JPH05320294A - Modified phenolic resin composition and production thereof - Google Patents

Modified phenolic resin composition and production thereof

Info

Publication number
JPH05320294A
JPH05320294A JP4133895A JP13389592A JPH05320294A JP H05320294 A JPH05320294 A JP H05320294A JP 4133895 A JP4133895 A JP 4133895A JP 13389592 A JP13389592 A JP 13389592A JP H05320294 A JPH05320294 A JP H05320294A
Authority
JP
Japan
Prior art keywords
phenols
tung oil
phenolic resin
phenol
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
JP4133895A
Other languages
Japanese (ja)
Inventor
Masayuki Kojima
正之 小島
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.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite 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 Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP4133895A priority Critical patent/JPH05320294A/en
Publication of JPH05320294A publication Critical patent/JPH05320294A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/03Use of materials for the substrate
    • H05K1/0313Organic insulating material
    • H05K1/032Organic insulating material consisting of one material
    • H05K1/0326Organic insulating material consisting of one material containing O

Landscapes

  • Phenolic Resins Or Amino Resins (AREA)

Abstract

PURPOSE:To obtain a modified phenolic resin compsn. capable of forming a cured product very excellent in flexibility, toughness and electrical properties, suitable for use in phenolic resin laminates, composite materials and coatings and as an industrial resin, and very useful in a phenolic resin laminate for use in a printed wiring board in particular, by using a highly modified resin having phenol and tung oil units sufficiently bonded to each other. CONSTITUTION:Tung oil having a phenol sufficiently added to the reactive double bonds thereof is reacted with a phenol and a formaldehyde in the presence of a basic catalyst to obtain a modified phenolic resin compsn.

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、フェノール類が十分に
付加した桐油とフェノール類とホルムアルデヒド類とを
塩基性触媒存在下で反応せしめたレゾール型の変性フェ
ノール樹脂組成物およびその製造方法に関するものであ
り、可撓性、機械的特性、電気特性の極めて優れた、印
刷配線板用フェノール樹脂積層板、複合材料、塗料など
に好適な変性フェノール樹脂組成物およびその製造方法
を提供するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a resol type modified phenolic resin composition obtained by reacting tung oil sufficiently added with phenols, phenols and formaldehydes in the presence of a basic catalyst, and a method for producing the same. And a modified phenolic resin composition having excellent flexibility, mechanical properties, and electrical properties, which is suitable for a phenolic resin laminate for printed wiring boards, composite materials, paints, and the like, and a method for producing the same. .

【0002】[0002]

【従来の技術】フェノール樹脂は耐熱性、電気的特性、
機械的特性が優れており、印刷配線板用積層板、成形材
料、複合材料、塗料などに広く用いられている。しか
し、一般にフェノール樹脂は固くて脆い欠点を有してい
るため、積層板に用いた場合は打抜き加工性が劣るなど
の欠点がある。この欠点を改良する方法として桐油、脱
水ひまし油、カシューナット核油、ウルシオール類など
の植物油やアルキルフェノールなどで変性された可撓性
を有するフェノール樹脂が知られている。しかし最近、
印刷配線板の例では、回路が益々高密度化されるに伴っ
て、打抜き加工性、強靱性の一層優れた積層板が必要と
され、可撓性と強靭性を兼ね備えたフェノール樹脂が必
要になっており、従来の樹脂ではこれらの特性を満足す
ることは困難である。
2. Description of the Related Art Phenolic resin has heat resistance, electrical characteristics,
It has excellent mechanical properties and is widely used for laminated boards for printed wiring boards, molding materials, composite materials, paints, etc. However, since the phenol resin generally has a defect that it is hard and brittle, it has a defect that the punching workability is poor when it is used for a laminated plate. As a method for improving this drawback, plant oils such as tung oil, dehydrated castor oil, cashew nut kernel oil and urushiols, and flexible phenol resins modified with alkylphenols are known. But recently
In the case of printed wiring boards, a laminated board with more excellent punching workability and toughness is required as the circuit becomes more dense, and a phenol resin that has both flexibility and toughness is needed. Therefore, it is difficult for conventional resins to satisfy these characteristics.

【0003】[0003]

【発明が解決しようとする課題】本発明は従来の方法で
は得られない優れた可撓性と高い機械強度とを有するフ
ェノール樹脂を得んとして研究した結果、従来の桐油変
性フェノール樹脂は桐油とフェノール類との反応が不完
全であったために、可撓性と強靭性とに限界があること
を見出し、フェノール類が十分に付加した桐油とフェノ
ール類とホルムアルデヒド類とを塩基性触媒存在下で反
応せしめたレゾール型の変性フェノール樹脂が可撓性、
機械的特性、電気特性に極めて優れているとの知見を
得、更にこの知見に基づき種々研究を進めて本発明を完
成するに至ったものである。その目的とするところは可
撓性、機械的特性、電気的特性の優れた極めて強靱な変
性フェノール樹脂組成物およびその製造方法を提供する
にある。
DISCLOSURE OF INVENTION Problems to be Solved by the Invention The present invention has been studied to obtain a phenol resin having excellent flexibility and high mechanical strength which cannot be obtained by the conventional method. As a result, the conventional tung oil-modified phenol resin is It was found that the flexibility and toughness are limited due to incomplete reaction with phenols, and tung oil with sufficient addition of phenols, phenols and formaldehydes in the presence of a basic catalyst. Resole-type modified phenolic resin made to react is flexible,
The present inventors have obtained the knowledge that they are extremely excellent in mechanical properties and electrical properties, and further advanced various studies based on this knowledge to complete the present invention. The object of the invention is to provide an extremely tough modified phenolic resin composition having excellent flexibility, mechanical properties and electrical properties, and a method for producing the same.

【0004】[0004]

【課題を解決するための手段】本発明はフェノール類が
十分に付加した桐油とフェノール類とホルムアルデヒド
類とを塩基性触媒存在下で反応せしめたレゾール型の変
性フェノール樹脂組成物に関するものであり、またフェ
ノール類(A)と桐油(B)とを重量比 X < A/B < 10 X=0.024×(fw−1)× M/fn (fnはフェノール類の数平均官能数、fwはフェノー
ル類の量平均官能数、Mはフェノール類の数平均分子量
である)で酸性触媒存在下で反応させ、フェノール類が
十分に付加した桐油とフェノール類とからなる反応組成
物を得、該反応組成物より未反応フェノール類の所定量
(C)を重量比 (A−C)/B=0.4〜1.3 となるように除去し、次いで塩基性触媒存在下でホルム
アルデヒド類と反応させることを特徴とするレゾール型
の変性フェノール樹脂組成物の製造方法に関するもので
ある。
The present invention relates to a resol type modified phenolic resin composition obtained by reacting tung oil sufficiently added with phenols, phenols and formaldehydes in the presence of a basic catalyst, Further, the weight ratio of phenols (A) and tung oil (B) is X <A / B <10 X = 0.024 x (fw-1) x M / fn (fn is the number average functional number of phenols, and fw is phenols. In the presence of an acidic catalyst to obtain a reaction composition consisting of tung oil and phenols to which phenols are sufficiently added. Further, a predetermined amount (C) of unreacted phenols is removed so that the weight ratio (AC) /B=0.4 to 1.3, and then the reaction is performed with formaldehydes in the presence of a basic catalyst. To a method of manufacturing le type modified phenolic resin composition.

【0005】本発明における桐油とは、エレオステアリ
ン酸のグリセリンエステルを主成分とする天然に産する
桐油を言い、エレオステアリン酸基中にある共役した3
個の二重結合がフェノール類との反応性を有しており、
この内2個までフェノール類が通常の反応条件下で付加
し得る性質を有している。本発明におけるフェノール類
が十分に付加した桐油とは、上記エレオステアリン酸基
の反応性を有する2重結合のうちの2個の二重結合の殆
どないし全てがフェノール類のオルトまたはパラ位と化
学結合したものを言う。
The tung oil in the present invention refers to naturally occurring tung oil mainly composed of glycerin ester of eleostearic acid, which is a conjugated 3 atom in the eleostearic acid group.
The double bond of each has reactivity with phenols,
Up to two of these phenols can be added under normal reaction conditions. The tung oil with sufficient addition of phenols in the present invention means that most or all of the two double bonds among the double bonds having reactivity of the eleostearic acid group are in the ortho or para position of the phenols. It refers to a chemically bonded substance.

【0006】本発明において用いられるフェノール類
は、フェノール、クレゾール、キシレノール、P-t-ブチ
ルフェノール、ビスフェノールA、レゾルシンなどの1
価並びに2価のフェノール類およびそれらの置換体の1
種以上が用いられ、少なくとも3官能以上のフェノール
類を50モル%以上含有するフェノール類が用いられる。
好ましいフェノール類はフェノールおよびクレゾールで
ある。
The phenols used in the present invention include phenol, cresol, xylenol, Pt-butylphenol, bisphenol A, resorcin and the like.
Of dihydric and dihydric phenols and their substitution products
Phenols containing at least 50 mol% of trifunctional or higher functional phenols are used.
Preferred phenols are phenol and cresol.

【0007】本発明において用いられるホルムアルデヒ
ド類は、ホルムアルデヒド、パラホルムアルデヒドなど
である。
The formaldehydes used in the present invention are formaldehyde, paraformaldehyde and the like.

【0008】本発明における塩基性触媒としては、アン
モニア、トリエチルアミン、エチレンジアミン、ヘキサ
メチレンテトラミン、トリエタノールアミン、水酸化バ
リウムなどのような触媒をあげることができる。
Examples of the basic catalyst in the present invention include catalysts such as ammonia, triethylamine, ethylenediamine, hexamethylenetetramine, triethanolamine and barium hydroxide.

【0009】本発明において、フェノール類が十分に付
加した桐油とフェノール類とホルムアルデヒド類とを塩
基性触媒存在下で反応せしめた変性フェノール樹脂組成
物の組成は、桐油に対し付加したものを含めた全フェノ
ール類が重量比で0.4〜1.3のものが好ましい。割合が1.
3以上では桐油成分の含有量が少なくなり樹脂組成物の
硬化物の可撓性が損なわれて硬くなり、0.4以下では桐
油成分が多くなり、硬化物の強度が低下する。
In the present invention, the composition of the modified phenolic resin composition obtained by reacting tung oil sufficiently added with phenols, phenols and formaldehydes in the presence of a basic catalyst includes those added to tung oil. It is preferable that all phenols have a weight ratio of 0.4 to 1.3. The ratio is 1.
When it is 3 or more, the content of the tung oil component is small and the cured product of the resin composition is impaired in flexibility, and when it is 0.4 or less, the tung oil component is large and the strength of the cured product is lowered.

【0010】フェノール類が十分に付加した桐油とフェ
ノール類とホルムアルデヒド類とを塩基性触媒存在下で
反応せしめた変性フェノール樹脂組成物中の桐油に対す
るフェノール類の割合として、重量比で0.4〜1.3のもの
を得る場合、桐油に対してフェノール類を、重量比で0.
4〜1.3で混合して反応させる方法で得ることは困難であ
る。この範囲の重量比での反応では、桐油中のエレオス
テアリン酸基の二重結合にフェノール類が十分に付加す
る前にゲル化するので、付加が不十分の状態で反応を完
了し、これをホルムアルデヒドと塩基性触媒下で反応さ
せざるを得ず、その結果、得られる樹脂は結合が不完全
であるため、可撓性と強靭性とに限界がある。
The ratio of phenols to tung oil in a modified phenolic resin composition obtained by reacting tung oil with sufficient addition of phenols, phenols and formaldehyde in the presence of a basic catalyst is 0.4 to 1.3 by weight ratio. To obtain a product, phenols are added to tung oil in a weight ratio of 0.
It is difficult to obtain it by a method of mixing and reacting with 4 to 1.3. In the reaction in the weight ratio within this range, the phenol gels before the sufficient addition to the double bond of the eleostearic acid group in tung oil, so the reaction is completed in an insufficient addition state. Has to be reacted with formaldehyde in the presence of a basic catalyst, and as a result, the resulting resin is incompletely bonded, which limits its flexibility and toughness.

【0011】本発明においては、フェノール類(A)と
桐油(B)とを重量比 X < A/B < 10 X=0.024×(fw−1)× M/fn (fnはフェノール類の数平均官能数、fwはフェノー
ル類の量平均官能数、Mはフェノール類の数平均分子量
である)で酸性触媒存在下で反応させ、フェノール類が
十分に付加した桐油とフェノール類とからなる反応組成
物を得、該反応組成物より未反応フェノール類の所定量
(C)を重量比 (A−C)/B=0.4〜1.3 となるように除去し、次いで塩基性触媒存在下でホルム
アルデヒド類と反応させることにより、本発明のフェノ
ール類が十分に付加した桐油とフェノール類とホルムア
ルデヒド類とを塩基性触媒存在下で反応せしめた変性フ
ェノール樹脂組成物を製造することができる。
In the present invention, the weight ratio of phenols (A) and tung oil (B) is X <A / B <10 X = 0.024 x (fw-1) x M / fn (fn is the number average of phenols. (Functional number, fw is the amount average functional number of phenols, M is the number average molecular weight of phenols) and reacted in the presence of an acidic catalyst, and a reaction composition comprising tung oil and phenols with sufficient addition of phenols From the reaction composition, a predetermined amount (C) of unreacted phenols is removed so that the weight ratio (AC) /B=0.4 to 1.3, and then the reaction is performed with formaldehydes in the presence of a basic catalyst. By doing so, the modified phenol resin composition of the present invention can be produced by reacting tung oil sufficiently added with phenols, phenols and formaldehydes in the presence of a basic catalyst.

【0012】本発明のフェノール類の数平均官能数と
は、フェノール類のベンゼン核上の反応性位置(即ち、
フェノール類の官能基)の合計モル数をフェノール類の
合計モル数で除した数を言う。本発明のフェノール類の
量平均官能数とは、フェノール類の官能基数の二乗とフ
ェノール類のモル数との積の合計値を、フェノール類の
官能基の合計モル数で除した数を言う。本発明のフェノ
ール類の数平均分子量とは、フェノール類の合計重量を
フェノール類の合計モル数で除した数を言う。
The number average functionality of the phenols of the present invention means the reactive position of the phenols on the benzene nucleus (ie,
The total number of moles of phenolic functional groups) is divided by the total number of moles of phenols. The amount average functional number of phenols of the present invention means the number obtained by dividing the total product of the square of the number of functional groups of phenols and the number of moles of phenols by the total number of moles of functional groups of phenols. The number average molecular weight of the phenols of the present invention means the number obtained by dividing the total weight of the phenols by the total number of moles of the phenols.

【0013】本発明において、フェノール類(A)と桐
油(B)との反応比は、重量比で(A)/(B)=X〜
10である。(A)/(B)がXより少ないと、桐油にフ
ェノール類が十分付加する前にゲル化してしまうか、著
しく粘度が増大し、桐油にフェノール類が十分に付加し
た反応組成物を得ることが困難となる。また10以上で
は、未反応フェノール類の除去量が増加し、経済的に不
利となる。好ましい反応比(A)/(B)はX〜5であ
る。該反応によって、フェノール類が十分に付加した桐
油と未反応のフェノール類とからなる反応組成物が得ら
れる。
In the present invention, the reaction ratio of the phenols (A) and tung oil (B) is (A) / (B) = X-by weight.
Is 10. When (A) / (B) is less than X, gelation occurs before the phenols are sufficiently added to the tung oil, or the viscosity is remarkably increased to obtain a reaction composition in which the phenols are sufficiently added to the tung oil. Becomes difficult. If it is 10 or more, the amount of unreacted phenols removed increases, which is economically disadvantageous. The preferred reaction ratio (A) / (B) is X-5. By the reaction, a reaction composition composed of tung oil sufficiently added with phenols and unreacted phenols is obtained.

【0014】本発明において、フェノール類(A)と桐
油(B)との反応に用いられる酸性触媒としては、パラ
トルエンスルホン酸、メタンスルホン酸、三弗化ほう
素、塩化第二錫、塩化第二鉄、パーフロロメタンスルホ
ン酸などのようなフリーデルクラフト形触媒をあげるこ
とができる。該酸性触媒の使用量は特に制限はないが、
反応物の合計量に対して0.01〜0.5重量%が好ましい。
また該反応は50〜120℃の温度で行なうのが好ましい。1
20℃以上では桐油のエステル結合が分解切断されるので
好ましくない。また、必要によりトルエンなどの溶媒中
で反応させてもよい。
In the present invention, the acidic catalyst used in the reaction of the phenols (A) and tung oil (B) includes paratoluenesulfonic acid, methanesulfonic acid, boron trifluoride, stannic chloride and stannic chloride. Friedel-Crafts type catalysts such as diiron, perfluoromethanesulfonic acid and the like can be mentioned. The amount of the acidic catalyst used is not particularly limited,
0.01 to 0.5% by weight, based on the total amount of reactants, is preferred.
The reaction is preferably carried out at a temperature of 50 to 120 ° C. 1
Above 20 ° C, ester bonds of tung oil are decomposed and cleaved, which is not preferable. If necessary, the reaction may be carried out in a solvent such as toluene.

【0015】本発明において、フェノール類が十分に付
加した桐油とフェノール類とからなる反応組成物から未
反応フェノール類の所定量(C)が重量比で (A−C)/B=0.4〜1.3 となるように除去され、本発明の変性フェノール樹脂組
成物の好ましいフェノール類の割合に調節される。次い
で塩基性触媒存在下で反応させるホルムアルデヒド類の
量は、所定量の未反応フェノール類除去後の全フェノー
ル類1モルに対して、ホルムアルデヒドとして0.6〜1.5
モルである。該反応は前記塩基性触媒下で、60〜100℃
の温度で行なうのが好ましい。必要により、トルエンな
どの溶媒中で反応させてもよい。
In the present invention, a predetermined amount (C) of unreacted phenols in a reaction composition consisting of tung oil and phenols to which phenols are sufficiently added is expressed in a weight ratio of (AC) /B=0.4 to 1.3. And the ratio of the preferred phenols in the modified phenolic resin composition of the present invention is adjusted. Then, the amount of formaldehyde to be reacted in the presence of a basic catalyst is 0.6 to 1.5 as formaldehyde based on 1 mol of all phenols after removal of a predetermined amount of unreacted phenols.
It is a mole. The reaction was carried out under the basic catalyst at 60 to 100 ° C.
It is preferable to carry out at the temperature of. If necessary, the reaction may be carried out in a solvent such as toluene.

【0016】本発明において、フェノール類(A)と桐
油(B)との反応比の下限を表わすXは次式 X=0.024×(fw−1)× M/fn で表され、実験値とフローリーのゲル化条件式とにより
求めることができる。
In the present invention, X, which represents the lower limit of the reaction ratio between the phenols (A) and tung oil (B), is represented by the following formula X = 0.024 × (fw-1) × M / fn, and the experimental value and Flory The gelling conditional expression of

【0017】本発明において、桐油の内の30重量%まで
を、脱水ひまし油、亜麻仁油などの他の乾性油で適宜置
き換えることができる。また、ロジン、アニリン、カシ
ュナット核油などの他の変性剤で20%以内で適宜変性す
ることができる。
In the present invention, up to 30% by weight of tung oil can be appropriately replaced with other drying oil such as dehydrated castor oil and linseed oil. Further, it can be appropriately modified within 20% with other modifiers such as rosin, aniline, and Kashnut kernel oil.

【0018】[0018]

【実施例】以下実施例により本発明を例示する。The present invention will be illustrated by the following examples.

【0019】(実施例1)フェノール類として、フェノ
ール(I)を準備した。フェノールの官能数は3、分子
量は94の単独成分である。したがって、その数平均およ
び量平均官能数は3であり、数平均分子量は94である。
Xは1.504である。5リットルの撹拌機付きフラスコに
フェノール(I)を2500g、桐油(II)を800g仕込み
(重量比(I)/(II)=3.125)、適量のパラトルエ
ンスルホン酸を触媒として、100℃で桐油の官能基の反
応が完結するまで反応させた。反応に要した時間は4時
間であった。桐油の官能基の反応状態は核磁気共鳴スペ
クトルで追跡した。得られた反応組成物は、フェノール
が十分に付加した桐油が36重量%、未反応フェノールが
64重量%であった。この反応組成物をトリエタノールア
ミンで中和し、反応組成物中の未反応フェノールが34重
量%になるまで、真空下で未反応フェノールを蒸発除去
し、仕込み桐油に対し、結合フェノールも含めた全フェ
ノール成分の重量比が1.25の混合物を得た。この混合物
の蒸気圧平衡法で測定した平均分子量は253であった。
次いで、これに触媒としてアンモニアを適量、パラホル
ムアルデヒドを430g、トルエンを500g添加し、樹脂の
150℃の熱板上でのゲル化時間が6分になるまで80℃で
反応させた後、真空下で脱水、脱溶媒を行い、トルエン
とメタノールの1/1の混合溶剤を添加して冷却し、樹
脂分52重量%のレゾール型変性フェノール樹脂組成物を
得た。
Example 1 Phenol (I) was prepared as a phenol. Phenol is a single component having a functional number of 3 and a molecular weight of 94. Therefore, its number average and number average functional number is 3, and number average molecular weight is 94.
X is 1.504. Charge a flask (5 liters) equipped with a stirrer with 2500 g of phenol (I) and 800 g of tung oil (II) (weight ratio (I) / (II) = 3.125), and use an appropriate amount of paratoluenesulfonic acid as a catalyst to tung oil at 100 ° C. The reaction was continued until the reaction of the functional group of 1 was completed. The time required for the reaction was 4 hours. The reaction state of functional groups of tung oil was traced by nuclear magnetic resonance spectroscopy. The reaction composition obtained contained 36% by weight of tung oil with sufficient addition of phenol and unreacted phenol.
It was 64% by weight. The reaction composition was neutralized with triethanolamine, and the unreacted phenol was removed by evaporation under vacuum until the unreacted phenol in the reaction composition became 34% by weight, and the bound phenol was also included in the charged tung oil. A mixture having a weight ratio of all phenol components of 1.25 was obtained. The average molecular weight of this mixture measured by the vapor pressure equilibrium method was 253.
Then, to this was added an appropriate amount of ammonia as a catalyst, 430 g of paraformaldehyde and 500 g of toluene, and
After reacting at 80 ° C until gelling time on a hot plate at 150 ° C reaches 6 minutes, dehydration and desolvation are performed under vacuum, and a 1/1 mixed solvent of toluene and methanol is added to cool. Then, a resole-type modified phenolic resin composition having a resin content of 52% by weight was obtained.

【0020】(実施例2)フェノール類として、m-クレ
ゾール60%、p-クレゾール40%からなる混合クレゾール
(III)を準備した。混合クレゾールの数平均官能数は
2.600、量平均官能数は 2.692、数平均分子量は108であ
る。Xは 1.687である。5リットルの撹拌機付きフラス
コに混合クレゾール(III)を2500g、桐油(II)を500
g仕込み(重量比(III)/(II)=5)、適量のパラ
トルエンスルホン酸を触媒として、100℃で桐油の官能
基の反応が完結するまで反応させた。反応に要した時間
は 4.5時間であった。桐油の官能基の反応状態は核磁気
共鳴スペクトルで追跡した。得られた反応組成物は、ク
レゾールが十分付加した桐油が26重量%、未反応クレゾ
ールが74重量%であった。この反応組成物をトリエタノ
ールアミンで中和し、反応組成物中の未反応クレゾール
が22重量%になるまで、真空下で未反応クレゾールを蒸
発除去し、仕込み桐油に対し、結合クレゾールも含めた
全クレゾール成分の重量比が1.0の混合物を得た。この
混合物の蒸気圧平衡法で測定した平均分子量は390であ
った。次いで、これに触媒としてトリエチルアミンを適
量、パラホルムアルデヒドを400g、トルエンを500g添
加し、樹脂の150℃の熱板上でのゲル化時間が6分にな
るまで80℃で反応させた後、真空下で脱水、脱溶媒を行
い、トルエンとメタノールの1/1の混合溶剤を添加し
て冷却し、樹脂分50重量%のレゾール型変性フェノール
樹脂組成物を得た。
(Example 2) As a phenol, mixed cresol (III) consisting of 60% m-cresol and 40% p-cresol was prepared. The number average functionality of mixed cresol is
2.600, the number average functional number is 2.692, and the number average molecular weight is 108. X is 1.687. In a 5 liter flask equipped with a stirrer, 2500 g of mixed cresol (III) and 500 g of tung oil (II) were mixed.
g (weight ratio (III) / (II) = 5), and an appropriate amount of paratoluenesulfonic acid as a catalyst was reacted at 100 ° C. until the reaction of the functional group of tung oil was completed. The time required for the reaction was 4.5 hours. The reaction state of functional groups of tung oil was traced by nuclear magnetic resonance spectroscopy. The reaction composition thus obtained contained 26% by weight of tung oil with sufficient addition of cresol and 74% by weight of unreacted cresol. This reaction composition was neutralized with triethanolamine, the unreacted cresol in the reaction composition was removed by evaporation under vacuum until the unreacted cresol in the reaction composition became 22% by weight, and the added cresol was also included in the tung oil charged. A mixture with a weight ratio of all cresol components of 1.0 was obtained. The average molecular weight of this mixture measured by the vapor pressure equilibrium method was 390. Then, triethylamine as a catalyst, 400 g of paraformaldehyde and 500 g of toluene were added thereto, and the mixture was reacted at 80 ° C. until the gelation time of the resin on a hot plate at 150 ° C. reached 6 minutes, and then under vacuum. Was dehydrated and desolvented, and a 1/1 mixed solvent of toluene and methanol was added and cooled to obtain a resol-type modified phenolic resin composition having a resin content of 50% by weight.

【0021】(比較例1)5リットルの撹拌機付きフラ
スコにフェノール(I)を1000g、桐油(II)を800g
仕込み(重量比(I)/(II)=1.25)、適量のパラト
ルエンスルホン酸を触媒として100℃で反応させた。 反
応開始後1.5時間経過すると急に粘度が上昇し、攪拌困
難となってゲル化した。この条件では桐油の官能基に十
分にフェノールを付加させることは困難であった。
(Comparative Example 1) 1000 g of phenol (I) and 800 g of tung oil (II) were placed in a 5-liter flask equipped with a stirrer.
Charged (weight ratio (I) / (II) = 1.25), and reacted at 100 ° C. using an appropriate amount of paratoluenesulfonic acid as a catalyst. After 1.5 hours from the start of the reaction, the viscosity suddenly increased and it became difficult to stir and gel. Under this condition, it was difficult to sufficiently add phenol to the functional group of tung oil.

【0022】(比較例2)比較例1と同様に、5リット
ルの撹拌機付きフラスコにフェノール(I)を1000g、
桐油(II)を800g仕込み(重量比(I)/(II)=1.2
5)、適量のパラトルエンスルホン酸を触媒として、100
℃でゲル化が起こる時間よりも短い時間の1時間反応さ
せ、トリエタノールアミンを添加して中和し、冷却して
反応を停止させた。この反応混合物の桐油の官能基の反
応率は核磁気共鳴スペクトルで測定したところ、55%で
あった。得られた反応組成物は、フェノールが不十分に
付加した桐油57重量%、未反応フェノールが43重量%で
あった。またこの反応組成物の蒸気圧平衡法で測定した
平均分子量は198であった。次いで、これに触媒として
アンモニアを適量、パラホルムアルデヒドを430g、ト
ルエンを500g添加し、樹脂の150℃の熱板上でのゲル化
時間が6分になるまで80℃で反応させた後、真空下で脱
水、脱溶媒を行い、トルエンとメタノールの1/1の混
合溶剤を添加して冷却し、樹脂分52重量%のレゾール型
変性フェノール樹脂組成物を得た。
(Comparative Example 2) As in Comparative Example 1, 1000 g of phenol (I) was added to a 5-liter flask equipped with a stirrer.
Charge 800g of tung oil (II) (weight ratio (I) / (II) = 1.2
5), using an appropriate amount of paratoluene sulfonic acid as a catalyst, 100
The reaction was carried out for 1 hour at a temperature shorter than the time at which gelation occurred, triethanolamine was added for neutralization, and the reaction was stopped by cooling. The reaction rate of functional groups of tung oil in this reaction mixture was 55% as measured by nuclear magnetic resonance spectrum. The reaction composition obtained was 57% by weight of tung oil with insufficient addition of phenol and 43% by weight of unreacted phenol. The average molecular weight of this reaction composition measured by the vapor pressure equilibrium method was 198. Then, a proper amount of ammonia as a catalyst, 430 g of paraformaldehyde and 500 g of toluene were added thereto, and the mixture was reacted at 80 ° C. until the gelation time of the resin on a hot plate at 150 ° C. reached 6 minutes, then under vacuum. Was dehydrated and desolvented, and a 1/1 mixed solvent of toluene and methanol was added and cooled to obtain a resole-type modified phenolic resin composition having a resin content of 52% by weight.

【0023】実施例1、2および比較例1、2より、従
来、桐油にフェノール類が十分に付加ないし結合した樹
脂を得ることは困難であり、本発明の変性フェノール樹
脂組成物の製造方法によりはじめてこれが可能になるこ
とがわかる。
From Examples 1 and 2 and Comparative Examples 1 and 2, it is conventionally difficult to obtain a resin in which phenols are sufficiently added to or combined with tung oil, and according to the method for producing the modified phenol resin composition of the present invention. For the first time, it turns out that this is possible.

【0024】実施例1、2および比較例2で得た変性フ
ェノール樹脂を150℃の熱板上に滴下して溶剤を蒸発さ
せ、次いで熱板温度を165℃にして、2時間反応、硬化
させ、厚さ約0.3mmのフィルムを形成した。比較例2の
樹脂のフィルムは少し濁っていたが、実施例1および2
の樹脂のフィルムは透明であった。またフィルムを折り
曲げたところ、比較例2の樹脂のフィルムは柔らかい
が、脆くて容易に破断した。しかし、実施例1および2
の樹脂のフィルムは強靭であり、柔らかいにも拘らず破
断しなかった。このように、本発明の変性フェノール樹
脂組成物は従来の同様の変性率の樹脂に比べて、可撓性
と強靭性に優れている。また、本発明の変性フェノール
樹脂組成物の製造方法により、はじめて優れた変性フェ
ノール樹脂組成物を得ることが可能になった。
The modified phenolic resins obtained in Examples 1 and 2 and Comparative Example 2 were dropped on a hot plate at 150 ° C. to evaporate the solvent, and then the hot plate temperature was set to 165 ° C. to react and cure for 2 hours. A film having a thickness of about 0.3 mm was formed. Although the resin film of Comparative Example 2 was slightly cloudy, Examples 1 and 2
The resin film of was transparent. When the film was bent, the resin film of Comparative Example 2 was soft, but was brittle and easily ruptured. However, Examples 1 and 2
The resin film of 1 was tough and did not break despite being soft. As described above, the modified phenolic resin composition of the present invention is superior in flexibility and toughness as compared with the conventional resin having the same modification rate. In addition, the method for producing a modified phenolic resin composition of the present invention makes it possible to obtain an excellent modified phenolic resin composition for the first time.

【0025】[0025]

【発明の効果】本発明のレゾール型の変性フェノール樹
脂組成物の硬化物は、極めて優れた可撓性と強靭性およ
び電気的特性を有しており、フェノール樹脂積層板用、
複合材料用、塗料用、工業用樹脂用として好適であり、
とりわけ印刷配線板に用いられるフェノール樹脂積層板
に極めて有用である。このように本発明の変性フェノー
ル樹脂組成物が可撓性と強靭性に極めて優れる理由は充
分には明らかではないが、本発明のフェノール樹脂組成
物では、桐油の官能基に十分ないし完全にフェノール類
が付加しているため、硬化物の架橋がより十分にでき、
さらに未反応の桐油、結合不十分な桐油が殆どないため
と考えられる。また、このような桐油とフェノール類と
が十分に結合した高い変性率の樹脂を得ることは従来困
難であったが、本発明によりはじめて可能になった。
The cured product of the resol type modified phenolic resin composition of the present invention has extremely excellent flexibility, toughness and electrical characteristics, and is suitable for phenol resin laminates,
Suitable for composite materials, paints, industrial resins,
Particularly, it is extremely useful for a phenol resin laminated board used for a printed wiring board. Thus, the reason why the modified phenolic resin composition of the present invention is extremely excellent in flexibility and toughness is not clear, but in the phenolic resin composition of the present invention, the functional group of tung oil is sufficiently or completely phenolic. Because of the addition of the class, the cured product can be crosslinked more sufficiently,
Furthermore, it is considered that there is almost no unreacted tung oil or tung oil with insufficient bonding. Further, it has been difficult to obtain a resin having a high modification rate in which such tung oil and phenols are sufficiently bound, but the present invention made it possible for the first time.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 反応可能な二重結合にフェノール類が十
分に付加した桐油とフェノール類とホルムアルデヒド類
とが塩基性触媒存在下で反応せしめられた変性フェノー
ル樹脂組成物。
1. A modified phenolic resin composition obtained by reacting tung oil in which phenols are sufficiently added to a reactive double bond, phenols and formaldehydes in the presence of a basic catalyst.
【請求項2】 フェノール類(A)と桐油(B)とを重
量比 X < A/B < 10 X=0.024×(fw−1)× M/fn (fnはフェノール類の数平均官能数、fwはフェノー
ル類の量平均官能数、Mはフェノール類の数平均分子量
である)で酸性触媒存在下で反応させ、フェノール類が
十分に付加した桐油とフェノール類とからなる反応組成
物を得、該反応組成物より未反応フェノール類の所定量
(C)を重量比 (A−C)/B=0.4〜1.3 となるように除去し、次いで塩基性触媒存在下でホルム
アルデヒド類と反応させることを特徴とする変性フェノ
ール樹脂組成物の製造方法。
2. A weight ratio of phenols (A) and tung oil (B): X <A / B <10 X = 0.024 × (fw-1) × M / fn (fn is the number average functional number of phenols, (fw is the number average functional number of phenols, M is the number average molecular weight of the phenols) and reacted in the presence of an acidic catalyst to obtain a reaction composition consisting of tung oil and phenols with sufficient addition of phenols, A predetermined amount (C) of unreacted phenols is removed from the reaction composition so that the weight ratio (AC) /B=0.4 to 1.3, and then reacted with formaldehyde in the presence of a basic catalyst. A method for producing a modified phenolic resin composition, which is characterized.
JP4133895A 1992-05-26 1992-05-26 Modified phenolic resin composition and production thereof Pending JPH05320294A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4133895A JPH05320294A (en) 1992-05-26 1992-05-26 Modified phenolic resin composition and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4133895A JPH05320294A (en) 1992-05-26 1992-05-26 Modified phenolic resin composition and production thereof

Publications (1)

Publication Number Publication Date
JPH05320294A true JPH05320294A (en) 1993-12-03

Family

ID=15115619

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4133895A Pending JPH05320294A (en) 1992-05-26 1992-05-26 Modified phenolic resin composition and production thereof

Country Status (1)

Country Link
JP (1) JPH05320294A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007297610A (en) * 2006-04-07 2007-11-15 Mitsubishi Gas Chem Co Inc Method for producing low-viscosity phenol-modified aromatic hydrocarbon formaldehyde resin

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007297610A (en) * 2006-04-07 2007-11-15 Mitsubishi Gas Chem Co Inc Method for producing low-viscosity phenol-modified aromatic hydrocarbon formaldehyde resin

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