPS5936668A (en) 1982-08-23 1982-08-23 Preparation of piperazine derivative

Publications (1)

Publication Number Publication Date
JPS5936668A true JPS5936668A (en) 1984-02-28

Family

ID=15397582

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14598882A Pending JPS5936668A (en) 1982-08-23 1982-08-23 Preparation of piperazine derivative

Country Status (1)

Country Link
JP (1) JPS5936668A (en)

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