JPS62195002A - Production of curable resin - Google Patents

Production of curable resin

Info

Publication number
JPS62195002A
JPS62195002A JP3695986A JP3695986A JPS62195002A JP S62195002 A JPS62195002 A JP S62195002A JP 3695986 A JP3695986 A JP 3695986A JP 3695986 A JP3695986 A JP 3695986A JP S62195002 A JPS62195002 A JP S62195002A
Authority
JP
Japan
Prior art keywords
acid anhydride
unsaturated
reaction
alcohol
copolymer
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.)
Pending
Application number
JP3695986A
Other languages
Japanese (ja)
Inventor
Noboru Suzuki
昇 鈴木
Nobuyuki Nagato
伸幸 永戸
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Denko KK filed Critical Showa Denko KK
Priority to JP3695986A priority Critical patent/JPS62195002A/en
Publication of JPS62195002A publication Critical patent/JPS62195002A/en
Pending legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

PURPOSE:To obtain the titled beautiful resin which causes no gelatinization in production process and has high transparency, by subjecting a partial esterified copolymer of an unsaturated acid anhydride and a vinyl compound to specific treatment and reacting the treated partially esterified copolymer with an unsaturated epoxy compound. CONSTITUTION:Firstly, an alpha, beta-unsaturated acid anhydride is copolymerized with a vinyl compound (preferably styrene) copolymerizable with it and the copolymer is esterified with >=3C monohydric alcohol such as propyl alcohol, etc., preferably at 40-100 deg.C. An unreacted acid anhydride group of the partially esterified polymer is esterified with an aliphatic monohydric alcohol such as methyl alcohol, etc., and a free carboxyl group of the polymer is reacted with an unsaturated epoxy compound such as glycidyl methacrylate, etc., preferably at 40-90 deg.C for 3-20hr to give the aimed resin.

Description

【発明の詳細な説明】 (産業上の利用分野〕 本発明は硬化性樹脂の製造方法に関し、さらに詳しくは
主鎖がビニル七ツマ−の重合によって得られたポリマー
からなり、かつ側鎖に炭素−炭素二重結合を右づる硬化
性樹脂の製造方法に関する。
Detailed Description of the Invention (Industrial Field of Application) The present invention relates to a method for producing a curable resin, and more specifically, the present invention relates to a method for producing a curable resin, and more specifically, the main chain is composed of a polymer obtained by polymerizing vinyl heptamer, and the side chain contains carbon atoms. -Regarding a method for producing a curable resin in which carbon double bonds are corrected.

〔従来の技術〕[Conventional technology]

側鎖に炭素−炭素二重結合を有するタイプの硬化性樹脂
は、主鎖に炭素−炭素二重結合およびエステル結合を有
づる不飽和ポリエステル樹脂のような硬化性樹脂と比べ
て、物性上優れた性能を有するため、その用途が各方面
に拡大しつつある。
Curable resins with carbon-carbon double bonds in their side chains have superior physical properties compared to curable resins such as unsaturated polyester resins, which have carbon-carbon double bonds and ester bonds in their main chains. Because of its excellent performance, its applications are expanding in various fields.

上記側鎖に炭素−炭素二重結合を有するタイプの硬化性
樹脂は、一般に炭素−炭素二重結合を有する化合物を主
鎖と反応させることによって製造されている。
The above-mentioned curable resin having a carbon-carbon double bond in the side chain is generally produced by reacting a compound having a carbon-carbon double bond with the main chain.

例えば、α、β−不飽和酸無水物と、これと共重合可能
なビニル化合物とを重合させた共重合体の酸無水物基を
アリルアルコール、2−ヒドロキシエヂルメタクリレ−
1〜、2−ヒドロキシエヂルアクリレ−1・のどとき不
飽和アル:1−ルによってエステル化した後、遊1tl
ltのカルボキシル基とアリルグリシジルエーテル、グ
リシジルメタクリレート、グリシジルアクリレートのご
とき不飽和エボキシ化合物とを反応させることによって
、側鎖に炭素−炭素二重結合を有する樹脂を製造するこ
とができる。
For example, the acid anhydride group of a copolymer obtained by polymerizing an α,β-unsaturated acid anhydride and a vinyl compound that can be copolymerized with the same is combined with allyl alcohol, 2-hydroxyethyl methacrylate, etc.
After esterification with 1-,2-hydroxyedyl acrylate-1, unsaturated alkyl, free 1 tl
A resin having a carbon-carbon double bond in the side chain can be produced by reacting the carboxyl group of lt with an unsaturated epoxy compound such as allyl glycidyl ether, glycidyl methacrylate, or glycidyl acrylate.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、上記方法は、遊離のカルボキシル基と不飽和エ
ポキシ化合物とを反応させる工程において、エポキシ化
合物の反応率が高くなると樹脂のゲル化が起り、成形不
能の固まりが生成する。また、樹脂のゲル化が起こらな
いようにするため、不飽和エポキシ化合物の反応率を抑
制すると、遊離のカルボキシル基の反応率が充分に上が
らないため、性能のよい樹脂が得られない。
However, in the above method, in the step of reacting a free carboxyl group with an unsaturated epoxy compound, when the reaction rate of the epoxy compound becomes high, gelation of the resin occurs and an unmoldable lump is formed. Furthermore, if the reaction rate of the unsaturated epoxy compound is suppressed in order to prevent gelation of the resin, the reaction rate of free carboxyl groups will not increase sufficiently, making it impossible to obtain a resin with good performance.

本発明者等は上記の事情に鑑み、不飽和エポキシ化合物
の反応率を高めてもゲル化の起こらない方法を鋭意研究
した結果、主鎖中に残存する酸無水物基がゲル化の原因
となっていることを発見した。
In view of the above circumstances, the present inventors conducted extensive research on a method that does not cause gelation even if the reaction rate of the unsaturated epoxy compound is increased, and as a result, they found that the acid anhydride group remaining in the main chain is the cause of gelation. I discovered that it is.

本発明は上記の発見に基づいて行なわれたもので、主鎖
がビニル重合体でかつ側鎖に炭素−炭素二重結合を有す
る硬化性樹脂を、ゲル化が発生することなく製造するこ
とが出来る硬化性樹脂の製造方法を捉供することを目的
とする。
The present invention was made based on the above discovery, and it is possible to produce a curable resin having a vinyl polymer main chain and a carbon-carbon double bond in the side chain without gelation. The purpose of this research is to provide a method for producing curable resins.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記の目的を達成するためになされたもので、
その要旨は、α、β−不飽和不飽和物無水物れに共重合
可能なビニル化合物とからなる共重合体の酸無水物基を
炭素数3以上の飽和または不飽和一価アルコールで部分
エステル化して得られるポリマーの遊薗のカルボキシル
基と不飽和エポキシ化合物とを反応させる硬化性樹脂の
製造方法において、上記部分エステル化ポリマーの遊離
のカルボキシル基と不飽和エポキシ化合物とを反応させ
る前に上記部分エステル化ポリマーを炭素数1または2
の脂肪族一価アルコールでエステル化することを特徴と
する硬化性樹脂の製造方法にある。
The present invention has been made to achieve the above objects,
The gist is that the acid anhydride group of a copolymer consisting of α, β-unsaturated unsaturated anhydride and a copolymerizable vinyl compound is partially esterified with a saturated or unsaturated monohydric alcohol having 3 or more carbon atoms. In the method for producing a curable resin in which the free carboxyl groups of the polymer obtained by esterification are reacted with an unsaturated epoxy compound, before the free carboxyl groups of the partially esterified polymer are reacted with the unsaturated epoxy compound, the above-mentioned Partially esterified polymer with 1 or 2 carbon atoms
A method for producing a curable resin, which comprises esterifying the resin with an aliphatic monohydric alcohol.

〔発明の具体的構成および作用〕[Specific structure and operation of the invention]

以十、本発明の詳細な説明する。 Hereinafter, the present invention will be explained in detail.

本発明において、α、β−、β−酸無水物とビニル化合
物との共重合体を@I造するために使用されるα、β−
、β−酸無水物としては、例えば無水マレイン酸、シ1
−ラコン酸無水物、無水2−エヂルマレイン酸、無水2
−、フェニルマレイン酸。
In the present invention, the α,β-
, As the β-acid anhydride, for example, maleic anhydride,
-laconic anhydride, 2-edylmaleic anhydride, anhydride 2
-, phenylmaleic acid.

無水2−クロロマレイン酸等があげられる。Examples include 2-chloromaleic anhydride.

また、α、β〜不飽和酸無水物と共重合させるビニル化
合物どしては、α、β−、β−酸無水物と共重合可能で
あればいずれも使用出来、2種以上併用してもよい。ビ
ニル化合物の代表例としては、例えばスチレン、α−メ
ヂルスチレン、アクリル酸エステル類、メタクリル酸エ
ステル類、酢酸ビニル、アクリロニトリル、塩化ビニル
等があげられるが、これらのうちでも特にスチレンが好
ましい。
In addition, as for the vinyl compound to be copolymerized with α, β-unsaturated acid anhydride, any one can be used as long as it can be copolymerized with α, β-, β-acid anhydride, and two or more types can be used in combination. Good too. Typical examples of vinyl compounds include styrene, α-methylstyrene, acrylic esters, methacrylic esters, vinyl acetate, acrylonitrile, vinyl chloride, etc. Among these, styrene is particularly preferred.

上記α、β−、β−酸無水物とビニル化合物との共重合
の際の比率は、目的とする樹脂の性能に合わせて、適宜
変化させることが出来る。
The ratio of the above α, β-, β-acid anhydride and vinyl compound during copolymerization can be changed as appropriate depending on the desired performance of the resin.

α、β−、β−酸無水物とビニル化合物との共重合体は
、従来公知の方法で製造することができるが、酸無水物
基が共重合体中に均一に分散し、かつ反応制御を容易に
するためには、ビニル化合物へα、β−、β−酸無水物
を添加して反応させることが好ましい。
A copolymer of α, β-, β-acid anhydride and a vinyl compound can be produced by a conventionally known method. In order to facilitate the reaction, it is preferable to add an α, β-, β-acid anhydride to the vinyl compound and cause the reaction to occur.

また、α、β−、β−酸無水物とビニル化合物との共重
合体の酸無水物基と反応させる炭素数3以上の飽和また
は不飽和一価アルコールとしては、例えばプロピルアル
コール、ブチルアルコール。
Examples of the saturated or unsaturated monohydric alcohol having 3 or more carbon atoms to be reacted with the acid anhydride group of the copolymer of α, β-, β-acid anhydride and vinyl compound include propyl alcohol and butyl alcohol.

ヘキシルアルコール、オクチルアルコール、2゜3−ジ
クロル−1−プロパツール、2,3−ジブロモ−1−プ
ロパツール、アリルアルコール、2−ヒドロキシエチル
メククリレート、2−ヒドロキシエチルアクリレート、
ベンジルアルコール等があげられる。
Hexyl alcohol, octyl alcohol, 2゜3-dichloro-1-propatol, 2,3-dibromo-1-propatol, allyl alcohol, 2-hydroxyethyl meccrylate, 2-hydroxyethyl acrylate,
Examples include benzyl alcohol.

共重合体の酸無水物基と炭素数3以上の飽和または不飽
和一価アルコニルとの反応は、共重合体の溶液に炭素数
3以上の飽和または不飽和一価アルコール、必要に応じ
て触媒を加えて加熱、撹拌下に行なわれる。溶媒は共重
合体を溶解するものであれば特に制限はなく、また溶液
中の共重合体の濃度は、最終反応液の樹脂濃度が10〜
90重量%程度になるように適宜選択される。共重合体
−〇  − の酸無水物基と反応させる炭素数3以上の飽和または不
飽和一価アルコールの量は、樹脂の性能に合わせて適宜
選択することができるが、一般には炭素数3以上の飽和
または不飽和−・価アルコールの使用量は、通常共重合
体の酸無水物基1モルに対して0.1〜1モルの範囲内
である。必要に応じて用いられる触媒としては、従来公
知のエステル化触媒が用いられる。加熱は、室温へ・1
30℃、好ましくは40〜100℃の範囲内ぐあり、ま
た反応時間は反応渇疫、炭素数3以上の飽和または不飽
和一価アルコールの反応性により決定されるが、一般に
は1 ヘ20時間が適当である1゜このようにして得ら
れたエステル化ボリン−は、共重合体の酸無水物基の8
0%未満の量が部分エステル化されている。この部分エ
ステル化されたポリマーは、次に炭素数1または2の脂
肪族一価アルコールと反応させる。
The reaction between the acid anhydride group of the copolymer and the saturated or unsaturated monohydric alkonyl having 3 or more carbon atoms is performed by adding a saturated or unsaturated monohydric alcohol having 3 or more carbon atoms to the solution of the copolymer, and optionally a catalyst. is added, heated, and stirred. The solvent is not particularly limited as long as it dissolves the copolymer, and the concentration of the copolymer in the solution is such that the resin concentration of the final reaction solution is 10 to 10.
The content is appropriately selected to be about 90% by weight. The amount of the saturated or unsaturated monohydric alcohol having 3 or more carbon atoms to be reacted with the acid anhydride group of the copolymer -〇- can be appropriately selected depending on the performance of the resin, but in general, the amount of saturated or unsaturated monohydric alcohol having 3 or more carbon atoms is used. The amount of the saturated or unsaturated alcohol used is usually within the range of 0.1 to 1 mole per mole of acid anhydride group of the copolymer. As the catalyst used as necessary, a conventionally known esterification catalyst is used. Heating to room temperature 1
30°C, preferably within the range of 40 to 100°C, and the reaction time is determined by reaction starvation and the reactivity of the saturated or unsaturated monohydric alcohol having 3 or more carbon atoms, but is generally 1 to 20 hours. The esterified borine thus obtained is suitable for 8 of the acid anhydride groups of the copolymer.
An amount of less than 0% is partially esterified. This partially esterified polymer is then reacted with an aliphatic monohydric alcohol having 1 or 2 carbon atoms.

共重合体の酸無水物基の80%以上の量がエステル化さ
れたポリマーでは、不飽和エポキシ化合物との反応にお
いて、不飽和エポキシ化合物の反応率が上がってもゲル
化は殆んど起こらないので、未反応の酸無水物基と炭素
数1またば2の脂肪族一価アルコールとを反応させる必
要がない。しかし、共重合体の酸無水物基の80%以上
の量をエステル化する場合は、炭素数3以上の飽和また
は不飽和一価アルコールを大過剰に使用しなければなら
ず、その結果、未反応のアルコールに起因するコストア
ップやポリマー物性の低下を招来J゛る。
In a polymer in which 80% or more of the acid anhydride groups in the copolymer are esterified, gelation hardly occurs in the reaction with an unsaturated epoxy compound even if the reaction rate of the unsaturated epoxy compound increases. Therefore, there is no need to react an unreacted acid anhydride group with an aliphatic monohydric alcohol having 1 or 2 carbon atoms. However, when esterifying 80% or more of the acid anhydride groups in the copolymer, a large excess of saturated or unsaturated monohydric alcohol having 3 or more carbon atoms must be used, resulting in This results in an increase in cost and a decrease in the physical properties of the polymer due to the presence of alcohol in the reaction.

未反応の酸無水物基と炭素数1または2の脂肪族一価ア
ルコールとは、メチルアルコール、エヂルアルコール等
である。炭素数が2より大きい一価のアルコールを使用
した場合は、酸無水物基との反応性が悪いために、未反
応の酸無水物基をエステル化づる作用が小さい。
The unreacted acid anhydride group and the aliphatic monohydric alcohol having 1 or 2 carbon atoms include methyl alcohol, edyl alcohol, and the like. When a monohydric alcohol having a carbon number of more than 2 is used, its reactivity with acid anhydride groups is poor, so that the effect of esterifying unreacted acid anhydride groups is small.

炭素数1または2の脂肪族一価アルコールの使用量は、
通常酸無水物基1モルに対して0.1〜1モルの範囲内
が好ましい。
The amount of aliphatic monohydric alcohol having 1 or 2 carbon atoms to be used is
Usually, the amount is preferably within the range of 0.1 to 1 mol per mol of acid anhydride group.

未反応の酸無水物基と炭素数1または2の脂肪族一価ア
ルコールとの反応は、前記共重合体の酸無水物基と炭素
数3以上の飽和または不飽和一価アルコールとの反応条
件とばぼ同様に行なわれる。
The reaction between the unreacted acid anhydride group and the aliphatic monohydric alcohol having 1 or 2 carbon atoms is carried out under the reaction conditions of the acid anhydride group of the copolymer and the saturated or unsaturated monohydric alcohol having 3 or more carbon atoms. It is done in the same way as Tobabo.

かくして得られたポリマーは酸無水物基の80%以上の
母がエステル化されている。
In the polymer thus obtained, 80% or more of the acid anhydride groups are esterified.

また、酸無水物基とアルコールとの反応によって生成し
た遊離のカルボキシル基と反応させることのできる不飽
和エポキシ化合物としては、例えばグリシジルメタクリ
レ−1〜、グリシジルアクリレート、アリルグリシジル
エーテル等があげられる。
Furthermore, examples of unsaturated epoxy compounds that can be reacted with free carboxyl groups produced by the reaction of acid anhydride groups and alcohol include glycidyl methacrylate-1, glycidyl acrylate, and allyl glycidyl ether.

上記酸無水物基とアルコールとの反応にJ、って生成し
たM離のカルボキシル基と反応させる不飽和エポキシ化
合物の量は、共重合反応後の共重合体中の酸無水物基1
モルに対して0.2〜0.8モルでよいが、樹脂の性能
に合わせて適宜選択することが出来る。
The amount of the unsaturated epoxy compound to be reacted with the carboxyl group produced by J and M in the reaction of the acid anhydride group and alcohol is determined by the amount of acid anhydride group 1 in the copolymer after the copolymerization reaction.
The amount may be 0.2 to 0.8 mol based on the mole, but it can be appropriately selected depending on the performance of the resin.

遊離のカルボキシル基と不飽和エポキシ化合物との反応
は、常圧、加圧、減圧下のいずれで行なってもよい。反
応温度は20〜120℃、好ましくは4.0〜90℃の
範囲内である。また、反応時間は、1〜30時間、好ま
しくは3〜20時間の範囲内である。この際、反応を促
進するために、触媒として四級アンモニウム塩、三級ア
ミン、亜鉛および鉛のカルボン酸塩、ジ−n−ブチルス
ズカルボン酸塩等の有機スズ化合物、p−トルエンスル
ボン酸等を用いてもよい。
The reaction between a free carboxyl group and an unsaturated epoxy compound may be carried out under normal pressure, increased pressure, or reduced pressure. The reaction temperature is in the range of 20-120°C, preferably 4.0-90°C. Moreover, the reaction time is within the range of 1 to 30 hours, preferably 3 to 20 hours. At this time, in order to accelerate the reaction, quaternary ammonium salts, tertiary amines, zinc and lead carboxylates, organotin compounds such as di-n-butyltin carboxylate, p-toluenesulfonic acid, etc. are used as catalysts. may also be used.

上記反応の一例を反応式で示せば下記のようになる。An example of the above reaction can be expressed as a reaction formula as follows.

但し、 (a)ビニル化合物:スチレン (b)α、β −不飽和酸無水物:無水マレイン酸(C
) ItOH、炭素数3以上の飽和または不飽和一価ア
ルコール (d) R’OH:炭素数1または2の脂肪族一価アル
コール (e)不飽和エポキシ化合物ニ ゲリシジルメタクリレート (al         (bl          
   (fl(cl                
     fQlCH2−CH−CH2−○−C−C−
CH2(e) 〔実施例〕 次に実施例を示して本発明を説明する。
However, (a) vinyl compound: styrene (b) α,β-unsaturated acid anhydride: maleic anhydride (C
) ItOH, saturated or unsaturated monohydric alcohol having 3 or more carbon atoms (d) R'OH: aliphatic monohydric alcohol having 1 or 2 carbon atoms (e) unsaturated epoxy compound nigericidyl methacrylate (al (bl
(fl(cl
fQlCH2-CH-CH2-○-C-C-
CH2(e) [Example] Next, the present invention will be described with reference to Examples.

実施例1 撹拌機、温度ム1.還流冷JJI器をイζjした1ノの
レバラブルレフラス=1に、l−/レー1ニン: 2 
E50 Q、スヂレン: 187 Gをイ1込力、過酸
化ベンゾイル:4g添加した後、窒素雰囲気下、85℃
にて無水マレイン酸:35oとトルエン: 170gの
混合物の85%を2時間かけて滴下した。次いで、過酸
化ベンゾイル=4gをさらに追加添加し、窒素雰囲気下
、85℃にて、残りの無水マレイン酸とトルエンの混合
物を3時間かけて滴下した。滴下終了後、110℃の温
度に保持して2.5時間反応させた。この反応が終了し
た液を樹脂溶液(A)とする。
Example 1 Stirrer, temperature control 1. 1 reversible refras with reflux cold JJI vessel = 1, l-/re 1 nin: 2
E50 Q, Sudrene: After adding 187 G and 4 g of benzoyl peroxide, heat at 85°C under nitrogen atmosphere.
85% of a mixture of 170 g of maleic anhydride and toluene was added dropwise over 2 hours. Next, 4 g of benzoyl peroxide was further added, and the remaining mixture of maleic anhydride and toluene was added dropwise at 85° C. over 3 hours under a nitrogen atmosphere. After the dropwise addition was completed, the temperature was maintained at 110°C and the reaction was carried out for 2.5 hours. The liquid after this reaction is referred to as a resin solution (A).

この樹脂溶液(A):650qにアリルアルコール12
.4q、トリエチルアミン:1.3Qおよびp−メトキ
シフェノール:0.2aを添加し、窒素雰囲気下、80
℃で15時間反応させた。反応終了後にお1プる酸無水
物基の反応率は約50%であった。この反応が終了した
液を樹脂溶液(B)とする。
This resin solution (A): 650q and allyl alcohol 12
.. 4q, triethylamine: 1.3Q and p-methoxyphenol: 0.2a were added, and under nitrogen atmosphere, 80
The reaction was carried out at ℃ for 15 hours. After the reaction was completed, the reaction rate of the acid anhydride group was approximately 50%. The liquid after this reaction is referred to as a resin solution (B).

この樹脂溶液(B):664gにメヂルアルコール:1
1.6Qを添加し、窒素雰囲気下、80℃で6時間反応
させた。その結果、酸無水物基の反応率は約90%とな
った。次いでアリルグリシジルエーテル:45gを添加
し、80℃で15時間反応させたところ、淡黄色透明な
均一の樹脂溶液(C)が得られた。樹脂溶液(C)の粘
度は、20℃において約30ボイスであった。
This resin solution (B): 664g and methyl alcohol: 1
1.6Q was added, and the mixture was reacted at 80° C. for 6 hours under a nitrogen atmosphere. As a result, the reaction rate of acid anhydride groups was approximately 90%. Next, 45 g of allyl glycidyl ether was added and reacted at 80° C. for 15 hours to obtain a pale yellow, transparent, uniform resin solution (C). The viscosity of the resin solution (C) was about 30 voices at 20°C.

この樹脂溶液(C):100qにジクミルパーオキサイ
ド:1.OQを添加溶解させた後、これを化粧紙に含浸
させ、80℃′c10分間乾燥した。
This resin solution (C): 100q and dicumyl peroxide: 1. After OQ was added and dissolved, decorative paper was impregnated with it and dried at 80°C for 10 minutes.

この乾燥した含浸紙を温度:150℃、圧力20に9 
/ cmで1時間プレスすることにより、硬度、耐薬品
性等の優れた硬化化粧板が得られた。
This dried impregnated paper was heated to 90°C at a temperature of 150°C and a pressure of 20°C.
/ cm for 1 hour, a cured decorative board with excellent hardness, chemical resistance, etc. was obtained.

比較例1 実施例1の樹脂溶液(B)664gにアリルグリシジル
エーテル=45gを添加し、80℃で15時間反応させ
たところ、ゲル化が起り、ゼラヂン状の固まりが生成し
、実施例1のように含浸硬化成形が出来なかった。
Comparative Example 1 When 45 g of allyl glycidyl ether was added to 664 g of the resin solution (B) of Example 1 and reacted at 80°C for 15 hours, gelation occurred and a geladine-like mass was formed. Impregnating and hardening molding was not possible.

実施例2 撹拌機、温度計、還流冷却器を付した1jのセパラブル
フラスコに、アセトン:3200、スヂレンー無°水マ
レイン酸共重体(Arco Chemica1社−1/
l − 製、 SHA 1000A )  :300CJを仕込
み、均一溶液とした後、2.3−ジブロモ−1−プロパ
ツール:259g、l〜リエヂルアミン:5.3gを加
え、窒素雰囲気下、60’Cr9時間反応さυ−た。こ
の場合の酸無水物基の反応率は約50%であった。
Example 2 In a 1J separable flask equipped with a stirrer, a thermometer, and a reflux condenser, acetone: 3200, styrene-maleic anhydride copolymer (Arco Chemica 1-1/
After preparing 300 CJ (manufactured by SHA 1000A) and making a homogeneous solution, 259 g of 2,3-dibromo-1-propatool and 5.3 g of L-liedylamine were added, and the mixture was reacted with 60'Cr for 9 hours under a nitrogen atmosphere. Saυ−ta. In this case, the reaction rate of the acid anhydride group was about 50%.

この反応によって得られた溶液を樹脂溶液(D>とする
The solution obtained by this reaction is referred to as a resin solution (D>).

この樹脂溶液(D):884gにメチルアルコール:9
.50を添加し、60°Cで9時間反応さぽた。その結
果、酸無水物基の反応率は約82%となった。次いでp
−メトキシフェノール二〇、7q、グリシジルメタクリ
レート:169gを加え、60℃で18時間反応させた
Methyl alcohol: 9 to this resin solution (D): 884 g
.. Add 50% sapota and react at 60°C for 9 hours. As a result, the reaction rate of acid anhydride groups was approximately 82%. Then p
-Methoxyphenol 2,7q and glycidyl methacrylate: 169g were added and reacted at 60°C for 18 hours.

この反応液を約75mHUに減圧して、アレトン:15
0gを留出除去した後、スヂレン:7/130を加え、
約25mHIJに減圧して更にアI? l−ン約170
9を留出除去した。
This reaction solution was depressurized to about 75 mHU, and aletone: 15
After removing 0g by distillation, add sutyrene: 7/130,
Depressurize to about 25mHIJ and further aI? l- about 170
9 was removed by distillation.

このようにし−C得られた樹脂は、淡黄色透明な高粘疫
溶液で、20℃にお(プる粘度は約160ポイズであっ
た。この溶液を樹脂溶液(E)とする。
The resin obtained in this way was a pale yellow transparent highly viscous solution, and the viscosity at 20° C. was about 160 poise. This solution was referred to as resin solution (E).

この樹脂溶液(E):10C)gにナフテン酸コバル1
〜:0.09g、二酸化アンチモン:1,4q、t−ブ
チルパーオキシベンゾエート=1.OQ、およびメチル
エチルケトンパーオキシドの55%ジメチルフタレート
溶液:1.Ogを添加し、よく撹拌した後、ポリエステ
ルフィルムを表面に張った2枚のステンレス製平板の間
に流し込んだ。これを80℃に2時間、次いで150℃
に1時間保持して硬化させた後、120℃で10時間、
アフターキュアを行なったところ、淡黄色透明な硬化体
が得られた。
This resin solution (E): 1 cobal naphthenate per 10 C) g
~: 0.09g, antimony dioxide: 1,4q, t-butyl peroxybenzoate = 1. OQ, and 55% dimethyl phthalate solution of methyl ethyl ketone peroxide: 1. After adding Og and stirring well, the mixture was poured between two stainless steel flat plates covered with a polyester film. This was heated to 80°C for 2 hours, then to 150°C.
After curing for 1 hour at 120°C for 10 hours,
When after-curing was performed, a pale yellow transparent cured product was obtained.

比較例2 実施例2の樹脂溶液(D):884qにp−メ[−キシ
フ1ノール:Q、7Q、グリシジルメタアクリレート:
169oを加え、60℃で18時間反応させたところ、
ゲル化が始まり、実施例2のような硬化成形が出来なか
った。
Comparative Example 2 Resin solution (D) of Example 2: 884q and p-me[-xifinol:Q, 7Q, glycidyl methacrylate:
When 169o was added and reacted at 60°C for 18 hours,
Gelation started, and hardening and molding as in Example 2 could not be performed.

比較例3 実施例1の樹脂溶液(B):664oにブチルアルコー
ル:10.6Qを添加した他は全く同じにして、樹脂溶
液(C)に相当する樹脂溶液(C′ )をつくったが、
グリシジルエーテルとの反応においてゲル化の発生が認
められた。
Comparative Example 3 A resin solution (C') corresponding to the resin solution (C) was prepared in exactly the same manner as in Example 1 except that butyl alcohol: 10.6Q was added to the resin solution (B): 664o.
Gelation occurred during the reaction with glycidyl ether.

実施例3 実施例1の樹脂溶液(A):650gに2−ヒドロキシ
エチルメタクリレート:27.8g、  トリエチルア
ミン:1.30およびp−メトキシフェノール:0.2
0を添加し、窒素雰囲気下、60℃で5時間反応させた
。反応終了後にお(プる酸無水物基の反応率は約40%
であった。この反応終了液を樹脂溶液(F)とする。
Example 3 Resin solution (A) of Example 1: 650 g, 2-hydroxyethyl methacrylate: 27.8 g, triethylamine: 1.30 and p-methoxyphenol: 0.2
0 was added thereto, and the mixture was reacted at 60° C. for 5 hours under a nitrogen atmosphere. After the reaction is completed, the reaction rate of the acid anhydride group is approximately 40%.
Met. This reaction-completed liquid is referred to as a resin solution (F).

この樹脂溶液(F):679qにメチルアルコール:4
.6(]を添加し、窒素雰囲気下、60℃3時間反応さ
けたところ、酸無水物基の反応率は80%となった。次
いで、アリルグリシジルエーテル:32.6qを添加し
、80℃で4時間反応させたところ、淡黄色透明な均一
の樹脂溶液(G)が得られた。樹脂溶液(G)の粘度は
20℃において約25ボイズであった。
Methyl alcohol: 4 to this resin solution (F): 679q
.. 6() was added and the reaction was allowed to proceed for 3 hours at 60°C under a nitrogen atmosphere, and the reaction rate of the acid anhydride group was 80%.Next, 32.6q of allyl glycidyl ether was added and the reaction was carried out at 80°C. After 4 hours of reaction, a pale yellow, transparent, uniform resin solution (G) was obtained.The viscosity of the resin solution (G) was about 25 voids at 20°C.

この樹脂溶液(G)+100<hにジクミルパーオキサ
イド:1.ooを添加溶解させた後、これを化粧紙に含
浸させ、80℃で10分間乾燥した。
Add dicumyl peroxide to this resin solution (G) + 100<h: 1. After adding and dissolving oo, decorative paper was impregnated with it and dried at 80° C. for 10 minutes.

この乾燥した含浸紙を温度150℃、圧ノ] 20 K
g/ airで1時間プレスすることにより、硬度、耐
薬品性等の優れた硬化化粧板が得られた。
This dried impregnated paper was heated at a temperature of 150°C and a pressure of 20K.
By pressing at g/air for 1 hour, a cured decorative board with excellent hardness, chemical resistance, etc. was obtained.

比較例4 実施例3の樹脂溶液(F):679qにアリルグリシジ
ルエーテル+32.60を添加し、80℃で4時間反応
させたところ、ゲル化の発生が認められ、実施例3のよ
うに含浸硬化成形が出来なかった。
Comparative Example 4 When allyl glycidyl ether +32.60 was added to the resin solution (F): 679q of Example 3 and reacted at 80°C for 4 hours, gelation was observed, and impregnation was performed as in Example 3. Hardening molding was not possible.

実施例4 撹拌機、温度計、還流冷却器を付した1Jのセパラブル
フラスコに、アセトン: 320 <y 、スヂレンー
無水マレイン酸共重体(Arco Chemica1社
製、 5)IA 100QA ) : 300gを仕込
み、均一溶液とした後、n−ブチルアルコール:66Q
、トリエチルアミン:5.3qを加え、窒素雰囲気下、
60℃で9時間反応させた。この場合の酸無水物基の反
応率は約45%であった。この反応によって得られた溶
液を樹脂溶液(11)とする。
Example 4 A 1J separable flask equipped with a stirrer, a thermometer, and a reflux condenser was charged with 300 g of acetone (320<y) and styrene-maleic anhydride copolymer (manufactured by Arco Chemica 1, 5) IA 100QA). After making a homogeneous solution, n-butyl alcohol: 66Q
, triethylamine: 5.3q was added, under nitrogen atmosphere,
The reaction was carried out at 60°C for 9 hours. In this case, the reaction rate of the acid anhydride group was about 45%. The solution obtained by this reaction is referred to as a resin solution (11).

この樹脂溶液(H):691gにエチルアルコール=2
7gを添加し、60℃、5時間反応ざぜた。その結東、
酸無水物基の反応率は約81%どなった。次いでp−メ
トキシフェノール=0.7q、グリシジルメタクリレー
ト: 169 <2を加え、60℃で10時間反応さけ
た。
This resin solution (H): 691g and ethyl alcohol = 2
7 g was added, and the reaction was stirred at 60°C for 5 hours. That connection,
The reaction rate of the acid anhydride group was approximately 81%. Next, 0.7 q of p-methoxyphenol and 169 <2 glycidyl methacrylate were added, and the reaction was allowed to proceed at 60°C for 10 hours.

この反応液を約75mmHHに減圧して、アセトン:1
50qを留出除去した後、スヂレン: 568C1を加
え、約25mmHClに減圧して更にアゼトンを約17
00を留出除去した。
This reaction solution was depressurized to about 75 mmHH, and acetone:1
After removing 50q by distillation, 568C1 was added, the pressure was reduced to about 25mmHCl, and about 17ml of azetone was added.
00 was removed by distillation.

このようにして得られた樹脂は、淡黄色透明な高粘度溶
液で、20℃にお【ノる粘度は約100ポイズであった
。この溶液を樹脂溶液(1)とする。
The resin thus obtained was a pale yellow, transparent, highly viscous solution with a viscosity of about 100 poise at 20°C. This solution will be referred to as resin solution (1).

この樹脂溶液<1):100gにナノテン酸コバルト+
Q、10Xt−プチルパーオキシベンゾ工−1〜:1.
0g、およびメヂルエチルケトンパーオキシドの55%
ジメヂルフタレート溶液=1、Oc+を添加し、よく撹
拌した後、ポリエステルフィルムを表面に張った2枚の
ステンレス製甲板の間に流し込んだ。これを80℃に2
時間、次いで150℃に1時間保持して硬化させた後、
120℃で10時間アフターキュアを行なったところ、
淡黄色透明な硬化体が得られた。
This resin solution <1): 100g of cobalt nanothenate +
Q, 10Xt-butylperoxybenzo-1~:1.
0 g, and 55% of medylethyl ketone peroxide
After adding dimedyl phthalate solution = 1 and Oc+ and stirring well, it was poured between two stainless steel decks covered with a polyester film. Heat this to 80℃ 2
After curing for 1 hour and then holding at 150°C for 1 hour,
After curing for 10 hours at 120℃,
A pale yellow transparent cured product was obtained.

比較例5 実施例4の樹脂溶液()−1):691oにp−メトキ
シフェノール:0.7Q、グリシジルメタアクリレート
:169CIを加え、60℃、10時間反応させたとこ
ろ、ゲル化が始まり、実施例4のような硬化成形が出来
なかった。
Comparative Example 5 When p-methoxyphenol: 0.7Q and glycidyl methacrylate: 169CI were added to the resin solution ()-1): 691o of Example 4 and reacted at 60°C for 10 hours, gelation started and implementation was carried out. It was not possible to perform hardening molding as in Example 4.

〔効果〕〔effect〕

以上述べたように、本発明に係る硬化性樹脂の製造方法
は、製造過程におけるゲル化の発生が全くなく、しかも
透明性の高い美しい硬化性樹脂が得られる優れた方法で
ある。
As described above, the method for producing a curable resin according to the present invention is an excellent method that does not cause any gelation during the production process and can produce a highly transparent and beautiful curable resin.

Claims (1)

【特許請求の範囲】[Claims] α,β−不飽和酸無水物と、これに共重合可能なビニル
化合物とからなる共重合体の酸無水物基を炭素数3以上
の飽和または不飽和一価アルコールで部分エステル化し
て得られるポリマーの遊離のカルボキシル基と不飽和エ
ポキシ化合物とを反応させる硬化性樹脂の製造方法にお
いて、上記部分エステル化ポリマーの遊離のカルボキシ
ル基と不飽和エポキシ化合物とを反応させる前に、上記
部分エステル化ポリマーを炭素数1または2の脂肪族一
価アルコールでエステル化することを特徴とする硬化性
樹脂の製造方法。
Obtained by partially esterifying the acid anhydride group of a copolymer consisting of an α,β-unsaturated acid anhydride and a vinyl compound copolymerizable therewith with a saturated or unsaturated monohydric alcohol having 3 or more carbon atoms. In the method for producing a curable resin in which free carboxyl groups of a polymer are reacted with an unsaturated epoxy compound, before reacting free carboxyl groups of the partially esterified polymer with the unsaturated epoxy compound, the partially esterified polymer is A method for producing a curable resin, which comprises esterifying with an aliphatic monohydric alcohol having 1 or 2 carbon atoms.
JP3695986A 1986-02-21 1986-02-21 Production of curable resin Pending JPS62195002A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3695986A JPS62195002A (en) 1986-02-21 1986-02-21 Production of curable resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3695986A JPS62195002A (en) 1986-02-21 1986-02-21 Production of curable resin

Publications (1)

Publication Number Publication Date
JPS62195002A true JPS62195002A (en) 1987-08-27

Family

ID=12484282

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3695986A Pending JPS62195002A (en) 1986-02-21 1986-02-21 Production of curable resin

Country Status (1)

Country Link
JP (1) JPS62195002A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6264791B1 (en) 1999-10-25 2001-07-24 Kimberly-Clark Worldwide, Inc. Flash curing of fibrous webs treated with polymeric reactive compounds
US6322665B1 (en) 1999-10-25 2001-11-27 Kimberly-Clark Corporation Reactive compounds to fibrous webs
WO2017154439A1 (en) * 2016-03-08 2017-09-14 住友ベークライト株式会社 Method for manufacturing polymer, method for manufacturing negative-type photosensitive resin composition, method for manufacturing resin film, method for manufacturing electronic device, and polymer

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6264791B1 (en) 1999-10-25 2001-07-24 Kimberly-Clark Worldwide, Inc. Flash curing of fibrous webs treated with polymeric reactive compounds
US6322665B1 (en) 1999-10-25 2001-11-27 Kimberly-Clark Corporation Reactive compounds to fibrous webs
WO2017154439A1 (en) * 2016-03-08 2017-09-14 住友ベークライト株式会社 Method for manufacturing polymer, method for manufacturing negative-type photosensitive resin composition, method for manufacturing resin film, method for manufacturing electronic device, and polymer
CN108779196A (en) * 2016-03-08 2018-11-09 住友电木株式会社 The manufacturing method of polymer, the manufacturing method of negative light-sensitive resin combination, the manufacturing method of resin film, the manufacturing method of electronic device and polymer
JPWO2017154439A1 (en) * 2016-03-08 2019-01-10 住友ベークライト株式会社 Method for producing polymer, method for producing negative photosensitive resin composition, method for producing resin film, method for producing electronic device, and polymer

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