JP2001058986A - Production of vinyloxazoline or isopropenyloxazoline derivative - Google Patents

Production of vinyloxazoline or isopropenyloxazoline derivative

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Publication number
JP2001058986A
JP2001058986A JP11234939A JP23493999A JP2001058986A JP 2001058986 A JP2001058986 A JP 2001058986A JP 11234939 A JP11234939 A JP 11234939A JP 23493999 A JP23493999 A JP 23493999A JP 2001058986 A JP2001058986 A JP 2001058986A
Authority
JP
Japan
Prior art keywords
derivative
adduct
diels
cyclopentadiene
meth
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
JP11234939A
Other languages
Japanese (ja)
Other versions
JP4379965B2 (en
Inventor
Isao Okidaka
勲 沖高
Tenmei Chin
天明 陳
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.)
Kohjin Holdings Co Ltd
Kohjin Co
Original Assignee
Kohjin Holdings Co Ltd
Kohjin Co
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Application filed by Kohjin Holdings Co Ltd, Kohjin Co filed Critical Kohjin Holdings Co Ltd
Priority to JP23493999A priority Critical patent/JP4379965B2/en
Publication of JP2001058986A publication Critical patent/JP2001058986A/en
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Publication of JP4379965B2 publication Critical patent/JP4379965B2/en
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  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce the subject compound in high yield by subjecting (A) cyclopentadiene and (B) a (meth)acrylic ester to a Diels-Alder reaction, amidating the obtained Diels-Alder adduct, dehydrating the amidation product to provide an oxazolylnorbornene derivative, and thermally decomposing the derivative. SOLUTION: (A) Cyclopentadiene and (B) a (meth)acrylic ester are subjected to a Diels-Alder reaction, and the obtained Diels-Alder adduct is amidated with (D) aminoethanol by using a catalyst preferably a sodium methylate or the like at 20-80 deg.C to provide an amide adduct. The amide adduct is heated preferably under a reduced pressure to 160-250 deg.C to carry out dehydration cyclization and to provide (E) an oxazolylnorbornene derivative of formula I (R1 is H or methyl; R2 to R5 are each an alkyl or an aryl), and the obtained oxazolylnorbornene derivative is thermally decomposed in vapor phase preferably at 200-500 deg.C to provide the objective compound of formula II.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はその分子中に重合性の二
重結合とオキサゾリン基を有する二官能性モノマーで、
水系塗料、接着剤、樹脂改質剤、架橋剤として有用なビ
ニルオキサゾリンまたはイソプロペニルオキサゾリン誘
導体の製造法に関する。
The present invention relates to a bifunctional monomer having a polymerizable double bond and an oxazoline group in its molecule.
The present invention relates to a method for producing a vinyloxazoline or isopropenyloxazoline derivative useful as a water-based paint, an adhesive, a resin modifier, or a crosslinking agent.

【0002】[0002]

【従来の技術】ビニルオキサゾリンまたはイソプロペニ
ルオキサゾリン誘導体の製造法としては、特開昭59−
24977号公報に示されるように、2−アルキル−2
−オキサゾリンをホルムアルデヒドと縮合させて2−
(α−ヒドロキシメチルアルキル)−2−オキサゾリン
を得、これをアルカリ触媒存在下に脱水する方法があ
る。この方法によれば、イソプロペニルオキサゾリンに
ついての縮合収率は96.5%、脱水収率は97.8%
と明示されているが、ビニルオキサゾリンの収率は明確
ではなく、またいずれのモノマーについても最終的な単
離方法、単離収率については何ら述べられていない。ま
た収率はホルムアルデヒド基準の収率であり、この方法
ではホルムアルデヒドに対して過剰のアルキルオキサゾ
リンを使用するため過剰のアルキルオキサゾリンの蒸留
回収が避けられず、オキサゾリン基準の収率は極めて低
いものと推定される。
2. Description of the Related Art A method for producing a vinyloxazoline or isopropenyloxazoline derivative is disclosed in
No. 24977, 2-alkyl-2
-Condensation of oxazoline with formaldehyde to give 2-
There is a method of obtaining (α-hydroxymethylalkyl) -2-oxazoline and dehydrating it in the presence of an alkali catalyst. According to this method, the condensation yield for isopropenyloxazoline is 96.5%, and the dehydration yield is 97.8%.
However, the yield of vinyloxazoline is not clear, and the final isolation method and isolation yield of any monomer are not described at all. In addition, the yield is based on formaldehyde.In this method, excess alkyloxazoline is inevitably distilled and recovered because excess alkyloxazoline is used relative to formaldehyde, and it is estimated that the yield based on oxazoline is extremely low. Is done.

【0003】一方、アクリル酸メチルなどの二重結合を
シクロペンタジエン等と反応して得たディールス-アル
ダー付加体をアミン等とのアミノリシスを行い、引き続
いて生成物を熱分解(逆ディールス-アルダー反応)す
ることにより、N−置換アクリルアミドを得ることは、
特開昭47−34311号公報に記載されているが、こ
れらはすべて比較的簡単なN−アルキル置換アクリルア
ミドに限られており、オキサゾリンのような活性な反応
性基をもつ環状化合物については何ら触れられていな
い。
On the other hand, a Diels-Alder adduct obtained by reacting a double bond such as methyl acrylate with cyclopentadiene or the like is subjected to aminolysis with an amine or the like, and then the product is thermally decomposed (reverse Diels-Alder reaction). ) To obtain an N-substituted acrylamide,
Although these are described in JP-A-47-34311, they are all limited to relatively simple N-alkyl-substituted acrylamides, and no mention is made of cyclic compounds having an active reactive group such as oxazoline. Not been.

【0004】[0004]

【発明が解決しようとする課題】本発明は高純度、高収
率でビニルオキサゾリンまたはイソプロペニルオキサゾ
リン誘導体を与える製造法を確立することを課題とす
る。
SUMMARY OF THE INVENTION An object of the present invention is to establish a process for producing a vinyloxazoline or isopropenyloxazoline derivative with high purity and high yield.

【0005】[0005]

【課題を解決する手段】本発明者らは、かかる課題を解
決するために鋭意研究の結果、シクロペンタジエンと
(メタ)アクリル酸エステルとのディールスアルダー付
加体を、アミノエタノールでアミド化した後、脱水して
得られる化1で示されるオキサゾリルノルボルネン誘導
体を熱分解して得られた粗モノマーを、比較的簡単な蒸
留をするだけで、高純度、高収率で、ビニルオキサゾリ
ンまたはイソプロペニルオキサゾリン誘導体が得られる
ことを見いだし、本発明を完成するに至った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, after amidating a Diels-Alder adduct of cyclopentadiene and (meth) acrylate with aminoethanol, The crude monomer obtained by thermally decomposing the oxazolyl norbornene derivative represented by the formula (1) obtained by dehydration can be converted into vinyloxazoline or isopropenyl in high purity and high yield by relatively simple distillation. The inventors have found that an oxazoline derivative can be obtained, and have completed the present invention.

【0006】以下、本発明を詳細に説明する。シクロペ
ンタジエンと(メタ)アクリル酸エステルとのディール
スアルダー反応は、攪拌装置、温度計、滴下装置を備え
た三つ口フラスコに、(メタ)アクリル酸エステルを加
え、これにシクロペンタジエンを徐々に加え反応を行わ
せる。アクリル酸エステルとしては(メタ)アクリル酸
メチル、(メタ)アクリル酸エチル、(メタ)アクリル
酸ブチルなどが使用できる。
Hereinafter, the present invention will be described in detail. The Diels-Alder reaction between cyclopentadiene and (meth) acrylate is performed by adding (meth) acrylate to a three-necked flask equipped with a stirrer, a thermometer, and a dropping device, and gradually adding cyclopentadiene thereto. Allow the reaction to take place. As the acrylate, methyl (meth) acrylate, ethyl (meth) acrylate, butyl (meth) acrylate and the like can be used.

【0007】シクロペンタジエンの滴下量は、(メタ)
アクリル酸エステルに対して当モルが使用されるが、反
応完結のために過剰のシクロペンタジエンを使用しても
よい。過剰量は20モル%以下が好ましい。さらなる過
剰量は反応の完結を早めるが、シクロペンタジエン自体
が2分子縮合して多量のジシクロペンタジエンの副生物
を招くため好ましくない。
The amount of cyclopentadiene added is (meth)
Although an equimolar amount is used based on the acrylate ester, an excess of cyclopentadiene may be used to complete the reaction. The excess amount is preferably 20 mol% or less. Although a further excess accelerates the completion of the reaction, it is not preferable because cyclopentadiene itself is condensed into two molecules to produce a large amount of by-products of dicyclopentadiene.

【0008】反応温度はいかなる温度でもかまわない
が、60℃以下で行うのが好ましい。これより高い温度
では、ジシクロペンタジエンの副生物が増加するので好
ましくない。
[0008] The reaction temperature may be any temperature, but it is preferably carried out at 60 ° C or lower. Higher temperatures are not preferred because dicyclopentadiene by-products increase.

【0009】このようにして得られたエステル付加体
は、必要ならば、減圧蒸留などで未反応のアクリル酸エ
ステルまたはシクロペンタジエンおよび副生するジシク
ロペンタジエンを回収し精製される。
The thus obtained ester adduct is, if necessary, purified by collecting unreacted acrylate or cyclopentadiene and dicyclopentadiene as a by-product by distillation under reduced pressure.

【0010】次に、このエステル付加体に対して、アミ
ノアルコールを反応させてアミド付加体を得る。アミノ
アルコールとしては、2−アミノエタノール、2−アミ
ノ−1−プロパノール、1−アミノ−2−プロパノー
ル、3−アミノ−2−ブタノール、およびこれらの同族
体がある。アミノエタノールは、反応を完結するため
に、通常エステル付加体に対して当モル以上が使用され
る。過剰量は50モル%以下で、20モル%が好まし
い。
Next, the ester adduct is reacted with an amino alcohol to obtain an amide adduct. Amino alcohols include 2-aminoethanol, 2-amino-1-propanol, 1-amino-2-propanol, 3-amino-2-butanol, and homologs thereof. Aminoethanol is usually used in an equimolar amount or more based on the ester adduct to complete the reaction. The excess amount is 50 mol% or less, preferably 20 mol%.

【0011】反応に使用される触媒としては、アルカリ
金属水酸化物、アルカリ金属アルコラートであり、通常
ナトリウムメチラートが好ましい。触媒は、アミノアル
コールによるエステル付加体のアミド化を触媒するに足
る量にて使用されるが、通常エステル付加体に対して
0.1モル%以上、10モル%以下であり、0.5モル
%以上、2モル%以下が好ましい。
The catalyst used in the reaction is an alkali metal hydroxide or an alkali metal alcoholate, and preferably sodium methylate. The catalyst is used in an amount sufficient to catalyze the amidation of the ester adduct with the amino alcohol, but is usually 0.1 mol% or more and 10 mol% or less and 0.5 mol % Or more and 2 mol% or less is preferable.

【0012】アミド化反応は、20℃以上、80℃以下
で行われる。好ましくは60℃以下である。温度が高す
ぎると、エステル付加体がアミノアルコールに2分子反
応した副生物などが生成するため好ましくない。
[0012] The amidation reaction is carried out at a temperature of not lower than 20 ° C and not higher than 80 ° C. Preferably it is 60 ° C. or lower. If the temperature is too high, it is not preferable because by-products such as two molecules of the ester adduct reacted with the amino alcohol are formed.

【0013】反応後、生成したアルコールおよび過剰の
アミノエタノールを蒸留回収して、アミド付加体を得
る。
After the reaction, the produced alcohol and excess aminoethanol are recovered by distillation to obtain an amide adduct.

【0014】次に、このアミド付加体を脱水閉環して、
オキサゾリルノルボルネン誘導体を得る。脱水閉環反応
は、触媒として、酸化亜鉛、塩化亜鉛、酢酸亜鉛、硫酸
亜鉛などの亜鉛塩、硫酸第二鉄、塩化第二鉄などの鉄塩
など、公知の触媒が使用できる。触媒は、アミド付加体
に対して1重量%以上、30重量%以下であり、好まし
くは5重量%以上、15重量%以下である。
Next, the amide adduct is dehydrated and ring-closed,
An oxazolyl norbornene derivative is obtained. Known catalysts such as zinc salts such as zinc oxide, zinc chloride, zinc acetate and zinc sulfate, and iron salts such as ferric sulfate and ferric chloride can be used as the catalyst in the dehydration ring closure reaction. The amount of the catalyst is 1% by weight or more and 30% by weight or less, preferably 5% by weight or more and 15% by weight or less based on the amide adduct.

【0015】溶媒は必ずしも必要ないが、反応系のスラ
リー濃度を調整するために有効であり、不活性な溶媒と
してスルホラン、ポリプロピレングリコール、脂肪族炭
化水素、芳香族炭化水素などの使用が好ましい。
Although a solvent is not always necessary, it is effective for adjusting the slurry concentration of the reaction system, and it is preferable to use sulfolane, polypropylene glycol, aliphatic hydrocarbon, aromatic hydrocarbon, or the like as an inert solvent.

【0016】反応はアミド付加体、触媒、溶媒からなる
スラリー溶液を、減圧下、160〜250℃で加熱する
ことで、脱水して生成した水とともに閉環したオキサゾ
リルノルボルネン誘導体が留出してくる。減圧度は、反
応温度と反応速度で変わってくるが、通常20mmHg
以下で行われる。
In the reaction, a slurry solution composed of an amide adduct, a catalyst and a solvent is heated at 160 to 250 ° C. under reduced pressure, whereby a ring-closed oxazolyl norbornene derivative is distilled out together with water generated by dehydration. . The degree of pressure reduction depends on the reaction temperature and the reaction rate, but is usually 20 mmHg.
This is done below.

【0017】化1で示されるオキサゾリルノルボルネン
誘導体の熱分解は、200〜500℃程度の気相で行う
ことが望ましい。熱交換を容易にするため、ガラス、ス
テンレス、磁製のラシヒリングなどを、必要に応じて充
填した加熱管に、気化させた化1の蒸気をそのまま或い
は窒素などの不活性ガスで希釈した状態で通すなどの方
法が用いられる。分解物は、水冷することで粗ビニルオ
キサゾリンを凝縮させ、もう一方のシクロペンタジエン
は、アセトン−ドライアイス浴で回収される。粗ビニル
オキサゾリンの重合を抑えるために、ハイドロキノン、
p−メトキシフェノール、フェノチアジン、4−t−ブ
チルピロカテコールなどの重合禁止剤を加えることが好
ましい。また熱分解時、気相の重合防止のために、クペ
ロン(N−ニトロソフェニルヒドロキシルアミン)、酸
化窒素などを利用することもできる。
The thermal decomposition of the oxazolyl norbornene derivative represented by Chemical formula 1 is desirably performed in a gas phase at about 200 to 500 ° C. To facilitate heat exchange, glass, stainless steel, porcelain Raschig rings or the like are filled as necessary in a heating tube, and the vaporized chemical vapor as it is or diluted with an inert gas such as nitrogen. A method such as passing through is used. The decomposed product is cooled with water to condense the crude vinyl oxazoline, and the other cyclopentadiene is recovered in an acetone-dry ice bath. Hydroquinone, to suppress the polymerization of crude vinyl oxazoline,
It is preferred to add a polymerization inhibitor such as p-methoxyphenol, phenothiazine, 4-t-butylpyrocatechol. In addition, at the time of thermal decomposition, cuperone (N-nitrosophenylhydroxylamine), nitric oxide, or the like can be used to prevent polymerization in the gas phase.

【0018】粗ビニルオキサゾリンは、シクロペンタジ
エン、ビニルオキサゾリンおよび未反応原料以外の副生
物をほとんど含まないので、これらの沸点差を利用し
て、簡単な蒸留で高純度のビニルオキサゾリンを得るこ
とが可能である。
Since crude vinyl oxazoline contains almost no by-products other than cyclopentadiene, vinyl oxazoline and unreacted raw materials, it is possible to obtain high-purity vinyl oxazoline by simple distillation by utilizing the difference in boiling points. It is.

【0019】[0019]

【実施例】以下実施例を挙げて本発明を更に詳細に説明
する。 実施例1 エステル付加体の製造 攪拌装置、温度計、滴下装置を備えた3000mlの三
つ口フラスコに、アクリル酸メチル1300gを仕込
み、これにシクロペンタジエン1000gを攪拌しなが
ら徐々に滴下した。その間、反応混合物の温度は35℃
以下に保った。滴下終了後、35℃以下で反応混合物を
一晩攪拌した。未反応物および副生したジシクロペンタ
ジエンを減圧蒸留により回収してエステル付加体225
7gを得た。収率は98%であった。
The present invention will be described in more detail with reference to the following examples. Example 1 Production of Ester Adduct In a 3000 ml three-necked flask equipped with a stirrer, a thermometer, and a dropping device, 1300 g of methyl acrylate was charged, and 1000 g of cyclopentadiene was gradually added dropwise with stirring. Meanwhile, the temperature of the reaction mixture was 35 ° C.
Kept below. After the addition was completed, the reaction mixture was stirred at 35 ° C. or lower overnight. The unreacted product and the by-produced dicyclopentadiene were recovered by distillation under reduced pressure to obtain the ester adduct 225.
7 g were obtained. The yield was 98%.

【0020】アミド付加体の製造 前記同様の反応装置に、エステル付加体2200g、2
−アミノエタノール1060g、ナトリウムメチラート
30%溶液52gを仕込み、60℃で6h反応した。そ
の後副生したメタノールを減圧蒸留で回収し反応を完結
した。反応液を、加えたナトリウムメチラートと当量の
濃硫酸で中和した後、過剰のアミノエタノールを蒸留回
収してアミド付加体2490gを得た。収率は95%で
あった。
Preparation of amide adduct In a similar reactor, 2200 g of ester adduct, 2
1060 g of aminoethanol and 52 g of a 30% sodium methylate solution were charged and reacted at 60 ° C. for 6 hours. Thereafter, by-product methanol was recovered by distillation under reduced pressure to complete the reaction. After the reaction solution was neutralized with the added sodium methylate and an equivalent amount of concentrated sulfuric acid, excess aminoethanol was recovered by distillation to obtain 2490 g of an amide adduct. The yield was 95%.

【0021】アミド付加体の脱水 攪拌機と蒸留塔を備えた反応器に、アミド付加体200
0g、ポリプロピレングリコール2000g、塩基性炭
酸亜鉛200g、重合防止剤としてMHQ4gを仕込
み、2mmHg減圧下マントルヒーターで160〜19
0℃に加熱、脱水してオキサゾリルノルボルネン126
0gを得た。収率は70%であった。
Dehydration of amide adduct The amide adduct 200 was placed in a reactor equipped with a stirrer and a distillation column.
0 g, 2000 g of polypropylene glycol, 200 g of basic zinc carbonate, and 4 g of MHQ as a polymerization inhibitor, and 160 to 19 with a mantle heater under reduced pressure of 2 mmHg.
Oxazolyl norbornene 126
0 g was obtained. The yield was 70%.

【0022】オキサゾリルノルボルネンの熱分解 オキサゾリルノルボルネン1200gを、60mmHg
の減圧下蒸発管で加熱気化させ、400〜420℃に加
熱したステンレス製熱分解管(内径21.4mm、長さ
600mm)に通すことにより熱分解を行った。運転時
間は約12時間であった。熱分解による生成物は、約5
0℃に保った凝縮器と、−60℃に冷却した凝縮器とで
トラップし、前者より粗ビニルオキサゾリン696gを
得、後者よりシクロペンタジエン479gを得た。オキ
サゾリルノルボルネン熱分解率96.9%、ビニルオキ
サゾリン収率は88%であった。
Thermal decomposition of oxazolyl norbornene 1200 g of oxazolyl norbornene was converted to 60 mmHg
Was heated and vaporized with an evaporating tube under reduced pressure, and passed through a stainless steel pyrolysis tube (inner diameter 21.4 mm, length 600 mm) heated to 400 to 420 ° C. to perform pyrolysis. The running time was about 12 hours. The product of pyrolysis is about 5
The mixture was trapped by a condenser kept at 0 ° C. and a condenser cooled to −60 ° C., to obtain 696 g of crude vinyloxazoline from the former, and 479 g of cyclopentadiene from the latter. The oxazolyl norbornene thermal decomposition rate was 96.9%, and the vinyl oxazoline yield was 88%.

【0023】次いで粗ビニルオキサゾリンを、マクマホ
ンパッキングを20cm充填した精留塔を通して減圧下
単蒸留した(沸点 50℃/25mmHg)。結果、純
度99%以上の留分460g(蒸留収率94%)を得
た。 総合収率は54%であった。
Next, the crude vinyl oxazoline was subjected to simple distillation under reduced pressure through a rectification column packed with 20 cm of McMahon packing (boiling point: 50 ° C./25 mmHg). As a result, 460 g of a fraction having a purity of 99% or more (distillation yield: 94%) was obtained. The overall yield was 54%.

【0024】実施例2 実施例1において、アクリル酸メチルの代わりにメタク
リル酸メチルを原料として、同様に各工程の反応を行っ
た結果、イソプロペニルオキサゾリンを総合収率51%
で得た。純度は99%以上であった。
Example 2 In Example 1, methyl methacrylate was used as a raw material instead of methyl acrylate, and the reaction in each step was carried out in the same manner. As a result, isopropenyl oxazoline was converted to a total yield of 51%.
I got it. Purity was over 99%.

【0025】[0025]

【発明の効果】シクロペンタジエンと(メタ)アクリル
酸エステルとのディールスアルダー付加体を、アミノエ
タノールでアミド化した後、脱水して得られるオキサゾ
リルノルボルネン誘導体を、気相熱分解することによ
り、ビニルオキサゾリン誘導体を、副生物がほとんどな
く、高収率で製造することができた。
The oxazolyl norbornene derivative obtained by amidating a Diels-Alder adduct of cyclopentadiene and (meth) acrylic acid ester with aminoethanol and then dehydrating the resultant is subjected to gas phase thermal decomposition. The vinyl oxazoline derivative could be produced in high yield with almost no by-products.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 シクロペンタジエンと(メタ)アクリル
酸エステルとのディールスアルダー付加体をアミノエタ
ノールでアミド化した後、脱水して得られる化1で示さ
れるオキサゾリルノルボルネン誘導体を熱分解すること
を特徴とする化2で示されるビニルオキサゾリンまたは
イソプロペニルオキサゾリン誘導体の製造法。 【化1】 (但し、式中R1 は水素またはメチル基を表し、R2
〜R5は水素、アルキル基またはアリール基を表す。) 【化2】 (但し、式中R1 は水素またはメチル基を表し、R2
〜R5 は水素、アルキル基またはアリール基を表
す。)
1. A method comprising subjecting a Diels-Alder adduct of cyclopentadiene and (meth) acrylic acid ester to amidation with aminoethanol, followed by dehydration to thermally decompose the oxazolylnorbornene derivative represented by Chemical Formula 1. A process for producing a vinyl oxazoline or isopropenyl oxazoline derivative represented by Chemical Formula 2. Embedded image (Wherein, R1 represents hydrogen or a methyl group;
To R5 represent hydrogen, an alkyl group or an aryl group. ) (Wherein, R1 represents hydrogen or a methyl group;
To R5 represent hydrogen, an alkyl group or an aryl group. )
JP23493999A 1999-08-23 1999-08-23 Method for producing vinyl oxazoline or isopropenyl oxazoline derivative Expired - Lifetime JP4379965B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23493999A JP4379965B2 (en) 1999-08-23 1999-08-23 Method for producing vinyl oxazoline or isopropenyl oxazoline derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23493999A JP4379965B2 (en) 1999-08-23 1999-08-23 Method for producing vinyl oxazoline or isopropenyl oxazoline derivative

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JP2001058986A true JP2001058986A (en) 2001-03-06
JP4379965B2 JP4379965B2 (en) 2009-12-09

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Country Link
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JP4379965B2 (en) 2009-12-09

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