JPH10101635A - New production of azo ester compound - Google Patents

New production of azo ester compound

Info

Publication number
JPH10101635A
JPH10101635A JP27716196A JP27716196A JPH10101635A JP H10101635 A JPH10101635 A JP H10101635A JP 27716196 A JP27716196 A JP 27716196A JP 27716196 A JP27716196 A JP 27716196A JP H10101635 A JPH10101635 A JP H10101635A
Authority
JP
Japan
Prior art keywords
reaction
hydrogen chloride
formula
concentration
compound
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
JP27716196A
Other languages
Japanese (ja)
Other versions
JP4092739B2 (en
Inventor
Seiji Hirose
聖二 広瀬
Hiroyuki Tsurumoto
浩之 鶴本
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.)
Fujifilm Wako Pure Chemical Corp
Original Assignee
Wako Pure Chemical Industries Ltd
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Filing date
Publication date
Application filed by Wako Pure Chemical Industries Ltd filed Critical Wako Pure Chemical Industries Ltd
Priority to JP27716196A priority Critical patent/JP4092739B2/en
Publication of JPH10101635A publication Critical patent/JPH10101635A/en
Application granted granted Critical
Publication of JP4092739B2 publication Critical patent/JP4092739B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a new method for producing an azoiminoether hydrochloride by which the azoiminoether hydrochloride useful as a synthesis intermediate, etc., for a polymerization initiator, etc., is produced with an easy control of the reaction, in high purity and yield by suspending a specific azonitrile compound in alcohols, introducing a prescribed amount of hydrogen chloride and reacting the compound. SOLUTION: This azoiminoether hydrochloride is obtained by suspending an azonitrile compound of formula I [R<1> to R<4> are each a (substituted) alkyl or a (substituted) phenyl; R<1> and R<2> , or R<3> and R<4> can form an alkylene] in alcohols of the formula R<5> OH (R<5> is a lower alkyl), introducing and reacting hydrogen chloride by keeping the content of the hydrogen chloride not to excess the saturating content in the alcohols but to maintain not less than 30% W/W to provide the objective azoiminoether hydrochloride of formula II. The azoester compound of formula III is preferably produced by hydrating the azoiminoether hydrochloride of formula II.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高分子化合物製造
に於ける重合開始剤として有用なアゾグアニル化合物や
アゾエステル化合物の重要中間体であるアゾイミノエー
テル塩酸塩の製造方法と、このアゾイミノエーテル塩酸
塩を用いたアゾエステル化合物の製造方法に関する。
The present invention relates to a process for producing an azoimino ether hydrochloride which is an important intermediate of an azoguanyl compound or an azo ester compound useful as a polymerization initiator in the production of a polymer compound, and a method for producing the azo imino ether hydrochloride. The present invention relates to a method for producing an azoester compound using a salt.

【0002】[0002]

【従来の技術】アゾイミノエーテル塩酸塩の製造方法と
しては、相当するアゾニトリル化合物を非水反応系中
で、アルコール類及び塩化水素と反応させる方法(米国
特許第2599299号)が知られており、ここでは、
使用アルコール類に対して飽和となるように塩化水素を
導入させ、反応を行っている。しかし、この方法では、
反応が急激に進行し、小実験スケールに於いてすら、冷
却等による反応の制御は極めて困難であり、スケールア
ップによる工業的スケールでの製造では大きな危険性が
伴い、大規模生産が不可能な状態であった。
2. Description of the Related Art As a method for producing azoimino ether hydrochloride, there is known a method of reacting a corresponding azonitrile compound with alcohols and hydrogen chloride in a non-aqueous reaction system (US Pat. No. 2,599,299). here,
The reaction is carried out by introducing hydrogen chloride so as to be saturated with respect to the alcohols used. But with this method,
The reaction progresses rapidly, and even on a small experimental scale, it is extremely difficult to control the reaction by cooling, etc., and large-scale production is not possible with large-scale production on an industrial scale by scale-up. Condition.

【0003】そこで、この問題点を解決する手段とし
て、塩化水素の溶解性が低い溶媒とアルコール類の混合
溶媒中に塩化水素を導入する方法(特公昭58−223
0号公報)や、酸を導入したアルコール類溶液中にアゾ
ビスニトリル類を逐次添加する方法(特開昭64−26
545号公報)が開示されている。しかしながら、これ
らの方法に於いてもなお、問題点を有していた。
In order to solve this problem, a method of introducing hydrogen chloride into a mixed solvent of a solvent having low solubility of hydrogen chloride and an alcohol (Japanese Patent Publication No. 58-223).
No. 0) or a method of sequentially adding azobisnitrile to an alcohol solution containing an acid (Japanese Patent Laid-Open No. 64-26).
No. 545). However, these methods still have problems.

【0004】即ち前者では、反応終了後に反応系からト
ルエン等の塩化水素溶解性の低い溶媒を完全に除去する
ことが困難であるため、例えば、得られたイミノエーテ
ル塩をそのまま加水分解してアゾエステル化合物を製造
する場合などには、アゾエステル化合物が、残存するト
ルエン等に溶解するため、これを除く操作が必要とな
り、単離回収操作が煩雑になるという問題点がある。
That is, in the former method, it is difficult to completely remove a solvent having low solubility in hydrogen chloride such as toluene from the reaction system after completion of the reaction. In the case of producing a compound or the like, the azoester compound is dissolved in the remaining toluene or the like, so that an operation for removing the azoester compound is required, and there is a problem that the isolation and recovery operation becomes complicated.

【0005】又、後者では、アゾビスニトリル類を、粉
末状態或いはアルコール類やその他の溶媒を用いて溶液
ないしはスラリー状にして逐次反応系に添加する必要が
あるが、大規模生産に於いて粉末状固体を反応系に逐次
添加することは作業性が悪い上に、作業員が常に系内の
塩化水素に曝される危険性を伴うため実用的ではなく、
又アゾビスニトリル類は、アルコール類やその他の一般
的な溶媒には溶けにくいため、スラリー状で添加すると
しても投入装置内で結晶が閉塞し、一定速度で結晶を添
加できず反応を十分に制御できないという問題がある。
In the latter case, it is necessary to add the azobisnitrile to the reaction system sequentially in the form of powder or in the form of a solution or slurry using alcohols or other solvents. It is not practical to add the solid in the reaction system sequentially to the reaction system because the workability is poor and there is a risk that the worker is always exposed to hydrogen chloride in the system.
Also, since azobisnitrile is hardly soluble in alcohols and other general solvents, even if it is added in a slurry form, the crystals are clogged in the charging device, and the crystals cannot be added at a constant rate and the reaction is sufficiently performed. There is a problem that it cannot be controlled.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記の如き
状況に鑑みなされたなされたもので、トルエン等の塩化
水素溶解性の低い溶媒を使用せず、反応の制御が容易
で、且つ作業性が良く危険性の少ないアゾイミノエーテ
ル塩酸塩及びアゾエステル化合物の製造方法を提供する
ことをその目的とする。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above situation, and does not use a solvent having low solubility in hydrogen chloride such as toluene, so that the reaction can be easily controlled and the operation can be easily performed. It is an object of the present invention to provide a method for producing an azoimino ether hydrochloride and an azo ester compound having good properties and low danger.

【0007】[0007]

【課題を解決するための手段】本発明は、(1)一般式
[1]
The present invention provides (1) a compound represented by the general formula [1]:

【0008】[0008]

【化5】 Embedded image

【0009】(式中、R1,R2,R3及びR4は、夫々独
立して、置換基を有していても良いアルキル基又は置換
基を有していても良いフェニル基を示し、R1とR2及び
/又はR3とR4とがアルキレン鎖を形成する場合を含
む。)で表されるアゾニトリル化合物をR5-OH(R5
は低級アルキル基を示す。)で表されるアルコール類に
懸濁させ、これに塩化水素を、その濃度が反応系中のア
ルコール類に対して飽和未満であり且つ30%W/Wを下
回らない値に維持されるように導入して反応を行わせる
事を特徴とする、一般式[2]
(Wherein, R 1 , R 2 , R 3 and R 4 each independently represent an alkyl group which may have a substituent or a phenyl group which may have a substituent. , R 1 and R 2 and / or R 3 and R 4 may form an alkylene chain) with R 5 —OH (R 5
Represents a lower alkyl group. ), And hydrogen chloride is added thereto so that the concentration thereof is maintained at a value that is less than saturation with respect to the alcohols in the reaction system and does not fall below 30% W / W. General formula [2], characterized in that the reaction is carried out by introduction.

【0010】[0010]

【化6】 Embedded image

【0011】(式中、R1,R2,R3,R4及びR5は前
記に同じ。)で表される、アゾイミノエーテル塩酸塩の
製造方法、及び(2)上記(1)の方法により、一般式
[2]
(Wherein R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above), and (2) the method of (1) According to the method, the general formula [2]

【0012】[0012]

【化7】 Embedded image

【0013】(式中、R1,R2,R3,R4及びR5は前
記に同じ。)で表される、アゾイミノエーテル塩酸塩を
製造し、次いでこれを加水分解することを特徴とする一
般式[3]
(Wherein R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above), characterized by producing an azoimino ether hydrochloride, and then hydrolyzing it. General formula [3]

【0014】[0014]

【化8】 Embedded image

【0015】(式中、R1,R2,R3,R4及びR5は前
記と同じ。)で表されるアゾエステル化合物の製造方
法、の発明である。
(Wherein R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above).

【0016】即ち、本発明者等は、上記の問題点を解決
するため、アゾイミノエーテル塩酸塩を生成する反応に
必要な塩化水素の濃度(使用するアルコール類に対す
る)について種々検討した。その結果、塩化水素の濃度
が反応系中に存在するアルコール類に対して30%W/W
未満であると、反応が完結しない。また、塩化水素の濃
度が30%W/W以上であれば反応は完結するが、飽和状
態に近づくほど反応が激しくなり反応の制御が難しくな
る。更に塩化水素を過剰に導入した場合は、反応が急激
に進行することは言うまでもなく、過剰な塩化水素によ
り作業環境が著しく悪化してしまう。即ち、イミノエー
テル化反応を安全に制御しつつ進行及び完結させるに
は、反応開始時から反応終了時にかけての反応系内に於
いて、反応に使われるアルコール類を考慮しても、塩化
水素の濃度を系内に存在するアルコール類に対して飽和
未満であり且つ30%W/Wを下回らないように導入すれ
ば良いということを見出し本発明を完成させるに到っ
た。
That is, the present inventors have conducted various studies on the concentration of hydrogen chloride (relative to the alcohol used) required for the reaction for producing azoimino ether hydrochloride in order to solve the above problems. As a result, the concentration of hydrogen chloride was 30% W / W with respect to alcohols existing in the reaction system.
If it is less than 3, the reaction is not completed. When the concentration of hydrogen chloride is 30% W / W or more, the reaction is completed. However, as the concentration approaches the saturated state, the reaction becomes violent and the control of the reaction becomes difficult. Furthermore, when hydrogen chloride is excessively introduced, it goes without saying that the reaction proceeds rapidly, and the working environment is significantly deteriorated by the excessive hydrogen chloride. That is, in order to safely proceed and complete the iminoetherification reaction while controlling the reaction, from the start of the reaction to the end of the reaction, the reaction system is made of hydrogen chloride in consideration of the alcohol used in the reaction. The inventors have found that the concentration should be introduced so as to be less than the saturation with respect to the alcohols present in the system and not less than 30% W / W, thereby completing the present invention.

【0017】一般式[1]及び[2]に於いて、R1
2,R3及びR4で示されるアルキル基としては、直鎖
状でも分枝状でもさらには環状の何れにても良く、例え
ば炭素数1〜6のアルキル基が挙げられ、具体的にはメ
チル基,エチル基,n-プロピル基,イソプロピル基,
n-ブチル基,イソブチル基,s-ブチル基,t-ブチル
基,n-ペンチル基,イソペンチル基,2-メチルブチル
基,1-メチルブチル基,ネオペンチル基,1-エチルプ
ロピル基,n-ヘキシル基,イソヘキシル基,シクロプロ
ピル基,シクロペンチル基,シクロヘキシル基等が挙げら
れる。また、その置換基としては反応に不活性なもので
あれば如何なるものでも良いが、例えばフェニル基,ト
リル基,キシリル基等が挙げられる。置換基を有してい
ても良いフェニル基としては、例えば、フェニル基,ト
リル基,キシリル基等が挙げられる。アルキレン鎖とし
ては、直鎖状でも分枝状でも何れにても良く、例えばn
−プロピレン基,n−ブチレン基,n−ペンチレン基等の
好ましくは炭素数3〜10更に好ましくは3〜6の直鎖
状アルキレン基、例えば、イソブチレン基,2−エチル
プロピレン基等の好ましくは炭素数4〜10更に好まし
くは4〜6の分枝状アルキレン基等が挙げられる。
In the general formulas [1] and [2], R 1 ,
The alkyl group represented by R 2 , R 3 and R 4 may be linear, branched or cyclic, and includes, for example, an alkyl group having 1 to 6 carbon atoms. Represents a methyl group, an ethyl group, an n-propyl group, an isopropyl group,
n-butyl group, isobutyl group, s-butyl group, t-butyl group, n-pentyl group, isopentyl group, 2-methylbutyl group, 1-methylbutyl group, neopentyl group, 1-ethylpropyl group, n-hexyl group, Examples include an isohexyl group, a cyclopropyl group, a cyclopentyl group, and a cyclohexyl group. Further, any substituent may be used as long as it is inert to the reaction, and examples thereof include a phenyl group, a tolyl group, and a xylyl group. Examples of the phenyl group which may have a substituent include a phenyl group, a tolyl group, and a xylyl group. The alkylene chain may be linear or branched, and may be, for example, n
-A linear alkylene group having preferably 3 to 10 carbon atoms, more preferably 3 to 6 carbon atoms, such as a propylene group, an n-butylene group, and an n-pentylene group, and preferably a carbon atom such as an isobutylene group or a 2-ethylpropylene group. Numerical Formulas 4 to 10 and more preferably 4 to 6 branched alkylene groups are exemplified.

【0018】又、R5-OHで表されるアルコール類にお
けるR5で示される低級アルキル基としては、直鎖状で
も分枝状でも何れにても良いが、好ましくは炭素数1〜
6の低級アルキル基、より好ましくはメチル基,エチル
基,プロピル基、更に好ましくはメチル基が挙げられ
る。このアルコール類は反応物質であると同時に反応溶
媒としても働くため、他に反応溶媒を使用しなくとも良
い。尚、反応溶媒という点を考慮するとアルコール類の
使用量はアゾニトリル化合物の重量に対して1〜2倍量
程度は必要である。
The lower alkyl group represented by R 5 in the alcohol represented by R 5 —OH may be linear or branched, but preferably has 1 to 5 carbon atoms.
6 lower alkyl groups, more preferably a methyl group, an ethyl group, and a propyl group, and further preferably a methyl group. Since these alcohols are a reactant and also act as a reaction solvent, it is not necessary to use another reaction solvent. In consideration of the reaction solvent, it is necessary to use the alcohol in an amount of about 1 to 2 times the weight of the azonitrile compound.

【0019】本発明方法に於いては、先ずアゾニトリル
化合物をアルコール類に懸濁させ、次いでこれに塩化水
素を導入する。塩化水素の導入方法は、反応開始時から
反応終了時までの反応系内の塩化水素の濃度が、存在す
るアルコール類に対して飽和未満且つ30%W/Wを下回
らないような量を反応開始時に反応系に添加しても良い
し、或いは反応開始時に、その時の塩化水素の濃度が反
応系内のアルコール類に対して飽和未満且つ30%W/W
を下回らないような量を先ず添加して反応を行い、更に
反応の進行に合わせて、塩化水素の濃度が飽和未満且つ
30%W/Wを下回らないよう適宜塩化水素の導入を繰り
返すのも良い。即ち、導入方法の如何を問わず、反応系
内のアルコール類に対する塩化水素の濃度が反応開始時
から反応終了後までの間、常に飽和未満且つ30%W/W
を下回らないよう、好ましくは30%W/W以上ではある
が30%W/Wにより近い濃度で保たれていればよい。
In the method of the present invention, first, an azonitrile compound is suspended in an alcohol, and then hydrogen chloride is introduced into the suspension. The method for introducing hydrogen chloride is such that the concentration of hydrogen chloride in the reaction system from the start of the reaction to the end of the reaction is less than the saturation with respect to the alcohols present and does not fall below 30% W / W. At the beginning of the reaction, or the concentration of hydrogen chloride at that time is less than 30% W / W of saturation with respect to alcohols in the reaction system.
The reaction may be carried out by first adding an amount such that the amount does not fall below, and as the reaction proceeds, the introduction of hydrogen chloride may be repeated as appropriate so that the concentration of hydrogen chloride is less than saturation and does not fall below 30% W / W. . That is, regardless of the method of introduction, the concentration of hydrogen chloride with respect to alcohols in the reaction system is always less than 30% W / W from the start of the reaction to the end of the reaction.
Is preferably 30% W / W or more, but may be maintained at a concentration closer to 30% W / W.

【0020】又、反応系内への塩化水素の導入時の温度
は、通常0℃〜30℃、好ましくは0℃〜20℃であ
り、導入後の反応温度は、通常0℃〜40℃、好ましく
は10℃〜30℃である。
The temperature at the time of introducing hydrogen chloride into the reaction system is usually 0 ° C. to 30 ° C., preferably 0 ° C. to 20 ° C. The reaction temperature after the introduction is usually 0 ° C. to 40 ° C. Preferably it is 10 to 30 degreeC.

【0021】反応後は、常法に従って後処理を行うこと
によりアゾイミノエーテル塩酸塩を単離すればよい。ま
た、かくして得られたアゾイミノエーテル塩酸塩を単離
後或いは単離せずに、常法に従いアンモニア或いはアミ
ン類と反応させれば各種アミジン類を高収率、高品質
(残存溶媒を殆ど含まない)で得ることができるし、更
に、前記アゾイミノエーテル塩酸塩を単離後或いは単離
することなく反応液のままで、加水分解処理に付すこと
により、対応するアゾエステル化合物を容易に且つ高収
率で得ることができる。尚、加水分解に用いる水の使用
量は副生成物として析出する塩化アンモニウムが全て溶
解する量であれば良い。以下に実施例及び比較例を挙げ
て本発明を詳細に説明するが、本発明はこれらによって
何等限定されるものではない。
After the reaction, the azoimino ether hydrochloride may be isolated by post-treatment according to a conventional method. If the azoimino ether hydrochloride thus obtained is reacted with ammonia or amines according to a conventional method after or without isolation, various amidines can be obtained in high yield and high quality (contain almost no residual solvent). ), And the azoimino ether hydrochloride is subjected to hydrolysis treatment after isolation or without isolation as a reaction solution, so that the corresponding azoester compound can be easily and with high yield. Can be obtained at a rate. The amount of water used for the hydrolysis may be such that all the ammonium chloride precipitated as a by-product is dissolved. Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples, but the present invention is not limited thereto.

【0022】[0022]

【実施例】【Example】

実施例1 2,2'−アゾビス(2−メチルプロピオニトリル)12
0gをメタノール200gに懸濁し、氷冷下18℃で塩
化水素120g(塩化水素濃度37.5%W/W,反応終了
時の塩化水素濃度30%W/W)を導入した。25〜30
℃で6時間攪拌を行ったところ、2,2'−アゾビス(1
−イミノ−1−メトキシ−2−メチルプロパン)2塩酸
塩が生成していることが確認できた。次いで反応液を1
5℃に冷却して一夜放置した後、水420gに注入して
加水分解を行い、水層を分液除去してジメチル2,2'−
アゾビス(2−プロピオネート)の黄色液体140gを
得た。(収率83%)
Example 1 2,2′-azobis (2-methylpropionitrile) 12
0 g was suspended in 200 g of methanol, and 120 g of hydrogen chloride (hydrogen chloride concentration 37.5% W / W, hydrogen chloride concentration at the end of the reaction 30% W / W) was introduced at 18 ° C under ice cooling. 25-30
After stirring at 6 ° C. for 6 hours, 2,2′-azobis (1
-Imino-1-methoxy-2-methylpropane) dihydrochloride was confirmed to be formed. Then, add 1
After cooling to 5 ° C. and standing overnight, the mixture was poured into 420 g of water to carry out hydrolysis, and the aqueous layer was separated and removed to give dimethyl 2,2′-.
140 g of a yellow liquid of azobis (2-propionate) was obtained. (83% yield)

【0023】実施例2 2,2'−アゾビス(2−メチルプロピオニトリル)12
0gをメタノール200gに懸濁し、氷冷下18℃で塩
化水素98g(塩化水素濃度33%W/W)を導入した。
25〜30℃で3時間攪拌を行った後、塩化水素22g
を再び導入(反応終了時の塩化水素濃度30%W/W)し
4時間攪拌を行った。2,2'−アゾビス(1−イミノ−
1−メトキシ−2−メチルプロパン)2塩酸塩が生成し
ていることを確認後、反応液を15℃に冷却して一夜放
置した後、水420gに注入して加水分解を行い、水層
を分液除去してジメチル2,2'−アゾビス(2−プロピ
オネート)の黄色液体135gを得た。(収率80%)
Example 2 2,2'-azobis (2-methylpropionitrile) 12
0 g was suspended in 200 g of methanol, and 98 g of hydrogen chloride (hydrogen chloride concentration 33% W / W) was introduced at 18 ° C. under ice cooling.
After stirring at 25-30 ° C. for 3 hours, hydrogen chloride 22 g
Was introduced again (the concentration of hydrogen chloride at the end of the reaction was 30% W / W), and the mixture was stirred for 4 hours. 2,2′-azobis (1-imino-
After confirming that 1-methoxy-2-methylpropane) dihydrochloride has been formed, the reaction solution was cooled to 15 ° C. and allowed to stand overnight, and then poured into 420 g of water to perform hydrolysis. Separation and removal gave 135 g of dimethyl 2,2'-azobis (2-propionate) as a yellow liquid. (80% yield)

【0024】実施例3 2,2'−アゾビス(2−メチルプロピオニトリル)12
0gをメタノール200gに懸濁し、氷冷下18℃で塩
化水素98g(塩化水素濃度33%W/W)を導入した。
25〜30℃で1.5時間攪拌した後、塩化水素11g
を再び導入した。更に25〜30℃で1.5時間攪拌し
た後、塩化水素11gを導入(反応終了時の塩化水素濃
度30%)し4時間攪拌を行った。2,2'−アゾビス
(1−イミノ−1−メトキシ−2−メチルプロパン)2
塩酸塩が生成していることを確認後、反応液を15℃に
冷却し一夜放置した後、水420gに注入して加水分解
を行い、水層を分液除去してジメチル2,2'−アゾビス
(2−メチルプロピオネート)の黄色液体133gを得
た。(収率79%)
Example 3 2,2'-azobis (2-methylpropionitrile) 12
0 g was suspended in 200 g of methanol, and 98 g of hydrogen chloride (hydrogen chloride concentration 33% W / W) was introduced at 18 ° C. under ice cooling.
After stirring at 25-30 ° C for 1.5 hours, 11 g of hydrogen chloride was added.
Was introduced again. After further stirring at 25 to 30 ° C. for 1.5 hours, 11 g of hydrogen chloride was introduced (the concentration of hydrogen chloride at the end of the reaction was 30%), and stirring was performed for 4 hours. 2,2′-azobis (1-imino-1-methoxy-2-methylpropane) 2
After confirming that the hydrochloride had been formed, the reaction solution was cooled to 15 ° C. and allowed to stand overnight, then poured into 420 g of water to carry out hydrolysis, and the aqueous layer was separated to remove dimethyl 2,2′- 133 g of a yellow liquid of azobis (2-methylpropionate) was obtained. (79% yield)

【0025】比較例1 2,2'−アゾビス(2−メチルプロピオニトリル)12
0gをメタノール200gに懸濁し、氷冷下18℃で塩
化水素180g(飽和濃度)を導入した。途中、反応が
急激に進行し、発熱を抑えるために大量の氷水を用いて
冷却したが温度制御ができず、内温が40℃以上に上昇
し多量の塩化水素の揮散が認められた。塩化水素導入
後、6時間攪拌反応させた後、反応液を水420gに注
入して加水分解を行い、水層を除去してジメチル2,2'
−アゾビス(2−メチルプロピオネート)の黄色液体1
20gを得たが、この黄色液体中には原料の2,2'−ア
ゾビス(2−メチルプロピオニトリル)が8%存在して
いた。
Comparative Example 1 2,2'-azobis (2-methylpropionitrile) 12
0 g was suspended in 200 g of methanol, and 180 g of hydrogen chloride (saturated concentration) was introduced at 18 ° C. under ice cooling. During the reaction, the reaction progressed rapidly, and cooling was performed using a large amount of ice water in order to suppress heat generation. However, the temperature could not be controlled, the internal temperature rose to 40 ° C. or more, and a large amount of hydrogen chloride was volatilized. After the introduction of hydrogen chloride, the mixture was stirred and reacted for 6 hours. Then, the reaction solution was poured into 420 g of water to carry out hydrolysis, the aqueous layer was removed, and dimethyl 2,2 ′ was obtained.
-Yellow liquid 1 of azobis (2-methylpropionate)
Although 20 g was obtained, 8% of the raw material 2,2'-azobis (2-methylpropionitrile) was present in this yellow liquid.

【0026】比較例2 2,2'−アゾビス(2−メチルプロピオニトリル)12
0gをメタノール200gに懸濁し、氷冷下18℃で塩
化水素105g(塩化水素濃度34.4%W/W、反応終了
時の塩化水素濃度25%)を導入した。25〜30℃で
6時間攪拌を行ったところ、2,2'−アゾビス(1−イ
ミノ−1−メトキシ−2−メチルプロパン)2塩酸塩が
生成していることが確認できた。次いで15℃に冷却し
て一夜放置した後、水420gに注入して加水分解を行
い、水層を分液除去してジメチル2,2'−アゾビス(2
−メチルプロピオネート)の黄色液体128gを得た
が、得られた黄色液体中には未反応の2,2'−アゾビス
(2−メチルプロピオニトリル)が5%残存していた。
Comparative Example 2 2,2'-azobis (2-methylpropionitrile) 12
0 g was suspended in 200 g of methanol, and 105 g of hydrogen chloride (hydrogen chloride concentration 34.4% W / W, hydrogen chloride concentration at the end of the reaction 25%) was introduced at 18 ° C under ice cooling. After stirring at 25 to 30 ° C. for 6 hours, it was confirmed that 2,2′-azobis (1-imino-1-methoxy-2-methylpropane) dihydrochloride had been formed. Then, the mixture was cooled to 15 ° C. and allowed to stand overnight, and then poured into 420 g of water for hydrolysis. The aqueous layer was separated and removed, and dimethyl 2,2′-azobis (2
As a result, 5% of unreacted 2,2′-azobis (2-methylpropionitrile) remained in the obtained yellow liquid.

【0027】[0027]

【発明の効果】本発明は、以下に記載されるような効果
を奏する。 (1) 従来、アルコール類に対する塩化水素の濃度を
飽和としていたが、本発明では、反応時の反応系中の塩
化水素濃度を、飽和未満であり且つ30%W/Wを下回ら
ないように調整すること、好ましくは30%W/W以上で
はあるが30%W/Wにより近い濃度に調整することで反
応が円滑に進行及び完結し、且つ反応を容易に制御でき
る。 (2)塩化水素の濃度を、アルコール類に対して30%
W/Wにより近い濃度に調整することで塩化水素の使用量
を大幅に減らすことができ作業環境が著しく改善される
と共に、トルエン等他の溶媒の使用が不必要となった。 (3)本発明では、原料であるアゾニトリル化合物をア
ルコール類に懸濁させ、そこに塩化水素を導入するとい
う方法であるため、アゾニトリル化合物を固体若しくは
スラリー状で反応系に添加する際にみられた投入装置内
での結晶による閉塞が生じない。 (4)反応系にはトルエン等の塩化水素の溶解性の低い
溶媒が含まれていない為、イミノエーテル化反応終了後
は、反応液をそのまま加水分解処理に付すことによりア
ゾエステル化合物の単離回収に当たって煩雑な操作が回
避できる。上記のような多くの優れた効果が期待できる
ため、本発明は工業的に極めて有用なアゾイミノエーテ
ル塩酸塩及びアゾエステル化合物の製造方法であるとい
うことができる。
The present invention has the following effects. (1) Conventionally, the concentration of hydrogen chloride with respect to alcohols was saturated, but in the present invention, the concentration of hydrogen chloride in the reaction system at the time of the reaction is adjusted so as to be less than saturation and not less than 30% W / W. By adjusting the concentration to preferably 30% W / W or more but closer to 30% W / W, the reaction proceeds and completes smoothly, and the reaction can be easily controlled. (2) The concentration of hydrogen chloride is 30% with respect to alcohols.
By adjusting the concentration closer to W / W, the amount of hydrogen chloride used was greatly reduced, the working environment was remarkably improved, and the use of other solvents such as toluene became unnecessary. (3) In the present invention, since the azonitrile compound as a raw material is suspended in alcohols and hydrogen chloride is introduced therein, it is observed when the azonitrile compound is added to the reaction system in a solid or slurry form. Clogging due to crystals in the charging device does not occur. (4) Since the reaction system does not contain a solvent having low solubility of hydrogen chloride such as toluene, after completion of the iminoetherification reaction, the reaction solution is directly subjected to hydrolysis treatment to isolate and recover the azoester compound. In this case, complicated operations can be avoided. Since many excellent effects as described above can be expected, it can be said that the present invention is a method for producing an azoimino ether hydrochloride and an azo ester compound which is extremely useful industrially.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】一般式[1] 【化1】 (式中、R1,R2,R3及びR4は、夫々独立して、置換
基を有していても良いアルキル基又は置換基を有してい
ても良いフェニル基を示し、R1とR2及び/又はR3
4とがアルキレン鎖を形成する場合を含む。)で表さ
れるアゾニトリル化合物をR5-OH(R5は低級アルキ
ル基を示す。)で表されるアルコール類に懸濁させ、こ
れに塩化水素を、その濃度が反応系中のアルコール類に
対して飽和未満であり且つ30%W/Wを下回らない値に
維持されるように導入して反応を行わせる事を特徴とす
る、一般式[2] 【化2】 (式中、R1,R2,R3,R4及びR5は前記に同じ。)
で表される、アゾイミノエーテル塩酸塩の製造方法。
1. A compound of the general formula [1] (Wherein, R 1, R 2, R 3 and R 4 are, each independently represents which may have a may have a substituent alkyl group or a substituted phenyl group, R 1 And R 2 and / or R 3 and R 4 form an alkylene chain), and an alcohol represented by R 5 —OH (R 5 represents a lower alkyl group). The reaction is carried out by introducing hydrogen chloride into the suspension so that the concentration thereof is maintained at a value which is less than saturation with respect to the alcohols in the reaction system and does not fall below 30% W / W. General formula [2] characterized by the following: (In the formula, R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above.)
A method for producing an azoimino ether hydrochloride represented by the formula:
【請求項2】反応開始時から反応終了時までの反応系内
に於ける塩化水素の濃度が、存在するアルコール類に対
して、飽和未満であり且つ30%W/Wを下回らない値に
維持されるように、反応開始時に塩化水素の濃度を調整
する請求項1に記載の方法。
2. The concentration of hydrogen chloride in the reaction system from the start of the reaction to the end of the reaction is maintained at a value which is less than saturation and does not fall below 30% W / W with respect to the alcohols present. The method according to claim 1, wherein the concentration of hydrogen chloride is adjusted at the beginning of the reaction so as to be performed.
【請求項3】反応開始時に反応系内に於けるその濃度
が、存在するアルコール類に対して飽和未満であり且つ
30%W/Wを下回らないように塩化水素を存在させ、且
つ反応進行に伴い、必要に応じて塩化水素を導入してそ
の濃度を飽和未満且つ30%W/Wを下回らない値に維持
する請求項1に記載の方法。
3. At the start of the reaction, hydrogen chloride is present so that its concentration in the reaction system is less than saturation with respect to the alcohols present and does not fall below 30% W / W. The method according to claim 1, wherein hydrogen chloride is introduced as necessary to maintain the concentration at a value less than saturation and not less than 30% W / W.
【請求項4】請求項1の方法により、一般式[2] 【化3】 (式中、R1,R2,R3,R4及びR5は前記に同じ。)
で表される、アゾイミノエーテル塩酸塩を製造し、次い
でこれを加水分解することを特徴とする一般式[3] 【化4】 (式中、R1,R2,R3,R4及びR5は前記と同じ。)
で表されるアゾエステル化合物の製造方法。
4. The method according to claim 1, wherein the compound of the general formula [2] (In the formula, R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above.)
Wherein azoimino ether hydrochloride represented by the formula is produced and then hydrolyzed. (In the formula, R 1 , R 2 , R 3 , R 4 and R 5 are the same as described above.)
A method for producing an azoester compound represented by the formula:
【請求項5】イミノエーテル化反応の反応液をそのまま
加水分解処理に付す請求項4に記載の製造方法。
5. The process according to claim 4, wherein the reaction solution of the iminoetherification reaction is subjected to a hydrolysis treatment as it is.
JP27716196A 1996-09-27 1996-09-27 Novel process for producing azoester compounds Expired - Lifetime JP4092739B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27716196A JP4092739B2 (en) 1996-09-27 1996-09-27 Novel process for producing azoester compounds

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Application Number Priority Date Filing Date Title
JP27716196A JP4092739B2 (en) 1996-09-27 1996-09-27 Novel process for producing azoester compounds

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JPH10101635A true JPH10101635A (en) 1998-04-21
JP4092739B2 JP4092739B2 (en) 2008-05-28

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100776703B1 (en) * 1999-01-15 2007-11-16 아르끄마 프랑스 Method for preparing azoiminoethers and azocarboxylic acid esters and novel azocarboxylic acid mixed esters
CN103193686A (en) * 2013-04-26 2013-07-10 山东师范大学 Esterification method for preparing azodicarbonic acid
CN107141234A (en) * 2016-07-06 2017-09-08 邢保林 A kind of azo-bis-iso-dimethyl synthetic method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100776703B1 (en) * 1999-01-15 2007-11-16 아르끄마 프랑스 Method for preparing azoiminoethers and azocarboxylic acid esters and novel azocarboxylic acid mixed esters
CN103193686A (en) * 2013-04-26 2013-07-10 山东师范大学 Esterification method for preparing azodicarbonic acid
CN107141234A (en) * 2016-07-06 2017-09-08 邢保林 A kind of azo-bis-iso-dimethyl synthetic method

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