JPS6372661A - Production of alkylhydrazines - Google Patents

Production of alkylhydrazines

Info

Publication number
JPS6372661A
JPS6372661A JP61218729A JP21872986A JPS6372661A JP S6372661 A JPS6372661 A JP S6372661A JP 61218729 A JP61218729 A JP 61218729A JP 21872986 A JP21872986 A JP 21872986A JP S6372661 A JPS6372661 A JP S6372661A
Authority
JP
Japan
Prior art keywords
hydrazine
formula
inorganic acid
reaction
mol
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
JP61218729A
Other languages
Japanese (ja)
Other versions
JPH0742260B2 (en
Inventor
Tsukasa Maekawa
司 前川
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.)
Otsuka Chemical Co Ltd
Original Assignee
Otsuka Chemical 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 Otsuka Chemical Co Ltd filed Critical Otsuka Chemical Co Ltd
Priority to JP61218729A priority Critical patent/JPH0742260B2/en
Publication of JPS6372661A publication Critical patent/JPS6372661A/en
Publication of JPH0742260B2 publication Critical patent/JPH0742260B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

Abstract

PURPOSE:To obtain the titled compound useful as a raw material for agricultural chemicals, drugs, blowing agents, etc., by the use of inexpensive raw materials economically and in high yield, by reacting hydrazine with an olefinic hydrocarbon in the presence of an inorganic acid. CONSTITUTION:Hydrazine is reacted with an olefinic hydrocarbon shown by formula I (R<1>, R<2> and R<3> may be same or different and are H or lower alkyl) in the presence of an inorganic acid usually at about 70-150 deg.C, preferably about 90-110 deg.C to give compounds shown by formula II and formula III. A hydrohalogenic acid, sulfuric acid, alkali hydrogensulfate, etc., are used as the inorganic acid and the amount of the inorganic acid used is preferably 1-5mol based on 1mol hydrazine. Hydrazine is usually used in an aqueous solution of an inorganic acid salt of hydrazine or hydrazine hydrate. The amount of the compound shown by formula I is preferably 0.5-1.5mol based on 1mol hydrazine when the compound shown by formula II is synthesized.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はアルキルヒドラノンの新規な製造方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a novel method for producing alkylhydranone.

(従来の技術) アルキルヒドラジン類は農薬、医薬、発泡剤等の原料と
して有用な化合物である。
(Prior Art) Alkylhydrazines are compounds useful as raw materials for agricultural chemicals, medicines, foaming agents, and the like.

従来より、ヒドラジンを原料とするアルキルヒドラノン
、特にtert−ブチルヒドラジンの製造方法が種々、
開発されている。米国特許第4.248,800号では
、クロラミンを水酸化カリウムおよびtert−ブチル
アミンと反応させて、tert−プチルヒドラジンを製
造する方法が開示されている。しかしtert−ブチル
7ミンはtert−ブチルクロライドとアンモニアより
製造されるものであり高価である。特公昭57−212
67号ではヒドラノンの無機酸塩とtert−ブチルハ
ライドを反応させてLert−ブチルヒドラノンの無機
酸塩を製造する方法が開示されている。しかしjerk
−ブチルハライドはtert−ブタノールとハロゲン化
水素から製造されるものであり高価である。特開昭59
−137453号ではヒドラジン・ハロゲン化水素酸塩
とtert −ブタノールとをヒドラジン・ジハロゲン
化水素酸塩またはハロゲン化水素の存在下に反応させて
、tert−ブチルヒドラジン・ハロゲン化水素酸塩を
製造する方法が開示されている。しかしtert−ブチ
ルアルコールはインブチレンの水利反応により製造され
るものであり高価である。
Conventionally, there have been various methods for producing alkylhydranone, especially tert-butylhydrazine, using hydrazine as a raw material.
being developed. U.S. Pat. No. 4,248,800 discloses a method for producing tert-butylhydrazine by reacting chloramine with potassium hydroxide and tert-butylamine. However, tert-butyl 7mine is produced from tert-butyl chloride and ammonia and is expensive. Tokuko Sho 57-212
No. 67 discloses a method for producing an inorganic acid salt of lert-butylhydranone by reacting an inorganic acid salt of hydranone with tert-butyl halide. But jerk
-Butyl halide is produced from tert-butanol and hydrogen halide and is expensive. Japanese Unexamined Patent Publication 1983
-137453 discloses a method for producing tert-butylhydrazine hydrohalide by reacting hydrazine hydrohalide and tert-butanol in the presence of hydrazine dihydrohalide or hydrogen halide. is disclosed. However, tert-butyl alcohol is produced by a water utilization reaction of inbutylene and is expensive.

(発明が解決しようとする問題点) 本発明は安価な原料を使用し、高収率でフルキルヒドラ
ジン類を得ることができる経済的に有利なフルキルヒド
ラジン類の製造方法を提供することにある。
(Problems to be Solved by the Invention) The purpose of the present invention is to provide an economically advantageous method for producing furkylhydrazines, which uses inexpensive raw materials and can obtain furkylhydrazines in high yields. be.

(問題点を解決するための手段) 本発明は無機酸の存在下で、ヒドラジンと式(1)%式
%(1) (式中、R’、R2およVB2は同一でも異なってもよ
く、それぞれ水素原子又は低級フルキル基を示す)で表
わされるオレフィン系炭化水素を反応させることを特徴
とする式(2) %式%(2) (式中、R’、R2およびR3は上記と同意義を有する
)および式(3) %式% (式中R’、R2およびR3は上記と同意残有する)で
表わされるフルキルヒドラノン類の製造方法に係る。
(Means for Solving the Problems) The present invention provides a method of combining hydrazine with formula (1)% formula% (1) (wherein R', R2 and VB2 may be the same or different) in the presence of an inorganic acid. , each representing a hydrogen atom or a lower furkyl group). and formula (3) (in which R', R2 and R3 have the same meanings as above).

上記において低級アルキル基としては炭素数1〜6のア
ルキル基を挙げることができる。
In the above, examples of lower alkyl groups include alkyl groups having 1 to 6 carbon atoms.

本発明のフルキルヒドラジンの製造方法における反応機
構の詳細は解明されていないが、無8!酸(これをHA
とする)の存在下でヒドラノンとオレフィン系炭化水素
を反応させて、アルキルヒドラノン類無磯酸塩が生成す
る際、以下のように反応が進行するものと推測される。
Although the details of the reaction mechanism in the method for producing furkylhydrazine of the present invention have not been elucidated, there is no 8! acid (this is HA
When hydranone and olefinic hydrocarbon are reacted in the presence of hydranone and olefinic hydrocarbon to produce an alkylhydranone-based salt, the reaction is presumed to proceed as follows.

但し本発明は上記の反応機構の推測によって、制限を受
けるものではない。
However, the present invention is not limited by the speculation of the reaction mechanism described above.

上記反応式(2)及び(3)によって形成されたアルキ
ルヒドラノン類の無機酸塩は、アルカリ例えば水酸化ナ
トリウムで中和することにより、対応するアルキルヒド
ラジン類に変換することができる。
The inorganic acid salts of alkylhydranones formed by the above reaction formulas (2) and (3) can be converted into the corresponding alkylhydrazines by neutralizing with an alkali such as sodium hydroxide.

本発明におけるヒドラジンは通常、ヒドラジンヒトラー
ドあるいはヒドラノンの無機酸塩の水溶液を使用する。
The hydrazine used in the present invention is usually an aqueous solution of an inorganic acid salt of hydrazine hittride or hydranone.

ヒドラジン水溶液の濃度は特に限定されないが、ヒドラ
ジンヒトラードの場合、好ましくは約60〜80重量%
の水溶液を使用する0本発明におけるオレフィン系炭化
水素を例示すると、エチレン、プロピレン、インブチレ
ン、ブテン−1、プデンー2.2−メチル−ブテン−2
、ペンテン−1等を挙げることができる。オレフィン系
炭化水素の使用量は、式(2)で表わされるモノアルキ
ルヒドラクンを製造する場合と式(3)で表わされるジ
アルキルヒドラジンを製造する場合とで異なる。モノア
ルキルヒドラジンを主目的として製造する場合、オレフ
ィン系炭化水素の使用量は、ヒドラジン1モルに対して
通常2モル以下、好ましくは0.5〜1.5モルの範囲
である。一方、ジアルキルヒドラジンを主目的として製
造する場合、オレフィン系炭化水素の使用量はヒドラノ
ン1モルに対して通常2モル以上、好ましくは5〜15
モルの範囲である。
The concentration of the hydrazine aqueous solution is not particularly limited, but in the case of hydrazine hydride, it is preferably about 60 to 80% by weight.
Examples of olefinic hydrocarbons in the present invention include ethylene, propylene, imbutylene, butene-1, pudene-2, and 2-methyl-butene-2.
, pentene-1, and the like. The amount of olefinic hydrocarbon used differs depending on whether the monoalkylhydracne represented by formula (2) is produced or the dialkylhydrazine represented by formula (3) is produced. When producing monoalkylhydrazine as the main objective, the amount of olefinic hydrocarbon used is usually 2 mol or less, preferably 0.5 to 1.5 mol, per 1 mol of hydrazine. On the other hand, when producing dialkylhydrazine as the main objective, the amount of olefinic hydrocarbon used is usually 2 mol or more, preferably 5 to 15 mol, per 1 mol of hydranone.
It is in the molar range.

本発明における無機酸は、例えばハロゲン化水素酸、硫
酸、硫酸水素アルカリ、リン酸等の1種または1種以上
である。ハロゲン化水素酸として、HCI、HBr、H
I等を挙げることができる。無機酸の使用量はヒドラジ
ン1モルに対して1モル以上、好ましくは1〜5モルの
範囲で使用する。
The inorganic acid in the present invention is, for example, one or more of hydrohalic acid, sulfuric acid, alkali hydrogen sulfate, phosphoric acid, and the like. As hydrohalic acid, HCI, HBr, H
Examples include I. The amount of inorganic acid used is 1 mol or more, preferably 1 to 5 mol, per 1 mol of hydrazine.

ヒドラジンがヒドラジンの無機酸塩の形で使用されると
きは、ヒドラジン無機酸塩1モルに対し、塩を形成して
いる無機酸のモル数と、塩を形成していない11離の無
機酸のモル数の合計が1〜5モルの範囲になるように使
用する。無機酸の形態は特に限定されないが、通常水溶
液で使用し濃度は20〜70重量%の範囲が好ましい。
When hydrazine is used in the form of an inorganic acid salt of hydrazine, the number of moles of the inorganic acid forming the salt and the number of moles of the inorganic acid not forming the salt per 1 mole of the inorganic acid salt of hydrazine. It is used so that the total number of moles is in the range of 1 to 5 moles. The form of the inorganic acid is not particularly limited, but it is usually used in the form of an aqueous solution and preferably has a concentration in the range of 20 to 70% by weight.

本発明において反応原料の添加順序は特に限定されず、
任意の順序で添加することができる。但しモノアルキル
ヒドラクンを製造する場合、無機酸とヒドラジンあるい
はヒドラノン無機酸塩溶液に、オレフィン系炭化水素を
徐々に導入しながら反応させた方が好ましい。またジア
ルキルヒドラジンを製造する場合、無機酸とオレフィン
系炭化水素の溶液に、ヒドラジンを徐々に導入しながら
反応させた方が好ましい。本発明の反応温度は通常約7
0〜150°C1好ましくは約90〜110℃の範囲で
ある。本発明の反応圧力は常圧下、密閉系における自発
主圧力下あるいは、不活性がス等による加圧下のいずれ
の場合でも実施することができる。
In the present invention, the order of addition of reaction raw materials is not particularly limited,
They can be added in any order. However, when producing monoalkyl hydracune, it is preferable to react the inorganic acid with the hydrazine or hydranone inorganic acid salt solution while gradually introducing the olefinic hydrocarbon. Further, when producing dialkylhydrazine, it is preferable to gradually introduce hydrazine into a solution of an inorganic acid and an olefinic hydrocarbon while causing the reaction. The reaction temperature of the present invention is usually about 7
The temperature is in the range of 0 to 150°C, preferably about 90 to 110°C. The reaction pressure of the present invention can be carried out under normal pressure, under spontaneous main pressure in a closed system, or under pressure using an inert gas or the like.

本発明の反応時間は反応温度に関与し、適宜決定するこ
とができる。例えば反応温度が100℃の場合、約2〜
4時間である。本発明の反応溶媒は反応に関与しない有
機溶媒、例えばトルエン等を使用することもできるが、
通常水を使用するのが好ましい。本発明の反応は回分式
、連続式のいずれでも実施することができる。
The reaction time of the present invention is related to the reaction temperature and can be determined as appropriate. For example, when the reaction temperature is 100°C, about 2 to
It is 4 hours. As the reaction solvent of the present invention, organic solvents that do not participate in the reaction, such as toluene, can also be used, but
It is usually preferred to use water. The reaction of the present invention can be carried out either batchwise or continuously.

本発明においては、反応終了後、反応液を冷却し犬にア
ルカリ性にすることにより生成したアルキルヒドラノン
類の無機酸塩を遊離のフルキルヒドラジン類とする。遊
離のフルキルヒドラノン類は、空気中の酸素と反応して
分解が進行する恐れがあるため窒素雰囲気にするのが好
ましい。このアルカリ水溶液を有機溶媒、例えばクロロ
ホルムを使用して抽出することにより、アルキルヒドラ
ノン類は有機層に移行する。この際、未反応ヒドラジン
は抽出されないで水層に残るため、ヒドラジンとフルキ
ルヒドラジン類を分離することができる0次叩アルキル
ヒドラジン類を含む有機層を水で逆抽出することにより
、モノアルキルヒドラジンは水層に移行し、N、N’−
ジアルキルヒドラジンは有機層に残るため、モノアルキ
ルヒドラノンとN、N’−ジアルキルヒドラジンを分離
することができる。モノアルキルヒドラジンを含む水層
をアルカリとともに蒸留することにより高純度のモノフ
ルキルヒドラジンを単離できる。またモノアルキルヒド
ラノンを含む水層に同モル数の無機酸を加え濃縮するこ
とにより、高純度のモノアルキルヒドラジン!!8!酸
塩を単離できる。N、N’−ジアルキルヒドラジンを含
む有機層を蒸留することにより、高純度のN、N’−ジ
アルキルヒドラジンを単離できる。またN、N’−ジア
ルキルヒドラジンを含む有機層を同モル数の無機酸水溶
液で逆抽出を行った後、水層を濃縮することにより、高
純度のN、N″−ジアルキルヒドラジン無機酸塩を単離
できる。
In the present invention, after the reaction is completed, the reaction solution is cooled and made alkaline to a dog, thereby converting the produced inorganic acid salts of alkylhydranones into free flukylhydrazines. Free fulkylhydranones may react with oxygen in the air and decompose, so it is preferable to use a nitrogen atmosphere. By extracting this alkaline aqueous solution using an organic solvent such as chloroform, the alkylhydranones are transferred to the organic layer. At this time, unreacted hydrazine remains in the aqueous layer without being extracted, so by back-extracting with water the organic layer containing zero-threaded alkylhydrazines that can separate hydrazine and furkylhydrazines, monoalkylhydrazine moves to the aqueous layer, N, N'-
Since dialkylhydrazine remains in the organic layer, monoalkylhydranone and N,N'-dialkylhydrazine can be separated. High purity monofurkylhydrazine can be isolated by distilling the aqueous layer containing monoalkylhydrazine together with an alkali. In addition, by adding the same number of moles of inorganic acid to the aqueous layer containing monoalkylhydranone and concentrating it, you can obtain highly pure monoalkylhydrazine! ! 8! Acid salts can be isolated. High purity N,N'-dialkylhydrazine can be isolated by distilling the organic layer containing N,N'-dialkylhydrazine. In addition, by back-extracting the organic layer containing N,N'-dialkylhydrazine with an inorganic acid aqueous solution of the same number of moles, and concentrating the aqueous layer, highly pure N,N''-dialkylhydrazine inorganic acid salts can be obtained. Can be isolated.

また本発明においては、反応終了後、未反応ヒドラジン
が少ない場合などは、反応液を冷却し生成した結晶をt
過分離し、必要に応じて再結晶することにより、高純度
のフルキルヒドラクン類の無機酸塩を単離できる。ある
いは反応液を冷却下、カセイソーダを添加した後、蒸留
することにより、高純度のフルキルヒドラジン類を単離
することもできる。
In addition, in the present invention, after the completion of the reaction, if there is little unreacted hydrazine, the reaction solution is cooled and the generated crystals are
High purity inorganic acid salts of furkylhydracunes can be isolated by excessive separation and recrystallization if necessary. Alternatively, highly pure fulkylhydrazines can be isolated by adding caustic soda to the reaction solution while cooling and then distilling the solution.

(実 施 例) 次に本発明を実施例を挙げて説明する。反応の結果につ
いて、転化率、選択率および収率として示す、これらは
次のように定義する。
(Example) Next, the present invention will be explained by giving examples. The results of the reaction are expressed as conversion rate, selectivity, and yield, which are defined as follows.

■転化率とは、反応に使用したヒドラジンに対する反応
で消費されたヒドラジンのモル%を示す。
(2) Conversion rate refers to the mol% of hydrazine consumed in the reaction relative to the hydrazine used in the reaction.

■選択率(A)とは、反応で消費されたヒドラノンに対
する生成モノアルキルヒドラジンのモル%を示す。
(2) Selectivity (A) indicates the mol% of the monoalkylhydrazine produced relative to the hydranone consumed in the reaction.

■選択率(B)とは、反応で消費されたヒドラジンに対
する生成ジアルキルヒドラジンのモル%を示す。
(2) Selectivity (B) indicates the mol% of the dialkylhydrazine produced relative to the hydrazine consumed in the reaction.

実施例1 温度計、圧力計、攪拌装置を備えた容量100m1のオ
ートクレーブに、30重1%HCl 24.3g(0,
20モル)を仕込み、これに80重量%ヒドラノンヒド
ラ−) 6.25g(0,10モル)を添加した。次に
内容物を一10℃に冷却し、イソブチレン5.6FK(
0,10モル)を導入後、系内を窒素がス雰囲気とし、
密閉後、徐々に95℃まで昇温し、同温度で3時間反応
を行なった。
Example 1 24.3 g of 30% HCl (0,
To this was added 6.25 g (0.10 mol) of 80% by weight hydranone hydra). Next, the contents were cooled to -10°C, and the contents were cooled to -10°C.
After introducing 0.10 mol), the inside of the system is made into a nitrogen gas atmosphere,
After sealing, the temperature was gradually raised to 95°C, and the reaction was carried out at the same temperature for 3 hours.

反応液の分析の結果、tert−ブチルヒドラノン塩酸
塩およびN、N’−ジーtcrt−ブチルヒドラノン塩
酸塩が生成しており、転化率93%、選択率(A)97
%、選択率(B)2%であった0反応液をカセイソーダ
でアルカリ性とし、ノクロルメタンで抽出することによ
り、未反応ヒドラジンを水層に、tert−ブチルヒド
ラジン及びN、N’−ノーtert−ブチルヒドラジン
を有n層に分離させた。
Analysis of the reaction solution revealed that tert-butylhydranone hydrochloride and N,N'-di-tcrt-butylhydranone hydrochloride were produced, with a conversion rate of 93% and a selectivity (A) of 97.
%, selectivity (B) 2% of the reaction solution was made alkaline with caustic soda and extracted with nochloromethane to remove unreacted hydrazine into the aqueous layer and tert-butylhydrazine and N,N'-not-tert-butyl Hydrazine was separated into n-layers.

有fi層を水で逆抽出し、tert−ブチルヒドラジン
を水/11こN、N’−ジーtert−ブチルヒドラノ
ンを有機層に分離させた。水層にtert−ブチルヒド
ラジンと同モル数の塩酸を加え、減圧濃縮し、110℃
で乾燥することにより白色結晶を単離した。この結晶に
ついてNMRスペクトル及びマススペクトル測定の結果
、標品のtert−ブチルヒドラジン塩酸塩のスペクト
ルと完全に一致し同定確認した。
The active layer was back-extracted with water, and tert-butylhydrazine was separated into water/11N,N'-di-tert-butylhydranone into an organic layer. Hydrochloric acid of the same number of moles as tert-butylhydrazine was added to the aqueous layer, concentrated under reduced pressure, and heated to 110°C.
White crystals were isolated by drying. As a result of NMR spectrum and mass spectrum measurements of this crystal, the spectrum completely matched that of the standard tert-butylhydrazine hydrochloride, confirming its identity.

N/20−K I O,還元滴定及びN / 10  
A g N Ox滴中の#早 大詰JLI+)、1l−
)−ゴ冬ルーVうSノソ檜酸塩の含量が99%であった
N/20-K I O, reductive titration and N/10
A g N Ox droplet # early Otsume JLI+), 1l-
) - Gofutoru V Usinoso linic acid salt content was 99%.

N、N’−ジーjerk−ブチルヒドラジンを含む有機
層に、同モル数の塩酸水溶液を加え逆抽出し、水層を減
圧濃縮し、110℃で乾燥することにより白色結晶を単
離した。この結晶はN、N’−ジーtcrt−ブチルヒ
ドラノン塩酸塩であり、含量が99%であった。
The same molar number of hydrochloric acid aqueous solution was added to the organic layer containing N,N'-jerk-butylhydrazine for back extraction, the aqueous layer was concentrated under reduced pressure, and white crystals were isolated by drying at 110°C. The crystals were N,N'-di-tcrt-butylhydranone hydrochloride with a content of 99%.

実施例2〜7 実施例1において、無機酸の種類と使用量、イソブチレ
ンの使用量および反応温度と反応時間を変化させた以外
は、同様にして反応を行った。結果を第1表に示す。
Examples 2 to 7 Reactions were carried out in the same manner as in Example 1, except that the type and amount of inorganic acid used, the amount of isobutylene used, and the reaction temperature and reaction time were changed. The results are shown in Table 1.

第  1  表 実施例8〜11 実施例1と同一装置に無機酸を仕込み、これに60重量
%ヒドラジンヒトラード8.33g(0,10モル)を
添加し、系内を窒素ガス雰囲気とし、密閉後、徐々に9
0’Cまで昇温した。これにオレフィン系炭化水素を3
時間を要して徐々に導入し、更に同温度で3時間反応を
行なった。結果を第2表に示す。
Table 1 Examples 8 to 11 Inorganic acid was charged into the same equipment as in Example 1, 8.33 g (0.10 mol) of 60% by weight hydrazine hydride was added, the system was made into a nitrogen gas atmosphere, and the system was sealed. After that, gradually 9
The temperature was raised to 0'C. Add 3 olefinic hydrocarbons to this
The mixture was gradually introduced over time, and the reaction was further carried out at the same temperature for 3 hours. The results are shown in Table 2.

第2表 本1  terL−ブチルヒドラジンおよびノ一体本2
 エチlレヒドラシンおよびノ一体木3 イソプロピル
ヒドラジンおよびシ一体本4 イソブチフレヒドラノン
およびノ一体°実施例12 実施例1と同一装置に、ヒドラジン2塩酸塩10.5g
(0,10モル)および水20gを仕込み、−10℃に
冷却しイソブチレン5.6g(0,10モル)を導入後
、県内を窒素がス雰囲気とし、密閉後、徐々に100℃
まで昇温し、同温度で3時間反応を行った0反応液の分
析の結果、tert−ブチルヒドラノン塩酸塩が生成し
ており、転化率94%、選択率(A)97%、選択率(
B)2%であった。
Table 2 Book 1 terL-butylhydrazine and monolithic book 2
3 ethyl rehydracin and hydrazine 4 hydrazine isopropylhydranone 4 isobutyfluhydranone and ethylehydranone Example 12 In the same apparatus as in Example 1, 10.5 g of hydrazine dihydrochloride was added.
(0.10 mol) and 20 g of water were charged, cooled to -10°C, and 5.6 g (0.10 mol) of isobutylene was introduced.The prefecture was made into a nitrogen atmosphere, and after being sealed, the temperature was gradually increased to 100°C.
As a result of analysis of the reaction solution obtained by raising the temperature to (
B) It was 2%.

実施例13 実施例1と同一装置に、35%HCl 20.9g(0
,20モル)を仕込み、これに80%ヒドラジンヒドラ
−) 6.25g(0,10モル)を添加した。これを
−10’Cに冷却しインブチレン14.Og(0,25
モル)を仕込み、系内を窒素ガス雰囲気とし、密閉後、
徐々に100℃まで昇温し、同温度で5時間反応を行っ
た。反応液の分析の結果、転化率98%、選択率(A)
47%、選択率(B)51%であった。
Example 13 In the same apparatus as in Example 1, 20.9 g of 35% HCl (0
, 20 mol), and 6.25 g (0.10 mol) of 80% hydrazine hydra) was added thereto. This was cooled to -10'C and inbutylene 14. Og(0,25
mol), create a nitrogen gas atmosphere in the system, and after sealing,
The temperature was gradually raised to 100°C, and the reaction was carried out at the same temperature for 5 hours. Analysis of the reaction solution showed a conversion rate of 98% and a selectivity (A).
The selectivity (B) was 47% and the selectivity (B) was 51%.

実施例14 実施例1と同一装置に、35%HCl 31.3g(0
,30モル)を仕込み、これを−10℃に冷却しイソブ
チレン56.0g(1,00モル)を仕込み、系内を窒
素ガス雰囲気とし、密閉後、徐々に90℃まで昇温した
Example 14 In the same apparatus as in Example 1, 31.3 g of 35% HCl (0
, 30 mol) was cooled to -10°C, 56.0 g (1,00 mol) of isobutylene was charged, the system was made into a nitrogen gas atmosphere, and after being sealed, the temperature was gradually raised to 90°C.

これに80%ヒドラノンヒドラ−) 6.25g(0,
10モル)を3時間を要して徐々に導入し、更に同温度
で5時間反応を行った。反応液の分析の結果、転化率1
00%、選択率(A)17%、選択率(B)82%であ
った。
Add to this 6.25g (80% hydranone hydra) (0,
10 mol) was gradually introduced over 3 hours, and the reaction was further carried out at the same temperature for 5 hours. As a result of analysis of the reaction solution, the conversion rate was 1.
The selectivity (A) was 17%, and the selectivity (B) was 82%.

(以 上)(that's all)

Claims (2)

【特許請求の範囲】[Claims] (1)無機酸の存在下で、ヒドラジンと式(1)▲数式
、化学式、表等があります▼(1) (式中、R^1、R^2およびR^3は同一でも異なつ
てもよく、それぞれ水素原子又は低級アルキル基を示す
)で表わされるオレフイン系炭化水素を反応させること
を特徴とする式(2) ▲数式、化学式、表等があります▼(2) (式中、R^1、R^2およびR^3は上記と同意義を
有する)および式(3) ▲数式、化学式、表等があります▼(3) (式中R^1、R^2およびR^3は上記と同意義有す
る)で表わされるアルキルヒドラジン類の製造方法。
(1) In the presence of an inorganic acid, hydrazine and the formula (1) ▲ have mathematical formulas, chemical formulas, tables, etc. ▼ (1) (In the formula, R^1, R^2 and R^3 may be the same or different. Formula (2) is characterized by reacting olefinic hydrocarbons represented by hydrogen atoms or lower alkyl groups, respectively) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(2) (In the formula, R^ 1, R^2 and R^3 have the same meanings as above) and formula (3) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(3) (In the formula, R^1, R^2 and R^3 are A method for producing an alkylhydrazine represented by (having the same meaning as above).
(2)無機酸がハロゲン化水素酸、硫酸、硫酸水素アル
カリ及びリン酸の群から選ばれる少なくとも1種である
特許請求の範囲第1項記載の方法。
(2) The method according to claim 1, wherein the inorganic acid is at least one selected from the group of hydrohalic acid, sulfuric acid, alkali hydrogen sulfate, and phosphoric acid.
JP61218729A 1986-09-16 1986-09-16 Method for producing alkylhydrazines Expired - Lifetime JPH0742260B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61218729A JPH0742260B2 (en) 1986-09-16 1986-09-16 Method for producing alkylhydrazines

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61218729A JPH0742260B2 (en) 1986-09-16 1986-09-16 Method for producing alkylhydrazines

Publications (2)

Publication Number Publication Date
JPS6372661A true JPS6372661A (en) 1988-04-02
JPH0742260B2 JPH0742260B2 (en) 1995-05-10

Family

ID=16724521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61218729A Expired - Lifetime JPH0742260B2 (en) 1986-09-16 1986-09-16 Method for producing alkylhydrazines

Country Status (1)

Country Link
JP (1) JPH0742260B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4946867A (en) * 1987-09-07 1990-08-07 Sumitomo Chemical Company, Limited Cyanoacetamide derivative, and plant disease protectant comprising the same as an active ingredient
US4954655A (en) * 1989-03-31 1990-09-04 Rohm And Haas Company Preparation of alkylhydrazines
EP0704427A1 (en) 1994-09-29 1996-04-03 Bayer Ag Process for the preparation of alkylhydrazine salz
EP0989204A1 (en) * 1998-09-25 2000-03-29 Japan Pionics Co., Ltd. Process for preparing nitride film

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610159A (en) * 1979-07-05 1981-02-02 Nippon Hidorajin Kogyo Kk Production of tertiary-butylhydrazine inorganic acid salt
JPS59137453A (en) * 1983-01-25 1984-08-07 Nippon Hidorajin Kogyo Kk Preparation of tert-butylhydrazine

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610159A (en) * 1979-07-05 1981-02-02 Nippon Hidorajin Kogyo Kk Production of tertiary-butylhydrazine inorganic acid salt
JPS59137453A (en) * 1983-01-25 1984-08-07 Nippon Hidorajin Kogyo Kk Preparation of tert-butylhydrazine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4946867A (en) * 1987-09-07 1990-08-07 Sumitomo Chemical Company, Limited Cyanoacetamide derivative, and plant disease protectant comprising the same as an active ingredient
US4954655A (en) * 1989-03-31 1990-09-04 Rohm And Haas Company Preparation of alkylhydrazines
EP0704427A1 (en) 1994-09-29 1996-04-03 Bayer Ag Process for the preparation of alkylhydrazine salz
EP0989204A1 (en) * 1998-09-25 2000-03-29 Japan Pionics Co., Ltd. Process for preparing nitride film

Also Published As

Publication number Publication date
JPH0742260B2 (en) 1995-05-10

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