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JPH06336516A - Production of epoxy resin - Google Patents

Production of epoxy resin

Info

Publication number
JPH06336516A
JPH06336516A JP14834893A JP14834893A JPH06336516A JP H06336516 A JPH06336516 A JP H06336516A JP 14834893 A JP14834893 A JP 14834893A JP 14834893 A JP14834893 A JP 14834893A JP H06336516 A JPH06336516 A JP H06336516A
Authority
JP
Japan
Prior art keywords
epoxy resin
formula
parts
water
reaction
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
JP14834893A
Other languages
Japanese (ja)
Inventor
Yasumasa Akatsuka
泰昌 赤塚
Hiromi Morita
博美 森田
Hiroaki Ono
博昭 大野
Kenichi Kuboki
健一 窪木
Yoshiro Shimamura
芳郎 嶋村
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.)
Nippon Kayaku Co Ltd
Original Assignee
Nippon Kayaku 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 Nippon Kayaku Co Ltd filed Critical Nippon Kayaku Co Ltd
Priority to JP14834893A priority Critical patent/JPH06336516A/en
Publication of JPH06336516A publication Critical patent/JPH06336516A/en
Pending legal-status Critical Current

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  • Epoxy Resins (AREA)

Abstract

PURPOSE:To obtain in high yield an epoxy resin which gives a cured resin excellent in heat resistance, toughness, and water resistance by reacting a given compound with an epihalohydrin in the presence of an alkali metal hydroxide. CONSTITUTION:A compound represented by formula I (wherein (n) is a positive number and R is H or Br) is reacted with an epihalohydrin (e.g., epichlorohydrin) in the presence of an alkali metal hydroxide (e.g., NaOH) at 50 deg.C or lower to obtain an epoxy resin represented by formula II (wherein each X is H or glycidyl, provided that 10-95% of the X's are glycidyl).

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は有用なるエポキシ樹脂の
製造方法に関するものであり、本発明で得られるエポキ
シ樹脂は種々の硬化剤と反応させることにより耐熱性、
靭性及び耐水性に優れた硬化物が得られ、成形材料,注
型材料,積層材料,複合材料,塗料,接着剤,レジスト
などの広範囲の用途に極めて有用である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a useful epoxy resin, in which the epoxy resin obtained by the present invention is heat resistant by reacting with various curing agents.
A cured product with excellent toughness and water resistance is obtained, and it is extremely useful for a wide range of applications such as molding materials, casting materials, laminated materials, composite materials, paints, adhesives, and resists.

【0002】[0002]

【従来の技術】エポキシ樹脂は種々の硬化剤で硬化させ
ることにより、一般的に機械的性質,耐水性,耐薬品
性,耐熱性,電気的性質などの優れた硬化物となり、接
着剤,塗料,積層板,成形材料,注型材料などの幅広い
分野に利用されている。従来、工業的に最も使用されて
いるエポキシ樹脂としてビスフェノ−ルAにエピクロル
ヒドリンを反応させて得られる液状および固形のビスフ
ェノ−ルA型エポキシ樹脂がある。その他液状のビスフ
ェノ−ルA型エポキシ樹脂にテトラブルムビスフェノ−
ルAを反応させて得られる難燃性固形エポキシ樹脂など
が汎用エポキシ樹脂として工業的に使用されている。
2. Description of the Related Art Epoxy resins, when cured with various curing agents, generally become cured products having excellent mechanical properties, water resistance, chemical resistance, heat resistance, electrical properties, etc. It is used in a wide range of fields such as laminates, molding materials, and casting materials. Conventionally, liquid and solid bisphenol A type epoxy resins obtained by reacting bisphenol A with epichlorohydrin have been used as the most industrially used epoxy resins. In addition to liquid bisphenol A type epoxy resin, Tetrabumu bisphenol
A flame-retardant solid epoxy resin obtained by reacting the resin A is industrially used as a general-purpose epoxy resin.

【0003】しかしながら、前記したような汎用エポキ
シ樹脂は分子量が大きくなるにつれて、それを使用して
得られる硬化物の強靭性は増加するものの耐熱性は低下
するという欠点がある。また、耐熱性の低下を補うため
にクレゾールノボラックエポキシ樹脂などの多官能エポ
キシ樹脂を混合した場合に得られる硬化物は耐熱性は高
くなるものの、靭性は低下し吸水率は高くなるという欠
点がある。一方、最近の電子産業などの目ざましい発達
に伴い、これらに使用される電気絶縁材料などに要求さ
れる耐熱性、靭性及び耐水性は益々厳しくなっており、
これらの特性に優れたエポキシ樹脂の出現が待ち望まれ
ている。
However, the general-purpose epoxy resin as described above has a drawback that as the molecular weight increases, the toughness of a cured product obtained by using the epoxy resin increases, but the heat resistance decreases. Further, although a cured product obtained by mixing a polyfunctional epoxy resin such as cresol novolac epoxy resin in order to compensate for the decrease in heat resistance has high heat resistance, it has a drawback that toughness decreases and water absorption increases. . On the other hand, with the recent remarkable development of the electronic industry and the like, the heat resistance, toughness and water resistance required for electric insulating materials used for these have become more and more severe,
The advent of epoxy resins excellent in these properties has been awaited.

【0004】一方、これらの特性を満たすエポキシ樹脂
として米国特許第4623701号明細書等に汎用エポ
キシ樹脂のアルコール性水酸基を全量グリシジルエーテ
ル化したものが報告されている。
On the other hand, as an epoxy resin satisfying these characteristics, US Pat. No. 4,623,701 and the like report a general-purpose epoxy resin obtained by completely converting alcoholic hydroxyl groups into glycidyl ether.

【発明が解決しようとする課題】[Problems to be Solved by the Invention]

【0005】しかしながら前記特許に記載された製造方
法では、反応温度が高く、アルカリ金属水酸化物が大過
剰の状態で反応を行っているため、副反応が多く起こり
目的とする構造を有するエポキシ樹脂の収率が悪い。さ
らに疎水性溶剤の存在下で脱ハロゲン化水素反応を行っ
ていないため、加水分解性塩素の多いエポキシ樹脂しか
製造できない。この加水分解性塩素の多いエポキシ樹脂
は硬化物の特性に悪影響を及ぼし、特に電気特性を低下
させるため電子材料の使用には適さない。
However, in the production method described in the above-mentioned patent, since the reaction temperature is high and the reaction is carried out in a state of a large excess of alkali metal hydroxide, many side reactions occur and the epoxy resin having the desired structure is produced. Yield is poor. Furthermore, since the dehydrohalogenation reaction is not carried out in the presence of a hydrophobic solvent, only an epoxy resin containing a large amount of hydrolyzable chlorine can be produced. This epoxy resin containing a large amount of hydrolyzable chlorine adversely affects the properties of the cured product and particularly deteriorates the electrical properties, and is not suitable for use in electronic materials.

【課題を解決するための手段】本発明者らはこうした実
状に鑑み、その硬化物が耐熱性、靭性及び耐水性に優
れ、かつ加水分解性塩素の少ないエポキシ樹脂を求めて
鋭意研究した結果、本発明の方法で得られる特定の構造
を有するエポキシ樹脂が、その硬化物に対して優れた耐
熱性、靭性及び耐水性を付与するものであることを見い
出して本発明を完成させるに到った。
In view of these circumstances, the inventors of the present invention have earnestly studied for an epoxy resin whose cured product is excellent in heat resistance, toughness and water resistance, and has little hydrolyzable chlorine. It was found that the epoxy resin having a specific structure obtained by the method of the present invention imparts excellent heat resistance, toughness and water resistance to the cured product, and has completed the present invention. .

【0006】すなわち本発明は(1)式(1A)That is, the present invention is based on the formula (1) (1A)

【0007】[0007]

【化3】 [Chemical 3]

【0008】(式中、nは正数を表し、Rは水素原子あ
るいは臭素原子を表し個々のRはお互いに同一であって
も異なっていてもよい。)で表される化合物とエピハロ
ヒドリンをアルカリ金属水酸化物の存在下50℃以下の
温度で反応させることを特徴とする式(1)
(In the formula, n represents a positive number, R represents a hydrogen atom or a bromine atom, and each R may be the same or different from each other.) And an epihalohydrin are alkaline. Formula (1) characterized by reacting at a temperature of 50 ° C. or lower in the presence of a metal hydroxide

【0009】[0009]

【化4】 [Chemical 4]

【0010】(式中nは正数を表す。Rは水素原子ある
いは臭素原子を表し個々のRはお互いに同一であっても
異なっていてもよい。またXは水素原子あるいはグリシ
ジル基を表し個々のXはお互いに同一であっても異なっ
ていてもよいが、Xの10%以上95%以下はグリシジ
ル基である。)で表されるエポキシ樹脂の製造方法、
(In the formula, n represents a positive number. R represents a hydrogen atom or a bromine atom, and each R may be the same or different from each other. X represents a hydrogen atom or a glycidyl group. X may be the same or different from each other, but 10% or more and 95% or less of X is a glycidyl group.).

【0011】(2)臭素化されていてもよビスフェノー
ルA型エポキシ樹脂と臭素化されていてもよいビスフェ
ノールAとを塩基性触媒の存在下に反応させ、次いで、
反応生成物とエピハロヒドリンをアルカリ金属水酸化物
の存在下50℃以下の温度で反応させることを特徴とす
る上記式(1)で表されるエポキシ樹脂の製造方法、に
関するものである。
(2) The bisphenol A type epoxy resin which may be brominated and bisphenol A which may be brominated are reacted in the presence of a basic catalyst, and then,
The present invention relates to a method for producing an epoxy resin represented by the above formula (1), which comprises reacting a reaction product with epihalohydrin at a temperature of 50 ° C. or lower in the presence of an alkali metal hydroxide.

【0012】本発明の製造方法によれば、その硬化物が
耐熱性、靭性及び耐水性に優れ、しかも加水分解性塩素
量の低いエポキシ樹脂を容易に得ることができる。前記
式(1A)及び式(1)において、nは平均値を示す
が、その好ましい値は0.3〜6であり、特に好ましい
値は0.5〜4である。又、式(1)において、Xの1
0〜95%はグリシジル基であるが、特にXの15〜9
5%がグリシジル基であることが好ましい。
According to the production method of the present invention, an epoxy resin whose cured product is excellent in heat resistance, toughness and water resistance and has a low hydrolyzable chlorine content can be easily obtained. In the formula (1A) and the formula (1), n represents an average value, and its preferable value is 0.3 to 6, and particularly preferable value is 0.5 to 4. Also, in the formula (1), 1 of X
0 to 95% is a glycidyl group, especially 15 to 9 of X
It is preferable that 5% is a glycidyl group.

【0013】式(1A)で表される化合物とエピハロヒ
ドリンをアルカリ金属水酸化物の存在下に反応させる際
の反応温度は50℃以下であるが好ましくは20〜45
℃である。式(1A)の化合物は公知の方法で合成する
ことができ、例えば式(3)
The reaction temperature for reacting the compound of formula (1A) with epihalohydrin in the presence of an alkali metal hydroxide is 50 ° C. or lower, preferably 20 to 45.
℃. The compound of formula (1A) can be synthesized by a known method, for example, the compound of formula (3)

【0014】[0014]

【化5】 [Chemical 5]

【0015】(式中、Rは前記と同じ意味を表す)で表
される化合物と式(4)
(Wherein R represents the same meaning as described above) and a compound of formula (4)

【0016】[0016]

【化6】 [Chemical 6]

【0017】(式中、Rは前記と同じ意味を表す)で表
される化合物とを、溶剤の存在下あるいは無溶剤下でト
リフェニルホスフィン、4級アンモニウム塩、NaO
H、イミダゾール類のような塩基性触媒を用いて反応さ
せることにより得ることが出来る。上記化合物(1A)
を得る際に用いる各成分の使用割合については、式
(3)で表されるエポキシ樹脂1当量に対し、式(4)
で表される化合物を0.2〜0.9当量用いるのが好ま
しく、特に0.3〜0.8当量用いることが好ましい。
塩基性触媒は式(3)で表されるエポキシ樹脂100重
量部に対し、0.005〜0.5重量部用いることが好
ましく、特に0.01〜0.3重量部用いることが好ま
しい。反応温度は80〜200℃が好ましく、特に10
0〜170℃が好ましい。
(Wherein R represents the same meaning as described above) and a compound represented by the formula: triphenylphosphine, quaternary ammonium salt, NaO 2 in the presence or absence of a solvent.
It can be obtained by reacting with a basic catalyst such as H and imidazoles. The compound (1A)
Regarding the use ratio of each component used in obtaining the formula, the formula (4) is used for 1 equivalent of the epoxy resin represented by the formula (3).
It is preferable to use 0.2 to 0.9 equivalent of the compound represented by, and it is particularly preferable to use 0.3 to 0.8 equivalent.
The basic catalyst is preferably used in an amount of 0.005 to 0.5 part by weight, particularly preferably 0.01 to 0.3 part by weight, based on 100 parts by weight of the epoxy resin represented by the formula (3). The reaction temperature is preferably 80 to 200 ° C, particularly 10
0-170 degreeC is preferable.

【0018】式(1A)で表される化合物のアルコール
性水酸基をエポキシ化する方法はアルコール性水酸基と
エピハロヒドリンとの反応をアルカリ金属水酸化物の存
在下50℃以下の温度で行なうことにより実施すること
ができ、その際ジメチルスルホキシドまたは4級アンモ
ニウム塩または1,3−ジメチル−2−イミダゾリジノ
ンを共存させるのが特に好ましい。
The method of epoxidizing the alcoholic hydroxyl group of the compound represented by the formula (1A) is carried out by reacting the alcoholic hydroxyl group with epihalohydrin at a temperature of 50 ° C. or lower in the presence of an alkali metal hydroxide. In that case, it is particularly preferable that dimethyl sulfoxide or a quaternary ammonium salt or 1,3-dimethyl-2-imidazolidinone is allowed to coexist.

【0019】式(1A)で表される化合物のアルコ−ル
性水酸基は一般のアルコ−ル類より反応性に富んでお
り、アルカリ金属水酸化物を存在させることにより、好
ましくは更にジメチルスルホキシドまたは4級アンモニ
ウム塩または1,3−ジメチル−2−イミダゾリジノン
を併用することにより、アルコ−ル性水酸基とエピハロ
ヒドリンとの反応を選択的に行え、さらにアルカリ金属
水酸化物の量を調節することにより式(1A)で表され
る化合物のアルコ−ル性水酸基を所望の割合にエポキシ
化することができる。
The alcoholic hydroxyl group of the compound represented by the formula (1A) is more reactive than general alcohols, and it is preferable to further add dimethylsulfoxide or dimethylsulfoxide by the presence of an alkali metal hydroxide. By using a quaternary ammonium salt or 1,3-dimethyl-2-imidazolidinone in combination, the reaction between the alcoholic hydroxyl group and the epihalohydrin can be selectively carried out and the amount of the alkali metal hydroxide can be adjusted. Thus, the alcoholic hydroxyl group of the compound represented by the formula (1A) can be epoxidized in a desired ratio.

【0020】ジメチルスルホキシド、4級アンモニウム
塩、1,3−ジメチル−2−イミダゾリジノンは一種の
み用いてもよく、又、二種以上併用してもよい。又、反
応は、溶剤例えばアルコ−ル類,芳香族炭化水素類,ケ
トン類,環状又は鎖状エ−テル化合物等の存在下に行な
ってもよい。
The dimethyl sulfoxide, quaternary ammonium salt and 1,3-dimethyl-2-imidazolidinone may be used alone or in combination of two or more. The reaction may be carried out in the presence of a solvent such as alcohols, aromatic hydrocarbons, ketones, cyclic or chain ether compounds and the like.

【0021】ジメチルスルホキシドあるいは1,3−ジ
メチル−2−イミダゾリジノンを用いる場合、その使用
量は式(1A)で表される化合物に対して5重量%〜3
00重量%が好ましい。式(1A)で表される化合物に
対して5重量%未満であると式(1A)で表される化合
物の水酸基とエピハロヒドリンとの反応が遅くなり、比
較的長時間の反応が必要となる。式(1A)で表される
化合物に対して300重量%を超えると増量した効果は
ほとんどなくなる一方容積効率も悪くなる。
When dimethyl sulfoxide or 1,3-dimethyl-2-imidazolidinone is used, the amount thereof used is 5% by weight to 3% based on the compound represented by the formula (1A).
00 wt% is preferred. If it is less than 5% by weight with respect to the compound represented by the formula (1A), the reaction between the hydroxyl group of the compound represented by the formula (1A) and epihalohydrin is delayed, and the reaction for a relatively long time is required. When it exceeds 300% by weight with respect to the compound represented by the formula (1A), the effect of increasing the amount is almost eliminated and the volume efficiency is deteriorated.

【0022】4級アンモニウム塩としてはテトラメチル
アンモニウムクロライド,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
等が挙げられ、これらを用いる場合、その使用量は式
(1A)で表される化合物のエポキシ化させたい水酸基
1当量に対して0.3〜50gが好ましい。エポキシ化
させたい水酸基1当量に対して0.3g未満であると式
(1A)で表される化合物の水酸基とエピハロヒドリン
との反応が遅くなり比較的長時間の反応が必要となる。
また50gを超えると増量した効果はほとんどなくなる
一方コストが高くなる。
Examples of the quaternary ammonium salt include tetramethylammonium chloride, tetramethylammonium bromide, trimethylbenzylammonium chloride and the like. When these are used, the amount used is such that the compound represented by the formula (1A) is epoxidized. 0.3 to 50 g is preferable with respect to 1 equivalent of hydroxyl group. If the amount of the hydroxyl group to be epoxidized is less than 0.3 g based on 1 equivalent, the reaction between the hydroxyl group of the compound represented by the formula (1A) and epihalohydrin is delayed and a relatively long reaction time is required.
On the other hand, if the amount exceeds 50 g, the effect of increasing the amount is almost eliminated, but the cost is increased.

【0023】エピハロヒドリンとしてはエピクロルヒド
リン、エピブロモヒドリン等が挙げられる。エピハロヒ
ドリンの使用量は式(1A)で表される化合物のエポキ
シ化させたい水酸基1当量に対して1当量以上使用すれ
ば良い。しかしながらエポキシ化させたい水酸基1当量
に対して20当量を超えると増量した効果はほとんどな
くなる一方容積効率も悪くなり好ましくない。
Examples of epihalohydrin include epichlorohydrin and epibromohydrin. The amount of epihalohydrin used may be 1 equivalent or more with respect to 1 equivalent of the hydroxyl group to be epoxidized in the compound represented by the formula (1A). However, if the amount exceeds 20 equivalents relative to 1 equivalent of the hydroxyl group to be epoxidized, the effect of increasing the amount will almost disappear and the volume efficiency will deteriorate, which is not preferable.

【0024】アルカリ金属水酸化物としては、苛性ソ−
ダ,苛性カリ,水酸化リチウムなどが使用できるが苛性
ソ−ダが好ましい。アルカリ金属水酸化物の使用量は式
(1A)で表される化合物のエポキシ化させたい水酸基
1当量に対して1〜2.0当量使用すれば良い。アルカ
リ金属水酸化物は固形でも水溶液でも構わない。また水
溶液を使用する場合は反応中、反応系内の水は常圧下又
は減圧下において反応系外に留去しながら反応を行うこ
ともできる。
Alkali metal hydroxides include caustic soda.
Although caustic soda, caustic potash, lithium hydroxide and the like can be used, caustic soda is preferred. The amount of the alkali metal hydroxide used may be 1 to 2.0 equivalents relative to 1 equivalent of the hydroxyl group to be epoxidized in the compound represented by the formula (1A). The alkali metal hydroxide may be solid or aqueous solution. When an aqueous solution is used, the reaction can be carried out during the reaction while distilling the water in the reaction system out of the reaction system under normal pressure or reduced pressure.

【0025】反応温度は50℃以下であり、反応温度が
50℃を超えると副反応が多く起こり好ましくない。反
応時間は通常20〜8時間である。
The reaction temperature is 50 ° C. or lower, and if the reaction temperature exceeds 50 ° C., many side reactions occur, which is not preferable. The reaction time is usually 20 to 8 hours.

【0026】反応終了後、水洗により生成塩及び過剰の
アルカリ金属水酸化物を除去し、さらに過剰のエピハロ
ヒドリン及び溶剤類を減圧下留去し、必要により更に後
処理を行う。後処理をする場合、疎水性溶剤に得られた
樹脂を溶解する。疎水性溶剤としては、メチルイソブチ
ルケトン、ベンゼン、トルエン、キシレン等が使用でき
るが、メチルイソブチルケトンが好ましい。これらは単
独もしくは混合系で使用できる。
After completion of the reaction, the salt formed and the excess alkali metal hydroxide are removed by washing with water, and the excess epihalohydrin and the solvents are distilled off under reduced pressure, and further post-treatment is carried out if necessary. When the post-treatment is performed, the obtained resin is dissolved in the hydrophobic solvent. As the hydrophobic solvent, methyl isobutyl ketone, benzene, toluene, xylene and the like can be used, but methyl isobutyl ketone is preferable. These can be used alone or in a mixed system.

【0027】その後、原料として用いた式(1A)の化
合物のアルコール性水酸基に対して、0.025〜0.
20倍モルのアルカリ金属水酸化物を加え、好ましくは
40〜90℃で30分〜3時間撹拌し、脱ハロゲン化水
素反応を行う。この際、アルカリ金属水酸化物は10〜
50%水溶液を用いるのが好ましい。
Then, with respect to the alcoholic hydroxyl group of the compound of the formula (1A) used as a raw material, 0.025 to 0.
A 20-fold molar amount of alkali metal hydroxide is added, and the mixture is stirred at 40 to 90 ° C. for 30 minutes to 3 hours to carry out the dehydrohalogenation reaction. At this time, the alkali metal hydroxide is 10 to
It is preferable to use a 50% aqueous solution.

【0028】反応終了後、樹脂溶液を数回水洗した後、
疎水性溶剤を減圧下で留去することにより、目的とする
エポキシ樹脂を得ることが出来る。
After completion of the reaction, the resin solution was washed with water several times,
The desired epoxy resin can be obtained by distilling off the hydrophobic solvent under reduced pressure.

【0029】本発明の方法で得られるエポキシ樹脂は、
ポリアミン系硬化剤、酸無水物系硬化剤、フェノール系
硬化剤など各種硬化剤で常法により硬化させることが出
来、成形材、ワニス、積層材、接着剤、複合材、粉体塗
料などに使用することが出来る。
The epoxy resin obtained by the method of the present invention is
Can be cured by a conventional method with various curing agents such as polyamine-based curing agents, acid anhydride-based curing agents, phenol-based curing agents, and used in molding materials, varnishes, laminates, adhesives, composite materials, powder coatings, etc. You can do it.

【0030】[0030]

【実施例】次に本発明を実施例、比較例により更に具体
的に説明するが、以下において部は特に断わりのない限
りすべて重量部である。
EXAMPLES Next, the present invention will be described in more detail with reference to Examples and Comparative Examples. In the following, all parts are parts by weight unless otherwise specified.

【0031】実施例1 撹拌機、コンデンサー、温度計を取り付けた丸底フラス
コに、式(3)で表されるエポキシ樹脂としてRがすべ
て水素原子であるビスフェノ−ルA型エポキシ樹脂(エ
ポキシ当量186g/eq)372部、式(4)で表さ
れる化合物としてビスフェノールA(フェノール性水酸
基当量114g/eq)113部を仕込み、150℃に
加熱し完全に溶融混合した後、触媒としてトリフェニル
ホスフィン0.37部を添加し150℃で90分反応さ
せた。この予備反応により得られたエポキシ樹脂(3
1)(式(1A)の化合物)のエポキシ当量は480g
/eqであった。得られたエポキシ樹脂(31)はエポ
キシ当量から計算すると式(1A)におけるnは2.1
8となった。更に得られたエポキシ樹脂(31)をエピ
クロルヒドリン1628部に溶解させた後、40℃でテ
トラメチルアンモニウムクロライド5.5部を添加し、
98.5%NaOH53.6部を90分かけて添加し
た。更に40℃で2時間反応を行った後水126部を加
えて2回水洗を行った。油水分離後、油層よりエピクロ
ルヒドリンを減圧下に蒸留回収した。得られた反応生成
物にメチルイソブチルケトン1320gを加えて溶解さ
せた後、30%NaOH水溶液7.4gを加え70℃で
1時間反応させ、次に2回水洗し、油水分離後、油層か
らメチルイソブチルケトンを留去してエポキシ当量29
6g/eq、加水分解性塩素1120ppmなるエポキ
シ樹脂504部を得た。得られたエポキシ樹脂はエポキ
シ当量から計算すると式(1)におけるnは2.18で
あり、Xのうち70%がグリシジル基であり、軟化点は
64.9℃、150℃における溶融粘度は2.8psで
あった。得られたエポキシ樹脂の物性等の測定結果は表
1にまとめた。
Example 1 A round-bottomed flask equipped with a stirrer, a condenser and a thermometer was placed in a bisphenol A type epoxy resin (epoxy equivalent: 186 g with an epoxy equivalent of 186 g) as an epoxy resin represented by the formula (3) in which all R are hydrogen atoms. / Eq) 372 parts, and 113 parts of bisphenol A (phenolic hydroxyl group equivalent 114 g / eq) as a compound represented by the formula (4) are charged, heated to 150 ° C. and completely melt-mixed, and then triphenylphosphine 0 is used as a catalyst. .37 parts was added and reacted at 150 ° C. for 90 minutes. The epoxy resin (3
1) (compound of formula (1A)) has an epoxy equivalent of 480 g.
It was / eq. When the obtained epoxy resin (31) was calculated from the epoxy equivalent, n in the formula (1A) was 2.1.
It became 8. Furthermore, after dissolving the obtained epoxy resin (31) in 1628 parts of epichlorohydrin, 5.5 parts of tetramethylammonium chloride was added at 40 ° C.,
53.6 parts of 98.5% NaOH was added over 90 minutes. After the reaction was further performed at 40 ° C. for 2 hours, 126 parts of water was added and the mixture was washed twice with water. After separating the oil and water, epichlorohydrin was recovered from the oil layer by distillation under reduced pressure. To the obtained reaction product, 1320 g of methyl isobutyl ketone was added and dissolved, 7.4 g of 30% NaOH aqueous solution was added and reacted at 70 ° C. for 1 hour, then washed twice with water, separated from oily water, and then methylated from the oil layer. Isobutyl ketone was distilled off to obtain an epoxy equivalent of 29.
504 parts of an epoxy resin having 6 g / eq and hydrolyzable chlorine of 1120 ppm was obtained. When the obtained epoxy resin was calculated from the epoxy equivalent, n in the formula (1) was 2.18, 70% of X was a glycidyl group, the softening point was 64.9 ° C., and the melt viscosity at 150 ° C. was 2 It was 0.8 ps. The measurement results of the physical properties of the obtained epoxy resin are summarized in Table 1.

【0032】比較例1 実施例1の予備反応で得られたエポキシ樹脂(31)を
エピクロルヒドリン1628部に溶解させた後、60℃
でテトラメチルアンモニウムクロライド5.5部を添加
し、98.5%NaOH58.1部を90分かけて添加
した。更に40℃で2時間反応を行った後水126部を
加えて2回水洗を行った。油水分離後、油層よりエピク
ロルヒドリンを減圧下に蒸留回収して、エポキシ当量2
99g/eq、加水分解性塩素2680ppmなるエポ
キシ樹脂459部を得た。得られたエポキシ樹脂の軟化
点は65.2℃、150℃における溶融粘度は3.0p
sであった。得られたエポキシ樹脂の物性等の測定結果
は表1にまとめた。
Comparative Example 1 The epoxy resin (31) obtained in the preliminary reaction of Example 1 was dissolved in 1628 parts of epichlorohydrin, and then 60 ° C.
Then, 5.5 parts of tetramethylammonium chloride was added thereto, and 58.1 parts of 98.5% NaOH was added over 90 minutes. After the reaction was further performed at 40 ° C. for 2 hours, 126 parts of water was added and the mixture was washed twice with water. After separation of oil and water, epichlorohydrin was distilled and recovered from the oil layer under reduced pressure to obtain an epoxy equivalent of 2
459 parts of an epoxy resin containing 99 g / eq and 2680 ppm of hydrolyzable chlorine was obtained. The obtained epoxy resin has a softening point of 65.2 ° C. and a melt viscosity at 150 ° C. of 3.0 p.
It was s. The measurement results of the physical properties of the obtained epoxy resin are summarized in Table 1.

【0033】[0033]

【表1】 表1 実施例1 比較例1 エポキシ当量(g/eq) 296 299 エポキシ化率(%) 70 68 加水分解性塩素(ppm) 1120 2680 軟化点(℃) 64.9 65.2 溶融粘度(150℃,ps) 2.8 3.0 収率(%) 95.5 87.2[Table 1] Table 1 Example 1 Comparative Example 1 Epoxy equivalent (g / eq) 296 299 Epoxidation rate (%) 70 68 Hydrolyzable chlorine (ppm) 1120 2680 Softening point (° C) 64.9 65.2 Melt viscosity (150 ° C) , Ps) 2.8 3.0 Yield (%) 95.5 87.2

【0034】エポキシ化率 式(1A)の化合物中の水酸基のうち、エポキシ化され
た水酸基の割合 加水分解性塩素 エポキシ樹脂を、ジオキサンに溶解し、1N−水酸化カ
リウムのエタノール溶液を加え、還流状態で30分間加
熱した時に脱離する塩素イオンを硝酸銀溶液で滴定して
定量し、エポキシ樹脂中の塩素原子の重量を、重量pp
mで表したもの
Epoxidation Ratio Ratio of Epoxidized Hydroxyl Group to Hydroxyl Group in Compound of Formula (1A) Hydrolyzable Chlorine Epoxy resin is dissolved in dioxane, 1N-potassium hydroxide ethanol solution is added and refluxed. Chlorine ions desorbed when heated for 30 minutes in this state were quantified by titration with a silver nitrate solution, and the weight of chlorine atoms in the epoxy resin was determined by weight pp
expressed in m

【0035】軟化点 メトラーFP80HTを用いて測定 溶融粘度 150℃、I.C.I コーン型粘度計を用いて測定 収率 得られたエポキシ樹脂の重量を、式(1A)の化合物が
上記エポキシ化率でエポキシ化された場合得られる理論
量で割った値
Softening point Measured using METTLER FP80HT Melt viscosity 150 ° C., I.V. C. I Measured using a cone type viscometer Yield value obtained by dividing the weight of the obtained epoxy resin by the theoretical amount obtained when the compound of the formula (1A) is epoxidized at the above epoxidation rate.

【0036】実施例2 ビスフェノールAの量を136部にした以外は実施例1
と同様に予備反応を行い、エポキシ当量が629g/e
qのエポキシ樹脂(32)(式(1A)の化合物)を得
た。得られたエポキシ樹脂(32)はエポキシ当量から
計算すると式(1A)におけるnは3.23となった。
更に得られたエポキシ樹脂(32)をエピクロルヒドリ
ン1939部に溶解させた後、40℃でテトラメチルア
ンモニウムクロライド6.6部を添加し、98.5%N
aOH63.8部を90分かけて添加した。更に40℃
で2時間反応を行った後水150部を加えて2回水洗を
行った。油水分離後、油層よりエピクロルヒドリンを減
圧下に蒸留回収した。得られた反応生成物にメチルイソ
ブチルケトン1400部を加えて溶解させた後、30%
NaOH水溶液8.9部を加え70℃で1時間反応さ
せ、次に2回水洗し、油水分離後、油層からメチルイソ
ブチルケトンを留去してエポキシ当量325g/eq、
加水分解性塩素1060ppmなるエポキシ樹脂540
部を得た。得られたエポキシ樹脂はエポキシ当量から計
算すると式(1)におけるnは3.23であり、Xのう
ち69%がグリシジル基であり、軟化点は73.5℃、
150℃における溶融粘度は7.0psであった。得ら
れたエポキシ樹脂の物性等の測定結果は表2にまとめ
た。
Example 2 Example 1 except that the amount of bisphenol A was 136 parts.
Preliminary reaction is carried out in the same manner as above, and the epoxy equivalent is 629 g / e.
A q epoxy resin (32) (compound of formula (1A)) was obtained. When the obtained epoxy resin (32) was calculated from the epoxy equivalent, n in the formula (1A) was 3.23.
Further, the obtained epoxy resin (32) was dissolved in 1939 parts of epichlorohydrin, and then 6.6 parts of tetramethylammonium chloride was added at 40 ° C. to obtain 98.5% N.
63.8 parts of aOH was added over 90 minutes. 40 ° C
After reacting for 2 hours at 150 ° C., 150 parts of water was added and the mixture was washed twice with water. After separating the oil and water, epichlorohydrin was recovered from the oil layer by distillation under reduced pressure. After adding 1400 parts of methyl isobutyl ketone to the obtained reaction product and dissolving it, 30%
After adding 8.9 parts of NaOH aqueous solution and reacting at 70 ° C. for 1 hour, washing with water twice and separating oil / water, methyl isobutyl ketone was distilled off from the oil layer to obtain an epoxy equivalent of 325 g / eq,
Epoxy resin 540 with 1060 ppm hydrolyzable chlorine
I got a part. When the obtained epoxy resin was calculated from the epoxy equivalent, n in the formula (1) was 3.23, 69% of X was a glycidyl group, and the softening point was 73.5 ° C.
The melt viscosity at 150 ° C. was 7.0 ps. The measurement results of the physical properties and the like of the obtained epoxy resin are summarized in Table 2.

【0037】比較例2 実施例2の予備反応で得られたエポキシ樹脂(32)を
エピクロルヒドリン1939部に溶解させた後、60℃
でテトラメチルアンモニウムクロライド6.6部を添加
し、98.5%NaOH69.1部を90分かけて添加
した。更に40℃で2時間反応を行った後水126部を
加えて2回水洗を行った。油水分離後、油層よりエピク
ロルヒドリンを減圧下に蒸留回収して、エポキシ当量3
23g/eq、加水分解性塩素3020ppmなるエポ
キシ樹脂495部を得た。得られたエポキシ樹脂の軟化
点は73.7℃、150℃における溶融粘度は7.4p
sであった。得られたエポキシ樹脂の物性等の測定結果
は表2にまとめた。
Comparative Example 2 The epoxy resin (32) obtained in the preliminary reaction of Example 2 was dissolved in 1939 parts of epichlorohydrin, and then 60 ° C.
Then, 6.6 parts of tetramethylammonium chloride was added thereto, and 69.1 parts of 98.5% NaOH was added over 90 minutes. After the reaction was further performed at 40 ° C. for 2 hours, 126 parts of water was added and the mixture was washed twice with water. After separation of oil and water, epichlorohydrin was distilled and recovered from the oil layer under reduced pressure to obtain an epoxy equivalent of 3
There were obtained 495 parts of an epoxy resin having 23 g / eq and 3020 ppm of hydrolyzable chlorine. The softening point of the obtained epoxy resin is 73.7 ° C, and the melt viscosity at 150 ° C is 7.4p.
It was s. The measurement results of the physical properties and the like of the obtained epoxy resin are summarized in Table 2.

【0038】[0038]

【表2】 表2 実施例2 比較例2 エポキシ当量(g/eq) 325 323 エポキシ化率(%) 69 71 加水分解性塩素(ppm) 1060 3020 軟化点(℃) 73.5 73.7 溶融粘度(150℃,ps) 7.0 7.4 収率(%) 96.1 88.0[Table 2] Table 2 Example 2 Comparative Example 2 Epoxy equivalent (g / eq) 325 323 Epoxidation rate (%) 69 71 Hydrolyzable chlorine (ppm) 1060 3020 Softening point (° C) 73.5 73.7 Melt viscosity (150 ° C) , Ps) 7.0 7.4 Yield (%) 96.1 88.0

【0039】実施例3 実施例1に於てビスフェノールAの代わりにテトラブロ
モビスフェノールA207部を用いた以外は実施例1と
同様に予備反応を行い、エポキシ当量が468g/eq
のエポキシ樹脂(33)(式(1A)の化合物)を得
た。得られたエポキシ樹脂(33)はエポキシ当量から
計算すると式(1A)におけるnは1.44となった。
更に得られたエポキシ樹脂(33)エピクロルヒドリン
1319部に溶解させた後、40℃でテトラメチルアン
モニウムクロライド4.5部を添加し、98.5%Na
OH50.6部を90分かけて添加した。更に40℃で
2時間反応を行った後水117部を加えて2回水洗を行
った。油水分離後、油層よりエピクロルヒドリンを減圧
下に蒸留回収した。得られた反応生成物にメチルイソブ
チルケトン1238部を加えて溶解させた後、30%N
aOH水溶液12.1部を加え70℃で1時間反応さ
せ、次に水で2回水洗し、油水分離後、油層からメチル
イソブチルケトンを留去してエポキシ当量320g/e
q、加水分解性塩素1310ppmなるエポキシ樹脂6
65部を得た。得られたエポキシ樹脂はエポキシ当量か
ら計算すると式(1)におけるnは1.44であり、X
のうち78%がグリシジル基であり、軟化点は64.0
℃、150℃における溶融粘度は3.1psであった。
得られたエポキシ樹脂の物性等の測定結果は表3にまと
めた。
Example 3 Preliminary reaction was carried out in the same manner as in Example 1 except that 207 parts of tetrabromobisphenol A was used in place of bisphenol A in Example 1, and the epoxy equivalent was 468 g / eq.
To obtain an epoxy resin (33) (compound of formula (1A)). The n in the formula (1A) of the obtained epoxy resin (33) was 1.44 when calculated from the epoxy equivalent.
After further dissolving 1319 parts of the obtained epoxy resin (33) epichlorohydrin, 4.5 parts of tetramethylammonium chloride was added at 40 ° C., and 98.5% Na was added.
50.6 parts of OH were added over 90 minutes. After further reacting at 40 ° C. for 2 hours, 117 parts of water was added and washed twice with water. After separating the oil and water, epichlorohydrin was recovered from the oil layer by distillation under reduced pressure. After adding 1238 parts of methyl isobutyl ketone to the obtained reaction product and dissolving it, 30% N
12.1 parts of aOH aqueous solution was added and reacted at 70 ° C. for 1 hour, then washed twice with water, oil-water separation was performed, and methyl isobutyl ketone was distilled off from the oil layer to obtain an epoxy equivalent of 320 g / e.
q, Epoxy resin 6 containing 1310 ppm of hydrolyzable chlorine
Obtained 65 parts. When the obtained epoxy resin is calculated from the epoxy equivalent, n in the formula (1) is 1.44, and X is
Of these, 78% are glycidyl groups and have a softening point of 64.0.
The melt viscosity at 300C and 150C was 3.1 ps.
The measurement results of the physical properties and the like of the obtained epoxy resin are summarized in Table 3.

【0040】比較例3 実施例3の予備反応で得られたエポキシ樹脂(33)を
エピクロルヒドリン1319部に溶解させた後、60℃
でテトラメチルアンモニウムクロライド4.5部を添加
し、98.5%NaOH54.3部を90分かけて添加
した。更に40℃で2時間反応を行った後水117部を
加えて2回水洗を行った。油水分離後、油層よりエピク
ロルヒドリンを減圧下に蒸留回収して、エポキシ当量3
17g/eq、加水分解性塩素3920ppmなるエポ
キシ樹脂599部を得た。得られたエポキシ樹脂の軟化
点は63.5℃、150℃における溶融粘度は3.0p
sであった。得られたエポキシ樹脂の物性等の測定結果
は表3にまとめた。
Comparative Example 3 The epoxy resin (33) obtained in the preliminary reaction of Example 3 was dissolved in 1319 parts of epichlorohydrin, and then 60 ° C.
Then, 4.5 parts of tetramethylammonium chloride was added, and 54.3 parts of 98.5% NaOH was added over 90 minutes. After further reacting at 40 ° C. for 2 hours, 117 parts of water was added and washed twice with water. After separation of oil and water, epichlorohydrin was distilled and recovered from the oil layer under reduced pressure to obtain an epoxy equivalent of 3
Thus, 599 parts of an epoxy resin having 17 g / eq and 3920 ppm of hydrolyzable chlorine was obtained. The softening point of the obtained epoxy resin is 63.5 ° C, and the melt viscosity at 150 ° C is 3.0 p.
It was s. The measurement results of the physical properties and the like of the obtained epoxy resin are summarized in Table 3.

【0041】[0041]

【表3】 表3 実施例3 比較例3 エポキシ当量(g/eq) 320 317 エポキシ化率(%) 78 80 加水分解性塩素(ppm) 1310 3920 軟化点(℃) 64.0 63.5 溶融粘度(150℃,ps) 3.1 3.0 収率(%) 95.9 86.2[Table 3] Table 3 Example 3 Comparative Example 3 Epoxy equivalent (g / eq) 320 317 Epoxidation rate (%) 78 80 Hydrolyzable chlorine (ppm) 1310 3920 Softening point (° C) 64.0 63.5 Melt viscosity (150 ° C) , Ps) 3.1 3.0 Yield (%) 95.9 86.2

【発明の効果】本発明のエポキシ樹脂の製造方法は従来
の製造法と比較して収率が高いため工業的に有利であ
る。また本発明の製造方法で得られたエポキシ樹脂は、
加水分解性塩素量が低いため電気・電子材料などの用途
にきわめて有用である。
INDUSTRIAL APPLICABILITY The method for producing an epoxy resin of the present invention is industrially advantageous because it has a higher yield than conventional methods. Further, the epoxy resin obtained by the production method of the present invention,
The low hydrolyzable chlorine content makes it extremely useful for electrical and electronic materials.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】式(1A) 【化1】 (式中、nは正数を表し、Rは水素原子あるいは臭素原
子を表し、個々のRはお互いに同一であっても異なって
いてもよい。)で表される化合物とエピハロヒドリンを
アルカリ金属水酸化物の存在下50℃以下の温度で反応
させることを特徴とする式(1) 【化2】 (式中nは正数を表す。Rは水素原子あるいは臭素原子
を表し個々のRはお互いに同一であっても異なっていて
もよい。またXは水素原子あるいはグリシジル基を表し
個々のXはお互いに同一であっても異なっていてもよい
が、Xの10%以上95%以下はグリシジル基であ
る。)で表されるエポキシ樹脂の製造方法。
1. A formula (1A): (In the formula, n represents a positive number, R represents a hydrogen atom or a bromine atom, and each R may be the same or different from each other.) And epihalohydrin are combined with alkali metal water. Formula (1) characterized by reacting at a temperature of 50 ° C. or lower in the presence of an oxide (In the formula, n represents a positive number. R represents a hydrogen atom or a bromine atom, and each R may be the same or different from each other. X represents a hydrogen atom or a glycidyl group, and each X represents They may be the same or different, but 10% or more and 95% or less of X is a glycidyl group.).
【請求項2】臭素化されていてもよいビスフェノールA
型エポキシ樹脂と臭素化されていてもよいビスフェノー
ルAとを塩基性触媒の存在下に反応させ、次いで、反応
生成物とエピハロヒドリンをアルカリ金属水酸化物の存
在下50℃以下の温度で反応させることを特徴とする請
求項1の式(1)で表されるエポキシ樹脂の製造方法。
2. Bisphenol A which may be brominated
-Type epoxy resin and optionally brominated bisphenol A are reacted in the presence of a basic catalyst, and then the reaction product and epihalohydrin are reacted in the presence of an alkali metal hydroxide at a temperature of 50 ° C or lower. A method for producing an epoxy resin represented by the formula (1) according to claim 1.
JP14834893A 1993-05-28 1993-05-28 Production of epoxy resin Pending JPH06336516A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14834893A JPH06336516A (en) 1993-05-28 1993-05-28 Production of epoxy resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14834893A JPH06336516A (en) 1993-05-28 1993-05-28 Production of epoxy resin

Publications (1)

Publication Number Publication Date
JPH06336516A true JPH06336516A (en) 1994-12-06

Family

ID=15450758

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14834893A Pending JPH06336516A (en) 1993-05-28 1993-05-28 Production of epoxy resin

Country Status (1)

Country Link
JP (1) JPH06336516A (en)

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