[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPH02145554A - Production of isocyanatoalkyl unsaturated carboxylate - Google Patents

Production of isocyanatoalkyl unsaturated carboxylate

Info

Publication number
JPH02145554A
JPH02145554A JP29958388A JP29958388A JPH02145554A JP H02145554 A JPH02145554 A JP H02145554A JP 29958388 A JP29958388 A JP 29958388A JP 29958388 A JP29958388 A JP 29958388A JP H02145554 A JPH02145554 A JP H02145554A
Authority
JP
Japan
Prior art keywords
reaction
ester
phosgene
carboxylic acid
unsaturated carboxylic
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
JP29958388A
Other languages
Japanese (ja)
Other versions
JP2632984B2 (en
Inventor
Shinya Matsuhira
松比良 伸也
Masaro Ogawa
小川 正郎
Shunsaku Mino
三野 俊作
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.)
Showa Rhodia Chemical Co
Original Assignee
Showa Rhodia Chemical Co
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 Showa Rhodia Chemical Co filed Critical Showa Rhodia Chemical Co
Priority to JP29958388A priority Critical patent/JP2632984B2/en
Publication of JPH02145554A publication Critical patent/JPH02145554A/en
Application granted granted Critical
Publication of JP2632984B2 publication Critical patent/JP2632984B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To obtain a compound useful as various synthetic intermediates in good yield without containing noxious impurities by reacting an imidazole derivative with phosgene and then with a monoalkanolamine and further esterifying the resultant product. CONSTITUTION:An imidazole derivative is reacted with phosgene in a solvent, such as dichloromethane, to provide a reaction product, which is then reacted with a monoalkanolamine. The resultant product is subsequently reacted with an unsaturated carboxylic acid, chloride or ester thereof at <=100 deg.C temperature, as necessary, under reduced pressure to afford the objective substance expressed by the formula (R is H, lower alkyl, aryl or vinyl; R' is H or methyl; A is 2-4C alkylene). A functional molecule having active hydrogen atom is added to the isocyanate group to synthesize a novel functional monomer.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は1種々の合成中間体として有用な、−取代(i
)にて表わされる不飽和カルボン酸イソシアナトアルキ
ルエステルの改良された製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention provides a method for producing - machining allowance (i), which is useful as a variety of synthetic intermediates.
) This invention relates to an improved method for producing an unsaturated carboxylic acid isocyanatoalkyl ester represented by:

C式中、Rは水素原子、低級アルキル基、アリール基、
又はビニル基を表わし、Roは水套原子又はメチル基を
表わす、又、Aは炭素a2〜4の直鎖又は分岐鎖フルキ
レン基を表わす、〕一般式〔!〕で表わされる不飽和カ
ルボン酸イソシアナトアルキルエステルは、−分子中に
C=C二重結合とインシアナト基を同時にもつため。
In formula C, R is a hydrogen atom, a lower alkyl group, an aryl group,
or represents a vinyl group, Ro represents an aqueous atom or a methyl group, and A represents a linear or branched fullkylene group having carbons a2 to 4,] general formula [! ] The unsaturated carboxylic acid isocyanatoalkyl ester represented by - has a C═C double bond and an incyanato group simultaneously in the molecule.

(A)単独で、又は他のビニルモノマーと共に重合させ
て、ポリマー鎖にインシアナト基をペンダントとしても
たせる。
(A) Polymerized alone or with other vinyl monomers to provide pendant incyanato groups on the polymer chain.

(B)−OH、−NH2のような活性水素をもつ官能基
を有するポリマーに付加させて、いわゆるマクロモノマ
ーを合成する。
(B) A so-called macromonomer is synthesized by adding it to a polymer having a functional group having active hydrogen such as -OH or -NH2.

(C)インシアナト基に活性水素をもつ機能性の分子(
例えば、生理活性物質など)を付加させて。
(C) Functional molecule with active hydrogen in the incyanato group (
For example, by adding physiologically active substances, etc.

新しい機能性七ツマ−を合成する。Synthesize a new functional 7-mer.

などの目的に使用土ることができる、工業上極めて有用
な化合物である。特に1式〔I〕に於てR=H,R’=
CH、n=2(7)化合物(メタクリル醜−2−イソシ
アナトエチルエステル)は、ホトレジスト、塗料、接着
剤等の分野で、特長ある製品を製造するための原料とし
て使用されている。
It is an extremely useful compound industrially, and can be used for various purposes. In particular, in formula 1 [I], R=H, R'=
CH, n=2(7) compound (methacrylic acid-2-isocyanatoethyl ester) is used as a raw material for manufacturing distinctive products in the fields of photoresists, paints, adhesives, etc.

〔従来の技術〕[Conventional technology]

不飽和カルボン酸イソシアナトアルキルエステルの製造
法としては、従来1次のような方法が提案されている。
As a method for producing an unsaturated carboxylic acid isocyanatoalkyl ester, the following method has been proposed.

(i)モノアルカノールアミンとクロロギ酸エチル及び
塩基性化合物(K2CO2)からヒドロキシカルバミン
酸エチルエステルを合成し、これに不飽和カルボン酸塩
化物を反応させてウレタンエステルとし、これを五塩化
リン又は塩化チオニルによってインシアナートに変える
方法、(米国特許第2.718.516号) この方法では、リンやイオウが不純物として残るという
問題があるほか、二重結合に基くと思われる副反応(例
えば1重合、MCIの付加)が起り易く、目的物を高収
率で得ることがむづかしい。
(i) Synthesize hydroxycarbamic acid ethyl ester from monoalkanolamine, ethyl chloroformate, and a basic compound (K2CO2), react this with an unsaturated carboxylic acid chloride to form a urethane ester, and convert this into phosphorus pentachloride or chloride. A method of converting thionyl into incyanate (U.S. Pat. No. 2,718,516) This method has the problem that phosphorus and sulfur remain as impurities, and side reactions that are thought to be based on double bonds (e.g. monopolymerization, MCI addition) is likely to occur, making it difficult to obtain the target product in high yield.

(2)不飽和カルボン酸塩化物とモノアルカノールアミ
ン塩酸塩とから不飽和カルボン酸アミノアルキルエステ
ル塩酸塩を合成し、これにホスゲンを反応させてインシ
アナートとする方法、(米国特許第2,821,544
号) この方法は収率が低いという欠点がある。
(2) A method of synthesizing unsaturated carboxylic acid aminoalkyl ester hydrochloride from unsaturated carboxylic acid chloride and monoalkanolamine hydrochloride and reacting it with phosgene to produce incyanate (U.S. Pat. No. 2,821, 544
No.) This method has the disadvantage of low yield.

(3)2−フルケニルオ午サシリンとホスゲンとの反応
、(特開昭54−5921) この方法では原料として高価なオキサゾリン化合物を使
用し、かつ工程が長し・ため、得られる製品も高価なも
のにならざるを得ない。
(3) Reaction of 2-flukenylomerosacillin and phosgene (JP-A-54-5921) This method uses an expensive oxazoline compound as a raw material, and the process is long, so the product obtained is also expensive. I have no choice but to become

また(i)〜(3)の各方法とも、製品中に塩素が不純
物として含まれるので1Ml子材料用途に用いるには不
適当である。
In addition, each of the methods (i) to (3) contains chlorine as an impurity in the product, and is therefore unsuitable for use as a 1M lubricant material.

(4)ジメチル−、ジエチル−1又はジビロピルカーボ
ネートとエタノールアミンの反応により。
(4) By reaction of dimethyl-, diethyl-1 or diviropyl carbonate with ethanolamine.

ヒドロキシウレタンを合成し、これを不飽和カルボン酸
、又はその塩化物もしくはエステルでウレタンエステル
とし、これを熱分解する方法、(特開昭62〜1953
54) この方法では、ウレタンエステルの熱分解がむづかしく
、例えば400℃という高温でも分解案は50〜60%
である。然るに、不飽和カルボン酸イソシアナトアルキ
ルエステルは極めて重合しやすいため、このような高温
にさらされると重合して、収率の低下、熱分解反応器の
閉塞、などの問題を起こしやすく、工業化するのは必ず
しも容易とは言い難い。
A method of synthesizing hydroxyurethane, converting it into a urethane ester with an unsaturated carboxylic acid, or its chloride or ester, and thermally decomposing it (JP-A-62-1953)
54) In this method, it is difficult to thermally decompose the urethane ester; for example, even at a high temperature of 400°C, the decomposition rate is 50-60%.
It is. However, unsaturated carboxylic acid isocyanatoalkyl esters are extremely easy to polymerize, so if they are exposed to such high temperatures, they tend to polymerize and cause problems such as reduced yields and blockages in thermal decomposition reactors, making them difficult to industrialize. It cannot be said that it is necessarily easy.

〔解決すべき問題点〕[Problems to be solved]

以上のような事情に鑑み、本発明者らは、高収率でかつ
、有害な不純物を含まない不飽和カルボン酸イソシアナ
トアルキルエステルを製造する方法について種々検討を
行なって来た。
In view of the above circumstances, the present inventors have conducted various studies on methods for producing unsaturated carboxylic acid isocyanato alkyl esters in high yield and free of harmful impurities.

〔問題点を解決する手段〕[Means to solve problems]

その結果、 (i) イミダゾール誘導体とホスゲンを反応させ(爾
)得られた反応生成物にモノアルカノールアミンを反応
させ ci目) (ii)の反応生成物を不飽和カルボン酸又
はその塩化物もしくはエステルを用いてエステル化する ことにより、収率よく不飽和カルボン酸のブロックされ
たイソシアナトアルキルエステルを合成することができ
、これを分解及び蒸留することにより181.リン、イ
オウ等の有害な不純物をほとんど含まない高純度の製品
が得られることを発見し1本発明を完成させるに至った
As a result, (i) reacting the imidazole derivative with phosgene; (d) reacting the obtained reaction product with a monoalkanolamine; By esterification using ester, a blocked isocyanatoalkyl ester of an unsaturated carboxylic acid can be synthesized in good yield, and by decomposition and distillation, 181. It was discovered that a highly pure product containing almost no harmful impurities such as phosphorus and sulfur could be obtained, and the present invention was completed.

本発明の第一工程で用いられるイミダゾール誘導体は、
ホスゲンと反応してカルバミン酸クロライドを生成する
必要があるため、>N−H結合をもっていなけらばなら
ず、従ってN−a換誘導体は使用できない。
The imidazole derivative used in the first step of the present invention is
Since it is necessary to react with phosgene to produce carbamic acid chloride, it must have a >N-H bond, and therefore N-a substituted derivatives cannot be used.

又、イミダゾール誘導体は比較的高価であるから、回収
して再利用することが望ましく、そのため、薄情できる
ものが好ましい。
Further, since imidazole derivatives are relatively expensive, it is desirable to collect and reuse them, and therefore, it is preferable to use one that can be treated in a light manner.

これらの観点から、・イミダゾール誘導体としては、イ
ミダゾール(無置換)、2−エチル−4−メチルイミダ
ゾール、2−メチルイミダゾール。
From these viewpoints, the imidazole derivatives include imidazole (unsubstituted), 2-ethyl-4-methylimidazole, and 2-methylimidazole.

2−エチルイミダゾール等が好ましい、イミダゾール誘
導体と反応させるホスゲンは1反応を完全に進行させる
ため、イミダゾール誘導体と等モル又はそれ以上、好ま
しくは1.1〜1.5倍モル用いるのがよい、未反応の
イミダゾールが残っていると好ましくない副反応の原因
となリラるので。
Phosgene to be reacted with the imidazole derivative, preferably 2-ethylimidazole, is preferably used in an amount equal to or more than the imidazole derivative, preferably 1.1 to 1.5 times the mole, in order to allow one reaction to proceed completely. Remaining reactive imidazole may cause undesirable side reactions.

反応は十分完全に進行させなければならない。The reaction must proceed to a sufficient degree of completeness.

本反応は1反応の円滑化のため、溶媒中で行うことが好
ましい、溶媒としては、ホスゲン、アミン、アルコール
、酸、インシアナート等と反応しないことが必要で、ジ
クロルメタンのようなハロゲン化炭化水素、トルエンの
ような芳香族炭化水素等が用いられる。
This reaction is preferably carried out in a solvent in order to facilitate one reaction.The solvent must not react with phosgene, amines, alcohols, acids, incyanates, etc., and must not react with halogenated hydrocarbons such as dichloromethane, Aromatic hydrocarbons such as toluene are used.

イミダゾール誘導体とホスゲンの反応の後。After the reaction of imidazole derivatives with phosgene.

過剰のホスゲンと、生成した塩化水素を追い出す方がよ
い、過肩のホスゲンや塩化水素が残留していると次のス
テップの反応の際にアルカノールアミンと反応し、好ま
しくない副生物を与える。
It is better to drive off the excess phosgene and hydrogen chloride that is formed; any excess phosgene or hydrogen chloride that remains will react with the alkanolamine during the next step reaction, giving undesirable by-products.

ホスゲン及び塩化水素を除くには、窒素等の不活性ガス
を常圧〜若干の減圧下で吹き込めばよい。
To remove phosgene and hydrogen chloride, an inert gas such as nitrogen may be blown in at normal pressure to slightly reduced pressure.

ホスゲンとイミダゾール誘導体との反応生成物(A)と
アルカノールアミンとを反応させる第2工程に於ては、
アルカ/−ルアミソ中に(A)を除々に加えて行くのが
よい、この場合、アルカノールアミンは(A)の合成に
用いたのと同じ溶媒に溶かしておくのが好ましい、又、
発生する塩化水素を除去するため、水素化ナトリウム、
炭酸カリウム、トリエチルアミン、ピリジン等のHC交
−受容体を共存させておくことが望ましい。
In the second step of reacting the reaction product (A) of phosgene and an imidazole derivative with an alkanolamine,
It is preferable to gradually add (A) to the alkaliamine. In this case, it is preferable that the alkanolamine be dissolved in the same solvent used for the synthesis of (A).
Sodium hydride, to remove hydrogen chloride generated.
It is desirable that HC cross-receptors such as potassium carbonate, triethylamine, pyridine, etc. coexist.

このようにして得られた、(A)とアルカノールアミン
の反応生成物(B)を、不飽和脂肪酸のエステルにする
には、常法通り不飽和脂肪酸、又はその酸塩化物によっ
てエステル化するか、その酸のエステルとのエステル交
換によることができる。この際1反応器度が100℃、
好ましくは80℃を越えないように、必要あらば減圧下
で反応させることが望ましい、i1度が上がりすざると
In order to convert the reaction product (B) of (A) and alkanolamine thus obtained into an ester of an unsaturated fatty acid, it can be esterified with an unsaturated fatty acid or its acid chloride in a conventional manner. , by transesterification with an ester of the acid. At this time, the temperature of one reactor is 100℃,
Preferably, the temperature should not exceed 80°C, and if necessary, the reaction should be carried out under reduced pressure, unless the temperature rises.

生成物が分解して、好ましくない副産物を与えるおそれ
がある。
The product may decompose giving undesirable by-products.

反応終了後、得られた溶液を、直接熱分解することがで
きるが、その前に炭酸水素ナトリウム等の弱アルカリ性
溶液及び水で洗すして、無機酸及び塩を除去する方が望
ましい。
After completion of the reaction, the resulting solution can be directly thermally decomposed, but before that, it is preferable to wash it with a weakly alkaline solution such as sodium hydrogen carbonate and water to remove inorganic acids and salts.

このようにして得られた不飽和脂肪酸のエステルを熱分
解すると目的とする不飽和脂肪酸イソシアナトエステル
が得られるが、これは前述のように極めて重合しやすい
ので、熱重合を起さない程度の温度で分解する必要があ
る。又、この熱分解反応は平衡反応であるため、生成物
を常時除去しながら反応させることが好ましい。
When the unsaturated fatty acid ester obtained in this way is thermally decomposed, the desired unsaturated fatty acid isocyanato ester is obtained, but as mentioned above, this is extremely easy to polymerize, so It must be decomposed by temperature. Furthermore, since this thermal decomposition reaction is an equilibrium reaction, it is preferable to carry out the reaction while constantly removing products.

このような観点から、熱分解反応は、反応蒸留の形式で
行うことが望ましい、即ち、¥tc圧下で溶媒を蒸発さ
せた後、触媒量の3級アミン又は有機スズ化合物を加え
、減圧下90〜120℃で蒸留することにより1分解と
目的生成物の蒸留精製が同時に行える0反応終了後の残
液は再び第一工程で使用することができる。
From this point of view, it is desirable to carry out the thermal decomposition reaction in the form of reactive distillation, that is, after evaporating the solvent under \tc pressure, a catalytic amount of tertiary amine or organotin compound is added, and the reaction is heated for 90 minutes under reduced pressure. By distilling at ~120°C, 1 decomposition and distillation purification of the target product can be performed simultaneously.The residual liquid after the completion of the reaction can be used again in the first step.

このあと必要に応じ、不純物として混入した溶媒を蒸留
により除き、更に純度の高い製品を得ることができる。
Thereafter, if necessary, the solvent mixed as an impurity can be removed by distillation to obtain a product with even higher purity.

〔実施例〕〔Example〕

次に実施例により1本発明を更に具体的に説明する。 Next, the present invention will be explained in more detail with reference to Examples.

支五負」 トルエン200m交、2−エチル−4−メチルイミダゾ
ール218gの混合物中に、ホスゲン250gを室温で
吹き込み(約1時間)、その後。
250 g of phosgene was blown into a mixture of 200 m of toluene and 218 g of 2-ethyl-4-methylimidazole at room temperature (about 1 hour), and then.

18時間放置した。温度を40〜50℃に保ったオイル
バス中に反応器を浸し、この中に窒素ガスを毎分l皇の
割合で8時間吹き込んだ。
It was left for 18 hours. The reactor was immersed in an oil bath whose temperature was maintained at 40 to 50°C, and nitrogen gas was blown into the oil bath at a rate of 1/min for 8 hours.

得られた混合物を、モノエタノールアミン122g、無
水炭酸カリウム173g、 トルエン100gの混合物
中に、よく撹拌しながら1時間かけて滴下した。そのま
ま8WIf間撹拌を続けた後、水500gで2回洗浄し
た。
The obtained mixture was added dropwise to a mixture of 122 g of monoethanolamine, 173 g of anhydrous potassium carbonate, and 100 g of toluene over 1 hour with thorough stirring. After continuing to stir for 8 WIf, the mixture was washed twice with 500 g of water.

次にP−)ルエンスルホンs5g及び、アクリル%15
0gを加え、ディーン・スタークトラップをつけた反紀
:器で、60〜70Torrの減圧下で8時間環流させ
、エステル化を行なった。
Next, P-) Luenesulfone s 5g and acrylic% 15
0 g was added and refluxed for 8 hours under reduced pressure of 60 to 70 Torr in a vessel equipped with a Dean-Stark trap to perform esterification.

反応終了後、5%炭酸水素ナトリウム水溶液500mu
で一回、水500m交で二回洗浄を行ない、次に、50
〜60Torrの減圧下でトルエンを留出させた後、ジ
ブチルスズジラウレート0.5gを加え加熱浴の温度を
100〜120℃に上げて減圧度を次第に増しながら反
応居留を行なった。
After the reaction is complete, add 500 mu of 5% sodium hydrogen carbonate aqueous solution.
Wash once with 500 m of water and twice with 500 m of water, then wash with 500 m of water.
After distilling toluene under a reduced pressure of ~60 Torr, 0.5 g of dibutyltin dilaurate was added, and the temperature of the heating bath was raised to 100 to 120°C, and reaction residence was carried out while gradually increasing the degree of vacuum.

この結果、187gのm2−インシアナトエチルアクリ
レートが得られた。この中にはトルエンが約5%(重量
)含まれていた。
As a result, 187 g of m2-incyanatoethyl acrylate was obtained. This contained about 5% (by weight) toluene.

支亙班ユ 2−エチル−4−メチルイミダゾールの代わりに、イミ
ダゾール136gを用い、実施例1と同様にしてホスゲ
ン化及び、モノエタノ−ルアミンセの反応を行わせた。
Phosgenation and monoethanolamine reaction were carried out in the same manner as in Example 1, using 136 g of imidazole instead of 2-ethyl-4-methylimidazole.

イミダゾール15g、4゜4−ジアザビシフel(2,
2,2)オクタン10g、及びメチルメタクリレート7
10gを加え。
15 g of imidazole, 4゜4-diazabisiful el (2,
2,2) Octane 10g and methyl methacrylate 7
Add 10g.

200〜250To rr(D減圧下生ずるメタノール
をメチルメタクリレートとの共S混合物として除きなが
ら反応させた。途中メチルメタクリレートを200gず
つ8時間毎に二回追加し、24時間反+5後、イミダゾ
ールでブロックされた2−インシアナトメチルメタクリ
レートが62%の収率で生成していた。
The reaction was carried out under reduced pressure of 200 to 250 Torr (D) while removing the generated methanol as a co-S mixture with methyl methacrylate. During the reaction, 200 g of methyl methacrylate was added twice every 8 hours, and after 24 hours of reaction, the reaction was blocked with imidazole. 2-incyanatomethyl methacrylate was produced in a yield of 62%.

支立貞ユ 2−エチル−4−メチルイミダゾールの代りに2−メチ
ルイミダゾール164gを用い、実施例1と同様にして
ホスゲン化及びモノエタノールアミンとの反応を行わせ
た。これに96%クロトン酸クロライド218gを加え
、70〜80℃で約2.5時間エステル化反応を行なっ
た。
Phosgenation and reaction with monoethanolamine were carried out in the same manner as in Example 1, using 164 g of 2-methylimidazole instead of 2-ethyl-4-methylimidazole. To this was added 218 g of 96% crotonic acid chloride, and an esterification reaction was carried out at 70 to 80°C for about 2.5 hours.

反応終了後実施例1と同様に洗浄、熱分解を行なった。After the reaction was completed, washing and thermal decomposition were performed in the same manner as in Example 1.

その結果、170gの粗2−インシアナトエチルクロト
ネートが得られた。この中にはトルエンが約5%と3−
クロロ#′v1%−2° −イソシアナトエチルエステ
ルが約3%含まれていた。
As a result, 170 g of crude 2-incyanatoethyl crotonate was obtained. This contains approximately 5% toluene and 3-
It contained about 3% of chloro #'v1%-2°-isocyanatoethyl ester.

支旅土1 モノエタノールアミンの代りにモノ(2−ヒドロキシプ
ロピル)アミン150gを、又クロトン酸クロライドの
代りに95%桂皮酸クロライド351gを用いた他は実
施例3と同様にして、エステル化反応を行なった。その
結果、2−メチルイミダゾールでブロックされた、桂皮
酸−2−イソシアキトプロピルエステルが67%の収率
で生成していた。
Substance 1 Esterification reaction was carried out in the same manner as in Example 3, except that 150 g of mono(2-hydroxypropyl)amine was used instead of monoethanolamine, and 351 g of 95% cinnamic acid chloride was used instead of crotonic acid chloride. I did it. As a result, cinnamic acid-2-isocyachitopropyl ester blocked with 2-methylimidazole was produced in a yield of 67%.

〔発明の効果〕〔Effect of the invention〕

本発明によれば有害な不純物を含まない不飽和カルボン
酸イソシアナトアルキルエステルを高収率で製造するこ
とができる。
According to the present invention, unsaturated carboxylic acid isocyanatoalkyl esters containing no harmful impurities can be produced in high yield.

Claims (1)

【特許請求の範囲】 (i)イミダゾール誘導体とホスゲンを反応させ、 (ii)(i)の反応生成物にモノアルカノールアミン
を反応させ、 (iii)(ii)の反応生成物を不飽和カルボン酸、
又はその塩化物もしくはエステルを用いてエステル化す
る ことを特徴とする一般式〔 I 〕で表わされる不飽和カ
ルボン酸イソシアナトアルキルエステルの製造法。 ▲数式、化学式、表等があります▼〔 I 〕 〔式中、Rは水素原子、低級アルキル基、アリール基、
又はビニル基を表わし、R’は水素原子又はメチル基を
表わす。又、Aは炭素数2〜4の直鎖又は分岐鎖アルキ
レン基を表わす。〕
[Claims] (i) reacting an imidazole derivative with phosgene, (ii) reacting the reaction product of (i) with a monoalkanolamine, and (iii) reacting the reaction product of (ii) with an unsaturated carboxylic acid. ,
A method for producing an unsaturated carboxylic acid isocyanatoalkyl ester represented by the general formula [I], which comprises esterifying the unsaturated carboxylic acid isocyanatoalkyl ester with the general formula [I] or its chloride or ester. ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [I] [In the formula, R is a hydrogen atom, a lower alkyl group, an aryl group,
or a vinyl group, and R' represents a hydrogen atom or a methyl group. Further, A represents a straight chain or branched alkylene group having 2 to 4 carbon atoms. ]
JP29958388A 1988-11-29 1988-11-29 Process for producing unsaturated carboxylic acid isocyanatoalkyl ester Expired - Lifetime JP2632984B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29958388A JP2632984B2 (en) 1988-11-29 1988-11-29 Process for producing unsaturated carboxylic acid isocyanatoalkyl ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29958388A JP2632984B2 (en) 1988-11-29 1988-11-29 Process for producing unsaturated carboxylic acid isocyanatoalkyl ester

Publications (2)

Publication Number Publication Date
JPH02145554A true JPH02145554A (en) 1990-06-05
JP2632984B2 JP2632984B2 (en) 1997-07-23

Family

ID=17874515

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29958388A Expired - Lifetime JP2632984B2 (en) 1988-11-29 1988-11-29 Process for producing unsaturated carboxylic acid isocyanatoalkyl ester

Country Status (1)

Country Link
JP (1) JP2632984B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102702028A (en) * 2012-06-12 2012-10-03 江苏快达农化股份有限公司 Method for synthesizing methacryloxyethyl isocyanate
JP2013523881A (en) * 2010-04-14 2013-06-17 スリーエム イノベイティブ プロパティズ カンパニー Isocyanate production method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013523881A (en) * 2010-04-14 2013-06-17 スリーエム イノベイティブ プロパティズ カンパニー Isocyanate production method
US9006480B2 (en) 2010-04-14 2015-04-14 3M Innovative Properties Company Process for producing isocyanates
CN102702028A (en) * 2012-06-12 2012-10-03 江苏快达农化股份有限公司 Method for synthesizing methacryloxyethyl isocyanate

Also Published As

Publication number Publication date
JP2632984B2 (en) 1997-07-23

Similar Documents

Publication Publication Date Title
FR2630444A1 (en) TIN COMPOUNDS USEABLE IN PARTICULAR AS LATENT CATALYSTS FOR THE PREPARATION OF POLYURETHANES
JPS63119456A (en) Manufacture of retinoylchloride
JPH02145554A (en) Production of isocyanatoalkyl unsaturated carboxylate
JP2554965B2 (en) Method for purifying dialkyl carbonate
FR2628106A1 (en) PROCESS FOR THE PREPARATION OF UREA N-SULFONYL DERIVATIVES
JPH03264549A (en) Production of unsaturated monomer
JPH07112986B2 (en) Process for producing carboxylic acid chloride and its catalyst
Ueda et al. 3, 3'-(Phenylphosphinylidene) bis (2 (3H)-benzoxazolone) and 3, 3'-(phenylphosphinylidene) bis (2 (3H)-benzothiazolone). New activating agents.
US3468934A (en) Acyloxyalkylamine hydrochlorides
JPS60255752A (en) Manufacture of 2-chloropropionic acid ester
JPS6059897B2 (en) Method for preparing chloroformates with terminal acrylic or methacrylic groups
JPS5941984B2 (en) Method for producing chlorothiol formate
JPH04312568A (en) Production of n,n&#39;-bis(2,6-dialkylphenyl)thiourea
EP0585165B1 (en) Process for the preparation of acyl isocyanates
JPH02129163A (en) Production of unsaturated carboxylic acid 2-isocyanatoalkyl ester
JP3640319B2 (en) Method for producing benzamide derivative
JPH02172969A (en) Production of dithiol di(meth)acrylate
JP2857742B2 (en) Method for producing metal salt of N, N-bis (hydroxyalkyl) sulfamic acid
JP3851990B2 (en) Method for producing acryloylcarbamate
RU2103260C1 (en) Method for production of 4-nitrobenzamide
JPS62181269A (en) Novel active esterification agent compound
EA001696B1 (en) Process for producing 1-chlorocarbonyl-4-piperidinopiperidine or hydrochloride thereof
JPH02200646A (en) Fluoroalkyl group-containing aromatic derivative and preparation thereof
JPH07103085B2 (en) Method for purifying unsaturated carboxylic acid isocyanatoalkyl ester
JPH0632768A (en) Production of unsaturated quaternary ammonium salt

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080425

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090425

Year of fee payment: 12

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090425

Year of fee payment: 12