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JPS6281378A - Acrylate compound and production thereof - Google Patents

Acrylate compound and production thereof

Info

Publication number
JPS6281378A
JPS6281378A JP22159985A JP22159985A JPS6281378A JP S6281378 A JPS6281378 A JP S6281378A JP 22159985 A JP22159985 A JP 22159985A JP 22159985 A JP22159985 A JP 22159985A JP S6281378 A JPS6281378 A JP S6281378A
Authority
JP
Japan
Prior art keywords
meth
acrylate
acid
acrylic acid
formula
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
JP22159985A
Other languages
Japanese (ja)
Other versions
JPH0629277B2 (en
Inventor
Yasuhiro Okamoto
康弘 岡本
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.)
Sanyo Kokusaku Pulp Co Ltd
Original Assignee
Sanyo Kokusaku Pulp 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 Sanyo Kokusaku Pulp Co Ltd filed Critical Sanyo Kokusaku Pulp Co Ltd
Priority to JP22159985A priority Critical patent/JPH0629277B2/en
Publication of JPS6281378A publication Critical patent/JPS6281378A/en
Publication of JPH0629277B2 publication Critical patent/JPH0629277B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

NEW MATERIAL:A (meth)acrylate compound shown by the formula (R is H or CH3). EXAMPLE:Epoxydicyclopentenyloxyethyl acrylate. USE:Useful as a raw material or improver for ink, coating compounds, adhesives, coating agents and molding resins, showing low viscosity, low smell and solubility in a wide range of resins. PREPARATION:Dicyclopentadiene is reacted with ethylene glycol in the presence of an acidic catalyst such as sulfuric acid, p-toluenesulfonic acid, trifluoroboric acid, etc., at 100-120 deg.C to give an adduct of dicyclopentadiene with ethylene glycol. Then, the adduct is reacted with (meth)acrylic acid or (meth)acrylic acid derivative and epoxidized with an organic peracid, to give a compound shown by the formula.

Description

【発明の詳細な説明】 A、産業上の利用分野 本発明は、下記一般式(I)で表わされる新規な(メタ
)アクリレート化合物およびその製造法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a novel (meth)acrylate compound represented by the following general formula (I) and a method for producing the same.

(式中、RはHまたはCH3を表わす)(I)式で表わ
される化合物は、熱、紫外線、イオン化放射線、ラジカ
ル重合開始剤の存在下で容易に単独重合または他の不飽
和基含有化合物と共重合を行なうことができる。
(In the formula, R represents H or CH3) The compound represented by formula (I) is easily homopolymerized or combined with other unsaturated group-containing compounds in the presence of heat, ultraviolet rays, ionizing radiation, or a radical polymerization initiator. Copolymerization can be carried out.

B、従来の技術 従来より各種のアクリル酸エステル類が知られている。B. Conventional technology Various acrylic esters have been known so far.

例えばメタクリル酸メチル、アクリル酸エチル、アクリ
ル12−エヂルヘキシル等の単官能上ツマ−およびトリ
メヂロールプロパントリアクリレート、トリメチロール
プロパントリメタクリレート、ペンタエリスリトールト
リアクリレート等の多官能上ツマ−が一般的に知られて
いる。
For example, monofunctional polymers such as methyl methacrylate, ethyl acrylate, and 12-edylhexyl acrylate, and polyfunctional polymers such as trimedylolpropane triacrylate, trimethylolpropane trimethacrylate, and pentaerythritol triacrylate are generally known. It is being

C0発明が解決しようとする問題点 しかしながら、上記のうち単官能上ツマ−は、印刷イン
キおよび塗料に用いた場合には、硬化後の未反応モノマ
ーの臭気がはなはだしく問題となる。また多官能上ツマ
−は、塗料および印刷インキの希釈剤として用いる場合
には、樹脂に対して多量に使用する必要があり、したが
って樹脂のもつ特性が失われるという欠点を有している
Problems to be Solved by the C0 Invention However, among the above monofunctional additives, when used in printing inks and paints, the odor of unreacted monomers after curing poses a significant problem. Furthermore, when polyfunctional additives are used as diluents for paints and printing inks, they have to be used in large amounts relative to the resin, and therefore have the disadvantage that the properties of the resin are lost.

D1問題を解決するための手段、作用および効果本発明
者らは、鋭意研究の結果、低粘度かつ低臭気で広範囲に
わたる樹脂への溶解性を有する新規な(メタ)アクリル
酸エステルを得るに至った。このものは、インキ、塗料
、接着剤、被覆剤、成型用樹脂の原料あるいは改質剤と
して有用である。
Means, action, and effect for solving the D1 problem As a result of intensive research, the present inventors have obtained a novel (meth)acrylic acid ester that has low viscosity, low odor, and solubility in a wide range of resins. Ta. This product is useful as a raw material or modifier for inks, paints, adhesives, coatings, and molding resins.

本発明の化合物(I)は、例えば以下の方法で製造する
ことかできる。
Compound (I) of the present invention can be produced, for example, by the following method.

ジシクロペンタジェンとエチレングリコールをWL酸、
p−トルエンスルホン酸、三フッ化ホウ素等の酸性触媒
下に100〜120 ’Cで5〜8時間反応させるとジ
シクロペンタジェンのエチレングリコール付加物が得ら
れる。この付加物を(メタ)アクリル酸または(メタ)
アクリル酸誘導体とエステル化することによってジシク
ロペンテニルオキシエチル(メタ)アクリレートを得る
ことができる。
Dicyclopentadiene and ethylene glycol as WL acid,
When the reaction is carried out at 100 to 120'C for 5 to 8 hours under an acidic catalyst such as p-toluenesulfonic acid or boron trifluoride, an ethylene glycol adduct of dicyclopentadiene is obtained. This adduct is (meth)acrylic acid or (meth)
Dicyclopentenyloxyethyl (meth)acrylate can be obtained by esterification with an acrylic acid derivative.

(メタ)アクリル酸を用いてエステル化を行なう場合に
は、触媒としてIia酸、p−トルエンスルホン酸等の
酸性触媒を用いるとよい。また反応工程で用いる重合禁
止剤としてはハイドロキノン、ハイドロキノンモノメチ
ルエーテル、塩化第1銅などのアルカリ水溶液による洗
浄で容易に除去できるものが望ましい。
When carrying out esterification using (meth)acrylic acid, it is preferable to use an acidic catalyst such as Iia acid or p-toluenesulfonic acid. The polymerization inhibitor used in the reaction step is preferably one that can be easily removed by washing with an alkaline aqueous solution, such as hydroquinone, hydroquinone monomethyl ether, or cuprous chloride.

エステル化反応によって生成する水を系外へ取り出すた
めに用いる共沸溶媒としてはベンゼン、トルエン、キシ
レン、n−ヘキサン、メチルイソブチルケトン等の水と
共沸混合物をつくり、実質的にには水と互いに混合しな
い有機溶媒の単独または混合物が使用し得る。
Azeotropic solvents used to remove water produced by the esterification reaction from the system include benzene, toluene, xylene, n-hexane, methyl isobutyl ketone, etc., which form an azeotropic mixture with water, and are essentially Single or mixtures of mutually immiscible organic solvents can be used.

また(メタ)アクリル酸誘導体例えば、(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、(メタ)アクリル酸ロープロピル、(メ
タ)アクリル酸イソプロピル等の(メタ)アクリル酸エ
ステル化合物を用いて、エステル交換反応によってジシ
クロペンテニルオキシエチル(メタ)アクリレートを製
造することも可能である。
Also, (meth)acrylic acid derivatives such as methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate, rhopropyl (meth)acrylate, isopropyl (meth)acrylate, etc. It is also possible to produce dicyclopentenyloxyethyl (meth)acrylate by transesterification using an acid ester compound.

この場合における重合禁止剤としてはエステル交換反応
の触媒として硫酸あるいはパラトルエンスルホン酸を用
いる場合にはハイドロキノン、ハイドロキノンモノメチ
ルエーテル等を使用するが、金属ナトリウム、ナトリウ
ムアルコラードなどアルカリ性の触媒を用いるときには
、アルカリ性の重合禁止剤例えばパラフェニレンジアミ
ン、フェニル−β−ナフチルアミンが使用される。生成
する当該低級アルコールを一部の(メタ)アクリル酸エ
ステル化合物と共に系外へ取り出すことによってエステ
ル交換反応は促進される。
In this case, the polymerization inhibitor used is hydroquinone, hydroquinone monomethyl ether, etc. when sulfuric acid or para-toluenesulfonic acid is used as a catalyst for the transesterification reaction, but when an alkaline catalyst such as sodium metal or sodium alcoholade is used, Alkaline polymerization inhibitors such as paraphenylenediamine and phenyl-β-naphthylamine are used. The transesterification reaction is promoted by taking out the generated lower alcohol out of the system together with a part of the (meth)acrylic acid ester compound.

このようにして、得られたジシクロペンテニルオキシエ
チル(メタ)アクリレートをギ酸、酢酸、プロピオン酸
、ブチル酸、コハク酸、アジピン酸、安息香酸等と過酸
化水素を用いて調製した有機過酸によってエポキシ化を
行なうと化合物(I)が得られる。
In this way, the obtained dicyclopentenyloxyethyl (meth)acrylate is treated with an organic peracid prepared using formic acid, acetic acid, propionic acid, butyric acid, succinic acid, adipic acid, benzoic acid, etc. and hydrogen peroxide. Compound (I) is obtained by epoxidation.

ジシクロペンテニルオキシエチル(メタ)アクリレート
と有機過酸の配合比は、ジシクロペンテニルオキシエチ
ル(メタ)アクリレートに対して、0.2〜2倍モル好
ましくは、0.5〜1倍モルである。
The mixing ratio of dicyclopentenyloxyethyl (meth)acrylate and organic peracid is 0.2 to 2 moles, preferably 0.5 to 1 mole, relative to dicyclopentenyloxyethyl (meth)acrylate. .

エポキシ化反応において、重合禁止剤としてハイドロキ
ノン、ハイドロキノンモノメチルエーテル、t−ブチル
カテコール 等を100〜i 、 000ppm添加するのがよい。
In the epoxidation reaction, 100 to 1,000 ppm of hydroquinone, hydroquinone monomethyl ether, t-butylcatechol, or the like is preferably added as a polymerization inhibitor.

E.実施例 以下、本発明を実施例によって説明する。E. Example Hereinafter, the present invention will be explained by examples.

(実施例1〕 ■ジシクロペンテニルオキシエタノールの製造エチレン
グリコール1249、三フッ化ホウ素エチルエーテルコ
ンプレックス5.7gを反応容器に仕込み、100℃に
昇温し、同温を保ちながらジシクロペンタジェン132
gを5時間かけて滴下した。滴下終了後2時間反応を続
けてジシクロペンタジェンを消失させた。反応物を室温
まで冷却し、15Nのアンモニア水溶液2.7mlをゆ
っくり添加して三フッ化ホウ素エチルエーテルコンプレ
ックスの中和を行なった。得られた反応物をn−ヘキサ
ンに抽出して水洗を行なった後ロータリーエバポレータ
ーでn−ヘキサン除去してジシクロペンテニルオキシエ
タノール1699を得た。
(Example 1) ■ Production of dicyclopentenyloxyethanol Ethylene glycol 1249 and 5.7 g of boron trifluoride ethyl ether complex were charged into a reaction vessel, heated to 100°C, and while maintaining the same temperature, dicyclopentadiene 132
g was added dropwise over 5 hours. After the completion of the dropwise addition, the reaction was continued for 2 hours to eliminate dicyclopentadiene. The reaction mixture was cooled to room temperature, and 2.7 ml of 15N aqueous ammonia solution was slowly added to neutralize the boron trifluoride ethyl ether complex. The obtained reaction product was extracted with n-hexane, washed with water, and then n-hexane was removed using a rotary evaporator to obtain dicyclopentenyloxyethanol 1699.

■ジシクロペンテニルオキシエチルアクリレ−1−の製
造 このようにして得られたジシクロペンテニルオキシエタ
ノール1949とアクリル酸79.2SF、触媒として
1)−1〜ルエンスルホン酸2.7g、重合禁止剤とし
てハイドロキノン七ツメチルエーテル0゜8gおよびト
ルエン200rrI!!を還流冷却器、水分離器、撹拌
器を備えた反応容器に仕込み、撹拌しながらトルエン還
流温度で5時間加熱した。留出したトルエン−水留分は
水分離器において水を分離した俊、トルエンは連続的に
反応器へ返却した。水が留出しなくなるまで反応を続け
た。この間に得られた水は18gであった。
■Production of dicyclopentenyloxyethyl acrylate-1- Dicyclopentenyloxyethanol 1949 thus obtained and 79.2 SF of acrylic acid, 1)-1 to 2.7 g of luenesulfonic acid as a catalyst, and a polymerization inhibitor. 0.8 g of hydroquinone methyl ether and 200 rr of toluene! ! was charged into a reaction vessel equipped with a reflux condenser, a water separator, and a stirrer, and heated at toluene reflux temperature for 5 hours while stirring. Water was separated from the distilled toluene-water fraction in a water separator, and the toluene was continuously returned to the reactor. The reaction was continued until no water was distilled out. 18 g of water was obtained during this time.

反応後室温まで冷却し、飽和炭酸ナトリウム水溶液50
0dで2回洗浄し、ついで飽和食塩水によってアルカリ
性を示さなくなるまで洗浄を繰返した。このものに1.
1′ −ビー2−ナフトール2.59を加え、減圧蒸留
を行なって、沸点が132〜b ペンテニルオキシエチルアクリレート171gを得た。
After the reaction, cool to room temperature and add 50% saturated aqueous sodium carbonate solution.
Washing was carried out twice at 0 d, and then washing was repeated with saturated saline until alkalinity was no longer exhibited. This one has 1.
2.59 g of 1'-bi-2-naphthol was added and distilled under reduced pressure to obtain 171 g of pentenyloxyethyl acrylate having a boiling point of 132-b.

■エポキシジシクロペンテニルオキシエチルアクリレー
トの製造 このようにして得られたジシクロペンテニルオキシエチ
ルアクリレート248gと酢112g、35%過酸化水
素水58gを反応容器に仕込み60℃で2時間反応した
。反応後、室温まで冷却し、酸性を示さなくなるまで飽
和食塩水で洗浄を繰返した。このものに1.1′ −ビ
ー2−ナフトール3gを加え、減圧蒸留を行なって沸点
が132〜135°C/lmHgの留分である未反応の
ジシクロペンテニルオキシエチルアクリレート・122
Uと沸点が、135〜140’C/ 1 rrunト1
9の留分である化合物(1)中のエポキシジシクロペン
テニルオキシエチルアクリレート121gを得た。この
ものの赤外吸収スペクトルおよび核磁気共鳴スペク1〜
ルをそれぞれ表1および表2に示す。
(2) Production of epoxy dicyclopentenyloxyethyl acrylate 248 g of dicyclopentenyloxyethyl acrylate thus obtained, 112 g of vinegar, and 58 g of 35% hydrogen peroxide were charged into a reaction vessel and reacted at 60°C for 2 hours. After the reaction, the mixture was cooled to room temperature and washed repeatedly with saturated brine until it no longer showed acidity. Add 3 g of 1.1'-bi-2-naphthol to this and perform vacuum distillation to obtain unreacted dicyclopentenyloxyethyl acrylate 122 with a boiling point of 132-135°C/lmHg.
U and boiling point are 135-140'C/1 rrunt1
121 g of epoxy dicyclopentenyloxyethyl acrylate in compound (1), which is a fraction of No. 9, was obtained. Infrared absorption spectrum and nuclear magnetic resonance spectrum of this product 1~
Tables 1 and 2 show the results, respectively.

(実施例2) 実施例1の■ジシクロペンテニルオキシエタノールの製
造で得られたジシクロペンテニルオキシエタノール19
4gとアクリル酸メチル2589、触媒としてテトラブ
チルヂタネ−1−109、重合禁止剤としてフェノチア
ジン0.3gを分留頭を備えたヴイグリュー型冷却管、
底部より窒素ガスを吹き込めるように毛細管をつけた反
応容器に仕込み、留出液が毎分数滴留出するように還流
を続ける。
(Example 2) Dicyclopentenyloxyethanol 19 obtained in the production of dicyclopentenyloxyethanol in Example 1
4 g and methyl acrylate 2589, tetrabutylditane-1-109 as a catalyst, and 0.3 g of phenothiazine as a polymerization inhibitor in a Vigreux type cooling tube equipped with a fractionating head.
The mixture is placed in a reaction vessel equipped with a capillary tube so that nitrogen gas can be blown into it from the bottom, and reflux is continued so that several drops of distillate are distilled out every minute.

8時間反応後、反応液の減圧蒸留を行なって沸点が13
2〜b シクロペンテニルオキシエチルアクリレート164gを
得た。
After 8 hours of reaction, the reaction solution was distilled under reduced pressure and the boiling point was 13.
2-b 164 g of cyclopentenyloxyethyl acrylate was obtained.

以下、実施例1の■エポキシジシクロペンテニルオキシ
エチルアクリレートの製造と同様にして化合物(I>中
のエポキシジシクロペンテニルオキシエチルアクリレー
トをjqた。
Thereafter, epoxy dicyclopentenyloxyethyl acrylate in compound (I>) was prepared in the same manner as in Example 1 (1) Production of epoxy dicyclopentenyloxyethyl acrylate.

〔実施例3〕 アクリル酸72.99をメタアクリル194.6gとす
る以外は、実施例1の■ジシクロペンテニルオキシエチ
ルアクリレートの製造と同様にして沸点が133〜b シクロペンテニルオキシエチルメタアクリレート173
gを2+9だ。
[Example 3] Cyclopentenyloxyethyl methacrylate 173 with a boiling point of 133-b was prepared in the same manner as in Example 1, except that 194.6 g of methacrylic acid was used instead of 72.99 g of acrylic acid.
G is 2+9.

このようにして得られたジシクロペンテニルオキシエチ
ルメタアクリレート262gを実施例1の■エポキシジ
シクロペンテニルオキシエチルアクリレートの製造と同
様にして、沸点が135〜b (I>中のエポキシジシクロペンテニルオキシエチルメ
タアクリレート142gを得た。このものの赤外吸収ス
ペクトルおよび核磁気共鳴スペクトルをそれぞれ表1お
よび表2に示す。
262 g of dicyclopentenyloxyethyl methacrylate thus obtained was treated in the same manner as in Example 1 (1) for the production of epoxydicyclopentenyloxyethyl acrylate, and the boiling point was 135-b (epoxydicyclopentenyloxy in I> 142 g of ethyl methacrylate was obtained.The infrared absorption spectrum and nuclear magnetic resonance spectrum of this product are shown in Tables 1 and 2, respectively.

〔実施例4〕 アクリル酸メチル258gをメタアクリル酸メチル30
0 gとする以外は、実施例2と同様にして沸点が13
3〜b ジシクロペンテニルオキシエチルメタアクリレート16
2gを得た。
[Example 4] 258 g of methyl acrylate was mixed with 30 g of methyl methacrylate.
The boiling point was 13 in the same manner as in Example 2 except that the amount was 0 g.
3-b dicyclopentenyloxyethyl methacrylate 16
2g was obtained.

以下、実施例1の■エポキシジシクロペンテニルオキシ
エチルアクリレートの製造と同様にして、化合物(I>
中のエポキシジシクロペンテニルオキシエチルメタアク
リレートを得た。
Hereinafter, the compound (I>
Epoxy dicyclopentenyloxyethyl methacrylate was obtained.

表1.赤外吸収スペクトル(液膜) *1・・・エポキシジシクロペ、ンテニルオキシエチル
アクリレート *2・・・エポキシジシクロペンテニルオキシエチルメ
タアクリレート 表2.核磁気共鳴スペク1〜ル(’3 C−NHR,C
DC,e3)表2つづき 手続ネ市正書 (自 発) 昭和61年2月18E1 特許庁長官 宇買)百alK  鴨 川L 1、事イ1の表示 昭和60年 特許願 第221599号2、デを明の名
称 アクリレート化合物およびその製造法 3、補正をする者 事件との関係 特許出願人 住  所   東京都千代田区丸の内1−4−5名  
称   (234>山陽国策パルプ株式会社4、代理人 住  所   東京都千代田区神田北乗物町16番地〒
101    英 ヒル3階 5、補正の対象 明細用の発明の詳細な説明の項 補正の内容 (1)明細古第13頁の表2中の式を下記の如く訂rF
Table 1. Infrared absorption spectrum (liquid film) *1... Epoxy dicyclopene, lentenyloxyethyl acrylate *2... Epoxy dicyclopentenyloxyethyl methacrylate Table 2. Nuclear magnetic resonance spectra 1~ ('3 C-NHR, C
DC, e3) Table 2 continued Procedure Ne City official letter (self-proposal) February 18, 1985 18E1 Commissioner of the Patent Office Ubuya) 100 alK Kamogawa L 1, Indication of fact A 1 1985 Patent application No. 221599 2, De Name of acrylate compound and its manufacturing method 3, relationship with the case of the person making the amendment Patent applicant address: 1-4-5 Marunouchi, Chiyoda-ku, Tokyo
Name (234> Sanyo Kokusaku Pulp Co., Ltd. 4, Agent Address: 16 Kanda Kita Jorimono-cho, Chiyoda-ku, Tokyo)
101 English Hill 3rd floor 5, Detailed description of the invention for the specification to be amended Contents of the amendment (1) The formula in Table 2 on page 13 of the old specification was revised as follows rF
.

)k (2)明細黒第14頁の表2つづき中の式を下記の如く
訂正。
)k (2) The formula in Table 2 continued on page 14 of the specification black was corrected as follows.

Claims (2)

【特許請求の範囲】[Claims] (1)下記の一般式( I )で表わされる(メタ)アク
リレート化合物。 ▲数式、化学式、表等があります▼( I ) (式中、RはHまたはCH_3を表わす)
(1) A (meth)acrylate compound represented by the following general formula (I). ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) (In the formula, R represents H or CH_3)
(2)ジシクロペンタジエンにエチレングリコールを付
加させ、その付加物と(メタ)アクリル酸または、(メ
タ)アクリル酸誘導体を反応させた後、有機過酸により
エポキシ化を行なうことを特徴とする下記の一般式(
I )で表わされる(メタ)アクリレート化合物の製造法
。 ▲数式、化学式、表等があります▼( I ) (式中、RはHまたはCH_3を表わす)
(2) The following method characterized by adding ethylene glycol to dicyclopentadiene, reacting the adduct with (meth)acrylic acid or a (meth)acrylic acid derivative, and then epoxidizing with an organic peracid. The general formula for (
A method for producing a (meth)acrylate compound represented by I). ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) (In the formula, R represents H or CH_3)
JP22159985A 1985-10-04 1985-10-04 Acrylate compound and method for producing the same Expired - Fee Related JPH0629277B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22159985A JPH0629277B2 (en) 1985-10-04 1985-10-04 Acrylate compound and method for producing the same

Publications (2)

Publication Number Publication Date
JPS6281378A true JPS6281378A (en) 1987-04-14
JPH0629277B2 JPH0629277B2 (en) 1994-04-20

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2656304A1 (en) * 1989-12-22 1991-06-28 Norsolor Sa PROCESS FOR THE SELECTIVE EPOXIDATION OF UNIFORMAL (METH) ACRYLIC (B) NITROGENIC ACRYLIC (METH) ACRYLIC COMPOUNDS OBTAINED.
EP0468840A2 (en) * 1990-07-06 1992-01-29 Elf Atochem S.A. Process for the selective epoxidation of unsaturated (meth)acrylates, new functional (meth)acrylates so obtained and their use in the synthesis of new polymers
WO2001019888A1 (en) * 1999-09-10 2001-03-22 Sartomer Company, Inc. Coating composition and method of coating substrates
WO2006035683A1 (en) * 2004-09-27 2006-04-06 Hitachi Chemical Co., Ltd. Photocurable resin composition
JP2006117897A (en) * 2004-09-27 2006-05-11 Hitachi Chem Co Ltd Photocurable resin composition for coating or adhesive
WO2006059564A1 (en) * 2004-11-30 2006-06-08 Daicel Chemical Industries, Ltd. Alicyclic epoxy (meth)acrylates, process for production thereof, and copolymers
JP2006151900A (en) * 2004-11-30 2006-06-15 Daicel Chem Ind Ltd Cycloaliphatic epoxy (meth)acrylate and its preparation method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2656304A1 (en) * 1989-12-22 1991-06-28 Norsolor Sa PROCESS FOR THE SELECTIVE EPOXIDATION OF UNIFORMAL (METH) ACRYLIC (B) NITROGENIC ACRYLIC (METH) ACRYLIC COMPOUNDS OBTAINED.
EP0468840A2 (en) * 1990-07-06 1992-01-29 Elf Atochem S.A. Process for the selective epoxidation of unsaturated (meth)acrylates, new functional (meth)acrylates so obtained and their use in the synthesis of new polymers
US5283360A (en) * 1990-07-06 1994-02-01 Atochem Selective epoxidation of unsaturated (meth)acrylates, new functional (meth)acrylates, and polymers thereof
WO2001019888A1 (en) * 1999-09-10 2001-03-22 Sartomer Company, Inc. Coating composition and method of coating substrates
WO2006035683A1 (en) * 2004-09-27 2006-04-06 Hitachi Chemical Co., Ltd. Photocurable resin composition
JP2006117897A (en) * 2004-09-27 2006-05-11 Hitachi Chem Co Ltd Photocurable resin composition for coating or adhesive
WO2006059564A1 (en) * 2004-11-30 2006-06-08 Daicel Chemical Industries, Ltd. Alicyclic epoxy (meth)acrylates, process for production thereof, and copolymers
JP2006151900A (en) * 2004-11-30 2006-06-15 Daicel Chem Ind Ltd Cycloaliphatic epoxy (meth)acrylate and its preparation method

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