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JPS5922700B2 - Method for producing indole derivatives - Google Patents
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JPS5922700B2 - Method for producing indole derivatives - Google Patents

Method for producing indole derivatives

Info

Publication number
JPS5922700B2
JPS5922700B2 JP49091736A JP9173674A JPS5922700B2 JP S5922700 B2 JPS5922700 B2 JP S5922700B2 JP 49091736 A JP49091736 A JP 49091736A JP 9173674 A JP9173674 A JP 9173674A JP S5922700 B2 JPS5922700 B2 JP S5922700B2
Authority
JP
Japan
Prior art keywords
indole
reaction
product
cupric acetate
diindolenylidene
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.)
Expired
Application number
JP49091736A
Other languages
Japanese (ja)
Other versions
JPS5119764A (en
Inventor
和彦 片山
昌彦 西垣
叙孝 谷
実 西沢
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP49091736A priority Critical patent/JPS5922700B2/en
Publication of JPS5119764A publication Critical patent/JPS5119764A/en
Publication of JPS5922700B2 publication Critical patent/JPS5922700B2/en
Expired 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)

Description

【発明の詳細な説明】 本発明はインドール誘導体の新規な製造方法に関するも
のであり、更に詳しくは酢酸第二銅−ピリジン錯体の存
在下に、インドールを反応せしめて3、3’−ジイソド
リルおよび/または3、3’−ジインドレニニリデンの
全く新規な製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for producing indole derivatives, and more specifically, indole is reacted in the presence of a cupric acetate-pyridine complex to produce 3,3'-diisodolyl and/or Alternatively, the present invention relates to a completely new method for producing 3,3'-diindolenylidene.

従来、3、3’−ジイソドリルは例えば「ガゼツタ・キ
ミカ・イタリアーナ(Ga22ettachimica
italiana)」、1939年、69巻、562頁
に示されている方法によつて合成されることが公知であ
り、また3、3’−ジインドレニニリデンは例えば、「
ジャーナル・オブ・ザ・ケミカル・ソサイアテイ(Jo
urnalofTheChemicalSociety
)」、1957年、4141頁に記載されている方法に
よつて合成されることが知られている。
Conventionally, 3,3'-diisodryl has been produced by, for example, "Ga22etta chimica Italiana".
Italiana), 1939, Vol. 69, p. 562, and 3,3'-diindoleninylidene is, for example,
Journal of the Chemical Society (Jo
urnalofTheChemicalSociety
), 1957, p. 4141.

すなわち、インドールを封管中でイオウと反応させ、3
、3’−ジイソドリルを得、更に3、3’−ジイソドリ
ルと二酸化鉛を酢酸エチル溶媒中で反応させて3、3’
−ジインドレニニリデンを得るという方法が採られてき
た。これらの従来の方法は、実験室規模で実施する際に
は一応満足のゆくものであるが、工業的規模で製造実施
する際には、例えば次の様な種々の問題点がある。
That is, indole is reacted with sulfur in a sealed tube, and 3
, 3'-diisodolyl was obtained, and 3,3'-diisodolyl and lead dioxide were further reacted in an ethyl acetate solvent to obtain 3,3'
- A method has been adopted to obtain diindolenylidene. These conventional methods are somewhat satisfactory when carried out on a laboratory scale, but when carried out on an industrial scale, there are various problems, such as the following.

(1)反応中に硫化水素ガスが発生するので耐圧容器を
用いなければならない。
(1) Since hydrogen sulfide gas is generated during the reaction, a pressure-resistant container must be used.

(2)発生する硫化水素が有毒であるので適当な処理を
施さなければならない。
(2) The hydrogen sulfide generated is toxic and must be treated appropriately.

(3)反応が二段階であつて工程が複雑である。(3) The reaction is two-stage and the process is complicated.

本発明者らは上記欠点を解消せんとして鋭意検討した結
果、酢酸第二銅−ピリジン錯体を用いることによりイン
ドールから一段階で3、3’−ジイソドリルおよび/ま
たは3、3’−ジインドレニニリデンを得ることができ
るという全く新規な製造方法を見い出し、本発明に到達
した。以下、本発明を詳細に説明する。
As a result of intensive studies by the present inventors in an effort to resolve the above-mentioned drawbacks, we found that by using a cupric acetate-pyridine complex, 3,3'-diisodolyl and/or 3,3'-diindoleninyl can be converted from indole in one step. The present invention was achieved by discovering a completely new manufacturing method capable of obtaining reden. The present invention will be explained in detail below.

本発明における反応様式は、耐圧容器を使う必要はなく
、常圧下において実施できる。
The reaction mode in the present invention does not require the use of a pressure vessel and can be carried out under normal pressure.

反応温度は反応時間との関連から一義的に決めることは
出来ないが、室温から115℃、好ましくは60℃から
115℃までの広い範囲を採用できる。また、ノ 反応
温度が比較的低いところでは3、3’−ジイソドリルが
生成し易く、反応温度が比較的高いところでは3、3’
−ジインドレニニリデンが生成し易くなる。また、反応
時間が長くなると3、3’−ジインドレニニリデンの生
成量が多くなる。5 本発明に用いられる溶媒としては
、ピリジン、ベンゼン、エタノール、メタノール等々の
各種溶媒を任意に選択して、単独、または二種以上の混
合物で用いることが出来る。
Although the reaction temperature cannot be determined uniquely in relation to the reaction time, a wide range from room temperature to 115°C, preferably from 60°C to 115°C can be adopted. Furthermore, where the reaction temperature is relatively low, 3,3'-diisodolyl is likely to be produced, and where the reaction temperature is relatively high, 3,3'-diisodolyl is likely to be produced.
- Diindolenylidene is more likely to be produced. Furthermore, as the reaction time increases, the amount of 3,3'-diindolenylidene produced increases. 5. As the solvent used in the present invention, various solvents such as pyridine, benzene, ethanol, methanol, etc. can be arbitrarily selected and used alone or in a mixture of two or more.

溶媒は一義的に決めることは出来ないがインドールおよ
び酢酸第二銅−ピリジン錯体および生成物の溶解性、溶
媒の沸点等々を考慮すればピリジンを用いるのが好まし
いO酢酸第二銅のインドールに対する仕込重量比は任意
であるが、例えばピリジンを溶媒として用いる場合には
1〜150重量%までの広い範囲を採用できる。
Although the solvent cannot be determined unambiguously, it is preferable to use pyridine in consideration of the solubility of indole and the cupric acetate-pyridine complex and the product, the boiling point of the solvent, etc.O Charge of cupric acetate to indole Although the weight ratio is arbitrary, for example, when pyridine is used as a solvent, a wide range of 1 to 150% by weight can be adopted.

また、酢酸第二銅のインドールに対する仕込重量比が比
較的小さいところでは3,3′−ジインドリルが生成じ
易く、比較的大きいところでは3,3′−ジインドレニ
ニリデンが生成し易くなる。反応生成物から3,3仁ジ
インドリルおよび/または3,3′−ジインドレニニリ
デンを単離精製するには次の様にして行なう。すなわち
、反応の際に用いた溶媒を減圧下において濃縮した後、
更に反応生成物中の酢酸第二銅−ピリジン錯体を除去す
るため、水洗するかあるいは適当な溶媒を用いて抽出す
るかいずれかの方法が採用される。また未反応インドー
ルは、所望なら、水蒸気蒸留および/または再結晶法に
よつて除去可能である。更に、高純度の目的物が所望な
らカラムクロマトグラフイ一によつて精製することがで
きる〇本発明の方法により得られた目的物は、ハロゲン
化ビニル単量体またはハロゲン化ビニル単量体およびこ
れと共重合可能なビニル系単量体混合物の懸濁重合もし
くは乳化重合に際し、重合機機壁等に生ずる重合体スケ
ールの付着を皆無にするための塗布剤として著効を有す
るものである。
Furthermore, when the weight ratio of cupric acetate to indole is relatively small, 3,3'-diindolyl is likely to be produced, and when it is relatively large, 3,3'-diindolenylidene is likely to be produced. Isolation and purification of 3,3 diindolyl and/or 3,3'-diindolenylidene from the reaction product is carried out as follows. That is, after concentrating the solvent used in the reaction under reduced pressure,
Furthermore, in order to remove the cupric acetate-pyridine complex in the reaction product, either washing with water or extraction using a suitable solvent is employed. Unreacted indole can also be removed, if desired, by steam distillation and/or recrystallization methods. Furthermore, if a highly pure target product is desired, it can be purified by column chromatography. During suspension polymerization or emulsion polymerization of a vinyl monomer mixture copolymerizable with this, it is highly effective as a coating agent for completely eliminating the adhesion of polymer scale on the walls of the polymerization machine.

以下、実施例を挙げて更に詳細に説明する力\本発明は
これらに除定されるものではない。実施例 1攪拌機、
温度計、還流冷却器および試料注入口を有する四つロフ
ラスコにピリジン100dを入れておき、その中に酢酸
第二銅7.5f!を攪拌しながら徐々に添加する。
Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. Example 1 Stirrer,
100 d of pyridine was placed in a four-bottle flask equipped with a thermometer, reflux condenser, and sample inlet, and 7.5 f of cupric acetate was placed in the flask. Gradually add while stirring.

内容物は発熱し濃青色となつて酢酸第二銅一ピリジン錯
体が生成する。更にインドール509をピリジン100
dに溶かし上記四つロフラスコ中へ注入する。80℃で
8時間反応せしめた後、反応生成物を減圧下に濃縮した
The contents generate heat and turn dark blue, producing a cupric acetate-pyridine complex. Furthermore, indole 509 is pyridine 100
d and injected into the above-mentioned four-hole flask. After reacting at 80° C. for 8 hours, the reaction product was concentrated under reduced pressure.

得られた生成物をアセトン500dで抽出し酢酸第二銅
一ピリジン錯体を可能な限り分離した。アセトン抽出液
を減圧下で濃縮し、乾固した。更に、微量の生成物中の
酢酸第二銅を除去するため得らノれた生成物をこれと等
重量の水で洗浄を繰り返し行つb未反応インドールは水
蒸気蒸留して取り除き生成物239を得た。
The obtained product was extracted with 500 d of acetone to separate as much of the cupric acetate-pyridine complex as possible. The acetone extract was concentrated under reduced pressure to dryness. Furthermore, in order to remove a trace amount of cupric acetate in the product, the obtained product is repeatedly washed with an equal weight of water.b Unreacted indole is removed by steam distillation and product 239 is obtained. Obtained.

この得られた生成物をエタノールリベンゼン=1:9に
溶解し、シリカゲルを用いたカラムクロマトグラフイ一
によつて分離精製し3,3′−ジインドリル59、3,
3′−ジィンドレニニリデン59を得た。生成物の構造
の確認は薄層クロマトグラフイ一、融点によつてガゼツ
タ・キミカ・イタリアーナ1939年、69巻、562
頁、およびジヤーナル・オブ・ザ・ケミカル・ソサイア
テイ、1957年、4141頁に記載されている方法に
よつて得られる3,3′−ジインドリルあるいは3,3
/−ジインドレニニリデンのそれらと比較して行つた。
The obtained product was dissolved in ethanolivenzene = 1:9, separated and purified by column chromatography using silica gel, and 3,3'-diindolyl 59,3,
3'-Diindolenylidene 59 was obtained. The structure of the product can be confirmed by thin-layer chromatography and its melting point.
and Journal of the Chemical Society, 1957, p. 4141.
/--diindolenylidene.

吸着剤としてシリカゲル(ワコーゲルB−5F)、展開
溶媒としてエタノールリベンゼン=1:9を用いて行つ
たときの薄層クロマトグラフイ一のRf値および融点を
表−1に示しtら上記結果から、3,3′−ジインドリ
ルおよび3,3′一ジインドレニニリデンが生成してい
ることが確認央れた。
Table 1 shows the Rf values and melting points of thin layer chromatography performed using silica gel (Wako Gel B-5F) as an adsorbent and ethanol livenzene = 1:9 as a developing solvent. , 3,3'-diindolyl and 3,3'-diindoleninylidene were confirmed to be produced.

実=温;を60℃とした以外は実施例1と同様の方法で
反応せしめた後、反応生成物を減圧下に濃縮した。
The reaction was carried out in the same manner as in Example 1 except that the temperature was 60° C., and then the reaction product was concentrated under reduced pressure.

得られた生成物と等重量の水で洗浄を5回繰り返した後
、水蒸気蒸留して未反応インドールを除去し反応生成物
16gを得た。また、反応生成物の精製は実施例1に示
した方法で行ない3,3′−ジインドリル59を得た。
実施例1と同様に行つた薄層クロマトグラフイ一および
融点の測定結果を表−2に示した。
After washing was repeated five times with water of the same weight as the obtained product, unreacted indole was removed by steam distillation to obtain 16 g of a reaction product. Further, the reaction product was purified by the method shown in Example 1 to obtain 3,3'-diindolyl 59.
The results of thin layer chromatography and melting point measurements performed in the same manner as in Example 1 are shown in Table 2.

3p3′−ジインドレニニリデンの生成は認められなか
つたO実施例 3 酢酸第二銅を759とした以外は実施例1の場合と同様
に反応および後処理を行ない、生成物259を得た。
No formation of 3p3'-diindoleninylidene was observed. Example 3 The reaction and post-treatment were carried out in the same manner as in Example 1, except that cupric acetate was changed to 759, and product 259 was obtained. .

実施例1の場合と同様に精製し、3,37−ジインドレ
ニニリデン69を得た。
Purification was performed in the same manner as in Example 1 to obtain 3,37-diindoleninylidene 69.

実施例1と同様に行つた薄層クロマトグラフイ一および
融点の測定結果を表−3に示した。3,3′−ジインド
リルの生成は認められなかつた。
The results of thin layer chromatography and melting point measurements performed in the same manner as in Example 1 are shown in Table 3. No formation of 3,3'-diindolyl was observed.

Claims (1)

【特許請求の範囲】[Claims] 1 インドールを出発原料として3,3′−ジインドリ
ルおよび3,3′−ジインドレニニリデンよりなる群よ
り選ばれたインドール誘導体を製造するにあたり、触媒
として酢酸第二銅−ピリジン錯体を用いることを特徴と
するインドール誘導体の製造方法。
1. In producing an indole derivative selected from the group consisting of 3,3'-diindolyl and 3,3'-diindolenylidene using indole as a starting material, it is recommended to use a cupric acetate-pyridine complex as a catalyst. Characteristic method for producing indole derivatives.
JP49091736A 1974-08-09 1974-08-09 Method for producing indole derivatives Expired JPS5922700B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49091736A JPS5922700B2 (en) 1974-08-09 1974-08-09 Method for producing indole derivatives

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49091736A JPS5922700B2 (en) 1974-08-09 1974-08-09 Method for producing indole derivatives

Publications (2)

Publication Number Publication Date
JPS5119764A JPS5119764A (en) 1976-02-17
JPS5922700B2 true JPS5922700B2 (en) 1984-05-28

Family

ID=14034791

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49091736A Expired JPS5922700B2 (en) 1974-08-09 1974-08-09 Method for producing indole derivatives

Country Status (1)

Country Link
JP (1) JPS5922700B2 (en)

Also Published As

Publication number Publication date
JPS5119764A (en) 1976-02-17

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