JPH06136080A - Production of silicone-modified novolak resin - Google Patents

Production of silicone-modified novolak resin

Info

Publication number
JPH06136080A
JPH06136080A JP29042692A JP29042692A JPH06136080A JP H06136080 A JPH06136080 A JP H06136080A JP 29042692 A JP29042692 A JP 29042692A JP 29042692 A JP29042692 A JP 29042692A JP H06136080 A JPH06136080 A JP H06136080A
Authority
JP
Japan
Prior art keywords
silicone
parts
reaction
resin
weight
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
JP29042692A
Other languages
Japanese (ja)
Inventor
Toru Saneto
徹 実藤
Tadashi Kotsuna
正 忽那
Sumiya Miyake
澄也 三宅
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
Sumitomo Durez Co Ltd
Original Assignee
Sumitomo Bakelite Co Ltd
Sumitomo Durez 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, Sumitomo Durez Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP29042692A priority Critical patent/JPH06136080A/en
Publication of JPH06136080A publication Critical patent/JPH06136080A/en
Pending legal-status Critical Current

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  • Phenolic Resins Or Amino Resins (AREA)
  • Silicon Polymers (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain a silicone-modified novolak resin excellent in curability and mechanical strength, also highly excellent in water resistance and flexibility by reaction between a phenolic compound, an aldehyde and a specific modifier in the presence of an acid catalyst. CONSTITUTION:The resin can be obtained by reaction, in the presence of an acid catalyst (pref. hydrochloric acid, salicylic acid), between (A) a phenolic compound, (B) an aldehyde and (C) as modifier, a silicone-based addition polymer prepared by reaction between (1) a hydrogenorganosiloxane of formula I (R1 and R2 are each alkyl or phenyl; n is 10-100) and a polyfunctional aromatic polyallyl compound of formula II (R3 is H, halogen, etc.; R4 is of formula III, SO2, etc.; m is 0-10) so as to be 10-50 pts.wt. of the component C based on 100 pts.wt. of the component A. It is preferable that the reaction be made using a reaction solvent such as an alcohol 80-200 deg.C in the boiling point at normal pressures.

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、硬化性と機械的強度に
優れ、かつ耐水性や可撓性にも極めて優れた特長を有す
るシリコーン変性ノボラック樹脂の製造方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a silicone-modified novolac resin which has excellent curability and mechanical strength, and is extremely excellent in water resistance and flexibility.

【0002】[0002]

【従来の技術】フェノール樹脂は耐熱性、耐摩耗性、機
械的強度、電気絶縁性、低発煙性、耐酸性などに優れた
特長を有するため、産業界のいろいろの分野で広く利用
されていることは周知の事実である。しかし耐水性や可
撓性は不十分であり、前記の優れた特長を生かしたまゝ
でこれらの欠点の改良をするために、変性フェノール樹
脂の研究が盛んに行われている。フェノール樹脂に機械
的強度を維持しつゝ可撓性や柔軟性を付与することがで
きる可能性のある樹脂としてはシリコーン変性フェノー
ル樹脂が期待されている。シリコーン変性フェノール樹
脂については特開昭58−47013号公報、特開昭6
2−124116号公報、特開昭62−136860号
公報、特開昭62―174222号公報などがある。し
かし、これらの特許公報などによると、硬化性や機械的
強度に優れ、かつ耐水性や可撓性も良好であるというシ
リコーン変性のフェノール樹脂は未だ実存していない。
実存しない原因はフェノール化合物とシリコーン系化合
物が元来非相溶であるため、変性反応条件の設定が極め
て難しく、シリコーン変性のフェノール樹脂といわれて
いてもシリコーン系化合物が化学的に殆ど結合していな
いためであり、またフェノール性OH基をシリコーン変
性時に官能基として使用する場合には、合成されたシリ
コーン変性のフェノール樹脂中のフェノール成分が少な
くなるためである、と考えられる。
BACKGROUND OF THE INVENTION Phenolic resins are widely used in various fields of industry because they have excellent characteristics such as heat resistance, abrasion resistance, mechanical strength, electrical insulation, low smoke generation, and acid resistance. This is a well-known fact. However, water resistance and flexibility are insufficient, and modified phenolic resins have been actively researched in order to improve these drawbacks while making the most of the above-mentioned excellent features. Silicone-modified phenolic resin is expected as a resin that may be capable of imparting flexibility and flexibility while maintaining mechanical strength to the phenolic resin. Regarding the silicone-modified phenol resin, JP-A-58-47013 and JP-A-6-
No. 2-124116, Japanese Patent Laid-Open No. 62-136860 and Japanese Patent Laid-Open No. 62-174222. However, according to these patent publications and the like, a silicone-modified phenolic resin that is excellent in curability and mechanical strength, and that is also excellent in water resistance and flexibility has not existed yet.
The reason why it does not exist is that it is extremely difficult to set the modification reaction conditions because the phenolic compound and the silicone compound are originally incompatible, and even if it is said to be a silicone-modified phenolic resin, the silicone compound is almost chemically bonded. It is considered that this is because the phenolic OH group is used as a functional group at the time of silicone modification, and the phenol component in the synthesized silicone-modified phenol resin is reduced.

【0003】[0003]

【発明が解決しようとする課題】本発明のシリコーン変
性ノボラック樹脂の製造方法は、硬化性や機械的強度な
どのノボラック樹脂本来の優れた特性と、従来から改良
要求のあった耐水性や可撓性の両特性を兼備したノボラ
ック樹脂を得ようとして鋭意研究を行った結果、フェノ
ール樹脂合成時にフェノール骨格を持ったオルガノシロ
キサン化合物を変性剤として反応させることからなる製
造方法によって得られるシリコーン変性ノボラック樹脂
が有効であるとの知見を得、さらにこの知見に基づいて
種々研究を重ねて完成するに至ったものである。本発明
の目的とするところは未変性のノボラック樹脂が有して
いる硬化性や機械的強度などの多くの優れた特長を損う
ことなく、耐水性や可撓性も極めて良好なシリコーン変
性ノボラック樹脂の製造方法を提供することにある。従
って、本発明の製造方法で得られた、耐水性や可撓性の
良好なノボラック樹脂は、砥石用、摩擦材用、ゴム配合
用、電気絶縁用、塗料用、成形材料用、及びいろいろの
有機物や無機物の結合用などの用途向けノボラック樹脂
として有効に使用することができる。
The method for producing a silicone-modified novolac resin according to the present invention has excellent properties inherent to the novolac resin such as curability and mechanical strength, and water resistance and flexibility which have been conventionally required to be improved. As a result of earnest research to obtain a novolak resin having both properties of silicone, a silicone-modified novolak resin obtained by a manufacturing method comprising reacting an organosiloxane compound having a phenol skeleton as a modifier during the synthesis of a phenol resin Has been found to be effective, and based on this finding, various studies have been repeated and completed. The object of the present invention is to obtain a silicone-modified novolak which is excellent in water resistance and flexibility without impairing many excellent features such as curability and mechanical strength of the unmodified novolac resin. It is to provide a method for producing a resin. Therefore, the novolak resin obtained by the production method of the present invention, which has good water resistance and flexibility, is used for grindstones, friction materials, rubber compounding, electrical insulation, paints, molding materials, and various It can be effectively used as a novolak resin for applications such as binding of organic substances and inorganic substances.

【0004】[0004]

【課題を解決するための手段】本発明は、フェノール類
(a)、アルデヒド類(b)、及び変性剤として下記式
[I]で示されるハイドロジェンオルガノシロキサンと
下記式[II]で示される多官能芳香属ポリアリル化合物
とを反応せしめて得られるシリコーン系付加重合体(c)
を用い、かつ、フェノール類(a)100重量部に対して
前記シリコーン系付加重合体(c)を10〜50重量部の
割合で、酸触媒の存在下で反応させることを特徴とする
シリコーン変性ノボラック樹脂の製造方法である。
MEANS FOR SOLVING THE PROBLEMS The present invention is represented by phenols (a), aldehydes (b), and hydrogenorganosiloxane represented by the following formula [I] as a modifier and the following formula [II]. Silicone-based addition polymer (c) obtained by reacting with polyfunctional aromatic polyallyl compound
And the silicone-based addition polymer (c) is reacted at a ratio of 10 to 50 parts by weight with respect to 100 parts by weight of the phenols (a) in the presence of an acid catalyst. It is a manufacturing method of a novolac resin.

【0005】[0005]

【化1】 [Chemical 1]

【0006】[0006]

【化2】 [Chemical 2]

【0007】以下、本発明に使用する各成分について説
明する。 (フェノール類)本発明に用いられるフェノール類(a)
としては、フェノール、オルソクレゾール、メタクレゾ
ール、パラクレゾール、エチルフェノール、キシレノー
ル、ビスフェノールA、ビスフェノールF、カテコー
ル、レゾルシン、ハイドロキノン、プロピルフェノー
ル、プロペニルフェノール、ブチルフェノール、オクチ
ルフェノール、ノニルフェノールなどから選ばれた1種
又は2種以上が使用できる。 (アルデヒド類)本発明に使用されるアルデヒド類(b)
としては、ホルムアルデヒド、パラホルムアルデヒド、
トリオキサン、アセトアルデヒド、ベンズアルデヒドな
どから選ばれた1種又は2種以上である。
Each component used in the present invention will be described below. (Phenols) Phenols (a) used in the present invention
As, one or more selected from phenol, orthocresol, metacresol, paracresol, ethylphenol, xylenol, bisphenol A, bisphenol F, catechol, resorcinol, hydroquinone, propylphenol, propenylphenol, butylphenol, octylphenol, nonylphenol, or the like. Two or more can be used. (Aldehydes) Aldehydes (b) used in the present invention
As formaldehyde, paraformaldehyde,
One or more selected from trioxane, acetaldehyde, benzaldehyde and the like.

【0008】(ポリシロキサン−芳香族ポリアリル化合
物付加重合体)本発明に使用されるポリシロキサン−芳
香族ポリアリル化合物付加重合体(c)は、通常、ハイド
ロジェンオルガノシロキサンと多官能芳香族ポリアリル
化合物を白金系触媒存在下で反応せしめて得られる反応
生成物である。用いられるハイドロジェンオルガノシロ
キサンは下記式[I]で示されるポリシロキサンであ
り、その重合度(n)は10〜100の範囲である。
(Polysiloxane-Aromatic Polyallyl Compound Addition Polymer) The polysiloxane-aromatic polyallyl compound addition polymer (c) used in the present invention usually comprises a hydrogenorganosiloxane and a polyfunctional aromatic polyallyl compound. It is a reaction product obtained by reacting in the presence of a platinum-based catalyst. The hydrogen organosiloxane used is a polysiloxane represented by the following formula [I], and its degree of polymerization (n) is in the range of 10 to 100.

【0009】[0009]

【化3】 [Chemical 3]

【0010】重合度(n)が10を下回ると樹脂硬化物の
耐水性向上効果が低下し、100を上回ると越えるとア
ルデヒド類との反応性が低下しシリコーン変性樹脂が得
がたい場合がある。多官能芳香族ポリアリル化合物は下
記式[II]で示され、その重合度(m)は0〜10の範囲
である。
If the degree of polymerization (n) is less than 10, the effect of improving the water resistance of the cured resin decreases, and if it exceeds 100, the reactivity with aldehydes decreases and it may be difficult to obtain a silicone-modified resin. The polyfunctional aromatic polyallyl compound is represented by the following formula [II], and its degree of polymerization (m) is in the range of 0-10.

【0011】[0011]

【化4】 [Chemical 4]

【0012】重合度(m)が10を上回る場合は樹脂硬化
物の低応力化の効果が低下する。更にポリシロキサンへ
の芳香族ポリアリル化合物の付加量はポリシロキサン中
のハイドロシリル基1個に対して、芳香族ポリアリル化
合物中のアリル基は2〜10個が好ましい。2を下回る
とポリシロキサン−芳香族ポリアリル化合物の分子量が
高くなりすぎアルデヒド類との反応性が低下し、シリコ
ーン変性ノボラック樹脂の合成時に未反応のシリコーン
が残存して、樹脂硬化物の耐湿性が低下し、10を上回
ると硬化物の強度が低下する。なお、反応方法は適宜選
択が可能であり、その際の触媒は白金系触媒がよく、特
に塩素酸白金のイソプロパノール溶液が好んで用いられ
る。反応終了後は室温で液状の茶褐色の付加重合体が得
られる。
If the degree of polymerization (m) exceeds 10, the effect of lowering the stress of the cured resin will be reduced. Further, the addition amount of the aromatic polyallyl compound to the polysiloxane is preferably 2 to 10 allyl groups in the aromatic polyallyl compound with respect to one hydrosilyl group in the polysiloxane. When it is less than 2, the molecular weight of the polysiloxane-aromatic polyallyl compound becomes too high and the reactivity with aldehydes decreases, and unreacted silicone remains during the synthesis of the silicone-modified novolac resin, resulting in a moisture resistance of the cured resin. When it exceeds 10, the strength of the cured product decreases. The reaction method can be appropriately selected, and the catalyst used at that time is preferably a platinum-based catalyst, and an isopropanol solution of platinum chlorate is particularly preferably used. After the reaction is complete, a liquid brown addition polymer is obtained at room temperature.

【0013】(溶媒)本発明においては、通常反応系を
均一化するために溶媒が使用される。使用される溶媒の
種類としては、好ましくは常圧の沸点が80〜200℃
のアルコール類、ケトン類、エーテル類、エステル類及
びセロソルブ類から選ばれた1種又は2種以上である。 (酸触媒)本発明に使用される酸触媒としては、塩酸、
硫酸、安息香酸、サリチル酸、パラトルエンスルホン
酸、蓚酸、燐酸等から選ばれた1種又は2種以上であ
る。
(Solvent) In the present invention, a solvent is usually used to homogenize the reaction system. As the type of solvent used, the boiling point at normal pressure is preferably 80 to 200 ° C.
1 or 2 or more selected from alcohols, ketones, ethers, esters, and cellosolves. (Acid catalyst) The acid catalyst used in the present invention includes hydrochloric acid,
One or more selected from sulfuric acid, benzoic acid, salicylic acid, paratoluenesulfonic acid, oxalic acid, phosphoric acid and the like.

【0014】次に、配合処方について説明する。シリコ
ーン変性ノボラックの製造方法において使用されるアル
デヒド類は、フェノール類1モルに対し0.5〜1.0モ
ル、好ましくは0.6〜0.9モルの範囲である。 0.5
モルを下回る場合は生成樹脂の分子量が小さく機械的強
度が低下する傾向にあり、1.0モルを上回ると生成樹脂
の融点が高く成形性に問題がでるようになる。フェノー
ル類100重量部に対するポリシロキサン−芳香族ポリ
アリル化合物の付加重合体の配合量は10〜50重量部
であり、好ましくは20〜40重量部の範囲である。1
0重量部未満であれば耐水性向上の効果が小さく、40
重量部を越えると強度が低下するようになる。溶媒の使
用量はフェノール類100部に対して5〜200重量部
が好ましいが、更に好ましくは10〜100重量部であ
る。溶媒の使用量が5重量部を下回ると変性反応時に反
応液が均一系になり難いために未反応シリコーンが残留
しやすくなり、200重量部を上回る場合は反応液の濃
度が薄まるために反応性が低下し未反応シリコーンが残
留しやすく、いずれも好ましくない。酸触媒の使用量
は、フェノール類100重量部に対し 0.1〜10重量
部、好ましくは 0.2〜5重量部の範囲である。反応方
法は通常のノボラック樹脂の場合と同様に行う。例えば
反応温度60〜200℃で1〜20時間脱水縮合反応を
行う。
Next, the formulation will be described. The aldehydes used in the method for producing the silicone-modified novolac are in the range of 0.5 to 1.0 mol, preferably 0.6 to 0.9 mol, per mol of the phenols. 0.5
When the amount is less than the molar amount, the molecular weight of the produced resin tends to be small and the mechanical strength tends to be lowered, and when it exceeds 1.0 mol, the melting point of the produced resin is high and the moldability becomes problematic. The compounding amount of the polysiloxane-aromatic polyallyl compound addition polymer with respect to 100 parts by weight of phenols is 10 to 50 parts by weight, and preferably 20 to 40 parts by weight. 1
If it is less than 0 parts by weight, the effect of improving the water resistance is small,
If it exceeds the weight part, the strength will decrease. The amount of the solvent used is preferably 5 to 200 parts by weight, more preferably 10 to 100 parts by weight, based on 100 parts of the phenol. If the amount of the solvent used is less than 5 parts by weight, it is difficult for the reaction solution to become a homogeneous system during the modification reaction, and unreacted silicone tends to remain, and if it exceeds 200 parts by weight, the concentration of the reaction solution decreases and the reactivity becomes low. And the unreacted silicone tends to remain, which is not preferable. The amount of the acid catalyst used is in the range of 0.1 to 10 parts by weight, preferably 0.2 to 5 parts by weight, based on 100 parts by weight of phenols. The reaction method is the same as in the case of a normal novolac resin. For example, the dehydration condensation reaction is performed at a reaction temperature of 60 to 200 ° C. for 1 to 20 hours.

【0015】[0015]

【実施例】【Example】

(ポリシロキサン−芳香族ポリアリル化合物の付加重合
体の合成) 《参考例1》平均重合度10の両末端に水素基を持つハ
イドロジェンジメチルポリシロキサン100重量部に1
重量%の塩化白金酸イソプロパノール溶液を2重量部を
添加した後90℃に加熱した。これにO,O'−ジアリル
ビスフェノールA60重量部を1時間にわたって滴下
し、その後系を100℃に昇温して反応を3時間続け
た。冷却後、粘度が 12700cpsの付加重合体を得た。 《参考例2》平均重合度50の両末端に水素基を持つハ
イドロジェンジメチルポリシロキサン100重量部に1
重量%の塩化白金酸イソプロパノール溶液を2重量部を
添加した後90℃に加熱した。これにO,O'−ジアリル
ビスフェノールA15重量部を1時間にわたって滴下
し、その後系を100℃に昇温して反応を3時間続け
た。冷却後、粘度が 3200cpsの付加重合体を得た。 《参考例3》平均重合度150の両末端に水素基を持つ
ハイドロジェンジメチルポリシロキサン100重量部に
1重量%の塩化白金酸イソプロパノール溶液を2重量部
を添加した後90℃に加熱した。これにO,O'−ジアリ
ルビスフェノールA25重量部を1時間にわたって滴下
し、その後系を100℃に昇温して反応を3時間続け
た。冷却後、粘度が 5400cpsの付加重合体を得た。
(Synthesis of Addition Polymer of Polysiloxane-Aromatic Polyallyl Compound) << Reference Example 1 >> 1 to 100 parts by weight of hydrogen dimethylpolysiloxane having hydrogen groups at both ends with an average degree of polymerization of 10
After adding 2 parts by weight of a wt% isopropanolic chloroplatinate solution, the mixture was heated to 90 ° C. To this, 60 parts by weight of O, O'-diallylbisphenol A was added dropwise over 1 hour, after which the system was heated to 100 ° C. and the reaction was continued for 3 hours. After cooling, an addition polymer having a viscosity of 12700 cps was obtained. Reference Example 2 1 to 100 parts by weight of hydrogen dimethyl polysiloxane having hydrogen groups at both ends with an average degree of polymerization of 50
After adding 2 parts by weight of a wt% isopropanolic chloroplatinate solution, the mixture was heated to 90 ° C. To this, 15 parts by weight of O, O'-diallylbisphenol A was added dropwise over 1 hour, after which the system was heated to 100 ° C and the reaction was continued for 3 hours. After cooling, an addition polymer having a viscosity of 3200 cps was obtained. Reference Example 3 To 100 parts by weight of hydrogendimethylpolysiloxane having hydrogen groups at both ends with an average degree of polymerization of 150, 2 parts by weight of a 1% by weight isopropanol chloroplatinate solution was added, and then heated to 90 ° C. To this, 25 parts by weight of O, O'-diallylbisphenol A was added dropwise over 1 hour, after which the system was heated to 100 ° C and the reaction was continued for 3 hours. After cooling, an addition polymer having a viscosity of 5400 cps was obtained.

【0016】《実施例1》撹拌機、熱交換器、温度計の
付いた反応装置にフェノール100部、37%ホルマリ
ン65部(フェノール1モルに対し0.75モル)、参考
例1によって得られたポリシロキサン−芳香族ポリアリ
ル化合物の付加重合体30部、及び溶媒としてメチルイ
ソブチルケトン100部、触媒として蓚酸1部を仕込
み、常圧で300分間の還流反応を行った後、液温が1
55℃になるまで常圧で脱水反応を行って初期縮合反応
を終了した。その後、液温が155℃、真空度が60To
rrで1時間の脱水縮合反応を行って軟化点92℃のシリ
コーン変性ノボラック樹脂を得た。 《実施例2》撹拌機、熱交換器、温度計の付いた反応装
置にメタクレゾール50部、パラクレゾール50部、3
7%ホルマリン49部(クレゾール1モルに対し0.65
モル)、参考例1によって得られたポリシロキサン−芳
香族ポリアリル化合物の付加重合体30部、及び溶媒と
してメチルイソブチルケトン100部、触媒として蓚酸
0.5部を仕込み、常圧で300分間の還流反応を行っ
た後、液温が155℃になるまで常圧で脱水反応を行っ
て初期縮合反応を終了した。その後、液温が155℃、
真空度が60Torrで1時間の脱水縮合反応を行って軟化
点91℃のシリコーン変性ノボラック樹脂を得た。
Example 1 100 parts of phenol, 65 parts of 37% formalin (0.75 mol per mol of phenol) in a reactor equipped with a stirrer, heat exchanger and thermometer, obtained by Reference Example 1 After adding 30 parts of an addition polymer of polysiloxane-aromatic polyallyl compound, 100 parts of methyl isobutyl ketone as a solvent, and 1 part of oxalic acid as a catalyst, a reflux reaction was carried out at normal pressure for 300 minutes, and then the liquid temperature was 1
The initial condensation reaction was completed by performing dehydration reaction at atmospheric pressure until the temperature reached 55 ° C. After that, the liquid temperature is 155 ° C and the vacuum degree is 60To.
A dehydration condensation reaction was performed for 1 hour at rr to obtain a silicone-modified novolac resin having a softening point of 92 ° C. << Example 2 >> 50 parts of meta-cresol, 50 parts of para-cresol in a reactor equipped with a stirrer, a heat exchanger, and a thermometer, 3
49% 7% formalin (0.65 for 1 mole of cresol)
Mol), 30 parts of an addition polymer of the polysiloxane-aromatic polyallyl compound obtained in Reference Example 1, 100 parts of methyl isobutyl ketone as a solvent, and 0.5 parts of oxalic acid as a catalyst, and refluxed under normal pressure for 300 minutes. After the reaction, the dehydration reaction was carried out at normal pressure until the liquid temperature reached 155 ° C. to complete the initial condensation reaction. After that, the liquid temperature is 155 ℃,
A dehydration condensation reaction was performed at a vacuum degree of 60 Torr for 1 hour to obtain a silicone-modified novolac resin having a softening point of 91 ° C.

【0017】《実施例3》撹拌機、熱交換器、温度計の
付いた反応装置にフェノール100部、85%パラホル
ムアルデヒド26.5部(フェノール1モルに対し0.7
0モル)、参考例2によって得られたポリシロキサン−
芳香族ポリアリル化合物の付加重合体40部、及び溶媒
としてメチルイソブチルケトン100部、触媒として蓚
酸1部を仕込み、常圧で300分間の還流反応を行った
後、液温が155℃になるまで常圧で脱水反応を行って
初期縮合反応を終了した。その後、液温が155℃、真
空度が60Torrで1時間の脱水縮合反応を行って軟化点
90℃のシリコーン変性ノボラック樹脂を得た。 《実施例4》撹拌機、熱交換器、温度計の付いた反応装
置にフェノール100部、37%ホルマリン63部(フ
ェノール1モルに対し0.75モル)、参考例2によって
得られたポリシロキサン−芳香族ポリアリル化合物の付
加重合体40部、及び溶媒としてnーブチルアルコール
100部、触媒として蓚酸1部を仕込み、常圧で300
分間の還流反応を行った後、液温が155℃になるまで
常圧で脱水反応を行って初期縮合反応を終了した。その
後、液温が155℃、真空度が60Torrで1時間の脱水
縮合反応を行って軟化点91℃のシリコーン変性ノボラ
ック樹脂を得た。
Example 3 100 parts of phenol and 26.5 parts of 85% paraformaldehyde in a reactor equipped with a stirrer, a heat exchanger and a thermometer (0.7 per 1 mol of phenol).
0 mol), the polysiloxane obtained in Reference Example 2
After charging 40 parts of an addition polymer of an aromatic polyallyl compound, 100 parts of methyl isobutyl ketone as a solvent, and 1 part of oxalic acid as a catalyst, a reflux reaction was carried out at normal pressure for 300 minutes, and then the liquid temperature was kept at 155 ° C. The dehydration reaction was performed under pressure to complete the initial condensation reaction. Thereafter, a dehydration condensation reaction was performed at a liquid temperature of 155 ° C. and a vacuum degree of 60 Torr for 1 hour to obtain a silicone-modified novolac resin having a softening point of 90 ° C. << Example 4 >> 100 parts of phenol, 63 parts of 37% formalin (0.75 mol per 1 mol of phenol) were placed in a reactor equipped with a stirrer, a heat exchanger, and a thermometer, and the polysiloxane obtained in Reference Example 2 was used. -Add 40 parts of an addition polymer of an aromatic polyallyl compound, 100 parts of n-butyl alcohol as a solvent, and 1 part of oxalic acid as a catalyst, and add 300 at normal pressure.
After carrying out a reflux reaction for 1 minute, a dehydration reaction was carried out under normal pressure until the liquid temperature reached 155 ° C. to complete the initial condensation reaction. Then, a dehydration condensation reaction was performed for 1 hour at a liquid temperature of 155 ° C. and a vacuum degree of 60 Torr to obtain a silicone-modified novolac resin having a softening point of 91 ° C.

【0018】《比較例1》撹拌機、熱交換器、温度計の
付いた反応装置にフェノール100部、37%ホルマリ
ン65部(フェノール1モルに対し0.75モル)、触媒
として蓚酸1部を仕込み、常圧で90分間の還流反応を
行った後、液温が155℃になるまで常圧で脱水反応を
行って初期縮合反応を終了した。その後、液温が155
℃、真空度が60Torrで1時間の脱水縮合反応を行って
軟化点92℃のノボラック樹脂を得た。 《比較例2》撹拌機、熱交換器、温度計の付いた反応装
置にフェノール100部、37%ホルマリン65部(フ
ェノール1モルに対し0.75モル)、参考例1によって
得られたポリシロキサン−芳香族ポリアリル化合物の付
加重合体5部、及び溶媒としてメチルイソブチルケトン
100部、触媒として蓚酸1部を仕込み、常圧で300
分間の還流反応を行った後、液温が155℃になるまで
常圧で脱水反応を行って初期縮合反応を終了した。その
後、液温が155℃、真空度が60Torrで1時間の脱水
縮合反応を行って軟化点93℃のシリコーン変性ノボラ
ック樹脂を得た。
Comparative Example 1 100 parts of phenol, 65 parts of 37% formalin (0.75 mol per mol of phenol), and 1 part of oxalic acid as a catalyst were placed in a reactor equipped with a stirrer, a heat exchanger and a thermometer. After charging, a reflux reaction was carried out at normal pressure for 90 minutes, and then a dehydration reaction was carried out at normal pressure until the liquid temperature reached 155 ° C. to complete the initial condensation reaction. After that, the liquid temperature is 155
A novolak resin having a softening point of 92 ° C. was obtained by performing a dehydration condensation reaction at a temperature of 60 ° C. and a vacuum degree of 60 Torr. << Comparative Example 2 >> 100 parts of phenol, 65 parts of 37% formalin (0.75 mol per 1 mol of phenol) were placed in a reactor equipped with a stirrer, a heat exchanger, and a thermometer, and the polysiloxane obtained in Reference Example 1 -Add 5 parts of an addition polymer of an aromatic polyallyl compound, 100 parts of methyl isobutyl ketone as a solvent, and 1 part of oxalic acid as a catalyst, and add 300 at normal pressure.
After carrying out a reflux reaction for 1 minute, a dehydration reaction was carried out under normal pressure until the liquid temperature reached 155 ° C. to complete the initial condensation reaction. Then, a dehydration condensation reaction was performed for 1 hour at a liquid temperature of 155 ° C. and a vacuum degree of 60 Torr to obtain a silicone-modified novolac resin having a softening point of 93 ° C.

【0019】《比較例3》撹拌機、熱交換器、温度計の
付いた反応装置にフェノール100部、37%ホルマリ
ン65部(フェノール1モルに対し0.75モル)、参考
例1によって得られたポリシロキサン−芳香族ポリアリ
ル化合物の付加重合体60部、及び溶媒としてメチルイ
ソブチルケトン100部、触媒として蓚酸1部を仕込
み、常圧で300分間の還流反応を行った後、液温が1
55℃になるまで常圧で脱水反応を行って初期縮合反応
を終了した。その後、液温が155℃、真空度が60To
rrで1時間の脱水縮合反応を行って軟化点82℃のシリ
コーン変性ノボラック樹脂を得た。 《比較例4》撹拌機、熱交換器、温度計の付いた反応装
置にフェノール100部、37%ホルマリン65部(フ
ェノール1モルに対し0.75モル)、参考例3によって
得られたポリシロキサン−芳香族ポリアリル化合物の付
加重合体40部、及び溶媒としてメチルイソブチルケト
ン100部、触媒として蓚酸1部を仕込み、常圧で30
0分間の還流反応を行った後、液温が155℃になるま
で常圧で脱水反応を行って初期縮合反応を終了した。そ
の後、液温が155℃、真空度が60Torrで1時間の脱
水縮合反応を行って軟化点85℃のシリコーン変性ノボ
ラック樹脂を得た。
Comparative Example 3 100 parts of phenol, 65 parts of 37% formalin (0.75 mol to 1 mol of phenol) were placed in a reactor equipped with a stirrer, a heat exchanger and a thermometer. After adding 60 parts of an addition polymer of polysiloxane-aromatic polyallyl compound, 100 parts of methyl isobutyl ketone as a solvent, and 1 part of oxalic acid as a catalyst, a reflux reaction was carried out at normal pressure for 300 minutes, and then the liquid temperature was 1
The initial condensation reaction was completed by performing dehydration reaction at atmospheric pressure until the temperature reached 55 ° C. After that, the liquid temperature is 155 ° C and the vacuum degree is 60To.
A dehydration condensation reaction was carried out for 1 hour at rr to obtain a silicone-modified novolac resin having a softening point of 82 ° C. << Comparative Example 4 >> 100 parts of phenol, 65 parts of 37% formalin (0.75 mol per 1 mol of phenol), and polysiloxane obtained in Reference Example 3 in a reactor equipped with a stirrer, a heat exchanger, and a thermometer. -Add 40 parts of an addition polymer of an aromatic polyallyl compound, 100 parts of methyl isobutyl ketone as a solvent, and 1 part of oxalic acid as a catalyst.
After performing a reflux reaction for 0 minutes, a dehydration reaction was performed at normal pressure until the liquid temperature reached 155 ° C. to complete the initial condensation reaction. Thereafter, a dehydration condensation reaction was performed at a liquid temperature of 155 ° C. and a vacuum degree of 60 Torr for 1 hour to obtain a silicone-modified novolac resin having a softening point of 85 ° C.

【0020】上記各実施例及び比較例で得られたシリコ
ーン変性ノボラック樹脂あるいはノボラック樹脂100
部にヘキサミン10部を加えて混合し、105μm篩残分が
1.0%以下になるように微粉砕して粉末樹脂とした。
粉末樹脂の融点、流れ及びゲル化時間を JIS K 6909 に
より測定した。測定結果は表1に示す通りであった。
The silicone-modified novolac resin or novolac resin 100 obtained in each of the above Examples and Comparative Examples
10 parts of hexamine was added to and mixed with each other, and finely ground to give a powder resin so that the 105 μm sieve residue was 1.0% or less.
The melting point, the flow and the gelation time of the powdered resin were measured according to JIS K 6909. The measurement results are as shown in Table 1.

【0021】[0021]

【表1】 [Table 1]

【0022】(試験片による特性の測定)実施例1〜2
により作製したシリコーン変性ノボラック樹脂及び比較
例1〜4により作製した比較用シリコーン変性ノボラッ
ク樹脂にヘキサミン 10phrを添加した粉末樹脂につい
て、常態曲げ強さ、湿態曲げ強さ、湿態強さ保持率、動
的曲げ弾性率を測定した。測定方法は次の通りである。 常態曲げ強さ 試験片作製:配合割合 粉末樹脂:アルミナ(#400)=4
0:60(容量%) 寸 法 20×120×10 mm 硬 化 160℃×15分間 後硬化 200℃×3時間 見掛比重 2.55±0.02 測 定 :テンシロン型曲げ強さ測定機使用 スパン100mm、負荷速度20mm/分
(Measurement of characteristics by test piece) Examples 1 and 2
For the silicone-modified novolac resin prepared in accordance with Example 1 and the powder resin obtained by adding 10 phr of hexamine to the comparative silicone-modified novolac resin prepared in Comparative Examples 1 to 4, normal bending strength, wet bending strength, wet strength retention rate, The dynamic flexural modulus was measured. The measuring method is as follows. Normal bending strength Specimen preparation: Mixing ratio Powder resin: Alumina (# 400) = 4
0:60 (% by volume) Size 20 × 120 × 10 mm Hardening 160 ° C × 15 minutes Post-curing 200 ° C × 3 hours Apparent specific gravity 2.55 ± 0.02 Measurement: Using Tensilon type bending strength measuring machine Span 100 mm, load speed 20 mm / min

【0023】 湿態曲げ強さ 試験片作製:状態曲げ強さと同条件の後硬化処理済試験
片をサンドペーパーで表面研磨後、110℃の加圧水中
に2時間浸漬処理 測 定 :状態曲げ強さに同じ 湿態強さ保持率 (湿態曲げ強さ/常態曲げ強さ)×100により算出 動的曲げ弾性率 試験片作製:状態曲げ強さと同条件の後硬化処理済の試
験片を裁断して、8×45×3.5 mmの寸法に研磨仕上
げした。 測 定 :東洋精機製作所製レオログラフピエゾ使
用、昇温速度2℃/分強制振動10Hz、測定温度常温〜
250℃(表1の記入測定値は200℃の時の読取値)
Wet bending strength Test piece preparation: Post-cured test piece under the same conditions as the state bending strength was surface-polished with sandpaper and then immersed in pressurized water at 110 ° C. for 2 hours. Measurement: State bending strength Calculated from the wet strength retention rate (wet flexural strength / normal flexural strength) x 100. Dynamic flexural modulus Test piece preparation: Cut post-cured test pieces under the same conditions as the state flexural strength. And polished to a size of 8 × 45 × 3.5 mm. Measurement: Rheograph piezo manufactured by Toyo Seiki Seisakusho, temperature rising rate 2 ℃ / min forced vibration 10Hz, measurement temperature room temperature ~
250 ° C (Measured values in Table 1 are readings at 200 ° C)

【0024】[0024]

【発明の効果】本発明によるシリコーン変性ノボラック
樹脂の製造方法によれば、通常のノボラック樹脂が有し
ている硬化性、機械的強度などの多くの優れた特長を損
うことなく、耐水性や可撓性にも極めて良好なノボラッ
ク樹脂を得ることができるので、工業的に耐水性や可撓
性の良好なノボラック樹脂を製造する方法として好適で
ある。この製造方法によるシリコーン変性ノボラック樹
脂は耐水性や可撓性の良好なノボラック樹脂の開発を強
く要求している砥石用、摩擦材用、ゴム配合用、電気絶
縁用、塗料用、成形材料用、及び種々の有機物あるいは
無機物の結合用などの用途に適用すると極めて有効であ
ると期待される。
According to the method for producing a silicone-modified novolac resin according to the present invention, water resistance and water resistance can be improved without deteriorating many excellent features such as curability and mechanical strength of ordinary novolac resins. Since it is possible to obtain a novolac resin having excellent flexibility, it is suitable as a method for industrially producing a novolac resin having good water resistance and flexibility. The silicone-modified novolac resin produced by this manufacturing method is strongly required for the development of a water-resistant and flexible novolac resin for grindstones, friction materials, rubber compounds, electrical insulation, paints, molding materials, Also, it is expected to be extremely effective when applied to applications such as bonding of various organic substances or inorganic substances.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 三宅 澄也 東京都千代田区内幸町1丁目2番2号 住 友ベークライト株式会社内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Sumiya Miyake 1-2-2 Uchisaiwaicho, Chiyoda-ku, Tokyo Sumitomo Bakelite Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 フェノール類(a)、アルデヒド類(b)、
及び変性剤として下記式[I]で示されるハイドロジェ
ンオルガノシロキサンと下記式[II]で示される多官能
芳香属ポリアリル化合物とを反応せしめて得られるシリ
コーン系付加重合体(c)を、 【化1】 【化2】 フェノール類(a)100重量部に対して前記シリコーン
系付加重合体(c)10〜50重量部の割合で用い、酸触
媒の存在下で反応させることを特徴とするシリコーン変
性ノボラック樹脂の製造方法。
1. Phenols (a), aldehydes (b),
And a silicone addition polymer (c) obtained by reacting a hydrogenorganosiloxane represented by the following formula [I] with a polyfunctional aromatic polyallyl compound represented by the following formula [II] as a modifier: 1] [Chemical 2] A method for producing a silicone-modified novolac resin, which comprises using 10 to 50 parts by weight of the silicone-based addition polymer (c) with respect to 100 parts by weight of a phenol (a) and reacting in the presence of an acid catalyst. .
JP29042692A 1992-10-28 1992-10-28 Production of silicone-modified novolak resin Pending JPH06136080A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29042692A JPH06136080A (en) 1992-10-28 1992-10-28 Production of silicone-modified novolak resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29042692A JPH06136080A (en) 1992-10-28 1992-10-28 Production of silicone-modified novolak resin

Publications (1)

Publication Number Publication Date
JPH06136080A true JPH06136080A (en) 1994-05-17

Family

ID=17755885

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29042692A Pending JPH06136080A (en) 1992-10-28 1992-10-28 Production of silicone-modified novolak resin

Country Status (1)

Country Link
JP (1) JPH06136080A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008189849A (en) * 2007-02-06 2008-08-21 Sumitomo Bakelite Co Ltd Rubber-modified phenol resin to be formulated with rubber, and rubber formulation
JP2015212721A (en) * 2014-05-01 2015-11-26 信越化学工業株式会社 Negative resist material and pattern forming method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008189849A (en) * 2007-02-06 2008-08-21 Sumitomo Bakelite Co Ltd Rubber-modified phenol resin to be formulated with rubber, and rubber formulation
JP2015212721A (en) * 2014-05-01 2015-11-26 信越化学工業株式会社 Negative resist material and pattern forming method

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