JPH0597777A - Method for purifying ethyleneamine - Google Patents

Method for purifying ethyleneamine

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Publication number
JPH0597777A
JPH0597777A JP29489591A JP29489591A JPH0597777A JP H0597777 A JPH0597777 A JP H0597777A JP 29489591 A JP29489591 A JP 29489591A JP 29489591 A JP29489591 A JP 29489591A JP H0597777 A JPH0597777 A JP H0597777A
Authority
JP
Japan
Prior art keywords
ethyleneamine
alkylated
ethylenediamine
pyrazines
ethylethylenediamine
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
JP29489591A
Other languages
Japanese (ja)
Other versions
JP3134418B2 (en
Inventor
Yasushi Hara
靖 原
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.)
Tosoh Corp
Original Assignee
Tosoh Corp
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Filing date
Publication date
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Priority to JP03294895A priority Critical patent/JP3134418B2/en
Publication of JPH0597777A publication Critical patent/JPH0597777A/en
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Publication of JP3134418B2 publication Critical patent/JP3134418B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PURPOSE:To obtain a method for removing an N-alkylated ethyleneamine and pyrazines produced as by-products in producing ethyleneamine. CONSTITUTION:An aqueous solution of ethylene amine is extracted with an organic solvent to separate an N-alkylated ethyleneamine and pyrazines in the organic phase from ethyleneamine in the water solution.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はエチレンアミンの精製方
法に関する。エチレンアミンは農薬,キレート剤,エポ
キシ硬化剤,湿潤紙力増強剤,潤滑油添加剤等に使用さ
れる有用な脂肪族アミン化合物である。
TECHNICAL FIELD The present invention relates to a method for purifying ethyleneamine. Ethyleneamine is a useful aliphatic amine compound used as a pesticide, a chelating agent, an epoxy curing agent, a wet paper strengthening agent, a lubricating oil additive and the like.

【0002】[0002]

【従来の技術】エチレンアミンの製造法として、二塩化
エチレン及びアンモニアから製造する方法が知られてい
る。この方法は広く実施されており、N−アルキル化エ
チレンアミン及び/又はピラジン類等の不純物の少ない
エチレンアミンを製造することが可能であるが、副生物
として多量の塩が生成するため、この分離及び処理に費
用がかかるという欠点を有する。そのため無機塩類を含
むエチレンアミン水溶液から有機溶媒でエチレンアミン
を抽出する方法,活性炭でエチレンアミンを吸着除去す
る方法などが研究されている。
2. Description of the Related Art As a method for producing ethyleneamine, a method for producing ethyleneamine from ethylene dichloride and ammonia is known. This method is widely practiced, and it is possible to produce ethylene amine having a small amount of impurities such as N-alkylated ethylene amine and / or pyrazines, but since a large amount of salt is produced as a by-product, this separation is performed. And has the drawback of being expensive to process. Therefore, research has been conducted on methods such as extracting ethyleneamine from an aqueous solution of ethyleneamine containing inorganic salts with an organic solvent and adsorbing and removing ethyleneamine with activated carbon.

【0003】二塩化エチレンを原料とする方法の他に、
エチレンアミンを製造する方法として、モノエタノール
アミンを原料とする方法も知られている。この方法は、
二塩化エチレンを原料とする方法に比べて、塩の副生問
題は無いが、N−アルキル化エチレンアミン及びピラジ
ン類等の不純物が多量に生成するという問題を有する。
N−アルキル化エチレンアミン及びピラジン類はエチレ
ンアミンの品質を低下させ、その利用分野を著しく減少
させる。したがってN−アルキル化エチレンアミン及び
ピラジン類をエチレンアミンから分離する必要がある
が、これらは、沸点が近いため蒸留では分離困難であ
る。
In addition to the method using ethylene dichloride as a raw material,
As a method for producing ethyleneamine, a method using monoethanolamine as a raw material is also known. This method
Compared with the method using ethylene dichloride as a raw material, there is no problem of by-product of salt, but there is a problem that impurities such as N-alkylated ethylene amine and pyrazines are produced in a large amount.
N-alkylated ethylene amines and pyrazines reduce the quality of ethylene amines and significantly reduce their field of use. Therefore, it is necessary to separate N-alkylated ethyleneamines and pyrazines from ethyleneamines, but these are difficult to separate by distillation because of their close boiling points.

【0004】また、エチレンアミンを製造する方法とし
て、青酸を原料とする方法も研究されているが、この方
法ではエチレンアミンと分離が困難なN−アルキル化エ
チレンアミンが多量に副生するため、工業化されていな
い。
As a method for producing ethyleneamine, a method using hydrocyanic acid as a raw material has also been studied. However, this method produces a large amount of N-alkylated ethyleneamine, which is difficult to separate from ethyleneamine. Not industrialized.

【0005】以上の様に、エチレンアミン中に含まれた
N−アルキル化エチレンアミン及びピラジン類を工業的
に分離する方法は未だ知られていない。
As described above, a method for industrially separating N-alkylated ethyleneamines and pyrazines contained in ethyleneamine has not been known yet.

【0006】[0006]

【発明が解決しようとする課題】上記の様に、エチレン
アミンの品質を低下させるN−アルキル化エチレンアミ
ン及びピラジン類を含むエチレンアミンを精製する方法
は未だ知られていない。
As described above, a method for purifying ethyleneamine containing N-alkylated ethyleneamine and pyrazines which deteriorates the quality of ethyleneamine has not yet been known.

【0007】特に、モノエタノールアミン又は青酸を原
料とするエチレンアミンの製造法において、副生するN
−アルキル化エチレンアミン及びピラジン類を含むエチ
レンアミンを精製することは工業的に極めて有意義なこ
とである。
In particular, N produced as a by-product in the method for producing ethyleneamine using monoethanolamine or hydrocyanic acid as a raw material.
-Purifying ethyleneamines, including alkylated ethyleneamines and pyrazines, is of great industrial significance.

【0008】したがって、N−アルキル化エチレンアミ
ン及びピラジン類を含むエチレンアミンを精製する方法
の開発が望まれている。
Therefore, it is desired to develop a method for purifying N-alkylated ethyleneamines and ethyleneamines including pyrazines.

【0009】[0009]

【課題を解決するための手段】本発明者らは、この現状
に鑑み、エチレンアミンの精製方法について鋭意検討し
た結果、N−アルキル化エチレンアミン及びピラジン類
を含むエチレンアミン水溶液を有機溶媒で抽出すること
によって、エチレンアミン中のN−アルキル化エチレン
アミン及びピラジン類を減少せしめることが可能である
という新規な事実を見出し、本発明を完成させるに至っ
た。
In view of this situation, the inventors of the present invention have made earnest studies on a method for purifying ethyleneamine, and as a result, extracted an ethyleneamine aqueous solution containing N-alkylated ethyleneamine and pyrazines with an organic solvent. By doing so, the novel fact that N-alkylated ethyleneamine and pyrazines in ethyleneamine can be reduced was found, and the present invention has been completed.

【0010】すなわち本発明は、N−アルキル化エチレ
ンアミン及び/又はピラジン類を含有するエチレンアミ
ンを精製する方法において、エチレンアミンの水溶液を
有機溶媒で抽出することを特徴とするエチレンアミンの
精製方法である。
That is, the present invention is a method for purifying ethyleneamine containing N-alkylated ethyleneamine and / or pyrazines, characterized in that an aqueous solution of ethyleneamine is extracted with an organic solvent. Is.

【0011】以下に本発明を更に詳しく説明する。The present invention will be described in more detail below.

【0012】本発明の方法においては、エチレンアミン
水溶液中のN−アルキル化エチレンアミン及び/又はピ
ラジン類を有機溶媒による抽出によって減少せしめる。
In the method of the present invention, N-alkylated ethyleneamines and / or pyrazines in the aqueous ethyleneamine solution are reduced by extraction with an organic solvent.

【0013】本発明の方法において、有機溶媒は水と相
分離するものならば使用可能である。有機溶媒として、
酢酸エチル,酢酸メチル等のエステル類、クロロメタ
ン,ジクロロメタン,クロロホルム,四塩化炭素,二塩
化エチレン等のハロゲノアルカン類、ベンゼン,トルエ
ン,キシレン等の芳香族炭化水素、メチルエチルケトン
等のケトン類、ジエチルエ−テル等のエ−テル類、n−
ブタノール,イソブタノール,sec−ブタノール,n
−アミルアルコール,活性アミルアルコール,イソアミ
ルアルコール、sec−アミルアルコール,3−ペンタ
ノール,tert−アミルアルコール,フーゼル油,n
−ヘキサノール,メチルアミルアルコール,2−エチル
ブタノール,n−ヘプタノール,2−ヘプタノール,3
−ヘプタノール,n−オクタノール,2−オクタノー
ル,2−エチルヘキサノール,3,5,5−トリメチル
ヘキサノール,ノナノール,n−デカノール,ウンデカ
ノール,n−ドデカノール,トリメチルノニルアルコー
ル,テトラデカノール,ヘプタデカノール,シクロヘキ
サノール,2−メチルシクロヘキサノール,ベンジルア
ルコール,フェネチルアルコール等のアルコ−ル類が使
用できるが、その中でも、N−アルキル化エチレンアミ
ン,ピラジン類を選択的に抽出できるエステル類及び/
又はハロゲノアルカン類、又はアルコ−ル類が好まし
い。これらの有機溶媒は単一で使用しても良いし、多成
分を混合して使用しても良い。
In the method of the present invention, any organic solvent can be used as long as it can be phase separated from water. As an organic solvent,
Esters such as ethyl acetate and methyl acetate, halogenoalkanes such as chloromethane, dichloromethane, chloroform, carbon tetrachloride and ethylene dichloride, aromatic hydrocarbons such as benzene, toluene and xylene, ketones such as methyl ethyl ketone and diethyl ether. Ethers such as tell, n-
Butanol, isobutanol, sec-butanol, n
-Amyl alcohol, active amyl alcohol, isoamyl alcohol, sec-amyl alcohol, 3-pentanol, tert-amyl alcohol, fusel oil, n
-Hexanol, methylamyl alcohol, 2-ethylbutanol, n-heptanol, 2-heptanol, 3
-Heptanol, n-octanol, 2-octanol, 2-ethylhexanol, 3,5,5-trimethylhexanol, nonanol, n-decanol, undecanol, n-dodecanol, trimethylnonyl alcohol, tetradecanol, heptadecanol, cyclo Alcohols such as hexanol, 2-methylcyclohexanol, benzyl alcohol and phenethyl alcohol can be used, and among them, esters and / or esters capable of selectively extracting N-alkylated ethyleneamine and pyrazines
Alternatively, halogenoalkanes or alcohols are preferable. These organic solvents may be used alone or as a mixture of multiple components.

【0014】本発明の方法においては、エチレンアミン
を水溶液とした後、有機溶媒によって抽出を行うが、逆
にエチレンアミンと有機溶媒を混合した後、これに水を
加えても良い。
In the method of the present invention, ethyleneamine is made into an aqueous solution and then extracted with an organic solvent. Conversely, ethyleneamine and an organic solvent may be mixed and then water may be added thereto.

【0015】本発明の方法において、エチレンアミンに
対して加える水の量は、有機溶媒の種類及び量によって
大きく変化するため限定することは困難であるが、有機
溶媒と相分離するに要する量以上を加えれば良い。
In the method of the present invention, the amount of water added to ethyleneamine is difficult to limit because it greatly changes depending on the type and amount of the organic solvent, but it is not less than the amount required for phase separation with the organic solvent. Should be added.

【0016】本発明の方法において、エチレンアミンと
はエチレン鎖の両端にアミノ基を有する化合物を意味
し、エチレンジアミン,ジエチレントリアミン,トリエ
チレンテトラミン,テトラエチレンペンタミン,ペンタ
エチレンヘキサミン,ピペラジン,N−(2−アミノエ
チル)ピペラジン等が例示される。その中でもエチレン
ジアミンは高い純度を要求され、特にN−アルキル化エ
チレンジアミン及びピラジン類との分離が困難であるた
め、本発明の効果が大きい。
In the method of the present invention, ethyleneamine means a compound having amino groups at both ends of an ethylene chain, and ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, piperazine, N- (2 -Aminoethyl) piperazine and the like are exemplified. Among them, ethylenediamine is required to have high purity, and it is particularly difficult to separate it from N-alkylated ethylenediamine and pyrazines, so that the effect of the present invention is great.

【0017】本発明の方法において、N−アルキル化エ
チレンアミンとはエチレンアミン中の窒素がアルキル化
された化合物を意味し、窒素がメチル化されたN−メチ
ルエチレンジアミン,N,N´−ジメチルエチレンジア
ミン,N,N−ジメチルエチレンジアミン,N,N,N
´−トリメチルエチレンジアミン,N,N,N´,N´
−テトラメチルエチレンジアミン,窒素がエチル化され
たN−エチルエチレンジアミン,N,N´−ジエチルエ
チレンジアミン,N,N−ジエチルエチレンジアミン,
N,N,N´−トリエチルエチレンジアミン,N,N,
N´,N´−テトラエチルエチレンジアミン等が例示さ
れる。ピラジン類とは、ピラジン及びピラジン環を有す
る化合物を意味し、ピラジン及びメチルピラジン,ジメ
チルピラジン,エチルピラジン,ジエチルピラジン等の
アルキル化ピラジンが例示される。
In the method of the present invention, N-alkylated ethyleneamine means a compound in which nitrogen in ethyleneamine is alkylated, and N-methylethylenediamine, N, N'-dimethylethylenediamine in which nitrogen is methylated. , N, N-dimethylethylenediamine, N, N, N
'-Trimethylethylenediamine, N, N, N', N '
-Tetramethylethylenediamine, nitrogen-ethylated N-ethylethylenediamine, N, N'-diethylethylenediamine, N, N-diethylethylenediamine,
N, N, N'-triethylethylenediamine, N, N,
N ', N'-tetraethyl ethylene diamine etc. are illustrated. The pyrazines mean a pyrazine and a compound having a pyrazine ring, and pyrazine and alkylated pyrazines such as methylpyrazine, dimethylpyrazine, ethylpyrazine and diethylpyrazine are exemplified.

【0018】本発明の方法において、抽出の方法には特
に制限はなく、回分式,半回分式,連続式のいずれを用
いても良く、抽出装置として、ミキサーセトラー抽出
器,向流微分型抽出塔,非撹拌式段型抽出塔,撹拌式段
型抽出塔,遠心式抽出機等があるがいずれを用いても一
向に差支えない。
In the method of the present invention, the extraction method is not particularly limited, and any of a batch type, a semi-batch type and a continuous type may be used. As the extraction device, a mixer-settler extractor or a countercurrent differential type extraction is used. There are towers, non-stirred plate extractors, stirred plate extractors, centrifugal extractors, etc. Whichever is used, there is no problem.

【0019】[0019]

【発明の効果】本発明は、N−アルキル化エチレンアミ
ン及び/又はピラジン類を含有するエチレンアミン類の
精製方法を提供するものであり、工業的に極めて有用で
ある。
INDUSTRIAL APPLICABILITY The present invention provides a method for purifying ethyleneamines containing N-alkylated ethyleneamines and / or pyrazines and is industrially very useful.

【0020】[0020]

【実施例】以下、本発明を具体的に実施例にて説明する
が、本発明はこれらの実施例にのみ特に限定されるもの
ではない。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.

【0021】実施例1 エチレンジアミンに対してN−エチルエチレンジアミン
が0.29重量%,エチルピラジンが0.18重量%,
ジメチルピラジンが0.09重量%含まれた0.66g
のエチレンジアミンに5.5gの水を加えた。これを1
0gの酢酸メチルで、室温にて1回抽出を行った。水相
と油相を分離し、水相をガスクロマトグラフィーで分析
した結果、エチレンジアミンに対してN−エチルエチレ
ンジアミンが0.12重量%,エチルピラジンが0.0
4重量%,ジメチルピラジンが0.03重量%となっ
た。
Example 1 0.29% by weight of N-ethylethylenediamine and 0.18% by weight of ethylpyrazine relative to ethylenediamine,
0.66 g containing 0.09% by weight of dimethylpyrazine
5.5 g of water was added to the ethylenediamine. This one
Extraction was carried out once with 0 g of methyl acetate at room temperature. The water phase and the oil phase were separated and the water phase was analyzed by gas chromatography. As a result, 0.12% by weight of N-ethylethylenediamine and 0.02% of ethylpyrazine relative to ethylenediamine.
4% by weight and dimethylpyrazine were 0.03% by weight.

【0022】実施例2 酢酸メチルの代わりにイソアミルアルコールを用いた以
外は、実施例1と同様に行った。水相をガスクロマトグ
ラフィーで分析した結果、エチレンジアミンに対してN
−エチルエチレンジアミンが0.07重量%,エチルピ
ラジンが0.02重量%,ジメチルピラジンが0.00
重量%となった。
Example 2 Example 2 was repeated except that isoamyl alcohol was used instead of methyl acetate. As a result of analyzing the aqueous phase by gas chromatography, N was compared with ethylenediamine.
-Ethylethylenediamine 0.07% by weight, ethylpyrazine 0.02% by weight, dimethylpyrazine 0.00
It became weight%.

【0023】実施例3 0.34gのエチレンジアミン,0.29gのN−メチ
ルエチレンジアミン及び0.31gのN−エチルエチレ
ンジアミンに20gの水を加えた。このうちの1mlを
取り、これに酢酸エチルを1ml加えて、室温で抽出を
行った。水相と油相を分離し油相をガスクロマトグラフ
ィ−で分析した結果、水相に存在するN−アルキル化エ
チレンアミンに対して、0.1%のN−メチルエチレン
ジアミン及び0.6%のN−エチルエチレンジアミンが
油相に抽出されていたが、エチレンジアミンは抽出され
なかった。
Example 3 20 g of water was added to 0.34 g of ethylenediamine, 0.29 g of N-methylethylenediamine and 0.31 g of N-ethylethylenediamine. 1 ml of this was taken, 1 ml of ethyl acetate was added to this, and extraction was performed at room temperature. The water phase and the oil phase were separated and the oil phase was analyzed by gas chromatography. As a result, 0.1% N-methylethylenediamine and 0.6% N were added to the N-alkylated ethyleneamine present in the water phase. -Ethylethylenediamine was extracted in the oil phase, but ethylenediamine was not extracted.

【0024】実施例4 0.34gのエチレンジアミン,0.29gのN−メチ
ルエチレンジアミン及び0.31gのN−エチルエチレ
ンジアミンに20gの水を加えた。このうちの1mlを
取り、これにジクロロメタンを1ml加えて、室温で抽
出を行った。水相と油相を分離し油相をガスクロマトグ
ラフィ−で分析した結果、水相に存在するN−アルキル
化エチレンアミンに対して、0.6%のN−メチルエチ
レンジアミン及び2.1%のN−エチルエチレンジアミ
ンが油相に抽出されていたが、エチレンジアミンは抽出
されなかった。
Example 4 20 g of water was added to 0.34 g of ethylenediamine, 0.29 g of N-methylethylenediamine and 0.31 g of N-ethylethylenediamine. 1 ml of this was taken, 1 ml of dichloromethane was added to this, and extraction was performed at room temperature. The water phase and the oil phase were separated, and the oil phase was analyzed by gas chromatography. As a result, 0.6% of N-methylethylenediamine and 2.1% of N were added to the N-alkylated ethyleneamine present in the water phase. -Ethylethylenediamine was extracted in the oil phase, but ethylenediamine was not extracted.

【0025】実施例5 0.2973gのエチレンジアミン,0.2919gの
N−メチルエチレンジアミン及び0.2923gのN−
エチルエチレンジアミンに20gの水を加えた。すなわ
ち、N−メチルエチレンジアミン,N−エチルエチレン
ジアミンともエチレンジアミンに対して98重量%の水
溶液を調製した。このうちの1mlをとり、これにイソ
アミルアルコールを1ml加えて、室温で抽出を行っ
た。水相と油相を分離し、水相をガスクロマトグラフィ
ーで分析した結果、N−メチルエチレンジアミンはエチ
レンジアミンに対して76重量%,N−エチルエチレン
ジアミンはエチレンジアミンに対して57重量%に減少
していた。
Example 5 0.2973 g ethylenediamine, 0.2919 g N-methylethylenediamine and 0.2923 g N-
20 g of water was added to ethylethylenediamine. That is, both N-methylethylenediamine and N-ethylethylenediamine were prepared as 98% by weight aqueous solutions with respect to ethylenediamine. 1 ml of this was taken, 1 ml of isoamyl alcohol was added thereto, and extraction was carried out at room temperature. The aqueous phase and the oil phase were separated, and the aqueous phase was analyzed by gas chromatography. As a result, N-methylethylenediamine was reduced to 76% by weight with respect to ethylenediamine and N-ethylethylenediamine was reduced to 57% by weight with respect to ethylenediamine. ..

【0026】実施例6 実施例5で調製したエチレンジアミン、N−メチルエチ
レンジアミン,N−エチルエチレンジアミン水溶液のう
ち1mlをとり、これにシクロヘキサノールを1ml加
えて、室温で抽出を行った。水相と油相を分離し、水相
をガスクロマトグラフィーで分析した結果、N−メチル
エチレンジアミンはエチレンジアミンに対して86重量
%,N−エチルエチレンジアミンはエチレンジアミンに
対して72重量%に減少していた。
Example 6 1 ml of the aqueous solution of ethylenediamine, N-methylethylenediamine and N-ethylethylenediamine prepared in Example 5 was taken, and 1 ml of cyclohexanol was added thereto, and extraction was carried out at room temperature. As a result of separating the aqueous phase and the oil phase and analyzing the aqueous phase by gas chromatography, N-methylethylenediamine was reduced to 86% by weight with respect to ethylenediamine, and N-ethylethylenediamine was reduced to 72% by weight with respect to ethylenediamine. ..

【0027】実施例7 実施例5で調製したエチレンジアミン、N−メチルエチ
レンジアミン,N−エチルエチレンジアミン水溶液のう
ち1mlをとり、これにベンジルアルコールを1ml加
えて、室温で抽出を行った。水相と油相を分離し、水相
をガスクロマトグラフィーで分析した結果、N−メチル
エチレンジアミンはエチレンジアミンに対して54重量
%,N−エチルエチレンジアミンはエチレンジアミンに
対して45重量%に減少していた。
Example 7 1 ml of the ethylenediamine, N-methylethylenediamine, N-ethylethylenediamine aqueous solution prepared in Example 5 was taken, 1 ml of benzyl alcohol was added thereto, and extraction was carried out at room temperature. The water phase and the oil phase were separated, and the water phase was analyzed by gas chromatography. As a result, N-methylethylenediamine was reduced to 54% by weight with respect to ethylenediamine and N-ethylethylenediamine was reduced to 45% by weight with respect to ethylenediamine. ..

【0028】実施例8 実施例5で調製したエチレンジアミン、N−メチルエチ
レンジアミン,N−エチルエチレンジアミン水溶液のう
ち1mlをとり、これにn−ブタノールを1ml加え
て、室温で抽出を行った。水相と油相を分離し、水相を
ガスクロマトグラフィーで分析した結果、N−メチルエ
チレンジアミンはエチレンジアミンに対して66重量
%,N−エチルエチレンジアミンはエチレンジアミンに
対して42重量%に減少していた。
Example 8 1 ml of the ethylenediamine, N-methylethylenediamine, N-ethylethylenediamine aqueous solution prepared in Example 5 was taken, and 1 ml of n-butanol was added thereto, and extraction was carried out at room temperature. The water phase and the oil phase were separated, and the water phase was analyzed by gas chromatography. As a result, N-methylethylenediamine was reduced to 66% by weight with respect to ethylenediamine and N-ethylethylenediamine was reduced to 42% by weight with respect to ethylenediamine. ..

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】N−アルキル化エチレンアミン及び/又は
ピラジン類を含有するエチレンアミンを精製する方法に
おいて、エチレンアミンの水溶液を有機溶媒で抽出する
ことを特徴とするエチレンアミンの精製方法。
1. A method for purifying ethyleneamine containing N-alkylated ethyleneamine and / or pyrazines, which comprises extracting an aqueous solution of ethyleneamine with an organic solvent.
【請求項2】有機溶媒がエステル類及び/又はハロゲノ
アルカン類である請求項1記載の精製方法。
2. The purification method according to claim 1, wherein the organic solvent is an ester and / or a halogenoalkane.
【請求項3】有機溶媒がアルコ−ル類である請求項1記
載の精製方法。
3. The purification method according to claim 1, wherein the organic solvent is an alcohol.
【請求項4】エチレンアミンがエチレンジアミンである
請求項1〜3のいずれかに記載の精製方法。
4. The purification method according to claim 1, wherein the ethyleneamine is ethylenediamine.
JP03294895A 1991-08-09 1991-10-16 Purification method of ethyleneamine Expired - Fee Related JP3134418B2 (en)

Priority Applications (1)

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JP22355691 1991-08-09
JP3-223556 1991-08-09
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012087553A1 (en) * 2010-12-21 2012-06-28 Dow Global Technologies Llc Processes for separating one or more amine byproducts from one or more desired amines
EP2487151A1 (en) * 2008-10-06 2012-08-15 Dow Global Technologies LLC Process for separating alkylethyleneamine(s) from ethyleneamine(s) compositions
US9783486B2 (en) 2013-12-02 2017-10-10 Dow Global Technologies Llc Preparation of high molecular weight, branched, acyclic polyalkyleneamines and mixtures thereof
CN109761818A (en) * 2019-03-13 2019-05-17 东莞市乔科化学有限公司 A kind of electron level polyethylene polyamine fine work, preparation method and application

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2487151A1 (en) * 2008-10-06 2012-08-15 Dow Global Technologies LLC Process for separating alkylethyleneamine(s) from ethyleneamine(s) compositions
JP2014193852A (en) * 2008-10-06 2014-10-09 Dow Global Technologies Llc Method for separating alkylethyleneamine or alkylethylenediamine
EP2487151B1 (en) 2008-10-06 2015-09-02 Dow Global Technologies LLC Process for separating alkylethyleneamine(s) from ethyleneamine(s) compositions
WO2012087553A1 (en) * 2010-12-21 2012-06-28 Dow Global Technologies Llc Processes for separating one or more amine byproducts from one or more desired amines
US9783486B2 (en) 2013-12-02 2017-10-10 Dow Global Technologies Llc Preparation of high molecular weight, branched, acyclic polyalkyleneamines and mixtures thereof
CN109761818A (en) * 2019-03-13 2019-05-17 东莞市乔科化学有限公司 A kind of electron level polyethylene polyamine fine work, preparation method and application

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