JPS60104044A - Production of n-alkyl-1,2-dimethylpropylamine - Google Patents

Production of n-alkyl-1,2-dimethylpropylamine

Info

Publication number
JPS60104044A
JPS60104044A JP21286083A JP21286083A JPS60104044A JP S60104044 A JPS60104044 A JP S60104044A JP 21286083 A JP21286083 A JP 21286083A JP 21286083 A JP21286083 A JP 21286083A JP S60104044 A JPS60104044 A JP S60104044A
Authority
JP
Japan
Prior art keywords
general formula
hydrogen
catalyst
primary amine
formula
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
JP21286083A
Other languages
Japanese (ja)
Other versions
JPS625898B2 (en
Inventor
Shinji Morishita
森下 真司
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.)
Koei Chemical Co Ltd
Original Assignee
Koei 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 Koei Chemical Co Ltd filed Critical Koei Chemical Co Ltd
Priority to JP21286083A priority Critical patent/JPS60104044A/en
Publication of JPS60104044A publication Critical patent/JPS60104044A/en
Publication of JPS625898B2 publication Critical patent/JPS625898B2/ja
Granted legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To produce the titled compound useful as a raw material of pharmaceuticals and pesticides, easily, by the catalytic reduction of methyl isopropyl ketone and a primary amine with hydrogen in the presence of a Pd catalyst. CONSTITUTION:The objective compound of formula I can be produced by the catalytic reduction of methyl isopropyl ketone (MIPK) and a primary amine of formula R-NH2 (R is 1-4C alkyl) with hydrogen in the presence of a Pd catalyst at 50-150 deg.C. The hydrogen partial pressure of the reaction system is >=1atm, preferably 5-100atm. EFFECT:The objective compound can be produced in high selectivity, yield and purity by the use of the Pd catalyst. There occurs little side reactions, and the production of the aldol condensation product of MIPK is negligible.

Description

【発明の詳細な説明】 本発明は一般式CI) (式中、Rは炭素数1〜4のアルキル基を示す) で表わされるN−アルキル−1,2−ジメチルプロヒル
アミンの製造法に関する。更に詳しくはメチルインプロ
ピルケトン(以下MI PKと略す)と一般式(II) R−NH2(II) (式中、Rは前記と同じ) で表わされる1級アミンとをパラジウム触媒のイf在下
接触水素還元せしめ一般式(I)の化合物を製造する方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing N-alkyl-1,2-dimethylproylamine represented by the general formula CI) (wherein R represents an alkyl group having 1 to 4 carbon atoms) . More specifically, methyl impropyl ketone (hereinafter abbreviated as MIPK) and a primary amine represented by the general formula (II) R-NH2(II) (wherein R is the same as above) were combined in the presence of a palladium catalyst. The present invention relates to a method for producing a compound of general formula (I) by catalytic hydrogen reduction.

一般式(I)の化合物は医薬、農薬の原料として有用で
ある。この一般式(I)の化合物の従来知られた製造法
としては2−アルキルアミノ−2−メチルブタン−3−
オールを出発原料として用いる方法のみである(G、H
enn1on箸J、O,C,302G50 (lae5
))。この方法によれば、出発原料をJ1!化水素及び
jiA化チオニルで処理して水酸基を111素に置換し
、次いで転位を伴なう脱塩酸反応を行ない得られたN−
アルキル−1,2−ジメチルアリルアミンを水素添加し
て一般式(I)の化合物を製造するという長い工程を経
なけれがならず、工業的に右利な製造法ではない。
The compound of general formula (I) is useful as a raw material for medicines and agricultural chemicals. A conventionally known method for producing the compound of general formula (I) is 2-alkylamino-2-methylbutane-3-
The only method using ol as a starting material (G, H
enn1on chopsticks J, O, C, 302G50 (lae5
)). According to this method, the starting material is J1! The resulting N-
It is not an industrially advantageous production method because it requires a long process of hydrogenating alkyl-1,2-dimethylallylamine to produce the compound of general formula (I).

木発明者らは、一般に入手が容易であるMIPKと一般
式(II)の1級アミンとを接触水素還元する方法を鋭
74検i・1シた結果、還元触媒として最も汎用される
ラネーニッケルやラネーコバルI・を使用した場合には
、生成物は複雑な混合物であり、目的物の一般式(I)
の化合物への選択率は極めて低いものであった。そこで
、更に鋭意検討した処、触媒としてパラジウムを用いる
ことにより始めて高選択的、高収率で高純度の一般式(
I)の化合物が得られることを見い出し、本発明を完成
するに至った。
The inventors conducted extensive research on a method for catalytic hydrogen reduction of MIPK, which is generally easily available, and the primary amine of general formula (II), and found that Raney nickel, which is the most commonly used reduction catalyst, When using Raney Kobal I, the product is a complex mixture, with the general formula (I) of the desired product
The selectivity to the compound was extremely low. After further intensive study, we discovered that by using palladium as a catalyst, we were able to achieve high selectivity, high yield, and high purity with the general formula (
It was discovered that the compound I) could be obtained, and the present invention was completed.

本発明において使用される一般式(II)の1級アミン
としては、例えばメチルアミン、エチルアミン、プロピ
ルアミン、又はブチルアミンであり、その使用早はMI
PKに対して0.8〜2イ8モルの割合である。パラジ
ウム触媒はアルミナ、ケインウ上、白土、又は活性炭の
ような担体にパラジウムを111持させたものである。
The primary amine of general formula (II) used in the present invention is, for example, methylamine, ethylamine, propylamine, or butylamine, and the early use thereof is MI
The ratio is 0.8 to 28 moles to PK. Palladium catalysts are palladium 111 supported on a support such as alumina, silica, clay, or activated carbon.

該触媒に含有されているパラジウムの星は昔通0.2〜
l O屯−hi%の範囲内で選択される。該触媒はMI
 PKに対して0.1〜20爪量%の割合で用いられる
The palladium star contained in this catalyst is traditionally 0.2 ~
It is selected within the range of l O ton - hi%. The catalyst is MI
It is used at a ratio of 0.1 to 20% by nail amount based on PK.

次いで反応条件としては、反応圧は常圧風−11、好ま
しくは5〜100気圧の水素分圧で行なうのが良い。反
応温度は室温以」−1好ましくは50〜150°Cの範
囲内で行なうのが適当である。本反応には溶媒は特に必
要としないか、溶媒の存在下でも行なうことができる。
Next, as for the reaction conditions, the reaction pressure is preferably atmospheric pressure air -11, preferably hydrogen partial pressure of 5 to 100 atmospheres. The reaction temperature is suitably carried out at room temperature or lower, preferably within the range of 50 to 150°C. This reaction does not particularly require a solvent, or can be carried out in the presence of a solvent.

溶媒としては反応条件ドで不活性な液体が選ばれるが、
その代表的なものとして、n−ヘキサンのような飽和炭
化水素、メタノールのような飽和アルコール、ジオキサ
ンのような環状エーテル及び水などが挙げられる。
As the solvent, an inert liquid is selected under the reaction conditions, but
Typical examples include saturated hydrocarbons such as n-hexane, saturated alcohols such as methanol, cyclic ethers such as dioxane, and water.

本発明に従えば、1〜5時間で反応が完結し、副反応は
殆ど起らず、高収率で接触水素還元が達成される。即ち
、高純度の一般式(I)の化合物はMI PKに対して
96%以上の収率で得られ、MI PKのアルド−ル縮
合物は実質的に生成しないと云う極めて有利な製造法で
ある。
According to the present invention, the reaction is completed in 1 to 5 hours, almost no side reactions occur, and catalytic hydrogen reduction is achieved in high yield. That is, it is an extremely advantageous production method in which a highly purified compound of general formula (I) can be obtained in a yield of 96% or more based on MI PK, and an aldol condensate of MI PK is not substantially produced. be.

次に、実施例を挙げて本発明を説明する。但し本発明は
これに限定されるものではなl、N。
Next, the present invention will be explained by giving examples. However, the present invention is not limited to this.

実施例1 1文容量の電磁攪拌式オートクレーブにMIPK258
g、 70%エチルアミン水溶液193g、及び5%P
d−カーホン2.6gを仕込み、それに水素を導入して
圧力を20気圧にし、60°Cで接触水素還元した。反
応が進行するにつれ水素圧力は減少するので、逐次水素
を追加した。2時間で水素の吸収はなくなり反応が終了
した。得られた反応液をろ過して触媒を除去し、分液し
て、油層を蒸留して純度(ガスクロマトグラフィーによ
る、以−ドl+t1様) 99.8%のN−エチル−1
,2−ジメチルプロピルアミン338g (収率98.
0%)を得た。
Example 1 MIPK258 in a 1-liter capacity electromagnetic stirring autoclave
g, 193 g of 70% ethylamine aqueous solution, and 5% P
2.6 g of d-carphone was charged, hydrogen was introduced thereto to make the pressure 20 atm, and catalytic hydrogen reduction was carried out at 60°C. As the reaction progressed, the hydrogen pressure decreased, so hydrogen was added sequentially. After 2 hours, hydrogen absorption stopped and the reaction was completed. The resulting reaction solution was filtered to remove the catalyst, separated, and the oil layer was distilled to obtain N-ethyl-1 with a purity of 99.8% (by gas chromatography, 1+t1).
, 2-dimethylpropylamine 338g (yield 98.
0%) was obtained.

実施例2 1文容hiの電磁攪拌式オートクレーブにMIPK25
8g、 40%メチルアミン水溶液233g、 5%P
d−カーボン2.6gを仕込み、それに水素を導入して
圧力を20気圧にし、50°Cで接触水素還元した。反
応が進行するにつれ水素圧力は減少するので、逐次水素
を追加した。1.5時間で水素の吸収はなくなり反応が
終了した。次いで実施例1と1i11様に処理して純度
99.5%のN−メチル−1,2=ニジメチルプロピル
アミン29g (収−9& !36 、7%)を得た。
Example 2 MIPK25 in a 1-liter electromagnetic stirring autoclave
8g, 40% methylamine aqueous solution 233g, 5%P
2.6 g of d-carbon was charged, hydrogen was introduced thereto to make the pressure 20 atm, and catalytic hydrogen reduction was carried out at 50°C. As the reaction progressed, the hydrogen pressure decreased, so hydrogen was added sequentially. After 1.5 hours, hydrogen absorption stopped and the reaction was completed. The mixture was then treated in the same manner as in Example 1 and 1i11 to obtain 29 g of N-methyl-1,2=nidimethylpropylamine with a purity of 99.5% (yield: -9&!36, 7%).

出卸人 広栄化学上業株式会ン1Distributor: Koei Chemical Industry Co., Ltd. 1

Claims (1)

【特許請求の範囲】 1、一般式(1): %式%() (式中、Rは炭素数1〜4のアルキル基を示す) で表わされるN−アルキル−1,2−ジメチルプロピル
アミンを製造するにあたり、メチルイソプロピルケトン
と一般式(II) :RNH2(II) (式中、Rは前記と同じ) で表わされる1級アミンとをパラジウム触媒のイl在下
接触水素還元することを特徴とするN−フルキル−1,
2−ジメチルプロピルアミンの製造法。 2、一般式(II)の1級アミンをメチルイソプロピル
ケトンに対し0.8〜2倍モルの割合で用い、50〜1
50°Cの反応温度で接触水素量光を行なう特許請求の
範囲第1項記載の方法。 3、一般式(IT)の1級アミンがエチルアミンである
特許請求の範囲第1項記載の方法。
[Claims] 1. General formula (1): N-alkyl-1,2-dimethylpropylamine represented by the formula % (in the formula, R represents an alkyl group having 1 to 4 carbon atoms) In producing , methyl isopropyl ketone and a primary amine represented by the general formula (II): RNH2(II) (wherein R is the same as above) are subjected to catalytic hydrogen reduction in the presence of a palladium catalyst. N-furkyl-1,
Method for producing 2-dimethylpropylamine. 2. Using the primary amine of general formula (II) in a molar ratio of 0.8 to 2 times to methyl isopropyl ketone, 50 to 1
The method according to claim 1, wherein the catalytic hydrogen quantification is carried out at a reaction temperature of 50°C. 3. The method according to claim 1, wherein the primary amine of general formula (IT) is ethylamine.
JP21286083A 1983-11-11 1983-11-11 Production of n-alkyl-1,2-dimethylpropylamine Granted JPS60104044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21286083A JPS60104044A (en) 1983-11-11 1983-11-11 Production of n-alkyl-1,2-dimethylpropylamine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21286083A JPS60104044A (en) 1983-11-11 1983-11-11 Production of n-alkyl-1,2-dimethylpropylamine

Publications (2)

Publication Number Publication Date
JPS60104044A true JPS60104044A (en) 1985-06-08
JPS625898B2 JPS625898B2 (en) 1987-02-07

Family

ID=16629499

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21286083A Granted JPS60104044A (en) 1983-11-11 1983-11-11 Production of n-alkyl-1,2-dimethylpropylamine

Country Status (1)

Country Link
JP (1) JPS60104044A (en)

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
SB VYS SK CHEM TECHNOL PRAZE ORG CHEM TECHNOL=1973 *

Also Published As

Publication number Publication date
JPS625898B2 (en) 1987-02-07

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