JPS6289660A - Production of 4-oxo-4,5,6,7-tetrahydroindole - Google Patents

Production of 4-oxo-4,5,6,7-tetrahydroindole

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Publication number
JPS6289660A
JPS6289660A JP23068585A JP23068585A JPS6289660A JP S6289660 A JPS6289660 A JP S6289660A JP 23068585 A JP23068585 A JP 23068585A JP 23068585 A JP23068585 A JP 23068585A JP S6289660 A JPS6289660 A JP S6289660A
Authority
JP
Japan
Prior art keywords
reaction
ammonia
cyclohexanedione
oxo
acetate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP23068585A
Other languages
Japanese (ja)
Other versions
JPH0511110B2 (en
Inventor
Keishirou Nagao
長尾 恵四郎
Akio Suzui
明男 鈴井
Masazumi Nakagawa
正澄 中川
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.)
Osaka Soda Co Ltd
Original Assignee
Osaka Soda Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Osaka Soda Co Ltd filed Critical Osaka Soda Co Ltd
Priority to JP23068585A priority Critical patent/JPS6289660A/en
Publication of JPS6289660A publication Critical patent/JPS6289660A/en
Publication of JPH0511110B2 publication Critical patent/JPH0511110B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled substance useful as an intermediate for medicines from a readily available raw material in good yield in one step and in a short time, by reacting 1,3-cyclohexanedione with such as a haloacetaldehyde, etc., in the presence of ammonia. CONSTITUTION:1,3-Cyclohexanedione is reacted with a haloacetaldehyde or a derivative thereof expressed by formula II or III (X is halogen atom; Y represents halogen atom, lower alkoxy or lower acyloxy; Ac represents acetyl) at 120-200 deg.C (preferably 135-150 deg.C) in the presence of 5-10 equivalents, based on the 1,3-cyclohexanedione, ammonia to obtain the titled substance. The reaction is preferably carried out in water or a homogeneous or two-layer system solvent such as water and alcohol, ether, hydrocarbon, etc., under pressure for 1-7hr in a hermetically sealed vessel.

Description

【発明の詳細な説明】 (発明の技術分野) 本発明は抗不整脈作用を有するピンドロールやプシロシ
ン、ブシロシビン等広範な4−置換インドール系医薬品
の合成中間体として有用な4−ヒドロキシインドールの
前駆体でめる4−オキソ−4,5,6,7−チトラヒド
ロインドールの製法に関する。
Detailed Description of the Invention (Technical Field of the Invention) The present invention is directed to a 4-hydroxyindole precursor useful as a synthetic intermediate for a wide range of 4-substituted indole drugs, such as pindolol, psilocin, and bushilocybin, which have antiarrhythmic effects. The present invention relates to a method for producing 4-oxo-4,5,6,7-titrahydroindole.

(従来技術) 従来知られている4−オキソ−4,5,6゜7−チトラ
ヒドロインドールの合成法の代表的なものとしては下記
のものがある。
(Prior Art) Typical conventionally known methods for synthesizing 4-oxo-4,5,6°7-titrahydroindole include the following.

(1)1.3−シクロヘキサンジオンとブロムピルビン
酸エステルを縮合させて得られる4−、オキソ−4,5
,6,7−チトラヒドロペンゾフランー3−カルボン酸
をアンモニア、尿素。
(1) 4-,oxo-4,5 obtained by condensing 1.3-cyclohexanedione and bromopyruvic acid ester
, 6,7-titrahydropenzofuran-3-carboxylic acid with ammonia and urea.

酢酸アンモニウム等と加熱する方法[Ann。Method of heating with ammonium acetate etc. [Ann.

Chem、655.20 (1962)、特開昭59−
5159号公報1 (2)1.3−シクロヘキサンジオンとアミノアセトア
ルデヒドジメチルアセタールを縮合させる方法[J、O
rq、Chem、43゜3541   (1978)] (3)1.3−シクロヘキサンジオンとエチルビニルエ
ーテルを電極酸化し、次いで生成物を炭酸アンモニウム
と処理する方法[Chem。
Chem, 655.20 (1962), Japanese Patent Application Publication No. 1983-
5159 Publication 1 (2) Method of condensing 1,3-cyclohexanedione and aminoacetaldehyde dimethyl acetal [J, O
rq, Chem, 43°3541 (1978)] (3) A method of electrooxidizing 1,3-cyclohexanedione and ethyl vinyl ether and then treating the product with ammonium carbonate [Chem.

Letters  1603 (1980)コ(4)1
.3−シクロヘキサンジオンとクロロアセトアルデヒド
を水酸化ナトリウム、炭酸ナトリウム等の塩基の存在下
に縮合させ、次いで酸処理により4−オキソ−4,5,
6,7−チトラヒドロペンゾフランとした後これをアン
モニアと反応させる方法[特開昭59−27869号公
報] (5>4− (2−ピロリル)酪酸を閉環させる方法[
フランス特許第1540484号明細書、Ch in、
Ther、5.279 (1970)](6)N−3−
オキソ−シクロへキシリデンエタノールアミンを脱水素
閉環させる方法[特開昭59−144757号公報、特
開昭59−144758号公報コ上号公報法のうち、(
1)、(2)、(3)の方法は1.3−シクロヘキサン
ジオンと反応さぜるC2単位として高価な試薬を必要と
するか試薬を大過剰に用いねばならない。(4)の方法
は高価な試薬を用いないという点では有利であるが、1
,3−シクロヘキサンジオンとクロロアセトアルデヒド
の縮合反応に長時間を要し、しかも比較的大量の溶媒を
必要とする。
Letters 1603 (1980) Ko (4) 1
.. 3-Cyclohexanedione and chloroacetaldehyde are condensed in the presence of a base such as sodium hydroxide or sodium carbonate, and then treated with acid to form 4-oxo-4,5,
A method of forming 6,7-titrahydropenzofuran and then reacting it with ammonia [JP-A-59-27869] A method of ring-closing (5>4-(2-pyrrolyl)butyric acid) [
French Patent No. 1540484, Ch in,
Ther, 5.279 (1970)] (6) N-3-
A method for dehydrogenating and ring-closing oxo-cyclohexylideneethanolamine [JP-A No. 59-144757, JP-A No. 59-144758, among the methods disclosed in No. 1, (
Methods 1), (2), and (3) require expensive reagents as the C2 unit to be reacted with 1,3-cyclohexanedione, or require the use of a large excess of reagents. Method (4) is advantageous in that it does not use expensive reagents, but
, 3-cyclohexanedione and chloroacetaldehyde takes a long time and requires a relatively large amount of solvent.

(5)の方法は高価なピロールから数工程を経て4−(
2−ピロリル)酪酸を合成した上で環化せねばならず操
作が煩雑である。(6)の方法は脱水素に回収不可能な
高価な負金属化合物を用いねばならず、また気相脱水素
反応の条件が難しい、等それぞれ難点がある。また4−
オキソ−4,5,6,7−チトラヒドロペンゾフランを
経由する(1)、(3)、(4)の方法では、これにア
ンモニアを反応させて4−オキソ−4,5,6,7−チ
トラヒドロインドールを得る反応に0.5〜2日間要す
るという欠点がある。
Method (5) involves starting with expensive pyrrole through several steps, and then using 4-(
The procedure is complicated because 2-pyrrolyl)butyric acid must be synthesized and then cyclized. Method (6) has its own drawbacks, such as the need to use an expensive negative metal compound that cannot be recovered for dehydrogenation, and the conditions for the gas phase dehydrogenation reaction being difficult. Also 4-
In methods (1), (3), and (4), which involve using oxo-4,5,6,7-titrahydropenzofuran, 4-oxo-4,5,6,7 -The disadvantage is that the reaction to obtain titrahydroindole takes 0.5 to 2 days.

(発明の目的) 本発明は、容易に入手しうる原料を用いて一段階反応で
短時間に、しかも好収率で目的とする4−オキソ−4,
5,6,7−チトラヒドロインドールを製造する方法を
提供するものである。
(Objective of the Invention) The present invention aims to achieve the desired 4-oxo-4,
A method for producing 5,6,7-titrahydroindole is provided.

(発明の構成) 本発明は、1.3−シクロヘキサンジオンと下記一般式
(II>又は一般式(In>で表わされるハロアセトア
ルデヒド又はその誘導体XCH2CHO(II> (但し、上記一般式(II)、  (In)において、
Xはハロゲン原子、Yはハロゲン原子又は炭素数1〜3
の低級アルコキシ基もしくは低級アシルオキシ基、AC
はアセチル基を表わす)をアンモニアの存在下120℃
〜200°Cで反応させることを特徴とする4−オキソ
−4,5,6゜7−チトラヒドロインドールの製法であ
る。
(Structure of the Invention) The present invention relates to 1,3-cyclohexanedione and a haloacetaldehyde represented by the following general formula (II> or general formula (In>) or its derivative XCH2CHO(II> (however, the above general formula (II), (In),
X is a halogen atom, Y is a halogen atom or has 1 to 3 carbon atoms
lower alkoxy group or lower acyloxy group, AC
represents an acetyl group) at 120°C in the presence of ammonia.
This is a method for producing 4-oxo-4,5,6°7-titrahydroindole, characterized by carrying out the reaction at ~200°C.

本発明は下記反応式に示されるように、1゜3−シクロ
ヘキサンジオン(I>にハロアセトアルデヒド(ff)
又はその誘導体(m)をアンモニアの存在下に反応させ
て4−オキソ−4゜5.6.7−チトラヒドロインドー
ル(IV)を得る方法である。
As shown in the reaction formula below, the present invention is characterized in that haloacetaldehyde (ff) is added to 1゜3-cyclohexanedione (I>).
Alternatively, 4-oxo-4°5.6.7-titrahydroindole (IV) is obtained by reacting the derivative (m) in the presence of ammonia.

[ (I)      (II)        (III
)(IV) 上記反応式を更に詳述すると、本発明の反応条件下では
下記式(A>を主体とした反応経路で上記式(B)にお
いては、化合物(I)の酸性度とアルコキシドの塩基性
からステップ(C)及び(d)はいずれも可逆反応と考
えられ、式(B)の律速段階はステップ(e)と考えら
れる。一方式(A>の律速段階は明らかにステップ(a
>である。式(B)のステップ(e)は分子内反応であ
るため活性化エネルギーは式(A)のステップ(a>よ
りはるかに小ざく、従って低温下の反応では式(B)の
反応が優先するものと考えられる。よって式(A>の反
応を行うには十分な反応熱が必要であると予想され、果
たして本発明の如く、アンモニアの存在下120℃以上
の温度で化合物(I>、  (II)を反応させること
によって予想以上の高収率で目的物(IV)を得ること
ができたものである。本発明において反応開始後1時間
程度の初期の段階では、前記式(B)の化合物(V)t
3よび(VI)は全く生成していないことが本発明者ら
によって確認された。前述したようにこの化合物(VI
)とアンモニアとの反応から目的物(IV)を得るには
かなりの長時間を要することから、本発明の目的物であ
る化合物(IV)は上記化合物(V)及びF)を経て生
成しているのではないことは明らかである。
[ (I) (II) (III
) (IV) To explain the above reaction formula in more detail, under the reaction conditions of the present invention, the reaction route is mainly based on the following formula (A>), and in the above formula (B), the acidity of compound (I) and the alkoxide Because of their basicity, steps (C) and (d) are both considered to be reversible reactions, and the rate-determining step in formula (B) is considered to be step (e).On the other hand, the rate-determining step in formula (A>) is clearly considered to be step (a).
> is. Since step (e) of formula (B) is an intramolecular reaction, the activation energy is much smaller than step (a> of formula (A)), so the reaction of formula (B) has priority in reactions at low temperatures. Therefore, it is expected that sufficient reaction heat is required to carry out the reaction of formula (A>, and as in the present invention, compound (I>, ( By reacting II), the target compound (IV) could be obtained in a higher yield than expected. In the present invention, in the early stage of about 1 hour after the start of the reaction, the reaction of the formula (B) Compound (V)t
The present inventors confirmed that 3 and (VI) were not produced at all. As mentioned above, this compound (VI
) and ammonia to obtain the target compound (IV), it takes a considerable time to obtain the target compound (IV), so the compound (IV), which is the target compound of the present invention, is produced through the above compounds (V) and It is clear that there is no such thing.

本発明において加えられるアンモニアはステップ(b)
の試剤であると共に、ステップ(a)に必要な塩基とし
て作用している。この際化合物(II)の代りにアンモ
ニアと反応して化合物(II)を与える前記化合物(I
II)を用いると更に良い収率が得られることも判った
In the present invention, the ammonia added in step (b)
as well as the base necessary for step (a). At this time, the compound (I) reacts with ammonia instead of compound (II) to give compound (II).
It has also been found that even better yields can be obtained using II).

本発明に用いられる原料化合物(II)としては、工業
的に入手可能なりロロアセトアルデヒドやブロムアセタ
ール又は後記原料化合物(III>の一つである1、2
−ジブロムエチルアセテートから容易に得られるブロム
アセトアルデヒドがあり、特にブロムアセトアルデヒド
が反応性及び収率の点で優れている。化合物(II>は
純粋な状態で取扱うことが難しく、いずれも水溶液とし
て使用するのが好ましい。
The raw material compound (II) used in the present invention may be industrially available loroacetaldehyde or bromoacetal, or one of the raw material compounds (III) listed below.
- There is bromoacetaldehyde that can be easily obtained from dibromoethyl acetate, and bromoacetaldehyde is particularly excellent in terms of reactivity and yield. Compound (II>) is difficult to handle in a pure state and is preferably used as an aqueous solution.

本発明に用いられる原料化合物(m)とじては、酢酸ビ
ニルより既知の方法で容易に合成できる1、2−ジハロ
ゲノエチルアセテート、1−アルコキシ−2−ハロゲン
エチルアセテート、1−アシルオキシ−2〜八〇ゲノエ
チルアセテートが挙げられ、これらのハロゲンとしては
塩素原子又は臭素原子がよく、1,2−ジハロゲノエチ
ルアセテートの場合ハロゲンは互に同一である方が好ま
しい。アルコキシ又はアシルオキシとしては炭素数1〜
3の低級アルコキシ又は炭素数1〜3の低級アシルオキ
シが好ましい。
The raw material compound (m) used in the present invention includes 1,2-dihalogenoethyl acetate, 1-alkoxy-2-halogenethyl acetate, 1-acyloxy-2- Examples include octogenoethyl acetate, and the halogen thereof is preferably a chlorine atom or a bromine atom, and in the case of 1,2-dihalogenoethyl acetate, it is preferable that the halogens are the same. Alkoxy or acyloxy has 1 or more carbon atoms
3 lower alkoxy or lower acyloxy having 1 to 3 carbon atoms is preferred.

本発明において原料化合物(m)としては、合成上の容
易さと収率及び刺激性の点から1,2−ジハロゲノエチ
ルアセテートがよく、殊に、1.2−ジハロゲノエチル
アセテートと1−アシルオキシ−2−ハI」ゲノエチル
アセテートとの混合物が特に好ましい。上記1.2−ジ
ハロゲノエチルアセテートとして好ましいものはハロゲ
ンが臭素である1、2−ジブロモエチルアセテートであ
る。また上記混合物の場合の好ましい例は、1.2−ジ
ブロモエチルアセテートと2−ブロム−1,1−エタン
ジオールジアセテートの混合物であり、これらモル比が
1:2〜2:1のものが特に好ましい。
In the present invention, the starting compound (m) is preferably 1,2-dihalogenoethyl acetate from the viewpoint of ease of synthesis, yield, and stimulation, and in particular, 1,2-dihalogenoethyl acetate and 1-acyloxy Particularly preferred is a mixture with -2-HaI''genoethyl acetate. Preferred as the 1,2-dihalogenoethyl acetate is 1,2-dibromoethyl acetate in which the halogen is bromine. A preferred example of the above mixture is a mixture of 1,2-dibromoethyl acetate and 2-bromo-1,1-ethanediol diacetate, and those with a molar ratio of 1:2 to 2:1 are particularly preferred. preferable.

原料化合物(1)としては、酢酸ビニル以外のビニルエ
ステルから得られる同様の化合物群も用いることができ
る。
As the raw material compound (1), similar compounds obtained from vinyl esters other than vinyl acetate can also be used.

本発明において、原料化合物(II>又は(I[I)の
使用量は、1,3−シクロヘキサンジオンに対して1〜
5当邑、好ましくは1.1〜1.5当量の範囲が適当で
ある。
In the present invention, the amount of starting compound (II> or (I[I)) to be used is 1 to 1 to 1 to 1,3-cyclohexanedione.
A suitable range is 5 equivalents, preferably 1.1 to 1.5 equivalents.

本発明に用いられるアンモニアはアンモニアガス、Sア
ンモニア水のいずれも使用できるが、アンモニアガスを
用いる方が反応の初期温度及び溶媒量を任意に決定でき
るので有利である。
The ammonia used in the present invention can be either ammonia gas or S ammonia water, but it is more advantageous to use ammonia gas because the initial reaction temperature and the amount of solvent can be arbitrarily determined.

アンモニアの使用量は1.3−シクロヘキサンジオンに
対して5〜30当量、好ましくは5〜10当量の範囲が
適当である。
The appropriate amount of ammonia to be used is 5 to 30 equivalents, preferably 5 to 10 equivalents, relative to 1,3-cyclohexanedione.

本発明を実施するに際しては、原料化合物(I>及び(
II>又は(III)を水又は水とアルコール類、エー
テル類、炭化水素類等の均−又は二層系溶媒に加え、ア
ンモニア存在下で加熱することによって達成される。
When carrying out the present invention, raw material compounds (I> and (
II> or (III) to water or a homogeneous or two-layer solvent such as water and alcohols, ethers, hydrocarbons, etc., and heating the mixture in the presence of ammonia.

上記溶媒のアルコール類としてはメタノール。The alcohol used as the solvent is methanol.

ブタノール等、エーテル類としてはテトラヒドロフラン
、ジオキサン等、炭化水素類としてはトルエン、ヘキサ
ン等がある。特に水又は水−アルコール類の溶媒が反応
の円滑性、収率の点で優れている。本発明においては水
を用いない反応系、例えばアルコール類のみの溶媒で行
うと収率が著しく低下する傾向がある。溶媒としてケト
ン類(アセトン等)、エステル類(酢酸エチル等)、ハ
ロゲン化炭化水素類(ジクロロメタン等)を用いると副
反応が多くなり、またカルボン酸類(酢酸等)では反応
系を酸性に傾けるため好ましくない。
Examples of ethers include butanol, such as tetrahydrofuran and dioxane, and examples of hydrocarbons include toluene and hexane. In particular, water or water-alcohol solvents are excellent in terms of reaction smoothness and yield. In the present invention, if the reaction system does not use water, for example, if the reaction is carried out using an alcohol-only solvent, the yield tends to decrease significantly. When ketones (acetone, etc.), esters (ethyl acetate, etc.), and halogenated hydrocarbons (dichloromethane, etc.) are used as solvents, side reactions increase, and carboxylic acids (acetic acid, etc.) tend to make the reaction system acidic. Undesirable.

本発明において目的物の収率は前記反応機構から推測さ
れるように反応温度に大きく左右される。反応の初期温
度が高いことは好ましく、また加温速度が早い方が好収
率を与える。しかしながら、あまり高い温度では化合物
(II)の分解を促進するため収率の低下は免れない。
In the present invention, the yield of the target product is largely influenced by the reaction temperature, as expected from the reaction mechanism described above. It is preferable that the initial temperature of the reaction is high, and a faster heating rate gives a better yield. However, if the temperature is too high, the decomposition of compound (II) will be promoted, resulting in a decrease in yield.

本発明における好適な反応温度は120〜200’C1
特に135〜150’Cの範囲である。
The preferred reaction temperature in the present invention is 120 to 200'C1
In particular, it is in the range of 135-150'C.

反応はアンモニアの揮散を防ぐため密封容器中加圧下に
行うのがよく、反応時間は通常1〜7時間で十分である
The reaction is preferably carried out in a sealed container under pressure to prevent volatilization of ammonia, and a reaction time of 1 to 7 hours is usually sufficient.

反応に際して、アンモニアと共に炭酸アンモニウムや酢
酸アンモニウム等のアンモニアの有機酸塩又は無機酸塩
を併用したり、他の塩基、例えば水酸化ナトリウム、炭
酸水素ナトリウム。
During the reaction, an organic or inorganic acid salt of ammonia such as ammonium carbonate or ammonium acetate may be used in combination with ammonia, or other bases such as sodium hydroxide or sodium bicarbonate may be used.

トリエチルアミン等を副生するハロゲン化水素酸や酢酸
等の除酸剤として用いることができる。
It can be used as an acid remover for hydrohalic acids, acetic acids, etc. that produce triethylamine and the like as by-products.

反応後目的物である4−オキンー4.5,6゜7−チト
ラヒドロインドールは、反応物の溶媒抽出によって高純
度で単離できる。更に再結晶、クロマトグラフィー等の
慣用の精製手段によって純粋の4−オキソ−4,5,6
,7−チトラヒドロインドールとすることができる。
After the reaction, the target product, 4-okine-4.5,6°7-titrahydroindole, can be isolated in high purity by solvent extraction of the reactant. Furthermore, pure 4-oxo-4,5,6 can be obtained by conventional purification methods such as recrystallization and chromatography.
, 7-titrahydroindole.

(発明の効果) 本発明は原料として容易に入手可能な化合物を用いて一
段階反応でしかも短時間で目的物を好収率に得ることが
できるので工業的製法として非常に有利である。
(Effects of the Invention) The present invention is very advantageous as an industrial production method because it is possible to obtain the desired product in a good yield in a short period of time through a one-step reaction using readily available compounds as raw materials.

(実施例) 実施例1 容量 200dlの耐圧ガラス管中に1,3−シクロヘ
キサンジオン1.120をとり、25重母%アンモニア
水7mlとメタノール5dを加えて溶かした。これに1
.2−ジブロムエチルアセテート2.95Clを加えて
密封しスターラー付油浴で加熱攪拌しながら145℃で
7時間反応させた。反応後反応液からメタノールを減圧
下で留去させ、残漬を温酢酸エチルで抽出し、該溶媒を
減圧下に留去して目的物4−オキソ−4,5,6,7−
チトラヒドロインドール0.98C]を得た(収率72
.4%)。このものはガスクロマトグラフィー分析(カ
ラム:0V−225(5%)/クロモソルブW  AW
−DMC3、以下GC分析という)により純度92.4
%であることが分った。また水から再結晶したものは融
点189.8〜191.0℃であり既知標品と一致した
(Example) Example 1 1.120 ml of 1,3-cyclohexanedione was placed in a pressure-resistant glass tube having a capacity of 200 dl, and 7 ml of 25% ammonia water and 5 d of methanol were added and dissolved. 1 for this
.. 2.95 Cl of 2-dibromoethyl acetate was added, the mixture was sealed, and the mixture was reacted at 145° C. for 7 hours while heating and stirring in an oil bath with a stirrer. After the reaction, methanol was distilled off from the reaction solution under reduced pressure, the residue was extracted with warm ethyl acetate, and the solvent was distilled off under reduced pressure to obtain the target product 4-oxo-4,5,6,7-
Titrahydroindole 0.98C] was obtained (yield 72
.. 4%). This product was analyzed by gas chromatography (column: 0V-225 (5%)/Chromosolve W AW
- Purity 92.4 as determined by DMC3 (hereinafter referred to as GC analysis)
It was found that %. Moreover, the melting point of the product recrystallized from water was 189.8-191.0°C, which was consistent with the known standard.

実施例2 容Wi INのオートクレーブに1,3−シクロヘキサ
ンジオン56.OC]、水5007 、メタノール25
Mを入れ、更に1,2−ジブロムエチルアセテート14
7.5 qを加えて密封し、135℃の油浴に浸けて加
熱攪拌した。内温が80℃になった時アンモニアガスを
導入しオートクレーブの内圧を5.0〜5.5気圧に保
持した。5分後に内温か135℃に達してから該温度で
30分間アンモニアガスの導入を続けこの間オートクレ
ーブの内圧を6.0気圧に保った。その後アンモニアガ
スの導入を断ち、同温度で2時間30分間反応を継続さ
せた。アンモニアの全導入量は51.2Qであった。反
応後反応液を冷却し減圧下に濃縮してこれを60℃の温
酢酸エチルで抽出した。抽出液を飽和食塩水で洗浄し、
該食塩水中に溶出した生成物を酢酸エチルで抽出回収し
、これら抽出液を脱水後活性倹約10を加えて濾過した
。濾液を減圧下に濃縮して目的物4−オキソ−4゜5.
6.7−チトラヒトロインドール48.3qを得た(収
率71.6%)。GC分析によりこのものの純度は97
.4%であった。
Example 2 1,3-cyclohexanedione was added to an autoclave with a volume of 56. OC], water 5007, methanol 25
Add M and then add 1,2-dibromoethyl acetate 14
After adding 7.5 q of the mixture, the mixture was sealed, immersed in a 135°C oil bath, and heated and stirred. When the internal temperature reached 80°C, ammonia gas was introduced to maintain the internal pressure of the autoclave at 5.0 to 5.5 atm. After 5 minutes, the internal temperature reached 135°C, and ammonia gas was continued to be introduced at this temperature for 30 minutes, during which time the internal pressure of the autoclave was maintained at 6.0 atm. Thereafter, the introduction of ammonia gas was cut off, and the reaction was continued for 2 hours and 30 minutes at the same temperature. The total amount of ammonia introduced was 51.2Q. After the reaction, the reaction solution was cooled, concentrated under reduced pressure, and extracted with warm ethyl acetate at 60°C. Wash the extract with saturated saline,
The product eluted in the saline solution was extracted and recovered with ethyl acetate, and these extracts were dehydrated and filtered with the addition of 10% active solution. The filtrate was concentrated under reduced pressure to obtain the target product 4-oxo-4゜5.
48.3q of 6.7-titrahydroindole was obtained (yield 71.6%). According to GC analysis, the purity of this product is 97.
.. It was 4%.

実施例3 1g 4号フラスコ中に酢酸ビニル148mf!と氷酢
酸35(7!をとり、5〜10℃で臭素78ml1を滴
下した。更に室温で1時間攪拌後、水400W11−四
塩化炭素40M中に反応液を投入し層分離した後、水層
から四塩化炭素50dによる抽出を3回行った。四塩化
炭素層を合わせ、水(100dX 2回)、飽和重曹水
(100m1X 1回)、飽和食塩水(50戒×1回)
の順による洗浄を行った後脱水し濾過した。濾過後の四
塩化炭素を減圧下に留去させ、残漬を減圧上蒸留して1
.2−ジブロムエチルアセテートと2−ブロム−1,1
−エタンジオールジアセテートの混合物(モル比1.5
  :  1   )  274.74CIを19Iこ
 (bp80〜125°C/35Torr>。
Example 3 148mf of vinyl acetate in a 1g No. 4 flask! and glacial acetic acid 35 (7!), and 78 ml of bromine was added dropwise at 5 to 10°C. After further stirring at room temperature for 1 hour, the reaction solution was poured into 400 W of water and 40 M of carbon tetrachloride, and the layers were separated. Extraction was carried out three times with 50 d of carbon tetrachloride.The carbon tetrachloride layers were combined, and water (100 d x 2 times), saturated sodium bicarbonate solution (100 ml x 1 time), and saturated saline (50 d x 1 time) were extracted.
After washing in the following order, it was dehydrated and filtered. Carbon tetrachloride after filtration is distilled off under reduced pressure, and the residue is distilled under reduced pressure to obtain 1
.. 2-dibromoethyl acetate and 2-bromo-1,1
- mixture of ethanediol diacetates (molar ratio 1.5
: 1) 274.74CI to 19I (bp80-125°C/35Torr>.

上記混合物から83.OC]を採取して各辺1でのオー
トクレーブに入れ、これに1,3−シクロヘキサンジオ
ン38.65 Q、水3907及びメタノール130m
1を加えて密封し、135℃の油浴に浸けて加熱攪拌し
た。内温か80℃になった時アンモニアガスを導入しオ
ートクレーブの内圧を5.0〜5.5気圧に保った。3
分後に内温か135℃に達してから該温度で45分間ア
ンモニアガスの導入を続はオートクレーブの内圧を5.
5気圧に保った。その後アンモニアガスの導入を断ち、
同温度で4時間15分間反応を継続した。アンモニアの
全導入量は36.2 gであった。
83. from the above mixture. OC] was collected and placed in an autoclave at 1 on each side, and to this was added 38.65 Q of 1,3-cyclohexanedione, 3907 Q of water, and 130 m of methanol.
1 was added thereto, sealed, immersed in a 135°C oil bath, and heated and stirred. When the internal temperature reached 80°C, ammonia gas was introduced to maintain the internal pressure of the autoclave at 5.0 to 5.5 atm. 3
After 135 minutes, the internal temperature of the autoclave reached 135°C, and then ammonia gas was introduced at that temperature for 45 minutes, and the internal pressure of the autoclave was increased to 5.
The pressure was maintained at 5 atm. After that, the introduction of ammonia gas was cut off,
The reaction was continued for 4 hours and 15 minutes at the same temperature. The total amount of ammonia introduced was 36.2 g.

反応後反応液を冷却し実施例2と同様の後処理を行い4
−オキソ−4,5,6,7−チトラヒドロインドール3
5.36gを得た(収率75.9%)。
After the reaction, the reaction solution was cooled and the same post-treatment as in Example 2 was carried out.
-oxo-4,5,6,7-titrahydroindole 3
5.36 g was obtained (yield 75.9%).

GO分析による純度は97.7%であった。Purity by GO analysis was 97.7%.

実施例4 容量 200allの耐圧ガラス管中に1,3−シクロ
ヘキサンジオン1.12qをとり40重量%クロロアセ
トアルデヒド水溶液2.4d、25重量%アンモニア水
4,2ml、メタノール5dを順次加えて密封し攪拌し
ながら145℃で7時間反応させた。
Example 4 1.12q of 1,3-cyclohexanedione was placed in a pressure-resistant glass tube with a capacity of 200all, and 2.4d of a 40% by weight aqueous chloroacetaldehyde solution, 4.2ml of 25% by weight aqueous ammonia, and 5d of methanol were sequentially added, sealed, and stirred. The reaction was continued at 145° C. for 7 hours.

反応後の処理は実施例1と同様にして目的物0.68C
lを得た(収率50.4%)。GC分析による純度は8
1.3%であった。
The treatment after the reaction was the same as in Example 1, and the target product was 0.68C.
1 was obtained (yield 50.4%). Purity by GC analysis is 8
It was 1.3%.

実施例5 容量200dの耐圧ガラス管中に25重四%アンモニア
水21m1をとり、60℃以下で1,2−ジブロムエチ
ルアセテート8.85 CIを加えて溶かしブロムアセ
トアルデヒドのアンモニア水溶液とした。これに1.3
−シクロヘキサンジオン3.36にlとメタノール15
dを加えて密封し135℃で5時間反応させた。反応後
の処理は実施例1と同様にして目的物2.41 Gを得
た(収率59.5%)。GC分析による純度は92.7
%であった。
Example 5 21 ml of 25x4% ammonia water was placed in a pressure-resistant glass tube with a capacity of 200 d, and 8.85 CI of 1,2-dibromoethyl acetate was added and dissolved at 60° C. or lower to obtain an ammonia aqueous solution of bromoacetaldehyde. 1.3 for this
- 3.36 liters of cyclohexanedione and 15 liters of methanol
d was added, sealed, and reacted at 135°C for 5 hours. The treatment after the reaction was the same as in Example 1 to obtain the target product 2.41G (yield 59.5%). Purity by GC analysis is 92.7
%Met.

実施例6 還流器付フラスコにブロムアセタール94.6CJ及び
水10heの混合物と酸性イオン交換樹脂(「ダイヤイ
オンPK−2284三菱化成社製)10gを加えて4時
間還流した。冷却後樹脂を濾別し、更に水300m1で
洗浄した。濾液を1,3−シクロヘキサンジオン44.
8qとメタノール20Mを含む容量1gのオートクレー
ブに加えて密封し135°Cの油浴につけて加熱攪拌し
た。
Example 6 A mixture of 94.6 CJ of bromoacetal and 10 he of water and 10 g of an acidic ion exchange resin (Diaion PK-2284 manufactured by Mitsubishi Chemical Corporation) were added to a flask equipped with a reflux device and refluxed for 4 hours. After cooling, the resin was filtered off. The filtrate was washed with 300ml of water.The filtrate was diluted with 44% of 1,3-cyclohexanedione.
The mixture was added to a 1 g autoclave containing 8 q and 20 M methanol, sealed, and heated in an oil bath at 135° C. with stirring.

内温か90℃になった時アンモニアガスを導入しオート
クレーブの内圧を5.0〜5.5気圧に保持した。7分
後に内温が135°Cに達してから該温度で30分間ア
ンモニアガスの導入を続はオートクレーブの内圧を6.
0気圧に保った。その後アンモニアガスの導入を断ち、
同温度で2時間30分間反応を継続した。アンモニアの
全導入量は40.30であった。反応後反応液を冷却し
、実施例2と同様の後処理を行って4−オキソ−4゜5
.6.7−チトラヒドロインドール30.99 CIを
得た(収率57.4%)。GC分析による純度は92.
2%であった。
When the internal temperature reached 90°C, ammonia gas was introduced to maintain the internal pressure of the autoclave at 5.0 to 5.5 atm. After 7 minutes, when the internal temperature reached 135°C, ammonia gas was introduced at that temperature for 30 minutes, and the internal pressure of the autoclave was increased to 6.
The pressure was maintained at 0 atmospheres. After that, the introduction of ammonia gas was cut off,
The reaction was continued for 2 hours and 30 minutes at the same temperature. The total amount of ammonia introduced was 40.30. After the reaction, the reaction solution was cooled and subjected to the same post-treatment as in Example 2 to obtain 4-oxo-4゜5.
.. 30.99 CI of 6.7-titrahydroindole was obtained (yield 57.4%). Purity by GC analysis is 92.
It was 2%.

実施例7 1.2−ジブロムエチルアセテート2.95CJの代り
に1,2−ジクロロエチルアセテート1.88gを用い
た以外は実施例1と同様にして目的物0.730を得た
(収率54,1%)。GO分析による純度は73.8%
であった。
Example 7 1.2-dibromoethyl acetate 0.730 of the target product was obtained in the same manner as in Example 1 except that 1.88 g of 1,2-dichloroethyl acetate was used instead of 2.95 CJ of 1.2-dibromoethyl acetate (yield: 54.1%). Purity by GO analysis is 73.8%
Met.

実施例8〜10 1.2−ジブロムエチルアセテートの代りに表1の一般
式(DI)の化合物を用い、反応を135℃、5時間行
った以外は実施例1と同様にして表1の結果を得た。
Examples 8 to 10 The procedures in Table 1 were carried out in the same manner as in Example 1, except that the compound of general formula (DI) in Table 1 was used instead of 1,2-dibromoethyl acetate, and the reaction was carried out at 135°C for 5 hours. Got the results.

一ニ 註 Me:メチル基、Pr:プロピル基比較例1 反応温度を100℃とした以外は実施例4と同様に行っ
たところ目的物0.27q (収率20%)が得られ、
このものの純度は79.3%であった。
Note: Me: methyl group, Pr: propyl group Comparative Example 1 The same procedure as in Example 4 was carried out except that the reaction temperature was 100°C, and 0.27q of the target product (yield 20%) was obtained.
The purity of this product was 79.3%.

Claims (1)

【特許請求の範囲】 1,3−シクロヘキサンジオンと下記一般式(II)又は
一般式(III)で表わされるハロアセトアルデヒド又は
その誘導体をアンモニアの存在下120℃〜200℃で
反応させることを特徴とする4−オキソ−4,5,6,
7−テトラヒドロインドールの製法。 一般式(II) XCH_2CHO 一般式(III) ▲数式、化学式、表等があります▼ (但し、上記一般式(II)、(III)において、Xはハ
ロゲン原子、Yはハロゲン原子又は炭素数1〜3の低級
アルコキシ基もしくは低級アシルオキシ基、ACはアセ
チル基を表わす)
[Claims] 1,3-cyclohexanedione and a haloacetaldehyde represented by the following general formula (II) or general formula (III) or a derivative thereof are reacted at 120°C to 200°C in the presence of ammonia. 4-oxo-4,5,6,
Method for producing 7-tetrahydroindole. General formula (II) XCH_2CHO General formula (III) ▲ Numerical formulas, chemical formulas, tables, etc. 3 lower alkoxy group or lower acyloxy group, AC represents an acetyl group)
JP23068585A 1985-10-16 1985-10-16 Production of 4-oxo-4,5,6,7-tetrahydroindole Granted JPS6289660A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23068585A JPS6289660A (en) 1985-10-16 1985-10-16 Production of 4-oxo-4,5,6,7-tetrahydroindole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23068585A JPS6289660A (en) 1985-10-16 1985-10-16 Production of 4-oxo-4,5,6,7-tetrahydroindole

Publications (2)

Publication Number Publication Date
JPS6289660A true JPS6289660A (en) 1987-04-24
JPH0511110B2 JPH0511110B2 (en) 1993-02-12

Family

ID=16911704

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23068585A Granted JPS6289660A (en) 1985-10-16 1985-10-16 Production of 4-oxo-4,5,6,7-tetrahydroindole

Country Status (1)

Country Link
JP (1) JPS6289660A (en)

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US8059992B2 (en) 2007-12-10 2011-11-15 Ricoh Company, Ltd. Corona charger, and process cartridge and image forming apparatus using same
US7937025B2 (en) 2008-09-12 2011-05-03 Ricoh Company, Ltd. Scorotron corona charger, process cartridge, and image forming apparatus
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