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JPS591273B2 - ether methacrylic sun ester - Google Patents
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JPS591273B2 - ether methacrylic sun ester - Google Patents

ether methacrylic sun ester

Info

Publication number
JPS591273B2
JPS591273B2 JP50129844A JP12984475A JPS591273B2 JP S591273 B2 JPS591273 B2 JP S591273B2 JP 50129844 A JP50129844 A JP 50129844A JP 12984475 A JP12984475 A JP 12984475A JP S591273 B2 JPS591273 B2 JP S591273B2
Authority
JP
Japan
Prior art keywords
compound
tables
ester
formulas
represents hydrogen
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.)
Expired
Application number
JP50129844A
Other languages
Japanese (ja)
Other versions
JPS5253850A (en
Inventor
宣人 高橋
正人 野中
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.)
Kojin Co Ltd
Original Assignee
Kojin 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 Kojin Co Ltd filed Critical Kojin Co Ltd
Priority to JP50129844A priority Critical patent/JPS591273B2/en
Publication of JPS5253850A publication Critical patent/JPS5253850A/en
Publication of JPS591273B2 publication Critical patent/JPS591273B2/en
Expired legal-status Critical Current

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  • Furan Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 本発明は一般式 R、 CH2■ムCOOCH2−V(■) (但し式中R1は水素又はメチル基を表わす。[Detailed description of the invention] The present invention is based on the general formula R, CH2■muCOOCH2-V(■) (However, in the formula, R1 represents hydrogen or a methyl group.

)で示されるエーテル基を含有したアクリル酸エステル
及びメタクリル酸エステルの製造方法に関するものであ
る。エーテル基を含有するアクリル酸エステル及びメタ
クリル酸エステルは塗料、架橋剤等幅広い用途を有する
有用なモノマーである。
) The present invention relates to a method for producing acrylic esters and methacrylic esters containing an ether group as shown in the following. Acrylic esters and methacrylic esters containing ether groups are useful monomers that have a wide range of uses such as paints and crosslinking agents.

これらの化合物は従来アクリル酸、メタクリル酸及びそ
のメチルエステルと式 HOCH2ク で表わされるアルコールとの脱水縮合エステル化反応、
あるいはエステル交換反応により製造されている。
These compounds are conventionally produced by dehydration condensation and esterification reactions of acrylic acid, methacrylic acid, and their methyl esters with alcohols represented by the formula HOCH2,
Alternatively, it is produced by transesterification.

しかるにこの従来法では活性な二重結合をそのままにし
て反応を行なう為、常に重合の危険性が伴なう。しかも
、本発明で使用されるエーテル基を含有するアルコール
類は、空気中の酸素により自動酸化を受け易く、その結
果、過酸化物を生成するといわれ、その為、エーテル基
を含有しないアクリル酸エステル、メタクリル酸エステ
ルと比べても更に、重合、着色等の問題をおこし易い。
However, in this conventional method, since the reaction is carried out with active double bonds intact, there is always a risk of polymerization. Moreover, the alcohols containing ether groups used in the present invention are said to be susceptible to autooxidation by oxygen in the air, and as a result, produce peroxides. Even compared to methacrylic acid esters, they are more likely to cause problems such as polymerization and coloring.

この問題を解決する為、種々の酸化防止剤、重合禁止剤
等を使用した特許が数多く出ているが、重合を完全に防
止するまでには到つていず、かなりのモノマーが重合物
として無駄に消費され、産業廃棄物となり、工程上のト
ラブルの原因となつている。本発明者等はこれらの問題
を解決する方法について鋭意検討を加えた結果、本発明
の完成に到つた。即ち、本発明の特徴は下記に示すよう
に化合物(I)を熱分解する事により化合楢■)を得る
事にある。(但し式中R,は水素又はメチル基を表わす
。)化合糎I)を熱分解する事によつて得られる生成物
は驚くべき事に、化合物(■)及びシクロペンタジエン
の2種類のみで製品及び工程に悪い影響を及ぼす何らの
副生物も得られない。しかも化合物(■)とシクロペン
タジエンは常圧で100℃以上の沸点の差を有する為、
蒸留による分離が極めて容易で、しかも高純度の化合糎
■)を得る事ができる。また、シクロペンタジエンは回
収し、何度でも再使用が可能であり、資源の節約も可能
である。更に詳しく本発明を説明する。本発明で原料と
して用いられる化合画I)は通常の方法により極めて容
易にかつ収率良く合成される。
In order to solve this problem, many patents have been published using various antioxidants, polymerization inhibitors, etc., but this has not yet reached the point where polymerization is completely prevented, and a considerable amount of monomer is wasted as polymerized products. It is consumed by many people, becomes industrial waste, and causes problems in the process. The inventors of the present invention have conducted extensive studies on methods to solve these problems, and as a result, have completed the present invention. That is, the feature of the present invention is that compound (I) is obtained by thermally decomposing compound (I) as shown below. (However, in the formula, R represents hydrogen or a methyl group.) Surprisingly, the product obtained by thermally decomposing compound starch I) consists of only two types, compound (■) and cyclopentadiene. and no by-products are obtained that adversely affect the process. Moreover, since compound (■) and cyclopentadiene have a boiling point difference of more than 100°C at normal pressure,
Separation by distillation is extremely easy, and it is possible to obtain a highly pure compound starch. In addition, cyclopentadiene can be recovered and reused any number of times, making it possible to save resources. The present invention will be explained in more detail. Compound I) used as a raw material in the present invention can be synthesized extremely easily and with high yield by a conventional method.

即ち、アクリル酸メチル又はメタクリル酸メチルとシク
ロペンタジエンとをDiel s−Alder反応せし
め、アクリル酸メチル又はメタクリル酸メチルの二重結
合を保護する。その際必要ならば、べンゼン、トルエン
、メタ/−ル、クロロホルム等の汎用有機溶媒の使用並
びに触媒として硫酸、塩酸、塩化アルミニウム、等の使
用、ハイドロキノン、カテコール等の重合禁止剤の添加
も有効である。
That is, methyl acrylate or methyl methacrylate and cyclopentadiene are subjected to a Diel s-Alder reaction to protect the double bond of methyl acrylate or methyl methacrylate. If necessary, it is also effective to use general-purpose organic solvents such as benzene, toluene, methanol, and chloroform, use sulfuric acid, hydrochloric acid, aluminum chloride, etc. as catalysts, and add polymerization inhibitors such as hydroquinone and catechol. It is.

上記Diels−Alder反応により得られた、一般
式(但し、R1は水素又はメチル基を表わす)で表わさ
れる化合物mは触媒存在下化合物(自);テトラハイド
ロフルフリルアルコールとエステル交換反応せしめるこ
とにより、容易に化合物(I)を85%以上の収率で得
る事ができる。
The compound m represented by the general formula (where R1 represents hydrogen or a methyl group) obtained by the above Diels-Alder reaction is transesterified with tetrahydrofurfuryl alcohol in the presence of a catalyst. , Compound (I) can be easily obtained in a yield of 85% or more.

触媒としてNaOCH3,NaOC2H5,Na0H等
の塩基触媒を化合物Dに対して1〜2 Omol%好ま
しくは3〜1 Omol%使用するのが良い。必要なら
ば系内を減圧にしてメタノールの留去を促進せしめ、反
応を進行させる事も有効である。この反応も何ら副反応
がおこらず、しかも生成撫1)と未反応原料町,(9の
沸点にかなりの差がある為、原料債),(匍の回収、生
成物(I)の精製が極めて容易である。本発明の特徴で
ある化合蝋I)の熱分解は、温度200℃〜500℃の
範囲内で気相或いは液相で行なわれる。熱分解生成物(
…)は、すみやかに反応系外にとり出され、急冷される
As a catalyst, it is preferable to use a base catalyst such as NaOCH3, NaOC2H5, NaOH, etc. in an amount of 1 to 2 Omol%, preferably 3 to 1 Omol%, based on Compound D. If necessary, it is also effective to reduce the pressure in the system to promote distillation of methanol and advance the reaction. This reaction also does not cause any side reactions, and furthermore, there is a considerable difference in the boiling points of the product (1) and the unreacted raw material (9), so the recovery of the raw material and the purification of the product (I) are difficult. The thermal decomposition of compound wax I), which is a feature of the present invention, is carried out in the gas phase or liquid phase at a temperature in the range of 200°C to 500°C. Pyrolysis products (
) is immediately taken out of the reaction system and rapidly cooled.

その滞留時間は高々数秒であり、従つて重合の可能性も
ほとんどない。
The residence time is at most a few seconds, so there is little possibility of polymerization.

ι気相で熱分解される場合、気化された化合物(I)
は、200゜C〜500℃に加熱された管の中に導かれ
、極めて短時間で熱分解される。
ιWhen thermally decomposed in the gas phase, the vaporized compound (I)
is introduced into a tube heated to 200°C to 500°C and is thermally decomposed in an extremely short time.

熱分解管は熱交換を容易にする為に必要に応じてガラス
、ステンレス、磁製のラツシヒリングを充填する。また
、窒素などの不活性ガスで、気化した化合物(I)を希
釈する事も有効である。液相で行なわれる楊合、化合f
!ff!!jl)を沸点以上にそのまま加熱するか、熱
安定性の高い不活性流体、例えばターフエニル、バラフ
イン等を所要の温度まで加熱した容器に化合撫I)を導
入し、熱分解を行なわしめ、生成物を生成と同時に留出
させるという方法が用いられる。
The pyrolysis tube is filled with glass, stainless steel, or porcelain Raschig rings as necessary to facilitate heat exchange. It is also effective to dilute the vaporized compound (I) with an inert gas such as nitrogen. Yang combination carried out in the liquid phase, compound f
! ff! ! Jl) is directly heated above its boiling point, or compound I) is introduced into a container in which a highly thermally stable inert fluid such as terphenyl, varafine, etc. has been heated to the required temperature, thermal decomposition is carried out, and the product is A method is used in which the gas is distilled off at the same time as it is produced.

その際、不活性流体中に、ハイドロキノン、カテコール
等の重合禁止剤を入れておくと分解生成物の重合防止上
好都合である。熱分解生成物である化合恒1)とシクロ
ペンタジエンはその沸点差が大である為、容易に分解さ
れ、純粋な化合物()を得る事ができる。上記の様にエ
ステル化反応及びエステル交換反応は活性な二重結合を
シクロペンタジエンにより保護してから行なわれ、又、
本発明の特徴である熱分解は極めて短時間で行なわれる
為、重合等の副反応は全くおこらない。しかも未反応原
料及びシクロペンタジエンは回収し、リサイクルして何
度でも使用可能である為、収率が良いのみならず、ほと
んど廃棄物を出さない製造工程が可能である。
At this time, it is convenient to include a polymerization inhibitor such as hydroquinone or catechol in the inert fluid in order to prevent polymerization of decomposition products. Since the thermal decomposition product Compound 1) and cyclopentadiene have a large difference in boiling point, they are easily decomposed and pure compound () can be obtained. As mentioned above, the esterification reaction and the transesterification reaction are carried out after protecting the active double bond with cyclopentadiene, and
Since the thermal decomposition, which is a feature of the present invention, is carried out in an extremely short time, side reactions such as polymerization do not occur at all. Furthermore, unreacted raw materials and cyclopentadiene can be recovered, recycled, and used any number of times, so that not only is the yield high, but a manufacturing process that produces almost no waste is possible.

以下実施例を挙げて本発明を具体的に説明する。The present invention will be specifically explained below with reference to Examples.

実施例テトラハイドロフルフリルアクリレートの製造(
イ) 5−ノルボルネン−2−カルボン酸メチルエステ
ルの製造還流冷却器、温度計、撹拌後、滴下ロードを付
けた500m1フラスコにアクリル酸メチル1729を
入れ、温度を40℃に調節しながらシクロペンタジエン
1329を滴下反応させ、5−ノルボルネン−2−カル
ボン酸メチルエステルを定量的に得た。
Example Production of tetrahydrofurfuryl acrylate (
b) Production of 5-norbornene-2-carboxylic acid methyl ester After stirring using a reflux condenser, thermometer, and stirring, put methyl acrylate 1729 into a 500 ml flask equipped with a dropping load, and add cyclopentadiene 1329 while adjusting the temperature to 40°C. was reacted dropwise to quantitatively obtain 5-norbornene-2-carboxylic acid methyl ester.

→ 5−ノルボルネン−2−カルボン酸テトラハイドロ
フルフリルエステルの製造5−ノルボルネン−2−カル
ボン酸メチルエステル152g、テトラハイドロフルフ
リルアルコール102θ触媒としてナトリウムメチラー
ト1629を110とC〜115℃で加熱攪拌しながら
系内を減圧にし、生成メタノールを順次留去して反応を
進行させた。
→ Production of 5-norbornene-2-carboxylic acid tetrahydrofurfuryl ester 152 g of 5-norbornene-2-carboxylic acid methyl ester, tetrahydrofurfuryl alcohol 10 Sodium methylate 1629 as a 2θ catalyst was heated and stirred at 110°C to 115°C. While doing so, the pressure inside the system was reduced, and the methanol produced was successively distilled off to allow the reaction to proceed.

反応後、硫酸1.479で中和した後、減圧蒸留(13
0〜1357C/5mmHg)により、5−ノルボルネ
ン−2−カルボン酸−テトラハイドロフルフリルエステ
ル200gを得た。
After the reaction, it was neutralized with 1.479 sulfuric acid, and then distilled under reduced pressure (13
0 to 1357 C/5 mmHg) to obtain 200 g of 5-norbornene-2-carboxylic acid-tetrahydrofurfuryl ester.

′→ テトラハイドロフルフリルアクリレートの製造圧
力10m7!LHgで、5−ノルボルネン−2−カルボ
ン酸テトラハイドロフルフリルエステル2229を加熱
蒸発させ、450℃に加熱したパイレツクスガラス製熱
分解管に通してテトラハイドロフルフリルアクリレート
(Bp92ラC/20m77!Hg)1489とシクロ
ペンタジエン62,89未分解原料1069を得た。
'→ Production pressure of tetrahydrofurfuryl acrylate 10m7! 5-Norbornene-2-carboxylic acid tetrahydrofurfuryl ester 2229 was heated and evaporated at LHg, and passed through a Pyrex glass pyrolysis tube heated to 450°C to obtain tetrahydrofurfuryl acrylate (Bp92C/20m77!Hg). ) 1489 and cyclopentadiene 62,89 undecomposed raw material 1069 were obtained.

Claims (1)

【特許請求の範囲】 1 一般式 ▲数式、化学式、表等があります▼( I )(但し、式
中R_1は水素又はメチル基を表わす。 )で示される化合物( I )を熱分解する事を特徴とす
る一般式▲数式、化学式、表等があります▼(II)(但
し、式中R_1は水素又はメチル基を表わす。 )で示されるエーテル基を含有するアクリル酸エステル
、またはメタクリル酸エステルの製造方法。2 化合物
( I )が、化合物(IV)とテトラハイドロフルフリル
アルコール(III)とのエステル交換反応により得られ
るものである特許請求の範囲第1項のエーテル基を含有
するアクリル酸エステルまたはメタクリル酸エステルの
製造方法。 ▲数式、化学式、表等があります▼(III)▲数式、化
学式、表等があります▼(IV)(但し、R_1は水素又
はメチル基を表わす。 )
[Claims] 1. A method for thermally decomposing a compound (I) represented by the general formula ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (I) (in the formula, R_1 represents hydrogen or a methyl group). Characteristic general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (II) (However, R_1 in the formula represents hydrogen or methyl group.) Acrylic ester or methacrylic ester containing an ether group Production method. 2. Acrylic acid ester or methacrylic acid containing an ether group according to claim 1, wherein compound (I) is obtained by transesterification reaction between compound (IV) and tetrahydrofurfuryl alcohol (III). Method for producing esters. ▲There are mathematical formulas, chemical formulas, tables, etc.▼(III) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(IV) (However, R_1 represents hydrogen or a methyl group.)
JP50129844A 1975-10-29 1975-10-29 ether methacrylic sun ester Expired JPS591273B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50129844A JPS591273B2 (en) 1975-10-29 1975-10-29 ether methacrylic sun ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50129844A JPS591273B2 (en) 1975-10-29 1975-10-29 ether methacrylic sun ester

Publications (2)

Publication Number Publication Date
JPS5253850A JPS5253850A (en) 1977-04-30
JPS591273B2 true JPS591273B2 (en) 1984-01-11

Family

ID=15019622

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50129844A Expired JPS591273B2 (en) 1975-10-29 1975-10-29 ether methacrylic sun ester

Country Status (1)

Country Link
JP (1) JPS591273B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5529976B2 (en) * 1972-09-08 1980-08-07
JPS5050313A (en) * 1973-09-07 1975-05-06

Also Published As

Publication number Publication date
JPS5253850A (en) 1977-04-30

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