JPS6289719A - Novel vinyl ester resin and production thereof - Google Patents
Novel vinyl ester resin and production thereofInfo
- Publication number
- JPS6289719A JPS6289719A JP22916485A JP22916485A JPS6289719A JP S6289719 A JPS6289719 A JP S6289719A JP 22916485 A JP22916485 A JP 22916485A JP 22916485 A JP22916485 A JP 22916485A JP S6289719 A JPS6289719 A JP S6289719A
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- Japan
- Prior art keywords
- resin
- vinyl ester
- acid
- ester resin
- 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.)
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Epoxy Resins (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ビニル単量体に溶解させ、その硬化体物か高
い耐熱性、可撓性を有する新規ビニルエステル樹脂およ
びその製造法に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a novel vinyl ester resin which is dissolved in vinyl monomer and whose cured product has high heat resistance and flexibility, and a method for producing the same. It is.
(従来の技術および発明か解決すべき問題点)近年、エ
ポキシ樹脂と不飽和−塩基酸との反応物をスチレンのよ
うな重合性単量体に溶解した不飽和エポキシエステル樹
脂(ビニルエステル樹脂)が、エポキシ樹脂の性能と不
飽和ポリエステル樹脂の作業性や硬化性の良さを兼ね陥
えたものとして着実に市場に利用されつつある。(Prior art and problems to be solved by the invention) In recent years, unsaturated epoxy ester resins (vinyl ester resins) are produced by dissolving a reaction product of an epoxy resin and an unsaturated basic acid in a polymerizable monomer such as styrene. However, it is steadily being used in the market as a product that combines the performance of epoxy resin with the workability and curing properties of unsaturated polyester resin.
かかるビニルエステル樹脂の使用分野は、不飽和ポリエ
ステル樹脂と同様に、耐蝕性強化プラスチック材、ライ
ニング材、被覆材、含浸材、接盾剤、注型材など広範囲
に及んでいる。Similar to unsaturated polyester resins, such vinyl ester resins are used in a wide range of fields, including corrosion-resistant reinforced plastic materials, lining materials, coating materials, impregnating materials, enclosing agents, and casting materials.
また、このビニルエステル樹脂は、エステル溝成部分で
あるエポキシ化合物の種類や重合度の異なったものを選
ぶことにより、あるいはこれらをブレンドすることによ
り多種多様な性能を持たせることができる。Furthermore, this vinyl ester resin can be made to have a wide variety of performances by selecting epoxy compounds with different types and degrees of polymerization as the ester groove component, or by blending these.
上記ビニルエステル樹脂は、エポキシ化合物のエポキシ
基を、アクリル酸、メタクリル酸等のような不飽和−塩
基酸のカルボキシル基で開環し、エステル化してエポキ
シエルテルを生成する反応により装)貴される。最も一
般的なビニルエステル樹脂に用いられるエポキシ樹脂と
しては、ビスフェノールAのジグリシジルエーテル型の
ものか用いられる。The above-mentioned vinyl ester resin is made by ring-opening the epoxy group of an epoxy compound with the carboxyl group of an unsaturated basic acid such as acrylic acid, methacrylic acid, etc., and esterifying it to produce epoxy ertel. . The most common epoxy resin used for vinyl ester resins is the diglycidyl ether type of bisphenol A.
しかし、これらヒスフェノールAのジグリシジルエーテ
ル型のエポキシを原料としたビニルエステル樹脂は、耐
酸性、耐アルカリ性においては、一般の不飽和ポリエス
テル樹脂より飛躍的に高い性能を持つものの、その熱変
形温度はたかだか110’C程度であって高温での使用
は著しく制限される。However, although these vinyl ester resins made from diglycidyl ether type epoxy of hisphenol A have significantly higher acid resistance and alkali resistance than general unsaturated polyester resins, their heat distortion temperature The temperature is about 110'C at most, and its use at high temperatures is severely restricted.
また、従来市販されているノボラック骨格を有するエポ
キシアクリレート樹脂は、フェノール化合物とポルマリ
ンとを反応させて冑だノボラックに、エピクロルヒドリ
ンを反応させて次式(III)で示されるノボラック型
エポキシ樹脂(式中RはHまたはCH3であり、nはO
〜10の整数を示す。〕
を1す、これとアクリル酸および/またはメタクリル酸
とをスチレン、メタクリル酸メチル等のビニル性単量体
の溶媒の存在下に反応させて樹脂のビニル単量体溶液と
して製造されている。In addition, conventionally commercially available epoxy acrylate resins having a novolac skeleton are produced by reacting a phenolic compound with a polymerine to form a solid novolac, and then reacting epichlorohydrin with a novolac type epoxy resin represented by the following formula (III) (in the formula R is H or CH3, n is O
Indicates an integer between ~10. ] This is reacted with acrylic acid and/or methacrylic acid in the presence of a vinyl monomer solvent such as styrene or methyl methacrylate to produce a resin vinyl monomer solution.
このノボラック骨格を有するエポキシアクリレート樹脂
(ビニルエステル樹脂)は次式(1v〕で示される。This epoxy acrylate resin (vinyl ester resin) having a novolac skeleton is represented by the following formula (1v).
(IV)
〔式中RはHまたはCH3であり、EXACは、CH3
であり、nはO〜10の整数を示す。〕しかしこのノボ
ラック骨格を有するエポキシアクリレート樹脂もその熱
変形温度の点で十分満足できるものではない。(IV) [In the formula, R is H or CH3, and EXAC is CH3
, n represents an integer of 0 to 10. ] However, this epoxy acrylate resin having a novolak skeleton is also not fully satisfactory in terms of its heat distortion temperature.
本発明はこれらの問題点を解消するためになされたもの
で、本発明は下記一般式(1)(式中Rはメチル基また
は水素原子、nはO〜15の整数を示す。)
で示される新規ビニルエステル樹脂およびその製造法を
提供したものである。The present invention has been made to solve these problems, and is represented by the following general formula (1) (wherein R is a methyl group or a hydrogen atom, and n is an integer from O to 15). The present invention provides a new vinyl ester resin and a method for producing the same.
本発明の上記一般式CI)で示される新規ビニルエステ
ル樹脂はビニル単量体に溶解させ、その硬化物が高い耐
熱性、可撓性を有していることを特徴としている。The novel vinyl ester resin of the present invention represented by the above general formula CI) is characterized in that it is dissolved in a vinyl monomer and the cured product thereof has high heat resistance and flexibility.
又本発明の一般式〔工)で示される新規ビニルエステル
樹脂は下記一般式(n)
(n)
(式中Rはメチル基または水素原子、nはO〜15の整
数を示す。〕
て示されるジシクロペンタジェン変性エポキシ樹脂にア
クリル酸またはアクリル酸の反応性誘導体を反応させる
ことにより得られる。The novel vinyl ester resin of the present invention represented by the general formula [Eng. It is obtained by reacting a dicyclopentadiene-modified epoxy resin with acrylic acid or a reactive derivative of acrylic acid.
本発明において上記一般式(II)で示されるジシクロ
ペンタジェン変性エポキシ樹脂は、ジシクロペンタジェ
ンとフェノール類(フェノール、オルソクレゾール、バ
ラクレゾール、イソプロピルフェノール等)をルイス酸
触媒中で重合させ、得られたジシクロペンタジェン変性
フェノール樹脂をエピクロルヒドリンと反応させて得る
ことができる。In the present invention, the dicyclopentadiene-modified epoxy resin represented by the above general formula (II) is produced by polymerizing dicyclopentadiene and phenols (phenol, orthocresol, valaclesol, isopropylphenol, etc.) in a Lewis acid catalyst. It can be obtained by reacting the obtained dicyclopentadiene-modified phenol resin with epichlorohydrin.
上記一般式(n)で示されるジシクロペンタジェン変性
エポキシ樹脂とアクリル酸とのエステル化反応は、エポ
キシ塁1当量当り、アクリル酸を0.5〜1.8当伍、
好ましくは0.7・〜1.1当岳の割合で混合し、エス
テル化触媒の存在下に70〜180’C好ましくは90
〜130’Cの温度で、得られる樹脂の酸価が1〜16
となるまで反応させることによって好適に製造すること
ができる。In the esterification reaction between the dicyclopentadiene-modified epoxy resin represented by the above general formula (n) and acrylic acid, 0.5 to 1.8 equivalents of acrylic acid per equivalent of epoxy base,
Preferably, the mixture is mixed at a ratio of 0.7 to 1.1 degrees centigrade, and heated to 70 to 180'C, preferably 90 degrees centigrade, in the presence of an esterification catalyst.
At a temperature of ~130'C, the acid value of the resulting resin is 1-16.
It can be suitably produced by reacting until it becomes.
かかるエステル反応は、酸素あるいは空気雰囲気下で行
うことが望ましい。Such ester reaction is preferably carried out in an oxygen or air atmosphere.
一般に反応時間は2〜16時間、好ましくは4〜8時間
である。反応溶媒としては、エステル化反応を阻害しな
い溶媒であれば必要に応じ用いることが出来る。また溶
媒を留去することなく硬化体を得るには、生成゛uしめ
るビニルエステル樹脂と共重合可能なスチレン、ジビニ
ルベンゼン等のビニル単量体を溶媒に用いると好都合で
ある。Generally the reaction time is 2 to 16 hours, preferably 4 to 8 hours. As the reaction solvent, any solvent that does not inhibit the esterification reaction can be used as necessary. Further, in order to obtain a cured product without distilling off the solvent, it is convenient to use a vinyl monomer such as styrene or divinylbenzene which is copolymerizable with the vinyl ester resin to be produced.
アクリル酸を過量に使用することは、エポキシ樹脂との
エステル化反応速度を低下させるとともに得られる硬化
物の耐アルカリ性を著しく悪化させるので好ましくない
。 (また、アクリル酸の一部を飽和
−塩基酸、飽和二塩基酸あるいは不飽和二塩基酸で置き
かえてもよい。これらの酸は、使用する全酸成分に (
対して80重Φ%まで、好ましくは10〜60重量%の
量で用いるのがよい。上記アクリル酸の一部の代りに使
用しうる酸の例としては、プ (ロピオン酸、安息香酸
、フタル酸、テレフタル酸、テトラヒドロ無水フタル酸
、コハク酸、ア (ジビン酸、フマール酸、無水マレ
イン酸などが挙げられる。
(本発明に用いられるエステル化触媒としては
、例えば、
(1)N、N−ジメヂルアニリン、ピリジン、トリエチ
ルアミン、ヘキサメチレンジアミン等の3@アミン及び
その無IIM例えば塩酸の塩あるいは有機酸例えば酢酸
の塩。It is not preferable to use an excessive amount of acrylic acid because it reduces the rate of esterification reaction with the epoxy resin and significantly deteriorates the alkali resistance of the cured product obtained. (Also, a portion of the acrylic acid may be replaced by a saturated-basic acid, a saturated dibasic acid, or an unsaturated dibasic acid. These acids may be added to the total acid component used (
On the other hand, it is preferable to use up to 80% by weight, preferably 10 to 60% by weight. Examples of acids that can be used in place of some of the above acrylic acids include propionic acid, benzoic acid, phthalic acid, terephthalic acid, tetrahydrophthalic anhydride, succinic acid, divicic acid, fumaric acid, maleic anhydride. Examples include acids.
(Esterification catalysts used in the present invention include, for example, (1) 3@amines such as N,N-dimedylaniline, pyridine, triethylamine, hexamethylene diamine, etc. and their non-IIM salts, such as salts of hydrochloric acid, or salts of organic acids, such as acetic acid. .
(2)テトラメチルアンモニウムブロマイド、トリメチ
ルベンジルアンモニウムクロライド等の4扱アンモニウ
ム塩。(2) 4-treated ammonium salts such as tetramethylammonium bromide and trimethylbenzylammonium chloride.
3)パラトルエンスルホン酸、トリノエニルスルホニウ
ムクロライド等のスルホン酸及びスルホニウム塩類。3) Sulfonic acids and sulfonium salts such as para-toluenesulfonic acid and trinoenylsulfonium chloride.
4)トリメチルスルホニウムクロライド、ジメチルフェ
ニルスルホニウムクロライド等のスルホニウム塩。4) Sulfonium salts such as trimethylsulfonium chloride and dimethylphenylsulfonium chloride.
5)ホスホニウムアイオダイド等のホスホニウム塩。5) Phosphonium salts such as phosphonium iodide.
6)塩化リチウム、臭化リチウム、塩化第1スズ、塩化
亜鉛等の金属ハロゲン化物。6) Metal halides such as lithium chloride, lithium bromide, stannous chloride, and zinc chloride.
7)水酸化カリウム、水酸化リチウム等の全屈水酸化物
等。7) Total hydroxides such as potassium hydroxide and lithium hydroxide.
これらエステル化触媒の中でもテトラエチルアンモニウ
ムブロマイドが、他のものに比較し、ジシクロペンタジ
ェン変性エポキシ樹脂との相溶性に格段と優れ、速い反
応速度を与えると共に、かつ、高い反応率に到達させる
ことができるので好ましい。Among these esterification catalysts, tetraethylammonium bromide has much better compatibility with the dicyclopentadiene-modified epoxy resin than other catalysts, provides a fast reaction rate, and achieves a high reaction rate. This is preferable because it allows
これらエステル化触媒は、工゛ボキシ樹脂と酸成分の混
合物100重但1に対し、0.005〜3ff1m部の
割合で用いる。These esterification catalysts are used at a ratio of 0.005 to 3 ff/m parts per 100 parts by weight of the mixture of the ethylene oxide resin and the acid component.
また、エステル反応は手合禁止剤の存在下で行うことが
好ましく、かかる手合禁止剤としては、例えば、p−ハ
イドロキノン、ナフトキノン、ヘンゾキノン、ジターシ
ャリ−ブチルハイドロキシトルエン、ハイドロキノンモ
ノメチルエーテル、ターシャリ−ブチルカテコールなど
のモノまたは多価フェノール類や、キノン類が挙げられ
る。その使用量は、前記反応混合物100重吊重四対し
て約0.001〜1.0重量部、好ましくは0.005
〜0.5重量部である。Further, the ester reaction is preferably carried out in the presence of a hand reaction inhibitor, such as p-hydroquinone, naphthoquinone, henzoquinone, di-tert-butyl hydroxytoluene, hydroquinone monomethyl ether, tert-butyl catechol, etc. Examples include mono- or polyhydric phenols and quinones. The amount used is about 0.001 to 1.0 parts by weight, preferably 0.005 parts by weight, per 100 parts by weight of the reaction mixture.
~0.5 parts by weight.
本発明の実施により”A造されたビニルエステル樹脂は
重合開始剤の存在下に単独で硬化させることができるが
、このビニルエステル樹脂はこれと共手合可能なビニル
単量体に)容屏させて低粘度の液状物とした方が取扱い
が容易となる。According to the practice of the present invention, the vinyl ester resin produced by "A" can be cured alone in the presence of a polymerization initiator, but the vinyl ester resin can be bulked with a vinyl monomer that can be coproduced with the vinyl ester resin. It will be easier to handle if it is made into a low viscosity liquid.
この際、ビニル単量体は、ビニルエステル樹脂100重
量部に対し、30〜120重量部、好ましくは40〜8
0重量部の割合で用いる。At this time, the vinyl monomer is 30 to 120 parts by weight, preferably 40 to 8 parts by weight, based on 100 parts by weight of the vinyl ester resin.
It is used in a proportion of 0 parts by weight.
かかるビニル単量体の例としては、スチレン、メタアク
リレート、メチルメタクリレート、ビニルトルエン、り
[]]ロスヂレンビニルペンビン・、アクリロニ1へリ
ル、メタクリロニトリル、シクロペンタジェン、シヒニ
ルベンゼン、ビニルピリジン、酢酸ビニル、ジアクリル
フタレート、グリシジルメタアクリレートなどが挙げら
れ、これらは一種又はそれ以上を併用することもできる
。Examples of such vinyl monomers include styrene, methacrylate, methyl methacrylate, vinyltoluene, poly[]]rosdylene vinylpenvin, acrylonitrile, methacrylonitrile, cyclopentadiene, cyhynylbenzene, vinylpyridine. , vinyl acetate, diacrylphthalate, glycidyl methacrylate, etc., and one or more of these can also be used in combination.
反応終了後、ポリアクリレートの貧溶媒、例えば水を投
入することによりポリアクリレートを析出させ、溶媒よ
り分離する。After the reaction is completed, polyacrylate is precipitated by adding a poor solvent for polyacrylate, such as water, and separated from the solvent.
また、有機酸の貧溶媒てめってポリアクリレートの良)
8媒、例えばメチルイソブチルケトン、トルエン、キシ
レン、クロロホルム、メチルエチルケトン等を添加し、
ポリアクリレートを有機酸層よりこれらの溶媒層に移行
させ、有機酸層を分離後、これら溶媒を留去してポリア
クリレートを分離する。In addition, polyacrylate is a poor solvent for organic acids.)
8 medium, such as methyl isobutyl ketone, toluene, xylene, chloroform, methyl ethyl ketone, etc.
After the polyacrylate is transferred from the organic acid layer to these solvent layers and the organic acid layer is separated, these solvents are distilled off to separate the polyacrylate.
このようにして得たポリアクリレートはアセトン、トル
エン、クロロホルム、酢酸メチル等の0は溶媒またはメ
チルメタクリレート、スチレン等のビニル単樋体に重合
開始剤とともに)8屏され、塗料、プリプレグに使用さ
れる。The polyacrylate thus obtained is mixed with a polymerization initiator in a solvent such as acetone, toluene, chloroform, methyl acetate, or a vinyl monolayer such as methyl methacrylate or styrene, and used for paints and prepregs. .
そして、ビニル単量体により希釈されたビニルトルエン
の液状物は、液状の不飽和ポリエステル樹脂組成物と同
様に、例えばメチルエチルケトンパーオキサイド−コバ
ルト塩の組合せの申合開始剤の存在下で常温で硬化する
ことも可能であり、ベンゾイルバーオキ1ノ゛イドの様
な高温分解手合開始剤の添加によって高温硬化すること
も可能てめる。The vinyl toluene liquid diluted with the vinyl monomer is then cured at room temperature in the presence of an initiator such as a combination of methyl ethyl ketone peroxide and cobalt salt, similar to the liquid unsaturated polyester resin composition. It is also possible to cure at a high temperature by adding a high temperature decomposition initiator such as benzoyl peroxide.
(実施例) 以下に実施例を挙げて本発明を更に説明する。(Example) The present invention will be further explained with reference to Examples below.
実施例中、部及び%は特にことわらない限り重量による
。In the examples, parts and percentages are by weight unless otherwise specified.
実施例1
ジシクロペンタジェン変性エポキシ樹脂(DCE−40
0、エポキシ当ff1280g/eQ)500部、アク
リル酸150部、テトラメチルアンモニウムブロマイド
3.0部、ハイドロギン20.3部およびトルエン15
00部を撹拌翼及びコンデン[ナーを協えたフラスコ内
に仕込み、油溶上で100’Cに加熱し反応を行ったと
ころ3時間後に酸価がほとんど零となった。Example 1 Dicyclopentadiene modified epoxy resin (DCE-40
0, 500 parts of epoxy (ff1280g/eQ), 150 parts of acrylic acid, 3.0 parts of tetramethylammonium bromide, 20.3 parts of hydrogin, and 15 parts of toluene.
00 parts was placed in a flask equipped with a stirring blade and a condenser, and the reaction was carried out by heating to 100'C over an oil solution, and the acid value became almost zero after 3 hours.
この反応液に10%炭酸水素ナトリウム水溶液200d
、蒸溜zi1oooyを加え過剰のアクリル酸を除去し
、更に蒸溜水10100O!で3回抽出洗浄後、有機層
を分離し、有機溶媒を留去すると、目的とする新規ビニ
ルエステル樹脂593gを得た。分析結果を表1に示す
。Add 200 d of 10% sodium hydrogen carbonate aqueous solution to this reaction solution.
, add distilled zi1oooy to remove excess acrylic acid, and distilled water 10100O! After extraction and washing three times, the organic layer was separated and the organic solvent was distilled off to obtain 593 g of the desired new vinyl ester resin. The analysis results are shown in Table 1.
この反応生成物100部に対し、スヂレン54部を加え
、混合してガードナー色相が7〜8.25°Cにおける
粘度か3.5小イズの粘稠な溶液を得た。To 100 parts of this reaction product, 54 parts of styrene were added and mixed to obtain a viscous solution with a Gardner hue of 3.5 sq. viscosity at 7 to 8.25°C.
実施例2
実施例1で用いたエステル化触媒を1〜リエチルベンジ
ルアンモニウムブロマイド2.5部に変えた以外は同様
な条件で、目的樹脂を得た。Example 2 A target resin was obtained under the same conditions as in Example 1, except that the esterification catalyst used in Example 1 was changed to 1 to 2.5 parts of ethylbenzylammonium bromide.
その分析結果を表1に示した。The analysis results are shown in Table 1.
表−1 1〉溶媒 CHC,? 、λmax。Table-1 1>Solvent CHC,? , λmax.
2>KBr法 3)13C−NMR1溶tJjA CDC,e32>KBr method 3) 13C-NMR1 tJjA CDC, e3
第1図は本発明の実施例1のビニルエステル樹脂の赤外
吸収スペクトルを示す図表、第2図は同上の樹脂のGP
C(限外濾過クロマトグラフ)を示す図表、第3図は本
発明の実施例2のビニルエステル樹脂のGPCを示す図
表、第4図は本発明の核磁気共鳴スペクトルを示す図表
である。Figure 1 is a chart showing the infrared absorption spectrum of the vinyl ester resin of Example 1 of the present invention, and Figure 2 is a chart showing the GP of the same resin.
FIG. 3 is a chart showing GPC of the vinyl ester resin of Example 2 of the present invention, and FIG. 4 is a chart showing the nuclear magnetic resonance spectrum of the present invention.
Claims (1)
数を示す。〕 で示される新規ビニルエステル樹脂。 2)一般式〔II〕 ▲数式、化学式、表等があります▼〔II〕 〔式中Rはメチル基または水素原子、nは0〜15の整
数を示す。〕 で示されるジシクロペンタジエン変性エポキシ樹脂にア
クリル酸またはアクリル酸の反応性誘導体を反応させる
こを特徴とする下記一般式〔 I 〕で示される新規ビニ
ルエステル樹脂の製造法。 ▲数式、化学式、表等があります▼〔 I 〕 〔式中Rはメチル基または水素原子、nは0〜15の整
数を示す。〕[Claims] 1) The following general formula [I] ▲ Numerical formulas, chemical formulas, tables, etc. are available▼ [I] [In the formula, R represents a methyl group or a hydrogen atom, and n represents an integer from 0 to 15. ] A new vinyl ester resin. 2) General formula [II] ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [II] [In the formula, R represents a methyl group or a hydrogen atom, and n represents an integer from 0 to 15. ] A method for producing a novel vinyl ester resin represented by the following general formula [I], which comprises reacting a dicyclopentadiene-modified epoxy resin represented by the following with acrylic acid or a reactive derivative of acrylic acid. ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [I] [In the formula, R represents a methyl group or a hydrogen atom, and n represents an integer from 0 to 15. ]
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22916485A JPS6289719A (en) | 1985-10-15 | 1985-10-15 | Novel vinyl ester resin and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22916485A JPS6289719A (en) | 1985-10-15 | 1985-10-15 | Novel vinyl ester resin and production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6289719A true JPS6289719A (en) | 1987-04-24 |
JPS6320850B2 JPS6320850B2 (en) | 1988-04-30 |
Family
ID=16887787
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22916485A Granted JPS6289719A (en) | 1985-10-15 | 1985-10-15 | Novel vinyl ester resin and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6289719A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6485949A (en) * | 1987-06-15 | 1989-03-30 | Daikin Ind Ltd | Fluorine-containing alicyclic and aromatic cyclic compounds and production thereof |
EP1655309A1 (en) | 2004-11-09 | 2006-05-10 | Sumitomo Chemical Company, Limited | Process for stopping continuous polymerization |
WO2021230097A1 (en) * | 2020-05-12 | 2021-11-18 | 日鉄ケミカル&マテリアル株式会社 | Epoxy acrylate resin, alkali-soluble resin, resin composition including same, and cured product thereof |
JPWO2021235299A1 (en) * | 2020-05-19 | 2021-11-25 |
-
1985
- 1985-10-15 JP JP22916485A patent/JPS6289719A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6485949A (en) * | 1987-06-15 | 1989-03-30 | Daikin Ind Ltd | Fluorine-containing alicyclic and aromatic cyclic compounds and production thereof |
EP1655309A1 (en) | 2004-11-09 | 2006-05-10 | Sumitomo Chemical Company, Limited | Process for stopping continuous polymerization |
WO2021230097A1 (en) * | 2020-05-12 | 2021-11-18 | 日鉄ケミカル&マテリアル株式会社 | Epoxy acrylate resin, alkali-soluble resin, resin composition including same, and cured product thereof |
JPWO2021230097A1 (en) * | 2020-05-12 | 2021-11-18 | ||
JPWO2021235299A1 (en) * | 2020-05-19 | 2021-11-25 | ||
WO2021235299A1 (en) * | 2020-05-19 | 2021-11-25 | 日鉄ケミカル&マテリアル株式会社 | Polymerizable-unsaturated-group-containing alkali-soluble resin, method for producing same, photosensive resin composition, and cured product thereof |
Also Published As
Publication number | Publication date |
---|---|
JPS6320850B2 (en) | 1988-04-30 |
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