JPH07173128A - Production of n-cyanoethaneimido ester - Google Patents

Production of n-cyanoethaneimido ester

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Publication number
JPH07173128A
JPH07173128A JP34380293A JP34380293A JPH07173128A JP H07173128 A JPH07173128 A JP H07173128A JP 34380293 A JP34380293 A JP 34380293A JP 34380293 A JP34380293 A JP 34380293A JP H07173128 A JPH07173128 A JP H07173128A
Authority
JP
Japan
Prior art keywords
acid ester
ammonia
cyanoethaneimidic
producing
reaction
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
JP34380293A
Other languages
Japanese (ja)
Other versions
JP3287682B2 (en
Inventor
Hideo Shirakawa
秀雄 白川
Matsuo Ono
松夫 小野
Akira Nakamura
晶 中村
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP34380293A priority Critical patent/JP3287682B2/en
Publication of JPH07173128A publication Critical patent/JPH07173128A/en
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Publication of JP3287682B2 publication Critical patent/JP3287682B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To economically and safely obtain an N-cyanoethaneimido ester in a relatively high yield by industrially extremely simple method using cyanogen chloride, ammonia and orthoacetic acid ester as starting raw materials without using anhydrous cyanamide. CONSTITUTION:In producing an N-cyanoethaneimido ester by reaction of cyanogen chloride with ammonia and an orthoacetic acid ester the characteristic of this method for producing the N-cyanoethaneimido ester comprises reacting cyanogen chloride with ammonia and an orthoacetic acid ester in an organic solvent at -20C to 40 deg.C.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は塩化シアン、アンモニ
ア、オルト酢酸エステルから出発して、N−シアノエタ
ンイミド酸エステル、特にメチルエステル、またはエチ
ルエステルを製造する方法に関する。
The invention relates to a process for preparing N-cyanoethaneimidic acid esters, in particular methyl or ethyl esters, starting from cyanogen chloride, ammonia, orthoacetic acid esters.

【0002】[0002]

【従来の技術】N−シアノエタンイミド酸エステルは、
たとえば殺虫剤として有用なN−シアノ−N′−(2−
クロロ−5−ピリジルメチル−N′−メチルアセトアミ
ジンを製造する原料として重要であり、また、スルホニ
ル尿素系除草剤の中間体である2−アミノ−4−メトキ
シ−6−メチル−s−トリアジンを製造する原料として
も重要な化合物である。
2. Description of the Related Art N-cyanoethaneimidic acid esters are
For example, N-cyano-N '-(2- that is useful as an insecticide
2-amino-4-methoxy-6-methyl-s-triazine, which is an important raw material for producing chloro-5-pyridylmethyl-N'-methylacetamidine, and which is an intermediate of sulfonylurea herbicides, It is an important compound as a raw material for production.

【0003】このN−シアノエタンイミド酸エステルの
製造方法として、次の三つの方法が知られている。すな
わち、第一の方法は、二段階の工程でアセトニトリル、
塩化水素ガス、アルコールおよびシアナミドから製造す
る方法(ドイツ特許第3411203号明細書)であ
り、また、第二の方法は、オルト酸エステルとシアナミ
ドを無水酢酸存在下で反応させてN−シアノエタンイミ
ド酸エステルを製造する方法(J.Org.Che
m.,28巻、1816ページ)、さらに、第三の方法
は、オルト酢酸エステルとシアナミドを酸性触媒の存在
下でアルコール性溶媒中でN−シアノエタンイミド酸エ
ステルを製造する方法(ドイツ特許第3815084号
明細書)である。
The following three methods are known as methods for producing this N-cyanoethaneimidic acid ester. That is, the first method is acetonitrile in a two-step process,
A method for producing hydrogen chloride gas, alcohol and cyanamide (German Patent No. 3411203), and a second method is to react an ortho acid ester with cyanamide in the presence of acetic anhydride to produce N-cyanoethaneimide. Method for producing acid ester (J. Org. Che
m. 28, 1816), and the third method is a method for producing an N-cyanoethaneimidic acid ester of an orthoacetic acid ester and cyanamide in an alcoholic solvent in the presence of an acidic catalyst (German Patent No. 3815084). Specification).

【0004】しかし、第一の方法では、著しく腐食性の
塩化水素ガスを用いるため高価な装置を必要としてい
た。また第二の方法では、副生物として多量の酢酸メチ
ル、酢酸が生じる欠点があり、第三の方法は前述の第
一、第二の方法の欠点を解決しているが、高価な無水の
シアナミドを用いなければならず、安価にN−シアノエ
タンイミド酸エステルを製造することができなかった。
However, the first method uses an extremely corrosive hydrogen chloride gas and thus requires an expensive apparatus. The second method has a drawback that a large amount of methyl acetate and acetic acid are produced as by-products, and the third method solves the above-mentioned drawbacks of the first and second methods, but it is expensive anhydrous cyanamide. Therefore, N-cyanoethaneimidic acid ester could not be produced at low cost.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、無水
シアナミドを用いないで、塩化シアンとアンモニアとオ
ルト酢酸エステルを出発原料としてN−シアノエタンイ
ミド酸エステルを経済的かつ安全に製造する方法を提供
することにある。
SUMMARY OF THE INVENTION An object of the present invention is to produce an N-cyanoethaneimidic acid ester economically and safely from cyanide chloride, ammonia and orthoacetic acid ester as starting materials without using anhydrous cyanamide. To provide.

【0006】[0006]

【課題を解決するための手段】本発明の方法は、有機溶
媒中で、塩化シアンとアンモニアとオルト酢酸エステル
とを、−20〜40℃の条件で反応させることを特徴と
するN−シアノエタンイミド酸エステルの製造方法に関
する。
The method of the present invention is characterized by reacting cyanogen chloride, ammonia and orthoacetic acid ester in an organic solvent under the condition of -20 to 40 ° C. The present invention relates to a method for producing an imidate ester.

【0007】本発明の方法は、N−シアノエタンイミド
酸エステル、特にそのメチルエステル、エチルエステル
の製造に適している。
The process of the present invention is suitable for the production of N-cyanoethaneimidic acid esters, especially their methyl and ethyl esters.

【0008】本発明における有機溶媒は、アセトニトリ
ル、エチルエーテル、イソプロピルエーテル、メタノー
ル、エタノールが好ましく、特にアセトニトリル、イソ
プロピルエーテルが、反応液を撹拌するうえでさらに好
ましい。
The organic solvent in the present invention is preferably acetonitrile, ethyl ether, isopropyl ether, methanol or ethanol, and particularly preferably acetonitrile or isopropyl ether for stirring the reaction solution.

【0009】有機溶媒の使用量に制限はないが、撹拌を
容易にするため、オルト酢酸エステル1モルあたりに使
用する有機溶媒の量は、100〜1000mlで、特に
300ml〜500mlが好ましい。
Although the amount of the organic solvent used is not limited, the amount of the organic solvent used is preferably 100 to 1000 ml, and particularly preferably 300 to 500 ml per mol of the orthoacetate ester in order to facilitate stirring.

【0010】また、オルト酢酸エステル1モルあたりの
塩化シアンは0.5〜2モル、アンモニアは1〜4モル
で、特に塩化シアン1.0〜1.5モル、アンモニア
2.0〜3.0モルが好ましい。塩化シアン1.0モル
以下では収率が低下し、1.5モル以上では、塩化シア
ン、アンモニアが無駄に消費される。
Further, cyan chloride is 0.5 to 2 mol and ammonia is 1 to 4 mol per mol of orthoacetic acid ester, particularly 1.0 to 1.5 mol of cyanogen chloride and 2.0 to 3.0 of ammonia. Molar is preferred. If the amount of cyanogen chloride is 1.0 mol or less, the yield will decrease, and if it is 1.5 mol or more, cyanogen chloride and ammonia will be wasted.

【0011】塩化シアンとアンモニアとオルト酢酸エス
テルの混合方法としては、塩化シアンとアンモニアとオ
ルト酢酸エステルとを同時に有機溶媒中で−20〜40
℃の条件で反応させる方法であっても、−20〜40℃
の条件で塩化シアンとアンモニアを有機溶媒中で反応さ
せた後に、−20〜40℃の条件でオルト酢酸エステル
を加える方法、あるいは、有機溶媒とオルト酢酸エステ
ルの混合溶液に、塩化シアンとアンモニアを−20〜4
0℃の条件で反応させる方法のいずれであってもよい。
As a method of mixing cyanogen chloride, ammonia and orthoacetate, cyanogen chloride, ammonia and orthoacetate are simultaneously mixed in an organic solvent at -20 to 40.
Even in the method of reacting under the condition of ℃, -20 to 40 ℃
After the reaction of cyanogen chloride and ammonia in an organic solvent under the conditions of 1), orthoacetic acid ester is added under the condition of -20 to 40 ° C, or cyanide chloride and ammonia are added to a mixed solution of the organic solvent and orthoacetic acid ester. -20 to 4
Any of the methods of reacting at 0 ° C. may be used.

【0012】塩化シアンとアンモニアを有機溶媒中で反
応させた後に、オルト酢酸エステルを加える方法の場合
においては、反応液を濾過し、析出した塩化アンモニウ
ムを除去し、さらに反応液を濃縮した後に、オルト酢酸
エステルを反応してもさしつかえない。
In the case of a method of adding orthoacetic acid ester after reacting cyanogen chloride and ammonia in an organic solvent, the reaction solution is filtered to remove precipitated ammonium chloride, and the reaction solution is further concentrated. It does not matter if the orthoacetic acid ester is reacted.

【0013】塩化シアンとアンモニアとオルト酢酸エス
テルとの混合時の反応温度は、−20以上40℃以下で
実施されるが、特に−5〜20℃が好ましい。不必要に
冷却することは、高性能の冷凍機を必要とするだけでし
かない。40℃以上ではアンモニアおよび塩化シアンが
気化し、収率が低下するだけでなく、反応器の上部やベ
ントラインに塩化アンモニウムが付着するため、反応に
支障をきたす。
The reaction temperature at the time of mixing cyanogen chloride, ammonia, and orthoacetic acid ester is -20 to 40 ° C, preferably -5 to 20 ° C. Unnecessarily cooling only requires a high performance refrigerator. At 40 ° C. or higher, ammonia and cyanogen chloride are vaporized to lower the yield, and ammonium chloride adheres to the upper part of the reactor and the vent line, which hinders the reaction.

【0014】塩化シアンとアンモニアとオルト酢酸エス
テルとを反応した後の熟成は、20〜130℃で実施さ
れるが、特に40〜90℃が好ましく、熟成は0.5〜
5時間で完了する。20℃以下では反応に長時間を要す
る。
The aging after the reaction of cyanogen chloride, ammonia and the orthoacetic acid ester is carried out at 20 to 130 ° C., preferably 40 to 90 ° C., and the aging is 0.5 to
It will be completed in 5 hours. The reaction takes a long time at 20 ° C or lower.

【0015】反応後の生成物の単離は、反応液を濃縮
し、反応で生成したアルコールと反応に用いた有機溶媒
を除いた後、水に難溶な有機溶媒で抽出し、水洗するこ
とにより実施される。この間必要であれば、反応系を濾
過してもさしつかえない。抽出用に用いる有機溶媒とし
ては、トルエン、塩化メチレン、ヘキサン、イソプロピ
ルエーテル、酢酸ブチルが好ましい。
The product after the reaction is isolated by concentrating the reaction solution, removing the alcohol produced in the reaction and the organic solvent used in the reaction, extracting with a poorly water-soluble organic solvent, and washing with water. It is carried out by. During this period, the reaction system may be filtered if necessary. The organic solvent used for extraction is preferably toluene, methylene chloride, hexane, isopropyl ether, or butyl acetate.

【0016】このようにして得られる粗生成物は、次工
程の医農薬の合成に十分利用可能な純度を持つものであ
るが、必要に応じて、蒸留、クロマトグラフィー等の通
常の有機化学的手法により、さらに精製することができ
る。
The crude product thus obtained has such a purity that it can be sufficiently used for the synthesis of pharmaceuticals and agricultural chemicals in the next step, but if necessary, it may be subjected to usual organic chemical reactions such as distillation and chromatography. It can be further purified by the technique.

【0017】以下実施例によって本発明を詳述するが、
本発明はこれによって限定されるものではない。
The present invention will be described in detail below with reference to Examples.
The present invention is not limited to this.

【0018】[0018]

【実施例】【Example】

実施例1 攪拌機、冷却器、温度計、ガス導入管2本を備えた50
0mlの4つ口反応釜に、アセトニトリル280gを仕
込んだ。この反応釜を0℃に冷却してから、塩化シアン
55ml(比重1.21 純度95.5% 1.03m
ol)をガス発生器で気化させ、反応釜に導入した。同
時にアンモニアガス35.6g(2.09mol)を反
応釜に導入した。この間、反応温度を−2〜2℃に保っ
た。
Example 1 50 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
In a 0 ml four-neck reaction kettle, 280 g of acetonitrile was charged. After cooling the reaction kettle to 0 ° C., 55 ml of cyanogen chloride (specific gravity 1.21 purity 95.5% 1.03 m
ol) was vaporized by a gas generator and introduced into a reaction kettle. At the same time, 35.6 g (2.09 mol) of ammonia gas was introduced into the reaction kettle. During this period, the reaction temperature was kept at -2 to 2 ° C.

【0019】ガス導入後、0℃で1時間撹拌してから、
析出した塩化アンモニウムを濾過し、アセトニトリル5
0gで洗浄した。濾液と洗浄液を合わせ減圧濃縮し、濃
縮液64.7gを得た。
After introducing gas, stir at 0 ° C. for 1 hour,
The precipitated ammonium chloride was filtered, and acetonitrile 5
It was washed with 0 g. The filtrate and the washing solution were combined and concentrated under reduced pressure to obtain 64.7 g of a concentrated solution.

【0020】この濃縮液にオルト酢酸トリメチル109
g(0.91mol)を加え、65℃で2時間撹拌した
後、反応液を蒸留し、生成したメタノールおよびアセト
ニトリル合計58.2gを留去させた。得られた濃縮液
114gを0℃に冷却し、塩化メチレン95g、冷水7
1gを加えて撹拌し分液した。水相はさらに塩化メチレ
ン95gを抽出した。
Trimethyl orthoacetate 109 was added to this concentrated solution.
After adding g (0.91 mol) and stirring at 65 degreeC for 2 hours, the reaction liquid was distilled and the produced | generated methanol and acetonitrile 58.2g in total were distilled off. 114 g of the obtained concentrated liquid was cooled to 0 ° C, and 95 g of methylene chloride and 7 g of cold water were added.
1 g was added, and the mixture was stirred and separated. The aqueous phase was further extracted with 95 g of methylene chloride.

【0021】得られた塩化メチレン溶液を合わせて、5
00mlの蒸留釜に入れ、塩化メチレンを留去させた
後、107℃/30mmHgの留分として、67.4g
のN−シアノエタンイミド酸メチルエステルを得た。オ
ルト酢酸トリメチルからの収率は75.3%であった。
The methylene chloride solutions obtained were combined and
After placing in a 00 ml distillation pot to distill off methylene chloride, 67.4 g as a fraction at 107 ° C./30 mmHg
N-cyanoethaneimidic acid methyl ester of was obtained. The yield from trimethyl orthoacetate was 75.3%.

【0022】実施例2 攪拌機、冷却器、温度計、ガス導入管2本を備えた50
0mlの4つ口反応釜に、アセトニトリル280gを仕
込んだ。この反応釜を0℃に冷却してから、塩化シアン
55ml(比重1.21 純度95.5% 1.03m
ol)をガス発生器で気化させ、反応釜に導入した。同
時にアンモニアガス35.6g(2.09mol)を反
応釜に導入した。この間、反応温度は0〜6℃に保っ
た。さらに0℃で1時間撹拌してから、反応液を濃縮
し、濃縮液136.5gを得た。
Example 2 50 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
In a 0 ml four-neck reaction kettle, 280 g of acetonitrile was charged. After cooling the reaction kettle to 0 ° C., 55 ml of cyanogen chloride (specific gravity 1.21 purity 95.5% 1.03 m
ol) was vaporized by a gas generator and introduced into a reaction kettle. At the same time, 35.6 g (2.09 mol) of ammonia gas was introduced into the reaction kettle. During this period, the reaction temperature was kept at 0 to 6 ° C. After further stirring at 0 ° C. for 1 hour, the reaction solution was concentrated to obtain 136.5 g of a concentrated solution.

【0023】この濃縮液にオルト酢酸トリメチル118
g(0.98mol)を加え、65℃で90分間撹拌
し、減圧蒸留し、生成したメタノールおよびアセトニト
リル83.3gを留去させて、N−シアノエタンイミド
酸メチルエステル含有の濃縮液167gを得た。
Trimethyl orthoacetate 118
g (0.98 mol) was added, the mixture was stirred at 65 ° C. for 90 minutes, and distilled under reduced pressure to distill off the produced methanol and acetonitrile 83.3 g to obtain 167 g of a concentrated liquid containing N-cyanoethaneimidic acid methyl ester. It was

【0024】濃縮液に、酢酸ブチル120g、冷水23
0gを加えて撹拌し分液した。水相を酢酸ブチル60g
でさらに抽出した。得られたN−シアノエタンイミド酸
メチルエステル含有の酢酸ブチル溶液を濃縮し、減圧蒸
留して97℃/20mmHgの留分68.4gを得た。
この留分のN−シアノエタンイミド酸メチルエステルの
純度は98.0%で、オルト酢酸トリメチルからの収率
は70.0%であった。
120 g of butyl acetate and 23 g of cold water were added to the concentrated liquid.
0 g was added, and the mixture was stirred and separated. 60g of butyl acetate in the aqueous phase
It was further extracted with. The obtained butyl acetate solution containing N-cyanoethaneimidic acid methyl ester was concentrated and distilled under reduced pressure to obtain 68.4 g of a fraction at 97 ° C / 20 mmHg.
The purity of N-cyanoethaneimidic acid methyl ester of this fraction was 98.0%, and the yield from trimethyl orthoacetate was 70.0%.

【0025】実施例3 攪拌機、冷却器、温度計、ガス導入管2本を備えた10
00mlの4つ口反応釜に、オルト酢酸トリメチル12
0g(1.00mol)とアセトニトリル280.9g
を仕込んだ。この反応釜を10℃に冷却してから、塩化
シアン53.1ml(比重1.21 純度95.5%
1.00mol)をガス発生器で気化させ、反応釜に導
入した。同時にアンモニアガス34.0g(2.00m
ol)を反応釜に導入した。この間、反応温度を8〜1
8℃に保った。
Example 3 10 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
Trimethyl orthoacetate 12 in a 00 ml 4-neck reaction kettle
0g (1.00mol) and acetonitrile 280.9g
Was charged. After cooling the reaction kettle to 10 ° C., 53.1 ml of cyanogen chloride (specific gravity 1.21 purity 95.5%
(1.00 mol) was vaporized by a gas generator and introduced into a reaction kettle. At the same time, 34.0 g of ammonia gas (2.00 m
ol) was introduced into the reaction kettle. During this time, the reaction temperature is 8 to 1
It was kept at 8 ° C.

【0026】その後、64℃で1時間撹拌した後、反応
液を濃縮し299.0gを留去させ、20℃に冷却して
濾過した。濾過物を塩化メチレン120gで洗浄し、濾
過液と洗浄液を合わせた。塩化メチレン溶液を120g
で洗浄し、塩化メチレンを留去させた後、減圧蒸留して
107℃/30mmHgの留分66.1gを得た。この
留分のN−シアノエタンイミド酸メチルエステルの純度
は98.0%で、オルト酢酸トリメチルからの収率は6
6.0%であった。
Then, after stirring at 64 ° C. for 1 hour, the reaction solution was concentrated to distill off 299.0 g, cooled to 20 ° C. and filtered. The filtered product was washed with 120 g of methylene chloride, and the filtrate and the washing liquid were combined. 120 g of methylene chloride solution
After that, methylene chloride was distilled off, and the residue was distilled under reduced pressure to obtain 66.1 g of a fraction at 107 ° C./30 mmHg. The purity of N-cyanoethaneimidic acid methyl ester in this fraction was 98.0%, and the yield from trimethyl orthoacetate was 6%.
It was 6.0%.

【0027】実施例4 攪拌機、冷却器、温度計、ガス導入管2本を備えた50
0mlの4つ口反応釜に、オルト酢酸トリメチル80g
(0.67mol)とアセトニトリル188.3gを仕
込んだ。この反応釜を5℃に冷却してから、塩化シアン
35.4ml(0.67mol)をガス発生器で気化さ
せ、反応釜に導入した。塩化シアンの導入開始と同時に
アンモニアガス22.7g(1.33mol)を反応釜
に導入した。この間、反応温度を6〜15℃に保った。
Example 4 50 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
In a 0 ml 4-neck reaction kettle, 80 g of trimethyl orthoacetate
(0.67 mol) and 188.3 g of acetonitrile were charged. After cooling the reaction kettle to 5 ° C., 35.4 ml (0.67 mol) of cyanogen chloride was vaporized by a gas generator and introduced into the reaction kettle. Simultaneously with the start of the introduction of cyanogen chloride, 22.7 g (1.33 mol) of ammonia gas was introduced into the reaction kettle. During this period, the reaction temperature was kept at 6 to 15 ° C.

【0028】17℃で19時間放置した後、メタノール
およびアセトニトリルを留去させ、20℃に冷却して濾
過し、濾過物を塩化メチレン80gで洗浄した。濾過液
と洗浄液を合わせ、水80gで洗浄し、溶媒を留去させ
た後、113〜117℃/40mmHgの留分43.6
gを得た。この留分のN−シアノエタンイミド酸メチル
エステルの純度は99.1%で、オルト酢酸トリメチル
からの収率は68.4%であった。
After standing at 17 ° C. for 19 hours, methanol and acetonitrile were distilled off, the mixture was cooled to 20 ° C. and filtered, and the filtered product was washed with 80 g of methylene chloride. The filtrate and the washing solution were combined, washed with 80 g of water, the solvent was distilled off, and then the fraction of 113 to 117 ° C./40 mmHg was 43.6.
g was obtained. The purity of N-cyanoethaneimidic acid methyl ester of this fraction was 99.1%, and the yield from trimethyl orthoacetate was 68.4%.

【0029】実施例5 攪拌機、冷却器、温度計、ガス導入管2本を備えた30
0mlの4つ口反応釜に、オルト酢酸トリエチル53.
5g(0.33mol)とイソプロピルエーテル13
1.1gを仕込んだ。この反応釜を5℃に冷却してか
ら、塩化シアン17.7ml(0.33mol)をガス
発生器で気化させ、反応釜に導入した。塩化シアンの導
入開始と同時にアンモニアガス11.3g(0.67m
ol)を反応釜に導入した。この間、反応温度を5〜2
1℃に保った。さらに30℃で30分間撹拌してから濾
過した。
Example 5 30 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
Triethyl orthoacetate 53.
5 g (0.33 mol) and isopropyl ether 13
1.1 g was charged. After cooling this reaction kettle to 5 ° C., 17.7 ml (0.33 mol) of cyanogen chloride was vaporized by a gas generator and introduced into the reaction kettle. At the same time when the introduction of cyanogen chloride was started, 11.3 g of ammonia gas (0.67 m
ol) was introduced into the reaction kettle. During this time, the reaction temperature is 5 to 2
It was kept at 1 ° C. The mixture was further stirred at 30 ° C. for 30 minutes and then filtered.

【0030】濾過液を65℃で3時間環流反応溶液14
9.6g中のN−シアノエタンイミド酸エテルエステル
濃度は15.6%で、N−シアノエタンイミド酸チスル
エステルの収率は62.9%であった。
The filtrate is refluxed at 65 ° C. for 3 hours to give a reaction solution 14
The concentration of N-cyanoethaneimidic acid ether ester in 9.6 g was 15.6%, and the yield of N-cyanoethaneimidic acid thisyl ester was 62.9%.

【0031】実施例6 攪拌機、冷却器、温度計、ガス導入管2本を備えた10
00mlの4つ口反応釜に、オルト酢酸トリメチル12
0g(1.00mol)とメタノール278.4gを仕
込んだ。この反応釜を10℃に冷却してから、塩化シア
ン53.1ml(1.00mol)をガス発生器で気化
させ反応釜に導入した。同時にアンモニアガス34.1
g(2.00mol)を塩化シアンと同時に反応釜に導
入した。この間、反応温度を10〜20℃に保った。
Example 6 10 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
Trimethyl orthoacetate 12 in a 00 ml 4-neck reaction kettle
0 g (1.00 mol) and methanol 278.4 g were charged. After cooling this reaction kettle to 10 ° C., 53.1 ml (1.00 mol) of cyanogen chloride was vaporized by a gas generator and introduced into the reaction kettle. At the same time ammonia gas 34.1
g (2.00 mol) was introduced into the reaction vessel at the same time as cyanogen chloride. During this period, the reaction temperature was kept at 10 to 20 ° C.

【0032】60℃で2時間撹拌した後、反応液を濃縮
し、20℃に冷却して濾過し、濾過物を塩化メチレン1
20gで洗浄した。濾過液と洗浄液を合わせ、水120
gで洗浄し、N−シアノエタンイミド酸メチルエステル
を12.7%含有する塩化メチレン溶液282.6gを
得た。N−シアノエタンイミド酸メチルエステルの収率
は36.7%であった。
After stirring at 60 ° C. for 2 hours, the reaction solution was concentrated, cooled to 20 ° C. and filtered.
Washed with 20 g. Combine the filtrate and the washing solution and wash with water 120
After washing with g, 282.6 g of a methylene chloride solution containing 12.7% of N-cyanoethaneimidic acid methyl ester was obtained. The yield of N-cyanoethaneimidic acid methyl ester was 36.7%.

【0033】比較例 攪拌機、冷却器、温度計、ガス導入管2本を備えた30
0mlの4つ口反応釜に、オルト酢酸トリメチル40g
(0.33mol)とトルエン180mlを仕込んだ。
この反応釜を5℃に冷却してから、塩化シアン17.7
ml(0.33mol)をガス発生器で気化させ、反応
釜に導入した。アンモニアガス11.3g(0.67m
ol)を塩化シアンと同時に65分間で反応釜に導入し
た。この間、反応温度を5〜16℃に保った。30℃で
30分間反応させた後濾過した。濾過液を70℃で4時
間撹拌した。その後反応液を20℃に冷却して濾過した
が濾過液182.1gの中のN−シアノエタンイミド酸
メチルエステル濃度は1.38%であり反応収率は7.
7%であった。
Comparative Example 30 equipped with a stirrer, a cooler, a thermometer, and two gas introduction pipes
In a 0 ml four-neck reaction kettle, 40 g of trimethyl orthoacetate
(0.33 mol) and 180 ml of toluene were charged.
The reaction kettle was cooled to 5 ° C. and then cyanide chloride 17.7.
ml (0.33 mol) was vaporized with a gas generator and introduced into a reaction kettle. Ammonia gas 11.3g (0.67m
ol) was introduced into the reaction vessel simultaneously with cyanogen chloride in 65 minutes. During this period, the reaction temperature was kept at 5 to 16 ° C. After reacting at 30 ° C. for 30 minutes, the mixture was filtered. The filtrate was stirred at 70 ° C. for 4 hours. Thereafter, the reaction solution was cooled to 20 ° C. and filtered. The concentration of N-cyanoethaneimidic acid methyl ester in the filtered solution 182.1 g was 1.38%, and the reaction yield was 7.
It was 7%.

【0034】[0034]

【発明の効果】以上述べたきたように、本発明は、塩化
シアン、アンモニアおよびオルト酢酸エステルとの反応
によってN−シアノエタンイミド酸エステルを製造する
にあたり、有機溶媒中で、塩化シアンとアンモニアとオ
ルト酢酸エステルとを−20〜40℃の条件で反応させ
ることを特徴とするN−シアノエタンイミド酸エステル
の製造方法であり、本発明によれば無水シアナミドを用
いないで、塩化シアンとアンモニアとオルト酢酸エステ
ルを出発原料として、N−シアノエタンイミド酸エステ
ルを比較的高収率で、経済的にかつ安全にしかも工業的
に極めて簡単な方法で得ることができるという利点があ
る。
As described above, according to the present invention, when N-cyanoethaneimidic acid ester is produced by the reaction with cyanogen chloride, ammonia and orthoacetic acid ester, cyanide chloride and ammonia are mixed with each other in an organic solvent. A method for producing an N-cyanoethaneimidic acid ester, which comprises reacting an orthoacetic acid ester under the condition of -20 to 40 ° C. According to the present invention, cyanide chloride and ammonia are used without using anhydrous cyanamide. There is an advantage that N-cyanoethaneimidic acid ester can be obtained in relatively high yield economically, safely and industrially by a very simple method using orthoacetic acid ester as a starting material.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 塩化シアン、アンモニアおよびオルト酢
酸エステルとの反応によってN−シアノエタンイミド酸
エステルを製造するにあたり、有機溶媒中で、塩化シア
ンとアンモニアとオルト酢酸エステルとを−20〜40
℃の条件で反応させることを特徴とするN−シアノエタ
ンイミド酸エステルの製造方法。
1. When producing N-cyanoethaneimidic acid ester by reaction with cyanogen chloride, ammonia and orthoacetic acid ester, cyanide chloride, ammonia and orthoacetic acid ester are mixed in an organic solvent at -20 to 40.
A method for producing an N-cyanoethaneimidic acid ester, which comprises reacting at a temperature of ° C.
【請求項2】 塩化シアン、アンモニアを有機溶媒中で
反応させた後に、オルト酢酸エステルを加える請求項1
記載のN−シアノエタンイミド酸エステルの製造方法。
2. The orthoacetic acid ester is added after reacting cyanogen chloride and ammonia in an organic solvent.
A method for producing the described N-cyanoethaneimidic acid ester.
【請求項3】 塩化シアン、アンモニアおよびオルト酢
酸エステルとの反応によってN−シアノエタンイミド酸
エステルを製造するにあたり、有機溶媒とオルト酢酸エ
ステルの混合溶液に、塩化シアンとアンモニアを加え−
20〜40℃の条件で反応させることを特徴とするN−
シアノエタンイミド酸エステルの製造方法。
3. When producing N-cyanoethaneimidic acid ester by reaction with cyanogen chloride, ammonia and orthoacetic acid ester, cyanide chloride and ammonia are added to a mixed solution of an organic solvent and orthoacetic acid ester.
N- characterized by reacting under the condition of 20-40 ° C
Method for producing cyanoethaneimidic acid ester.
【請求項4】 オルト酢酸エステル1モルあたり塩化シ
アン0.6〜1.4モル、アンモニア1.2〜2.8モ
ルを使用する請求項1〜3記載のN−シアノエタンイミ
ド酸エステルの製造方法。
4. The production of N-cyanoethaneimidic acid ester according to claim 1, wherein 0.6 to 1.4 mol of cyanogen chloride and 1.2 to 2.8 mol of ammonia are used per mol of orthoacetic acid ester. Method.
【請求項5】 有機溶媒がメタノール、エタノール、エ
チルエーテル、イソプロピルエーテル、アセトニトリル
の一種または2種以上である請求項1〜4記載のN−シ
アノエタンイミド酸エステルの製造方法。
5. The method for producing an N-cyanoethaneimidic acid ester according to claim 1, wherein the organic solvent is one kind or two or more kinds of methanol, ethanol, ethyl ether, isopropyl ether and acetonitrile.
【請求項6】 オルト酢酸エステルが、オルト酢酸トリ
メチルまたはオルト酢酸トリエチルである請求項1〜5
記載のN−シアノエタンイミド酸エステルの製造方法。
6. The orthoacetic acid ester is trimethyl orthoacetate or triethyl orthoacetate.
A method for producing the described N-cyanoethaneimidic acid ester.
JP34380293A 1993-12-17 1993-12-17 Method for producing N-cyanoethane imidate Expired - Fee Related JP3287682B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34380293A JP3287682B2 (en) 1993-12-17 1993-12-17 Method for producing N-cyanoethane imidate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34380293A JP3287682B2 (en) 1993-12-17 1993-12-17 Method for producing N-cyanoethane imidate

Publications (2)

Publication Number Publication Date
JPH07173128A true JPH07173128A (en) 1995-07-11
JP3287682B2 JP3287682B2 (en) 2002-06-04

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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000014056A1 (en) * 1998-09-09 2000-03-16 Nippon Carbide Kogyo Kabushiki Kaisha Process for producing o-alkyl-n-cyanoimidate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000014056A1 (en) * 1998-09-09 2000-03-16 Nippon Carbide Kogyo Kabushiki Kaisha Process for producing o-alkyl-n-cyanoimidate

Also Published As

Publication number Publication date
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