JP2000143769A - Liquid epoxy resin, production of liquid epoxy resin, epoxy resin composition and its cured material - Google Patents

Liquid epoxy resin, production of liquid epoxy resin, epoxy resin composition and its cured material

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Publication number
JP2000143769A
JP2000143769A JP10318239A JP31823998A JP2000143769A JP 2000143769 A JP2000143769 A JP 2000143769A JP 10318239 A JP10318239 A JP 10318239A JP 31823998 A JP31823998 A JP 31823998A JP 2000143769 A JP2000143769 A JP 2000143769A
Authority
JP
Japan
Prior art keywords
epoxy resin
amount
hydrolyzable chlorine
formula
resin composition
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
JP10318239A
Other languages
Japanese (ja)
Inventor
Yasumasa Akatsuka
泰昌 赤塚
Koji Nakayama
幸治 中山
Katsuhiko Oshimi
克彦 押見
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 JP10318239A priority Critical patent/JP2000143769A/en
Publication of JP2000143769A publication Critical patent/JP2000143769A/en
Pending legal-status Critical Current

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  • Epoxy Resins (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the subject liquid resin capable of providing a solidified material having excellent heat resistance and water resistance, containing a small amount of hydrolyzable chlorine, having low viscosity, useful as an electric/electronic part by specifying the amount of hydrolyzable chlorine. SOLUTION: This resin comprises a compound of formula I having <=2,000 ppm hydrolyzable chlorine amount when refluxed in 1N solution of sodium hydroxide in ethanol for 30 minutes and titrated with 0.01N aqueous solution of silver nitrate. The resin is obtained by a method including a process for reacting a compound of formula II with an excessive epihalohydrin in the presence of a quaternary ammonium salt (e.g. tetramethylammonium chloride, etc.), and a solid alkali metal hydroxide (e.g. sodium hydroxide, etc.), at 20-70 deg.C with stirring, for example, for about 3-25 hours.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は耐熱性、耐水性に優
れる硬化物を与え、しかも粘度が低く加水分解性塩素量
の少ない液状エポキシ樹脂及びその製造方法、該エポキ
シ樹脂を含有するエポキシ樹脂組成物及びその硬化物に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid epoxy resin which provides a cured product having excellent heat resistance and water resistance, has a low viscosity and a small amount of hydrolyzable chlorine, a process for producing the same, and an epoxy resin composition containing the epoxy resin. And a cured product thereof.

【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、電気的性質などに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、液状エポキシ樹脂組成物
において、エポキシ樹脂としては液状のビスフェノ−ル
A型エポキシ樹脂が最も一般的に使用されている。更に
低粘度が要求される分野等においては水添化されたビス
フェノールAをジグリシジルエーテル化した液状エポキ
シ樹脂が広く知られている。水添化ビスフェノールA型
エポキシ樹脂は、原料の水添加ビスフェノールAのエピ
ハロヒドリンに対する反応性が極めて低く、溶剤溶解性
も非常に低いため、例えば三フッ化ホウ素錯体等のルイ
ス酸触媒を用いて、エピハロヒドリンをアルコール性水
酸基に付加させた後、アルカリ金属水酸化物を添加し、
脱塩酸反応により製造するといった方法が従来採用され
ていた。
2. Description of the Related Art Epoxy resins can be cured with various curing agents to give cured products having generally excellent mechanical properties, water resistance, chemical resistance, heat resistance, and electrical properties. It is used in a wide range of fields, such as laminates, molding materials, and casting materials. Conventionally, in a liquid epoxy resin composition, a liquid bisphenol A type epoxy resin is most generally used as an epoxy resin. In fields where low viscosity is required, liquid epoxy resins obtained by diglycidyl etherification of hydrogenated bisphenol A are widely known. Hydrogenated bisphenol A type epoxy resin has extremely low reactivity of raw material hydrogenated bisphenol A with epihalohydrin and very low solvent solubility. For example, epihalohydrin using a Lewis acid catalyst such as boron trifluoride complex is used. Is added to the alcoholic hydroxyl group, then an alkali metal hydroxide is added,
Conventionally, a method of producing by a dehydrochlorination reaction has been employed.

【0003】[0003]

【発明が解決しようとする課題】しかしながら前記のよ
うな製法では三フッ化ホウ素錯体のような酸化力の強い
触媒を用いるため危険性を伴い、更に得られたエポキシ
樹脂は、加水分解性塩素量が前記の方法で2〜5%と非
常に高いため、高信頼性を要求される電気・電子部品の
分野での使用は極めて限定されたものにならざるを得な
かった。
However, the above-mentioned production method involves a danger since a catalyst having a strong oxidizing power such as a boron trifluoride complex is used, and the obtained epoxy resin has a low hydrolyzable chlorine content. Is very high, 2 to 5% by the above method, so that its use in the field of electric and electronic parts that require high reliability has to be extremely limited.

【0004】[0004]

【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、加水分解性塩素量が低く低粘度な液状エポキ
シ樹脂を求めて鋭意研究した結果、本発明を完成させる
に到った。
Means for Solving the Problems In view of such circumstances, the present inventors have intensively studied for a liquid epoxy resin having a low amount of hydrolyzable chlorine and a low viscosity, and as a result, have completed the present invention.

【0005】すなわち本発明は(1)式(1)That is, the present invention provides the following equation (1).

【0006】[0006]

【化3】 Embedded image

【0007】で表される化合物であって、1N水酸化カ
リウムのエタノール溶液中で30分間還流して0.01
N硝酸銀水溶液で滴定した場合の加水分解性塩素量が2
000ppm以下であるエポキシ樹脂、
A compound represented by the following formula:
The amount of hydrolyzable chlorine when titrated with an N silver nitrate aqueous solution is 2
Epoxy resin not more than 000 ppm,

【0008】(2)式(2)(2) Equation (2)

【0009】[0009]

【化4】 Embedded image

【0010】で表される化合物とエピハロヒドリンを4
級アンモニウム塩及び固形のアルカリ金属水酸化物の共
存下で20〜70℃で撹拌し反応る工程を含むエポキシ
樹脂の製造方法、
And a compound represented by the formula
A method for producing an epoxy resin comprising a step of stirring and reacting at 20 to 70 ° C. in the presence of a quaternary ammonium salt and a solid alkali metal hydroxide,

【0011】(3)(a)上記(1)記載或いは(2)
記載の製造方法で得られるエポキシ樹脂 (b)硬化剤を含有してなるエポキシ樹脂組成物、
(3)硬化促進剤を含有する上記(2)記載のエポキシ
樹脂組成物、(4)上記(2)または(3)記載のエポ
キシ樹脂組成物を硬化してなる硬化物を提供するもので
ある。
(3) (a) The above (1) or (2)
Epoxy resin obtained by the production method described above, (b) an epoxy resin composition containing a curing agent,
(3) An epoxy resin composition according to the above (2) containing a curing accelerator, and (4) a cured product obtained by curing the epoxy resin composition according to the above (2) or (3). .

【0012】[0012]

【発明の実施の形態】本発明のエポキシ樹脂は、前記式
(2)で表される化合物とエピハロヒドリンとを固形の
アルカリ金属水酸化物及び4級アンモニウム塩の共存下
で反応させることにより得ることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The epoxy resin of the present invention is obtained by reacting a compound represented by the formula (2) with epihalohydrin in the presence of a solid alkali metal hydroxide and a quaternary ammonium salt. Can be.

【0013】本発明のエポキシ樹脂の製造方法におい
て、固形のアルカリ金属水酸化物としては水酸化ナトリ
ウム、或は水酸化カリウム等が挙げられるが、特に水酸
化ナトリウムが好ましい。その形状としてはフレーク
状、マーブル状などがあるがフレーク状が好ましい。該
アルカリ金属水酸化物の使用量は式(2)で表される化
合物のアルコール性水酸基1当量に対し通常1〜5モ
ル、好ましくは1.5〜4モルである。
In the method for producing an epoxy resin of the present invention, the solid alkali metal hydroxide may be sodium hydroxide or potassium hydroxide, but sodium hydroxide is particularly preferred. Examples of the shape include a flake shape and a marble shape, but a flake shape is preferable. The amount of the alkali metal hydroxide to be used is generally 1 to 5 mol, preferably 1.5 to 4 mol, per 1 equivalent of the alcoholic hydroxyl group of the compound represented by the formula (2).

【0014】また、触媒として用いられる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、トリエチルベンジルアン
モニウムクロライド等が挙げられる。4級アンモニウム
塩の使用量は式(2)で表される化合物の量に対し通常
0.1〜5重量%、好ましくは0.2〜3重量%であ
る。
The quaternary ammonium salt used as a catalyst includes tetramethylammonium chloride,
Examples thereof include tetramethylammonium bromide, trimethylbenzylammonium chloride, and triethylbenzylammonium chloride. The amount of the quaternary ammonium salt to be used is generally 0.1 to 5% by weight, preferably 0.2 to 3% by weight, based on the amount of the compound represented by the formula (2).

【0015】エピハロヒドリンの使用量は式(2)で表
される化合物の水酸基1当量に対し通常1〜20モル、
好ましくは2〜10モルである。
The amount of epihalohydrin used is usually 1 to 20 mol per 1 equivalent of the hydroxyl group of the compound represented by the formula (2),
Preferably it is 2 to 10 mol.

【0016】反応はこれらの成分を反応器に同時に仕込
み、一定時間撹拌して行う。個々の固形成分は始めは溶
解せずに不均一の状態だが、徐々に一部が溶解し始め反
応が進行する。反応時間としては3〜25時間が好まし
く、5〜20時間がより好ましい。反応温度は、20〜
70℃であるが、25〜65℃が好ましい。
The reaction is carried out by simultaneously charging these components into a reactor and stirring for a certain period of time. The individual solid components are not dissolved at first and are in an inhomogeneous state, but a part of them is gradually dissolved and the reaction proceeds. The reaction time is preferably 3 to 25 hours, more preferably 5 to 20 hours. The reaction temperature is between 20 and
The temperature is 70C, but preferably 25-65C.

【0017】反応終了後、反応液から濾過、及び/また
は水洗等により生成塩、反応触媒等を除去し、加熱減圧
下、100〜150℃、圧力10mmHg以下でエピハ
ロヒドリン等を除去し本発明のエポキシ樹脂を得ること
ができる。こうして得られた本発明のエポキシ樹脂の加
水分解性塩素は、通常2000ppm以下、好ましい条
件下で得られたものは1800ppm以下となる。尚、
加水分解性塩素は、通常、樹脂を溶剤に溶解し、これに
アルカリ(KOHまたはNaOH)をアルコール等に溶
解した所定の規定液を所定量加えた後、所定温度で所定
時間反応させて塩素を分解(抽出)し、これを所定規定
度の硝酸銀溶液で電位差滴定して測定される。この方法
により測定される加水分解性塩素量は、塩素を分解する
温度や時間により異なり、例えばEOCN−1027
(商品名、o−クレゾールノボラック型エポキシ樹脂、
日本化薬(株)製)を例にとり、測定法による加水分解
性量の違いを下表に示す。
After completion of the reaction, the salt formed, the reaction catalyst, etc. are removed from the reaction solution by filtration and / or water washing, and epihalohydrin and the like are removed under heating and reduced pressure at 100 to 150 ° C. and a pressure of 10 mmHg or less. A resin can be obtained. The thus obtained hydrolyzable chlorine of the epoxy resin of the present invention is usually 2000 ppm or less, and that obtained under preferable conditions is 1800 ppm or less. still,
The hydrolyzable chlorine is usually obtained by dissolving a resin in a solvent, adding a predetermined amount of a predetermined solution obtained by dissolving an alkali (KOH or NaOH) in an alcohol or the like, and reacting at a predetermined temperature for a predetermined time to remove chlorine. Decomposition (extraction) is measured by potentiometric titration with a silver nitrate solution having a predetermined normality. The amount of hydrolyzable chlorine measured by this method varies depending on the temperature and time at which chlorine is decomposed. For example, EOCN-1027
(Product name, o-cresol novolak type epoxy resin,
Taking Nippon Kayaku Co., Ltd.) as an example, the difference in the amount of hydrolyzability according to the measurement method is shown in the table below.

【0018】[0018]

【表1】 (1) (2) 樹脂溶解溶媒 メチルエチルケトン ジオキサン 滴定溶液 3N NaOH− 1N KOH− エチレングリコール メタノール モノブチルエーテル 分解温度 室温 環流 分解時間 2時間 30分 加水分解性塩素量 最大10 最大100 (ppm) (3) (4) 樹脂溶解溶媒 ジオキサン ジオキサン 滴定溶液 1N KOH− 1N KOH− エタノール エタノール 分解温度 環流 環流 分解時間 30分 3時間 加水分解性塩素量 80〜150 240〜310 (ppm) (新保正樹編「エポキシ樹脂ハンドブック」(日刊工業新聞社))Table 1 (1) (2) Resin dissolving solvent Methyl ethyl ketone Dioxane Titration solution 3N NaOH-1N KOH-Ethylene glycol methanol Monobutyl ether Decomposition temperature Room temperature Reflux Decomposition time 2 hours 30 minutes Hydrolytic chlorine content Max. (3) (4) Resin dissolving solvent dioxane dioxane titration solution 1N KOH-1N KOH-ethanol ethanol Epoxy Resin Handbook "(Nikkan Kogyo Shimbun)

【0019】このように分解条件が穏和な(1)の方法
(ISO法)では、他の方法に較べ加水分解性塩素量が
1オーダー小さく出る傾向があり、このほかのエポキシ
樹脂についても下表に示すように同様な現象が知られて
いる。
As described above, in the method (1) in which the decomposition conditions are mild (ISO method), the amount of hydrolyzable chlorine tends to be smaller by one order than in the other methods. A similar phenomenon is known as shown in FIG.

【0020】[0020]

【表2】 分析条件 (1) (2) (3) (4) エポキシ樹脂 EOCN-1020 最大10 150〜200 330〜400 550〜700 EOCN-1025 最大10 最大100 180〜250 340〜410 EOCN-102S 最大30 250〜400 700〜800 1000〜1200 注)表中、エポキシ樹脂はいずれもo−クレゾールノボラック型エポキシ樹脂、 日本化薬(株)製。また数値は加水分解性塩素量(ppm)を表す。 (新保正樹編「エポキシ樹脂ハンドブック」(日刊工業新聞社))[Table 2] Analysis conditions (1) (2) (3) (4) Epoxy resin EOCN-1020 max. 10 150-200 330-400 550-700 EOCN-1025 max. 10 max. 100 180-250 340-410 EOCN-102S Maximum 30 250-400 700-800 1000-1200 Note) In the table, all epoxy resins are o-cresol novolak type epoxy resin, manufactured by Nippon Kayaku Co., Ltd. The numerical values represent the amount of hydrolyzable chlorine (ppm). (Epoxy Resin Handbook, edited by Masaki Shinbo (Nikkan Kogyo Shimbun))

【0021】このように測定条件により加水分解性塩素
量は異なるが、本発明のエポキシ樹脂の加水分解性塩素
量は溶媒に溶解した樹脂を1N水酸化カリウムのエタノ
ール溶液中で30分間還流して0.01N硝酸銀水溶液
で滴定した場合(3)の方法により測定された加水分解
性塩素量をさす。
As described above, the amount of hydrolyzable chlorine varies depending on the measurement conditions, but the amount of hydrolyzable chlorine in the epoxy resin of the present invention is determined by refluxing the resin dissolved in a solvent in a 1N potassium hydroxide ethanol solution for 30 minutes. It refers to the amount of hydrolyzable chlorine measured by the method of (3) when titrated with a 0.01 N silver nitrate aqueous solution.

【0022】また更に加水分解性塩素量の少ないエポキ
シ樹脂とするために、回収したエポキシ樹脂を再びトル
エン、メチルイソブチルケトン、メチルエチルケトンな
どの溶剤に溶解し、水酸化ナトリウム、水酸化カリウム
などのアルカリ金属水酸化物の水溶液を加えて更に反応
を行い閉環を確実なものにすることもできる。この場合
アルカリ金属水酸化物の使用量はエポキシ化に使用した
フェノール樹脂の水酸基1当量に対して好ましくは0.
01〜0.3モル、特に好ましくは0.05〜0.2モ
ルである。反応温度は50〜120℃、反応時間は通常
0.5〜2時間である。反応終了後、生成した塩等を濾
過または水洗などにより除去し、更に加熱減圧下トルエ
ン、メチルイソブチルケトン、メチルエチルケトンなど
の溶剤を留去することにより加水分解性塩素量の少ない
本発明のエポキシ樹脂が得られる。このように精製処理
したエポキシ樹脂の加水分解性塩素量は通常1800p
pm以下、好ましい条件下で得られたものは1500p
pm以下となる。
In order to further reduce the amount of hydrolyzable chlorine to an epoxy resin, the recovered epoxy resin is dissolved again in a solvent such as toluene, methyl isobutyl ketone, methyl ethyl ketone and the like. An aqueous solution of a hydroxide may be added for further reaction to ensure ring closure. In this case, the amount of the alkali metal hydroxide used is preferably 0.1 to 1 equivalent of the hydroxyl group of the phenol resin used for the epoxidation.
The amount is from 0.01 to 0.3 mol, particularly preferably from 0.05 to 0.2 mol. The reaction temperature is 50 to 120 ° C, and the reaction time is usually 0.5 to 2 hours. After the completion of the reaction, the formed salts and the like are removed by filtration or washing with water, etc., and the epoxy resin of the present invention having a small amount of hydrolyzable chlorine is obtained by distilling off solvents such as toluene, methyl isobutyl ketone and methyl ethyl ketone under reduced pressure under heating. can get. The amount of hydrolyzable chlorine in the epoxy resin thus purified is usually 1800 p.
pm or less, obtained under preferable conditions is 1500p
pm or less.

【0023】以下、本発明のエポキシ樹脂組成物につい
て説明する。前記(2)、(3)記載のエポキシ樹脂組
成物において本発明のエポキシ樹脂は単独でまた他のエ
ポキシ樹脂と併用して使用することが出来る。併用する
場合、本発明のエポキシ樹脂の全エポキシ樹脂中に占め
る割合は10重量%以上が好ましく、特に20重量%以
上が好ましい。本発明のエポキシ樹脂と併用しうる他の
エポキシ樹脂としてはノボラック型エポキシ樹脂、ビス
フェノールA型エポキシ樹脂、ビスフェノールF型エポ
キシ樹脂、ビフェニル型エポキシ樹脂などが挙げられる
がこれらは単独で用いてもよく、2種以上併用してもよ
い。
Hereinafter, the epoxy resin composition of the present invention will be described. In the epoxy resin compositions described in the above (2) and (3), the epoxy resin of the present invention can be used alone or in combination with another epoxy resin. When used in combination, the proportion of the epoxy resin of the present invention in the total epoxy resin is preferably at least 10% by weight, particularly preferably at least 20% by weight. Other epoxy resins that can be used in combination with the epoxy resin of the present invention include novolak type epoxy resin, bisphenol A type epoxy resin, bisphenol F type epoxy resin, biphenyl type epoxy resin and the like, but these may be used alone. Two or more kinds may be used in combination.

【0024】本発明のエポキシ樹脂組成物において使用
される硬化剤としては、例えばアミン系化合物、酸無水
物系化合物、アミド系化合物、フェノ−ル系化合物など
が使用できる。用い得る硬化剤の具体例としては、ジア
ミノジフェニルメタン、ジエチレントリアミン、トリエ
チレンテトラミン、ジアミノジフェニルスルホン、イソ
ホロンジアミン、ジシアンジアミド、リノレン酸の2量
体とエチレンジアミンとより合成されるポリアミド樹
脂、無水フタル酸、無水トリメリット酸、無水ピロメリ
ット酸、無水マレイン酸、テトラヒドロ無水フタル酸、
メチルテトラヒドロ無水フタル酸、無水メチルナジック
酸、ヘキサヒドロ無水フタル酸、メチルヘキサヒドロ無
水フタル酸、フェノ−ルノボラック、及びこれらの変性
物、イミダゾ−ル、BF3 −アミン錯体、グアニジン誘
導体などが挙げられるがこれらに限定されるものではな
い。これらは単独で用いてもよく、2種以上併用しても
よい。
As the curing agent used in the epoxy resin composition of the present invention, for example, amine compounds, acid anhydride compounds, amide compounds, phenol compounds and the like can be used. Specific examples of the curing agent that can be used include diaminodiphenylmethane, diethylenetriamine, triethylenetetramine, diaminodiphenylsulfone, isophoronediamine, dicyandiamide, a polyamide resin synthesized from a dimer of linolenic acid and ethylenediamine, phthalic anhydride, and trianhydride. Melitic acid, pyromellitic anhydride, maleic anhydride, tetrahydrophthalic anhydride,
Methyltetrahydrophthalic anhydride, methylnadic anhydride, hexahydrophthalic anhydride, methylhexahydrophthalic anhydride, phenol novolak, and modified products thereof, imidazole, BF 3 -amine complex, guanidine derivative and the like. It is not limited to these. These may be used alone or in combination of two or more.

【0025】本発明のエポキシ樹脂組成物において硬化
剤の使用量は、エポキシ樹脂のエポキシ基1当量に対し
て0.7〜1.2当量が好ましい。エポキシ基1当量に
対して、0.7当量に満たない場合、あるいは1.2当
量を超える場合、いずれも硬化が不完全となり良好な硬
化物性が得られない恐れがある。
The amount of the curing agent used in the epoxy resin composition of the present invention is preferably 0.7 to 1.2 equivalents per equivalent of the epoxy group of the epoxy resin. If the amount is less than 0.7 equivalents or more than 1.2 equivalents with respect to 1 equivalent of epoxy group, curing may be incomplete and good cured physical properties may not be obtained.

【0026】また上記硬化剤を用いる際に硬化促進剤を
併用しても差し支えない。用いうる硬化促進剤の具体例
としては例えば2−メチルイミダゾール、2−エチルイ
ミダゾール、2−エチル−4−メチルイミダゾール等の
イミダゾ−ル類、2−(ジメチルアミノメチル)フェノ
ール、1,8−ジアザ−ビシクロ(5,4,0)ウンデ
セン−7等の第3級アミン類、トリフェニルホスフィン
等のホスフィン類、オクチル酸スズ等の金属化合物等が
挙げられる。硬化促進剤はエポキシ樹脂100重量部に
対して0.1〜5.0重量部が必要に応じ用いられる。
When the above curing agent is used, a curing accelerator may be used in combination. Specific examples of the curing accelerator that can be used include, for example, imidazoles such as 2-methylimidazole, 2-ethylimidazole, 2-ethyl-4-methylimidazole, 2- (dimethylaminomethyl) phenol, and 1,8-diaza. Tertiary amines such as -bicyclo (5,4,0) undecene-7; phosphines such as triphenylphosphine; and metal compounds such as tin octylate. The curing accelerator is used in an amount of 0.1 to 5.0 parts by weight based on 100 parts by weight of the epoxy resin as required.

【0027】本発明のエポキシ樹脂は必要により無機充
填材を含有する。用いうる無機充填材の具体例としては
シリカ、アルミナ、タルク等が挙げられる。無機充填材
は本発明のエポキシ樹脂組成物中において0〜90重量
%を占める量が用いられる。更に本発明のエポキシ樹脂
組成物には、シランカップリング剤、ステアリン酸、パ
ルミチン酸、ステアリン酸亜鉛、ステアリン酸カルシウ
ム等の離型剤、顔料等の種々の配合剤を添加することが
できる。
The epoxy resin of the present invention optionally contains an inorganic filler. Specific examples of the inorganic filler that can be used include silica, alumina, and talc. The inorganic filler is used in an amount occupying 0 to 90% by weight in the epoxy resin composition of the present invention. Further, to the epoxy resin composition of the present invention, various compounding agents such as a silane coupling agent, a release agent such as stearic acid, palmitic acid, zinc stearate, and calcium stearate, and a pigment can be added.

【0028】本発明のエポキシ樹脂組成物は、各成分を
均一に混合することにより得られる。本発明のエポキシ
樹脂組成物は従来知られている方法と同様の方法で容易
に硬化物とすることができる。例えば本発明のエポキシ
樹脂と硬化剤、必要により硬化促進剤及び無機充填材等
を必要に応じて押出機、ニ−ダ、ロ−ル等を用いて均一
になるまで充分に混合してエポキシ樹脂組成物を得、そ
のエポキシ樹脂組成物を溶融後注型あるいはトランスフ
ァ−成形機などを用いて成形し、さらに80〜200℃
で2〜10時間加熱することにより本発明の硬化物を得
ることができる。
The epoxy resin composition of the present invention can be obtained by uniformly mixing the components. The epoxy resin composition of the present invention can be easily made into a cured product by a method similar to a conventionally known method. For example, the epoxy resin of the present invention is thoroughly mixed with the epoxy resin of the present invention, a curing agent, if necessary, a curing accelerator, an inorganic filler, and the like, using an extruder, a kneader, a roll, or the like, as necessary, until the epoxy resin becomes uniform. A composition is obtained, and the epoxy resin composition is melted and then molded using a casting or transfer molding machine.
For 2 to 10 hours to obtain the cured product of the present invention.

【0029】また本発明のエポキシ樹脂組成物をトルエ
ン、キシレン、アセトン、メチルエチルケトン、メチル
イソブチルケトン等の溶剤に溶解させ、ガラス繊維、カ
−ボン繊維、ポリエステル繊維、ポリアミド繊維、アル
ミナ繊維、紙などの基材に含浸させ加熱乾燥して得たプ
リプレグを熱プレス成形して硬化物を得ることもでき
る。この際の溶剤は、本発明のエポキシ樹脂組成物と該
溶剤の混合物中で通常10〜70重量%、好ましくは1
5〜70重量%、このましくは15〜65重量%を占め
る量を用いる。
Further, the epoxy resin composition of the present invention is dissolved in a solvent such as toluene, xylene, acetone, methyl ethyl ketone, methyl isobutyl ketone, etc., and is used to prepare glass fiber, carbon fiber, polyester fiber, polyamide fiber, alumina fiber, paper, etc. A prepreg obtained by impregnating a substrate and drying by heating may be subjected to hot press molding to obtain a cured product. The solvent in this case is usually 10 to 70% by weight, preferably 1% by weight in the mixture of the epoxy resin composition of the present invention and the solvent.
An amount occupying 5 to 70% by weight, preferably 15 to 65% by weight, is used.

【0030】[0030]

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

【0031】実施例1 温度計、滴下ロート、冷却管、撹拌器を取り付けたフラ
スコに窒素ガスパージを施しながら前記式(2)で表さ
れる結晶性化合物120部、フレーク状水酸化ナトリウ
ム80部、トリエチルベンジルアンモニウムクロライド
1.2部及びエピクロルヒドリン370部を同時に仕込
み40℃に加熱し、その後15時間40℃で撹拌を続け
た。反応終了後濾過し生成塩などを除去した後、水洗を
1回行い4級アンモニウム塩等を除去した。ロータリー
エバポレーターを使用し、130℃で加熱減圧下で過剰
のエピクロルヒドリン等を留去し、残留物に352部の
メチルイソブチルケトンを加え溶解した。
Example 1 A nitrogen gas purge was applied to a flask equipped with a thermometer, a dropping funnel, a cooling tube, and a stirrer, while 120 parts of the crystalline compound represented by the above formula (2), 80 parts of flaky sodium hydroxide, 1.2 parts of triethylbenzylammonium chloride and 370 parts of epichlorohydrin were simultaneously charged and heated to 40 ° C, and thereafter, stirring was continued at 40 ° C for 15 hours. After completion of the reaction, the resultant was filtered to remove generated salts and the like, and washed once with water to remove quaternary ammonium salts and the like. Using a rotary evaporator, excess epichlorohydrin and the like were distilled off under heating and reduced pressure at 130 ° C., and 352 parts of methyl isobutyl ketone were added to the residue and dissolved.

【0032】更にこのメチルイソブチルケトンの溶液を
70℃に加熱し30重量%の水酸化ナトリウム水溶液1
0部を添加し1時間反応させた後、反応混合物の水洗浄
液のpHが中性となるまで水洗を繰り返した。更に水層
は分離除去し、ロータリエバポレーターを使用して油層
から加熱減圧下メチルイソブチルケトンを留去し、前記
式(1)で表される本発明のエポキシ樹脂(A)127
部を得た。得られたエポキシ樹脂は黄色の液状であり2
5℃での粘度は1470cps、エポキシ当量は218
g/eqであった。また加水分解性塩素量につき、得ら
れたエポキシ樹脂をジオキサンに溶解して、1Nの水酸
化カリウム /エタノール溶液で30分間還流下で加水
分解した後、0.01Nの硝酸銀水溶液で滴定を行い測
定したところ630ppmであった。
Further, the solution of methyl isobutyl ketone was heated to 70 ° C., and a 30% by weight aqueous sodium hydroxide solution 1 was added.
After adding 0 parts and reacting for 1 hour, washing with water was repeated until the pH of the washing solution of the reaction mixture became neutral. Further, the aqueous layer was separated and removed, and methyl isobutyl ketone was distilled off from the oil layer under reduced pressure by heating using a rotary evaporator to obtain the epoxy resin (A) 127 of the present invention represented by the above formula (1).
Got a part. The obtained epoxy resin is a yellow liquid and has 2
The viscosity at 5 ° C. is 1470 cps, and the epoxy equivalent is 218.
g / eq. The amount of hydrolyzable chlorine was measured by dissolving the obtained epoxy resin in dioxane, hydrolyzing with a 1N potassium hydroxide / ethanol solution under reflux for 30 minutes, and then titrating with a 0.01N silver nitrate aqueous solution. As a result, it was 630 ppm.

【0033】実施例2 フレーク状水酸化ナトリウムの量を120部にした以外
は実施例1と同様に反応を行い前記式(1)で表される
本発明のエポキシ樹脂(B)152部を得た。得られた
エポキシ樹脂は黄色の液状であり25℃での粘度は87
0cps、エポキシ当量は201g/eqであった。ま
た加水分解性塩素量につき、実施例1と同様にして測定
したところ710ppmであった。
Example 2 A reaction was carried out in the same manner as in Example 1 except that the amount of the flaky sodium hydroxide was changed to 120 parts to obtain 152 parts of the epoxy resin (B) of the present invention represented by the above formula (1). Was. The obtained epoxy resin is a yellow liquid and has a viscosity of 87 at 25 ° C.
0 cps and the epoxy equivalent was 201 g / eq. The amount of hydrolyzable chlorine was measured in the same manner as in Example 1 and found to be 710 ppm.

【0034】比較例1 比較例として市販の水添ビスフェノールA型エポキシ樹
脂(旭電化製、商品名EP−4080、エポキシ樹脂
(C))の樹脂物性を同様にして測定した。エポキシ樹
脂(C)の25℃における粘度は2100cps、エポ
キシ当量は237g/eqであり、実施例1と同様にし
て加水分解性塩素量を測定した値は39000ppmで
あった。
Comparative Example 1 As a comparative example, the resin properties of a commercially available hydrogenated bisphenol A type epoxy resin (trade name: EP-4080, manufactured by Asahi Denka, epoxy resin (C)) were measured in the same manner. The viscosity at 25 ° C. of the epoxy resin (C) was 2100 cps, the epoxy equivalent was 237 g / eq, and the value of the amount of hydrolyzable chlorine measured in the same manner as in Example 1 was 39000 ppm.

【0035】[0035]

【発明の効果】本発明のエポキシ樹脂は、従来一般的に
使用されてきた水添ビスフェノールA型エポキシ樹脂と
比較して純度が極めて高いため信頼性に優れた硬化物を
与えることができ、成形材料、注型材料、積層材料、塗
料、接着剤、レジストなどの広範囲の用途にきわめて有
用である。
The epoxy resin of the present invention has an extremely high purity as compared with the conventionally used hydrogenated bisphenol A type epoxy resin, so that a cured product having excellent reliability can be obtained. It is extremely useful in a wide range of applications such as materials, casting materials, laminate materials, paints, adhesives, resists, and the like.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】式(1) 【化1】 で表される化合物であって、1N水酸化カリウムのエタ
ノール溶液中で30分間還流して0.01N硝酸銀水溶
液で滴定した場合の加水分解性塩素量が2000ppm
以下であるエポキシ樹脂。
(1) Formula (1) Wherein the amount of hydrolyzable chlorine is 2,000 ppm when refluxed in a 1N potassium hydroxide ethanol solution for 30 minutes and titrated with a 0.01 N silver nitrate aqueous solution.
An epoxy resin that is:
【請求項2】式(2) 【化2】 で表される化合物と過剰のエピハロヒドリンを4級アン
モニウム塩及び固形のアルカリ金属水酸化物の共存下で
20〜70℃で撹拌し反応させる工程を含むエポキシ樹
脂の製造方法。
(2) Formula (2) A method for producing an epoxy resin comprising a step of reacting the compound represented by the formula (1) with an excess epihalohydrin in the presence of a quaternary ammonium salt and a solid alkali metal hydroxide at 20 to 70 ° C with stirring.
【請求項3】(a)請求項1記載或いは請求項2記載の
製造方法で得られたエポキシ樹脂 (b)硬化剤を含有してなるエポキシ樹脂組成物。
3. An epoxy resin composition comprising (a) an epoxy resin obtained by the method according to claim 1 or (b) and (b) a curing agent.
【請求項4】硬化促進剤を含有する請求項3記載のエポ
キシ樹脂組成物。
4. The epoxy resin composition according to claim 3, further comprising a curing accelerator.
【請求項5】請求項2または3記載のエポキシ樹脂組成
物を硬化してなる硬化物。
5. A cured product obtained by curing the epoxy resin composition according to claim 2 or 3.
JP10318239A 1998-11-10 1998-11-10 Liquid epoxy resin, production of liquid epoxy resin, epoxy resin composition and its cured material Pending JP2000143769A (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
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Publication Number Publication Date
JP2000143769A true JP2000143769A (en) 2000-05-26

Family

ID=18096988

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002308963A (en) * 2001-04-11 2002-10-23 Nippon Kayaku Co Ltd Process for producing epoxy resin
US6998463B2 (en) 2001-02-06 2006-02-14 Mitsubishi Chemical Corporation Polyester resin and process for its production
WO2008068205A1 (en) * 2006-12-07 2008-06-12 Basf Se Epoxy resin compositions and method for the production thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5731921A (en) * 1980-08-01 1982-02-20 Dainippon Ink & Chem Inc Production of epoxy compound
JPH04142326A (en) * 1990-10-04 1992-05-15 Nippon Kayaku Co Ltd Epoxy resin and its production
JPH06136092A (en) * 1992-10-27 1994-05-17 New Japan Chem Co Ltd Epoxy resin composition
JPH08134178A (en) * 1994-11-10 1996-05-28 New Japan Chem Co Ltd Photocurable epoxy resin composition
JPH107761A (en) * 1996-06-21 1998-01-13 Asahi Denka Kogyo Kk Production of aliphatic polyglycidyl ether
JPH11199645A (en) * 1998-01-16 1999-07-27 Mitsubishi Chemical Corp Epoxy resin composition

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5731921A (en) * 1980-08-01 1982-02-20 Dainippon Ink & Chem Inc Production of epoxy compound
JPH04142326A (en) * 1990-10-04 1992-05-15 Nippon Kayaku Co Ltd Epoxy resin and its production
JPH06136092A (en) * 1992-10-27 1994-05-17 New Japan Chem Co Ltd Epoxy resin composition
JPH08134178A (en) * 1994-11-10 1996-05-28 New Japan Chem Co Ltd Photocurable epoxy resin composition
JPH107761A (en) * 1996-06-21 1998-01-13 Asahi Denka Kogyo Kk Production of aliphatic polyglycidyl ether
JPH11199645A (en) * 1998-01-16 1999-07-27 Mitsubishi Chemical Corp Epoxy resin composition

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6998463B2 (en) 2001-02-06 2006-02-14 Mitsubishi Chemical Corporation Polyester resin and process for its production
JP2002308963A (en) * 2001-04-11 2002-10-23 Nippon Kayaku Co Ltd Process for producing epoxy resin
JP4674884B2 (en) * 2001-04-11 2011-04-20 日本化薬株式会社 Production method of epoxy resin
WO2008068205A1 (en) * 2006-12-07 2008-06-12 Basf Se Epoxy resin compositions and method for the production thereof
JP2010511758A (en) * 2006-12-07 2010-04-15 ビーエーエスエフ ソシエタス・ヨーロピア Epoxy resin composition and production method thereof
US8399596B2 (en) 2006-12-07 2013-03-19 Basf Aktiengesellschaft Epoxy resin compositions and process for preparing them

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