JPH0570429A - Production of 3-azabicyclo(3,3,0)octane - Google Patents

Production of 3-azabicyclo(3,3,0)octane

Info

Publication number
JPH0570429A
JPH0570429A JP4044372A JP4437292A JPH0570429A JP H0570429 A JPH0570429 A JP H0570429A JP 4044372 A JP4044372 A JP 4044372A JP 4437292 A JP4437292 A JP 4437292A JP H0570429 A JPH0570429 A JP H0570429A
Authority
JP
Japan
Prior art keywords
azabicyclo
octane
catalyst
catalytic hydrogenation
inert solvent
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
JP4044372A
Other languages
Japanese (ja)
Inventor
Tsunesuke Hirashima
恒亮 平嶋
Ikuzo Nishiguchi
郁三 西口
Yoshio Ishino
義夫 石野
Haruo Kasamatsu
晴夫 笠松
Yoshiaki Iwasaki
義昭 岩崎
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.)
HONSYU KAGAKU KOGYO KK
Honshu Chemical Industry Co Ltd
Osaka City
Original Assignee
HONSYU KAGAKU KOGYO KK
Honshu Chemical Industry Co Ltd
Osaka City
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 HONSYU KAGAKU KOGYO KK, Honshu Chemical Industry Co Ltd, Osaka City filed Critical HONSYU KAGAKU KOGYO KK
Publication of JPH0570429A publication Critical patent/JPH0570429A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Indole Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To easily obtain the title compound in an industrially advantageous way through, so called, one-pot process. CONSTITUTION:A 2-cyano-1-cyclopentenecarboxylic ester is first put to catalytic hydrogenation in an inert solvent in the presence of a Raney catalyst followed by filtering off the catalyst. Thence, the product is further put to catalytic hydrogenation in the same solvent as the above in the presence of copper chromite and an alkali metal oxide or alkaline earth metal oxide to obtain the objective 3-azabicyclo[3,3,0] octane.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、糖尿病、狭心症等の医
薬品の原料として有用である3−アザビシクロ〔3, 3,
0〕オクタン
The present invention relates to 3-azabicyclo [3,3,3] which is useful as a raw material for pharmaceuticals such as diabetes and angina.
0] Octane

【0002】[0002]

【化1】 [Chemical 1]

【0003】の製造方法に関する。The manufacturing method of

【0004】[0004]

【従来の技術】例えば、特開昭50−62971号公報
に記載されているように、2−シアノ−1−シクロペン
テンカルボン酸エステルをイソプロパノール中、アンモ
ニアの存在下にラネーニッケル触媒を用いて、温度60
〜100℃、水素圧17〜20Kg/cm2 の条件下に第1
段の接触水素化を行なつて、3−アザビシクロ〔3, 3,
0〕オクタン−2−オンとし、これを取出し、精製した
後、ジオキサン中、Cu−Ba−CrO 触媒の存在下で温度3
00℃、水素圧130〜140Kg/cm2 の条件下に第2
段の接触水素化を行なつて、3−アザビシクロ〔3, 3,
0〕オクタンを収率39%で得る方法が知られている。
2. Description of the Related Art For example, as described in JP-A No. 50-62971, 2-cyano-1-cyclopentenecarboxylic acid ester in isopropanol in the presence of ammonia using a Raney nickel catalyst at a temperature of 60.
1st under the condition of -100 ℃ and hydrogen pressure of 17-20Kg / cm 2 .
3-azabicyclo [3,3,3,3
0] octane-2-one, and after taking it out and purifying it, dioxane was used in the presence of a Cu—Ba—CrO 2 catalyst at a temperature of
Second under the condition of 00 ℃, hydrogen pressure 130 ~ 140Kg / cm 2.
3-azabicyclo [3,3,3,3
A method is known for obtaining [0] octane with a yield of 39%.

【0005】しかし、この方法は、このように、一旦、
反応混合物から生成物を取出し、精製した後、これを別
の溶媒中で再度、接触水素化するものである。更に、上
記の方法においては、第1段の接触水素化にて得た反応
混合物をそのまま、第2段の接触水素化に用いるとき
は、N−アルキル化物が生成するおそれがあるので、第
2段の接触水素化においては、第1段における溶媒であ
るイソプロパノールを用いることができない。
However, this method is
The product is taken out from the reaction mixture, purified, and then catalytically hydrogenated again in another solvent. Furthermore, in the above method, when the reaction mixture obtained in the first-stage catalytic hydrogenation is used as it is in the second-stage catalytic hydrogenation, an N-alkylated product may be produced. In the catalytic hydrogenation of the stage, the solvent in the first stage, isopropanol, cannot be used.

【0006】また、上記公報には、3−アザビシクロ
〔3, 3, 0〕オクタン−2−オンをテトラヒドロフラン
中、ジボランにて還元する方法も記載されている。しか
し、ジボランは高価であるうえに、水分との接触によつ
て発火する等、取扱いに特別の注意を必要とする。
The above publication also describes a method of reducing 3-azabicyclo [3,3,0] octane-2-one with diborane in tetrahydrofuran. However, diborane is expensive and requires special handling, such as ignition due to contact with moisture.

【0007】[0007]

【発明が解決しようとする課題】本発明者らは、上記し
たような3−アザビシクロ〔3, 3, 0〕オクタンの従来
の製造における問題を解決するために鋭意研究した結
果、2−シアノ−1−シクロペンテンカルボン酸エステ
ルを不活性溶媒中、ラネー系触媒の存在下に接触水素化
した後、触媒を濾別し、引き続いて、前記と同じ不活性
溶媒中にて、亜クロム酸銅と、アルカリ金属酸化物又は
アルカリ土類金属酸化物との存在下に更に接触水素化す
ることによつて、工業的に有利に且つ容易に3−アザビ
シクロ〔3, 3, 0〕オクタンを製造し得ることを見出し
て、本発明に至つたものである。
DISCLOSURE OF INVENTION Problems to be Solved by the Invention The present inventors have earnestly studied to solve the problems in the conventional production of 3-azabicyclo [3,3,0] octane as described above, and as a result, 2-cyano- After catalytic hydrogenation of 1-cyclopentenecarboxylic acid ester in an inert solvent in the presence of a Raney catalyst, the catalyst is filtered off, and subsequently, in the same inert solvent as above, with copper chromite, Industrially advantageous and easy production of 3-azabicyclo [3,3,0] octane by further catalytic hydrogenation in the presence of an alkali metal oxide or an alkaline earth metal oxide. That is, the present invention has been achieved.

【0008】[0008]

【課題を解決するための手段】本発明による3−アザビ
シクロ〔3, 3, 0〕オクタンの製造方法は、2−シアノ
−1−シクロペンテンカルボン酸エステルを不活性溶媒
中、ラネー系触媒の存在下に接触水素化した後、触媒を
濾別し、引き続いて、前記と同じ不活性溶媒中にて亜ク
ロム酸銅と、アルカリ金属酸化物又はアルカリ土類金属
酸化物との存在下に更に接触水素化することを特徴とす
る。
The method for producing 3-azabicyclo [3,3,0] octane according to the present invention comprises a 2-cyano-1-cyclopentenecarboxylic acid ester in an inert solvent in the presence of a Raney catalyst. After catalytic hydrogenation, the catalyst is filtered off, followed by further catalytic hydrogenation in the presence of copper chromite and an alkali metal oxide or alkaline earth metal oxide in the same inert solvent as above. It is characterized by

【0009】本発明の方法において用いる2−シアノ−
1−シクロペンテンカルボン酸エステルは、通常、アル
キルエステルが好ましく、特に、メチルエステル又はエ
チルエステルが好ましい。本発明の方法において、2−
シアノ−1−シクロペンテンカルボン酸エステルの接触
水素化(第1段の接触水素化)は、ジオキサン、シクロ
ヘキサン等の不活性溶媒中で行なわれる。
2-cyano-used in the method of the present invention
The 1-cyclopentenecarboxylic acid ester is usually preferably an alkyl ester, and particularly preferably a methyl ester or an ethyl ester. In the method of the present invention, 2-
Catalytic hydrogenation of cyano-1-cyclopentenecarboxylic acid ester (first stage catalytic hydrogenation) is carried out in an inert solvent such as dioxane or cyclohexane.

【0010】この第1段の接触水素化は、かかる不活性
溶媒中、アンモニアや、或いは水酸化ナトリウム、水酸
化カルシウム等のようなアルカリ金属水酸化物やアルカ
リ土類金属水酸化物のような塩基の存在下に、ラネーニ
ッケル、ラネーコバルト等のラネー系触媒を用いて、温
度50〜280℃、圧力10〜200Kg/cm2 、好まし
くは、温度100〜200℃、圧力20〜100Kg/cm
2 の条件下に行なわれる。
This first-stage catalytic hydrogenation is carried out in such an inert solvent as ammonia, alkali metal hydroxides such as sodium hydroxide or calcium hydroxide, or alkaline earth metal hydroxides. In the presence of a base, using a Raney catalyst such as Raney nickel or Raney cobalt, a temperature of 50 to 280 ° C., a pressure of 10 to 200 Kg / cm 2 , preferably a temperature of 100 to 200 ° C., a pressure of 20 to 100 Kg / cm.
It is performed under the conditions of 2 .

【0011】本発明の方法によれば、このようにして、
第1段の接触水素化を行なつた後、用いた触媒を濾別
し、引き続いて、前記と同じ不活性溶媒中で第2段の接
触水素化を行なう。この第2段の接触水素化において
は、酸化ナトリウム、酸化カルシウム等のようなアルカ
リ金属酸化物又はアルカリ土類金属酸化物の存在下に、
亜クロム酸銅触媒を用いて、温度150〜280℃、圧
力100〜250Kg/cm2 、好ましくは、温度200〜
250℃、圧力150〜200Kg/cm2 の条件下に行な
われる。
According to the method of the present invention, in this way,
After carrying out the first-stage catalytic hydrogenation, the catalyst used is filtered off and subsequently the second-stage catalytic hydrogenation is carried out in the same inert solvent as described above. In this second stage catalytic hydrogenation, in the presence of alkali metal oxides or alkaline earth metal oxides such as sodium oxide, calcium oxide, etc.,
Using a copper chromite catalyst, a temperature of 150 to 280 ° C., a pressure of 100 to 250 kg / cm 2 , preferably a temperature of 200 to
It is carried out under the conditions of 250 ° C. and a pressure of 150 to 200 kg / cm 2 .

【0012】かかる本発明の方法によれば、所謂ワン・
ポット反応によつて、3−アザビシクロ〔3, 3, 0〕オ
クタンを得ることができる。
According to the method of the present invention, a so-called one
The 3-azabicyclo [3,3,0] octane can be obtained by the pot reaction.

【0013】[0013]

【実施例】以下に実施例を挙げて本発明を説明するが、
本発明はこれら実施例により何ら限定されるものではな
い。 実施例1 2−シアノ−1−シクロペンテンカルボン酸メチル5.0
gをジオキサン50.0gと濃アンモニア水2.15gとの
混合物に溶解させ、ラネーニッケルの存在下、温度20
0℃、水素圧50Kg/cm2 の条件下に、副生するメタノ
ールを留去しながら、4時間攪拌した。反応終了後、触
媒を濾別し、反応液を得た。
The present invention will be described below with reference to examples.
The present invention is not limited to these examples. Example 1 Methyl 2-cyano-1-cyclopentenecarboxylate 5.0
g was dissolved in a mixture of 5.0 g of dioxane and 2.15 g of concentrated aqueous ammonia, and the temperature was adjusted to 20 in the presence of Raney nickel.
The mixture was stirred at 0 ° C. and hydrogen pressure of 50 kg / cm 2 for 4 hours while distilling off by-produced methanol. After completion of the reaction, the catalyst was filtered off to obtain a reaction solution.

【0014】次いで、ジオキサン21.0gに亜クロム酸
銅2.50gと酸化カルシウム5.32gを懸濁させた溶液
を上記反応液に加え、温度250℃、水素圧150Kg/
cm2 の条件下に4時間攪拌した。得られた反応液から触
媒を濾別し、溶媒を留去した後、反応混合物を蒸留し
て、3−アザビシクロ〔3, 3, 0〕オクタン1.69g
(収率39.7%)を得た。 沸点: 97℃/143mmHg GC-MS: m/z=111 λmax (cm-1): 3250 (NH), 2910, 1445, 1080, 855, 8
30 実施例2 2−シアノ−1−シクロペンテンカルボン酸メチル4.5
gをシクロヘキサン60.0gと液体アンモニア0.45g
との混合物に溶解させ、ラネーコバルトの存在下、温度
200℃、水素圧80Kg/cm2 の条件下に、副生するメ
タノールを留去しながら、5時間攪拌した。反応終了
後、触媒を濾別し、反応液を得た。
Then, a solution prepared by suspending 2.50 g of copper chromite and 5.32 g of calcium oxide in 21.0 g of dioxane was added to the above reaction solution, and the temperature was 250 ° C. and the hydrogen pressure was 150 kg /.
The mixture was stirred under cm 2 for 4 hours. The catalyst was filtered off from the resulting reaction solution, the solvent was distilled off, and the reaction mixture was distilled to give 1.69 g of 3-azabicyclo [3,3,0] octane.
(Yield 39.7%) was obtained. Boiling point: 97 ℃ / 143mmHg GC-MS: m / z = 111 λ max (cm -1 ): 3250 (NH), 2910, 1445, 1080, 855, 8
30 Example 2 Methyl 2-cyano-1-cyclopentenecarboxylate 4.5
g of cyclohexane 60.0 g and liquid ammonia 0.45 g
The mixture was dissolved in a mixture of and, and the mixture was stirred for 5 hours in the presence of Raney cobalt at a temperature of 200 ° C. and a hydrogen pressure of 80 kg / cm 2 while distilling off by-produced methanol. After completion of the reaction, the catalyst was filtered off to obtain a reaction solution.

【0015】次いで、得られた反応液に亜クロム酸銅1.
35gと酸化ナトリウム1.00gを加え、温度250
℃、水素圧160Kg/cm2 の条件下に4時間攪拌した。
得られた反応液から触媒を濾別し、溶媒を留去した後、
反応混合物を蒸留して、3−アザビシクロ〔3, 3, 0〕
オクタン1.12g(収率30.6%)を得た。 実施例3 2−シアノ−1−シクロペンテンカルボン酸エチル7.0
gをジオキサン70.0gと40%水酸化ナトリウム水溶
液4.12gとの混合物に溶解させ、ラネーニッケルの存
在下、温度190℃、水素圧50Kg/cm2 の条件下に、
副生するエタノールを留去しながら、8時間攪拌した。
反応終了後、触媒を濾別し、反応液を得た。
Then, copper chromite 1.
Add 35 g and 1.00 g of sodium oxide, and add 250
The mixture was stirred for 4 hours under the condition of ℃ and hydrogen pressure of 160 kg / cm 2 .
After the catalyst was filtered off from the obtained reaction solution and the solvent was distilled off,
The reaction mixture was distilled to give 3-azabicyclo [3,3,0]
1.12 g of octane (yield 30.6%) was obtained. Example 3 Ethyl 2-cyano-1-cyclopentenecarboxylate 7.0
g was dissolved in a mixture of dioxane 70.0 g and 40% sodium hydroxide aqueous solution 4.12 g, and in the presence of Raney nickel at a temperature of 190 ° C. and a hydrogen pressure of 50 kg / cm 2 ,
The mixture was stirred for 8 hours while distilling off by-product ethanol.
After completion of the reaction, the catalyst was filtered off to obtain a reaction solution.

【0016】次いで、ジオキサン30.0gに亜クロム酸
銅2.81gと酸化カルシウム4.59gを懸濁させた溶液
を上記反応液に加え、温度250℃、水素圧170Kg/
cm2 の条件下に6時間攪拌した。得られた反応液から触
媒を濾別し、溶媒を留去した後、反応混合物を蒸留し
て、3−アザビシクロ〔3, 3, 0〕オクタン1.82g
(収率33.8%)を得た。
Next, a solution prepared by suspending 2.81 g of copper chromite and 4.59 g of calcium oxide in 30.0 g of dioxane was added to the above reaction solution, and the temperature was 250 ° C. and the hydrogen pressure was 170 kg /.
The mixture was stirred for 6 hours under the condition of cm 2 . The catalyst was filtered off from the resulting reaction solution, the solvent was distilled off, and the reaction mixture was distilled to obtain 1.82 g of 3-azabicyclo [3,3,0] octane.
(Yield 33.8%) was obtained.

【0017】[0017]

【発明の効果】本発明の方法によれば、2−シアノ−1
−シクロペンテンカルボン酸エステルを不活性溶媒中、
ラネー系触媒の存在下に接触水素化した後、触媒を濾別
し、次いで、前記と同じ溶媒中にて、亜クロム酸銅と、
アルカリ金属酸化物又はアルカリ土類金属酸化物との存
在下に更に接触水素化することによつて、3−アザビシ
クロ〔3, 3, 0〕オクタンを得ることができる。従つ
て、本発明の方法によれば、所謂ワン・ポツト反応によ
つて、簡単に3−アザビシクロ〔3, 3, 0〕オクタンを
得ることができる。
According to the method of the present invention, 2-cyano-1
-Cyclopentenecarboxylic acid ester in an inert solvent,
After catalytic hydrogenation in the presence of a Raney catalyst, the catalyst is filtered off, then in the same solvent as above, with copper chromite,
By further catalytic hydrogenation in the presence of alkali metal oxides or alkaline earth metal oxides, 3-azabicyclo [3,3,0] octane can be obtained. Therefore, according to the method of the present invention, 3-azabicyclo [3,3,0] octane can be easily obtained by the so-called one-pot reaction.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 笠松 晴夫 和歌山県那賀郡貴志川町長山563番地 (72)発明者 岩崎 義昭 和歌山県和歌山市宇須3丁目3番39号 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Haruo Kasamatsu Inventor, 563 Nagayama, Kishigawa-cho, Naga-gun, Wakayama Prefecture (72) Yoshiaki Iwasaki 3-39 Usu, Wakayama City, Wakayama Prefecture

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】2−シアノ−1−シクロペンテンカルボン
酸エステルを不活性溶媒中、ラネー系触媒の存在下に接
触水素化した後、触媒を濾別し、引き続いて、前記と同
じ不活性溶媒中にて亜クロム酸銅と、アルカリ金属酸化
物又はアルカリ土類金属酸化物との存在下に更に接触水
素化することを特徴とする3−アザビシクロ〔3, 3,
0〕オクタンの製造方法。
1. A 2-cyano-1-cyclopentenecarboxylic acid ester is catalytically hydrogenated in an inert solvent in the presence of a Raney catalyst, then the catalyst is filtered off, and subsequently in the same inert solvent as described above. Copper chromite and further catalytic hydrogenation in the presence of an alkali metal oxide or an alkaline earth metal oxide, 3-azabicyclo [3,3,3]
0] A method for producing octane.
【請求項2】不活性溶媒がジオキサン又はシクロヘキサ
ンであることを特徴とする請求項1記載の3−アザビシ
クロ〔3, 3, 0〕オクタンの製造方法。
2. The method for producing 3-azabicyclo [3,3,0] octane according to claim 1, wherein the inert solvent is dioxane or cyclohexane.
JP4044372A 1991-03-14 1992-03-02 Production of 3-azabicyclo(3,3,0)octane Pending JPH0570429A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP3-49724 1991-03-14
JP4972491 1991-03-14

Publications (1)

Publication Number Publication Date
JPH0570429A true JPH0570429A (en) 1993-03-23

Family

ID=12839137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4044372A Pending JPH0570429A (en) 1991-03-14 1992-03-02 Production of 3-azabicyclo(3,3,0)octane

Country Status (1)

Country Link
JP (1) JPH0570429A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005049568A1 (en) * 2003-11-24 2005-06-02 Potluri Ramesh Babu A process for industrially viable preparation of (s,s,s) phenylmethyl-2-azabicyclo-[3.3.0]-octane-3-carboxylate tosylate
WO2013102634A1 (en) 2012-01-06 2013-07-11 Lonza Ltd Method for preparation of octahydrocyclopenta[c]pyrrole

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005049568A1 (en) * 2003-11-24 2005-06-02 Potluri Ramesh Babu A process for industrially viable preparation of (s,s,s) phenylmethyl-2-azabicyclo-[3.3.0]-octane-3-carboxylate tosylate
WO2013102634A1 (en) 2012-01-06 2013-07-11 Lonza Ltd Method for preparation of octahydrocyclopenta[c]pyrrole
JP2015509089A (en) * 2012-01-06 2015-03-26 ロンザ リミテッドLonza Limited Method for producing octahydrocyclopenta [c] pyrrole
US9126930B2 (en) 2012-01-06 2015-09-08 Lonza Ltd. Method for preparation of octahydrocyclopenta[c]pyrrole

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