JPS60135418A - Production of modified phenolic resin - Google Patents

Production of modified phenolic resin

Info

Publication number
JPS60135418A
JPS60135418A JP24253583A JP24253583A JPS60135418A JP S60135418 A JPS60135418 A JP S60135418A JP 24253583 A JP24253583 A JP 24253583A JP 24253583 A JP24253583 A JP 24253583A JP S60135418 A JPS60135418 A JP S60135418A
Authority
JP
Japan
Prior art keywords
compound
phenol
reaction
formula
resin
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.)
Granted
Application number
JP24253583A
Other languages
Japanese (ja)
Other versions
JPS635414B2 (en
Inventor
Haruhisa Harada
治久 原田
Hiroshi Maki
真木 洋
Shigeru Sasaki
茂 佐々木
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 Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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 Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP24253583A priority Critical patent/JPS60135418A/en
Priority to EP19840303352 priority patent/EP0126625B1/en
Priority to DE8484303352T priority patent/DE3484994D1/en
Publication of JPS60135418A publication Critical patent/JPS60135418A/en
Publication of JPS635414B2 publication Critical patent/JPS635414B2/ja
Granted legal-status Critical Current

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  • Phenolic Resins Or Amino Resins (AREA)

Abstract

PURPOSE:To obtain a modified phenolic resin excellent in flexibility and heat resistance and useful for paints, adhesives and molding materials, by reacting a reaction product between a specified compound and a phenol with an aldehyde. CONSTITUTION:1mol of a phenol of formula I (wherein R1 is H, a 1-8C alkyl or alkenyl, OH, a group of formula II or the like, and R2 is H, 1-8C alkyl or alkenyl) is reacted with 0.05-3mol of a compound of formula III (wherein R3-4 are each a group of formula IV or V) at 0-180 deg.C in the presence of an acidic catalyst such as sulfuric acid, and the product is neutralized and then dehydrated to obtain a compound (A). Compound A is reacted with an aldehyde in an amount to provide a ratio of the total number of moles of the OH groups in component A and OH groups in the phenol of formula I to the number of moles of the aldehyde groups of 1:0.1-2 at 80 deg.C-refluxing temperature for 30min-4hr in the presence (or absence) of a phenol of formula I in the presence of an acidic or alkaline catalyst to obtain the titled resin.

Description

【発明の詳細な説明】 本発明は塗料、接着剤、成形材料等として非常に有用な
変性フェノール系樹脂の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing modified phenolic resins which are very useful as paints, adhesives, molding materials and the like.

従来フェノール系樹脂の製造方法として、フェノール類
を酸性触媒存在Fでホルムアルデヒド等のアルキル化剤
と反応させる方法が知られている。本発明者等は、この
ようにして得られるフェノール系樹脂の可撓性、耐熱性
の改良を鋭意検討の結果、従来のホルムアルデヒド等ア
ルデヒド類に代え、一般式中) す、、几4の定義はR8と同じであり、同一であっても
異っていてもよい。) で表わされる化合物を酸性触媒の存在−Fに反応させて
得られるフェノール系樹脂を、フェノールノボラック樹
脂等に配合して用いることにより従来のフェノールノボ
ラック樹脂等の可撓性、耐熱性が著るしく改良されるこ
とを見いだし特願昭58−87978号を出願した。
As a conventional method for producing phenolic resins, a method is known in which phenols are reacted with an alkylating agent such as formaldehyde in the presence of an acidic catalyst F. As a result of intensive studies to improve the flexibility and heat resistance of the phenolic resin obtained in this way, the present inventors replaced conventional aldehydes such as formaldehyde with the following: is the same as R8, and may be the same or different. ) The flexibility and heat resistance of conventional phenol novolak resins can be improved by blending the phenolic resin obtained by reacting the compound represented by (-F) with the presence of an acidic catalyst into a phenol novolak resin, etc. He discovered that it could be improved and filed Japanese Patent Application No. 87978/1983.

さらに、本発明者らは、特願昭58−87978号をふ
まえてフェノールノボラック樹脂等の改質をはかるべく
鋭意検討を進めた結果、本発明を見い出すに至った。
Further, the present inventors have conducted intensive studies to modify phenol novolak resins based on Japanese Patent Application No. 58-87978, and as a result, they have discovered the present invention.

即ち本発明は一般式(イ) R+ 凡2 (式中、R1はH1炭素数1〜8のアルキル基、炭素数
1〜8のアルケニル基、−on基、基を、R2はH1炭
素数1〜8のアルキル基または炭素数1〜8のアルケニ
ル基を示す。)で表わされるフェノール類と一般式田)
示す。孔4の定義はRsと同じであり、同一であっても
異っていてもよい。) で表わされる化合物とを酸性触媒の存在下に反応して得
られる化合物を 一般式四 1 (式中、損 はH1炭素数1〜8のアルキル基、炭素数
1〜8のアルケニル基、−(JR基、を、几2 は■、
炭素数1〜8のアルキル基または炭素数1〜8のアルケ
ニル基を示す。)で表わされるフェノール類の存在下又
は実質的に非存在下に酸性触媒下又はアルカリ性触媒下
でアルデヒド類と反応させることを特徴とする変性フェ
ノール系樹脂の製造法である。
That is, the present invention is based on the general formula (A) R+ 2 (wherein, R1 is an alkyl group with H1 having 1 to 8 carbon atoms, an alkenyl group having 1 to 8 carbon atoms, a -on group, and R2 is an alkyl group having H1 having 1 to 8 carbon atoms; ~8 alkyl group or C1-8 alkenyl group) and general formulas)
show. The definition of hole 4 is the same as Rs, and may be the same or different. ) in the presence of an acidic catalyst to form a compound obtained by the general formula 41 (wherein H1 is an alkyl group having 1 to 8 carbon atoms, an alkenyl group having 1 to 8 carbon atoms, - (JR group, 几2 is ■,
It represents an alkyl group having 1 to 8 carbon atoms or an alkenyl group having 1 to 8 carbon atoms. ) is a method for producing a modified phenolic resin, which is characterized by reacting the modified phenolic resin with an aldehyde in the presence or substantially absence of the phenol represented by the following formula under an acidic catalyst or an alkaline catalyst.

以下水′発明の詳細な説明する。The invention will be described in detail below.

本発明の一般式四で表わされるフェノール類の具体例は
、フェノール、クレゾール、エチルフェノール、イソプ
ロピルフェノール、イソプロペニルフェノール、ターシ
ャリブチルフェノール、オクチルフェノール、キシレノ
ール、レゾルシノール、カテコール、ハイドロキノン、
フェニルフェノール、クミルフェノール、4゜4′−ジ
ヒドロキシ−ジフェニル−2,2−プロパン等である。
Specific examples of the phenols represented by the general formula 4 of the present invention include phenol, cresol, ethylphenol, isopropylphenol, isopropenylphenol, tert-butylphenol, octylphenol, xylenol, resorcinol, catechol, hydroquinone,
These include phenylphenol, cumylphenol, 4°4'-dihydroxy-diphenyl-2,2-propane, and the like.

一般式の)の化合物の具体例は1.8−ジイソプロペニ
ルベンゼン、■、4−ジイソプロペニルベンゼン、8−
(2−ヒドロキシ−2−プロピル)−イソプロペニルベ
ンゼン、4−(2−ヒドロキシ−2−プロピル)−イソ
プロペニルベンゼン、1.8−ジ(2−ヒドロキシ−2
−ブロビル)ベンゼン、1.4−ジ(2−ヒドロキシ−
2−プロピル)ベンゼン等である。これらの化合物は、
単独または2[以上を併用することもできる。
Specific examples of compounds of general formula) are 1,8-diisopropenylbenzene, 4-diisopropenylbenzene, 8-diisopropenylbenzene,
(2-hydroxy-2-propyl)-isopropenylbenzene, 4-(2-hydroxy-2-propyl)-isopropenylbenzene, 1,8-di(2-hydroxy-2
-brobyl)benzene, 1,4-di(2-hydroxy-
2-propyl)benzene, etc. These compounds are
They can be used alone or in combination of two or more.

一般式四の化合物は、その製造は特に限定されないが、
例えば、ジイソプロピルベンゼンの脱水素によって得る
ことができ、あるいはジイソプロピルベンゼンの空気酸
化によって得ることができる一般式+a+ 示す。) で表わされるヒドロペルオキシドの亜硫酸ソーダ、水素
等による還元処理によっても得ることができる。さらに
一般式向で表わされるカルビノール類を脱水して一般式
の〕で表わされるオレフィン類を得る仁ともできる。こ
れらの化合物は単独でも2つ以上の混合物としても反応
に供することができる。
The production of the compound of general formula 4 is not particularly limited, but
For example, the general formula +a+ can be obtained by dehydrogenation of diisopropylbenzene or by air oxidation of diisopropylbenzene. ) It can also be obtained by reducing the hydroperoxide represented by the formula with sodium sulfite, hydrogen, etc. Furthermore, carbinols represented by the general formula can be dehydrated to obtain olefins represented by the general formula. These compounds can be used alone or as a mixture of two or more in the reaction.

本発明に於ける一般式(3)のフェノール類と一般式(
B)の化合物とを、酸性触媒の存在下に反応して得られ
る化合物の製法に於いて、フェノール類と一般式の)で
表わされる化合物との反応仕込割合は特に制限されず、
得られる化合物の目的の性状に合せて決められる。つま
りフェノール類の仕込割合が多い程、一般にフェノール
類が多く反応した化合物となり、耐熱性の高いものを得
ることができる。通常、フェノール類1モル当り、一般
式(Blの化合物は0.05〜8倍モル量が用いられる
。触媒としては、硫酸、塩酸、リン酸などの鉱酸、シリ
カ−アルミナ、酸性白土などの固体酸、ギ酸、シュウ酸
、P−トルエンスルホン酸などの有機酸、塩化アルミ、
塩化鉄、塩化亜鉛などのフリーデルタラフト触媒等が例
示される。その使用量は特に制限を受けず、反応温度と
の兼合いで、得られる化合物の目的の性状に合せて決め
られるが、通常フェノール類と一般式(Blの化合物の
合計の1重量部当たり0.001〜aooxm部の範囲
で用いられる。
In the present invention, phenols of general formula (3) and general formula (
In the method for producing a compound obtained by reacting the compound B) in the presence of an acidic catalyst, the proportion of the phenols and the compound represented by the general formula) is not particularly limited,
It is determined according to the desired properties of the compound to be obtained. In other words, the higher the proportion of phenols added, the more phenols react in the resulting compound, and the higher the heat resistance can be obtained. Usually, the compound of the general formula (Bl) is used in an amount of 0.05 to 8 times the mole per mole of phenols.As a catalyst, mineral acids such as sulfuric acid, hydrochloric acid, phosphoric acid, silica-alumina, acid clay, etc. Solid acids, organic acids such as formic acid, oxalic acid, P-toluenesulfonic acid, aluminum chloride,
Examples include free delta raft catalysts such as iron chloride and zinc chloride. The amount used is not particularly limited and is determined in consideration of the reaction temperature and the desired properties of the compound to be obtained, but it is usually 0.00% per 1 part by weight of the total of the phenols and the compound of the general formula (Bl). It is used in the range of .001 to aooxm parts.

反応温度は通常0°C−180℃であるが一般に温度が
低い程、反応の効率を良くするために酸性触媒を多く使
用し、温度が高い程、酸性触媒は少なくて良い。さらに
、一般式03)の化合物として、カルビノール類を用い
る場合、反応を効率良く行なわせるために反応で生成す
る水を反応系外へ除去しながら行なうこともでき、又反
応をより円滑に行なわせるために適当な有機fd剤、例
えば、ベンセン、トルエン、ヘキサン、ヘプタンなどを
用いることもできる。反応圧力は、通常は大気圧Fで行
なわれるが反応で水が生成する場合は、水を反応系外へ
除去する意味で減圧下で行なうこともでき、又酸性触媒
が気体の場合は加圧下で行なうこともできる。
The reaction temperature is usually 0°C to 180°C, and generally, the lower the temperature, the more acidic catalyst is used to improve the efficiency of the reaction, and the higher the temperature, the less acidic catalyst is needed. Furthermore, when carbinols are used as the compound of general formula 03), water generated in the reaction can be removed from the reaction system in order to carry out the reaction efficiently, or the reaction can be carried out more smoothly. Suitable organic fd agents, such as benzene, toluene, hexane, heptane, etc., can also be used to increase the concentration. The reaction pressure is usually atmospheric pressure F, but if water is produced in the reaction, it can be carried out under reduced pressure to remove water from the reaction system, or under increased pressure if the acidic catalyst is a gas. You can also do it with

この様なフェノール類と一般式Φ)の化合物との反応に
よって得られる化合物は、室温で液状のものから200
℃の軟化点を有する固体のものまで得ることができ、本
発明目的の変性フェノール系樹脂の使用目的によって調
節可能である。
The compound obtained by the reaction of such phenols with the compound of the general formula Φ) ranges from liquid at room temperature to 200%
It is possible to obtain a solid material having a softening point of .degree. C., and it can be adjusted depending on the intended use of the modified phenolic resin for the purpose of the present invention.

フェノール類と一般式の)の化合物との反応で得られる
化合物は通常反応後、中和処理、脱水及び親有機溶媒等
の操作後次のアルデヒド類との反応に供しても良く、中
和処理、脱水及び親有機溶媒等の操作に、未反応のフェ
ノール類を留出除去後、この缶液を次のアルデヒド類と
の反応に供しても良く、さらに未反応のフェノール類を
留出除去後の缶液を有機だ媒等で再結晶等の操作を行な
い、精製品を得て次のアルデヒド類との反応に供しても
良く、特に制限はされない。通常変性フェノール系樹脂
の使用目的により次のアルデヒド類との反応に於けるフ
ェノ−ル類の−UkL基とアルデヒド基の所要モル比で
任意に調節されてこの操作方法が決められる。
The compound obtained by the reaction of phenols with the compound of the general formula () may be subjected to the next reaction with aldehydes after the reaction, neutralization treatment, dehydration, and operations such as organophilic solvent. After removing unreacted phenols by distillation, this bottom liquid may be subjected to the next reaction with aldehydes for dehydration and organic solvent operations, and further, after removing unreacted phenols by distillation. The distilled liquid may be subjected to operations such as recrystallization using an organic solvent, etc. to obtain a purified product, and the purified product may be subjected to the next reaction with aldehydes, and there is no particular restriction. Usually, this operation method is determined by arbitrarily adjusting the required molar ratio of the -UkL group of the phenol and the aldehyde group in the following reaction with the aldehyde, depending on the intended use of the modified phenolic resin.

一般式四のフェノール類と一般式の)の化合物との反応
で得られる化合物とアルデヒド類との反応は一般式四の
フェノール類の存在下又は実質的に非存在下に通常のフ
ェノール樹脂のノボラック、レゾール製造と同様な方法
で行なわれる。一般式四のフェノール類と一般式の)の
化合物との反応で得られる化合物と一般式囚のフェノー
ル類の混合割合は特に制限はされず変性フェノール樹脂
の使用目的によって決められろ。
The reaction of the compound obtained by the reaction of the phenol of general formula 4 with the compound of general formula ) and the aldehyde is carried out in the presence or substantially absence of the phenol of general formula , carried out in a similar manner to resol production. The mixing ratio of the compound obtained by the reaction of the phenol of the general formula 4 with the compound of the general formula () and the phenol of the general formula is not particularly limited and may be determined depending on the intended use of the modified phenol resin.

この反応で用いる、アルデヒド類は、特に制限はされな
いが、得られる変性フェノール樹脂の使用目的によって
通常、フェノール類と一般弐〇の化合物との反応で得ら
れる化合物の一01i基及び一般式四のフェノール類の
−OR基の合計−囲碁モル数とアルデヒド基のモル数の
比カ酸性触媒の場合t:o、t−t、o、アルカリ性触
媒の場合l:1.0〜2.0の範囲となる様調節して用
いられる。
The aldehydes used in this reaction are not particularly limited, but depending on the purpose of use of the resulting modified phenol resin, the aldehydes used are usually the 101i group of the compound obtained by the reaction of the phenol with the compound of general formula 2 and the compound of general formula 4. The ratio of the total number of -OR groups of phenols to the number of moles of Go and the number of moles of aldehyde groups: t: o, t-t, o for acidic catalysts, l: range of 1.0 to 2.0 for alkaline catalysts It is used by adjusting it so that it becomes .

本発明の変性フェノール系樹脂の製造に於いて使用する
アルデヒド類は一般的なホルムアルデヒド、パラホルム
アルデヒド、フルフラールアセトアルデヒド類が用いら
れ、酸性触媒は、硫酸、塩酸、シュウ酸、ギ酸、パラト
ルエンスルホン酸等が、又、アルカリ性触媒は、水酸化
ナトリウム、水酸化カリウム、水酸化バリウム、消石灰
、アンモニア水、トリエタノールアミン、トリエチルア
ミン等が用いられる。通常、この反応は80°C〜還流
下の温度で80分〜4時間反応を行ない、必要に応じて
中和、水洗、減圧脱水等の操作を行なった後、内容物を
冷却して固型又は液状の変性フェノール系樹脂として回
収される。
The aldehydes used in the production of the modified phenolic resin of the present invention include general formaldehyde, paraformaldehyde, and furfural acetaldehyde, and the acidic catalysts include sulfuric acid, hydrochloric acid, oxalic acid, formic acid, paratoluenesulfonic acid, etc. However, as the alkaline catalyst, sodium hydroxide, potassium hydroxide, barium hydroxide, slaked lime, aqueous ammonia, triethanolamine, triethylamine, etc. are used. Usually, this reaction is carried out at a temperature of 80°C to reflux for 80 minutes to 4 hours, and if necessary, after performing operations such as neutralization, washing with water, and dehydration under reduced pressure, the contents are cooled and solidified. Alternatively, it can be recovered as a liquid modified phenolic resin.

本発明で得られる変性フェノール系樹脂は多種、多用途
に使用されるが、この多用途への適用性はこの樹脂のも
つ−OH基、及び その代表的な例は従来のフェノール樹脂の改良である。
The modified phenolic resin obtained in the present invention is used for a wide variety of purposes, and its applicability to various uses is due to the -OH group of this resin, and a typical example is the improvement of conventional phenolic resins. be.

例えば−フェノールとホルムアルデヒドとを酸性ドで反
応して得られるフェノールノボラック樹脂に配合して、
又は、本発明の方法で得られる樹脂を単独でシェルモー
ルド用粘結剤として供した場合、砂鋳型の強度の付与、
並びに低膨張化剤となる。さらに本発明の方法で得られ
る樹脂をフェノールノボラック樹脂に配合して、又は、
本発明の方法で得られる樹脂を単独で、ヘキサメチレン
チトラミン硬化させることによって硬化物の耐熱性を向
上させることができる。
For example, by blending phenol novolac resin obtained by reacting phenol and formaldehyde with acidic solution,
Alternatively, when the resin obtained by the method of the present invention is used alone as a binder for shell molds, it can provide strength to sand molds,
It also serves as a low expansion agent. Furthermore, by blending the resin obtained by the method of the present invention with a phenol novolak resin, or
The heat resistance of the cured product can be improved by curing the resin obtained by the method of the present invention alone with hexamethylene lentithramine.

又、ウレタン樹脂やエポキシ樹脂の硬化剤成分として配
合することによって塗料、成形材料、積層板などの耐熱
性を向上させることができる。
Furthermore, by blending it as a curing agent component in urethane resins and epoxy resins, the heat resistance of paints, molding materials, laminates, etc. can be improved.

こうした反応性を利用した応用法の他にその粘着性を与
えるためにホットメルト接着剤、ゴム系接着剤への配合
や、ホルムアルデヒド、ロジン、カシューなど、による
変性フェノール系樹脂としても用いられる。
In addition to application methods that take advantage of such reactivity, it is also used as a phenolic resin modified with formaldehyde, rosin, cashew, etc., and blended into hot melt adhesives and rubber adhesives to provide adhesive properties.

この様に本発明により得られる変性フェノール系樹脂は
塗料、成形材料、積層板、接着剤、鋳物砂粘結剤など多
くの用途に使用することができる。
As described above, the modified phenolic resin obtained according to the present invention can be used in many applications such as paints, molding materials, laminates, adhesives, and foundry sand binders.

以下実施例により本発明をさらに詳細に説明するが、本
発明の範囲は、これらlこよって制限を受けるものでは
ない。
The present invention will be explained in more detail with reference to Examples below, but the scope of the present invention is not limited thereby.

実施例1 温度計、かくはん機、滴゛ドロー斗及び還流冷却器をつ
けた反応器にフェノール141.2f(1,5モル)、
1.8−ジ(2−ヒドロキシ−2−プロピル)ベンゼン
194.8 f(1,0モル)を仕込み100°Cに昇
温しな。次いで滴下ロー斗より濃塩酸8.85Fを滴下
し、還流下4時間反応を行なった。
Example 1 Phenol 141.2f (1.5 mol) was added to a reactor equipped with a thermometer, stirrer, dropping funnel and reflux condenser.
1. Charge 194.8 f (1.0 mol) of 8-di(2-hydroxy-2-propyl)benzene and raise the temperature to 100°C. Next, concentrated hydrochloric acid (8.85 F) was added dropwise from the dropping funnel, and the reaction was carried out under reflux for 4 hours.

コ(7)後、87%ホルマリン水40.6 F(0,5
0モル)を滴丁ロー斗より除々に滴下〇、滴下終了後、
還流ド80分間反応を継続した。反応終了後、重ソー水
で中和、200−温水で2回水洗し、反応生成物を加熱
減圧脱水して、透明で淡黄上色の固型樹脂295fを得
た。
After (7), 87% formalin water 40.6F (0.5
Gradually drop 0 mol) from the dropping funnel〇, after the dropping is completed,
The reaction was continued at reflux for 80 minutes. After the reaction was completed, the reaction product was neutralized with sodium chloride water, washed twice with 200-warm water, and the reaction product was dehydrated under reduced pressure to obtain a transparent solid resin 295f with a pale yellow color.

この樹脂の軟化点は105℃であった。The softening point of this resin was 105°C.

参考例1 温度計、かくはん機、還流冷却器をつけた反応器にフェ
ノール752.9g(8,0モル)1.8−ジ(2−ヒ
ドロキシ−2プロピル)ヘンセン194.8 f (1
,0モ# ) 、溶媒としてトルエン1200−を仕込
み、塩化水素を吹込みながら25〜80”Cの温度範囲
で2時間反応を行なった。反応終了後10%NaOH水
で中和、さらに水洗し、加熱減圧下で脱水脱溶媒、脱フ
ェノールを行なった。得られた内容物をトルエンで再結
晶して、分子量846の1.8−ジ(2−p−ヒドロキ
シフェニル−2−プロピル)ベンゼン(以下化合物−(
イ)とする。>2251を得た。(融点187〜140
℃)。さらに再結晶P液から1,8−シ(2−p−ヒド
ロキシフェニル−2−プロピル)ベンゼンを69重量%
含む化合物−(ロ)を125f回収し、以下本発明実施
例の反応に供した。
Reference Example 1 In a reactor equipped with a thermometer, a stirrer, and a reflux condenser, 752.9 g (8.0 mol) of phenol and 194.8 f (1
, 0 mo#), toluene 1200- was charged as a solvent, and the reaction was carried out for 2 hours at a temperature range of 25 to 80"C while blowing hydrogen chloride. After the reaction was completed, it was neutralized with 10% NaOH water and further washed with water. , dehydration, solvent removal, and phenol removal were performed under heating and reduced pressure.The obtained contents were recrystallized from toluene to obtain 1.8-di(2-p-hydroxyphenyl-2-propyl)benzene (2-p-hydroxyphenyl-2-propyl)benzene (with a molecular weight of 846). The following compound -(
b). >2251 was obtained. (Melting point 187-140
℃). Furthermore, 69% by weight of 1,8-si(2-p-hydroxyphenyl-2-propyl)benzene was extracted from the recrystallized P solution.
125f of the containing compound -(b) was recovered and subjected to the reaction in the following examples of the present invention.

実施例2 反応器に参考例1で得られた化合物−(イ)を27.7
F(0,08モル)と、フェノール79,0f(0,8
4モル)とを仕込み加熱溶解した。
Example 2 27.7% of the compound (a) obtained in Reference Example 1 was placed in a reactor.
F (0.08 mol) and phenol 79.0f (0.8 mol)
4 mol) and heated to dissolve.

次いで触媒としてシュウ酸1、ofを添加し、引続いて
、87%ホルマリン水67.4F(0,88モル)を添
加して還流下1.5時間の反応を行なった。
Next, 1.0 ml of oxalic acid was added as a catalyst, followed by 67.4 F (0.88 mol) of 87% formalin water, and the reaction was carried out under reflux for 1.5 hours.

反応終了後、200−の温水で2回、デカンチーシラン
水洗し、反応生成物を、加熱、減圧脱水して、透明で淡
黄上色の固型樹脂105fを得た。この樹脂の軟化点は
107℃であった。
After the reaction was completed, the reaction product was washed with decane silane twice with 200-g warm water, and the reaction product was heated and dehydrated under reduced pressure to obtain a transparent, pale yellow solid resin 105f. The softening point of this resin was 107°C.

実施例8 参考例1で得られた化合物−(ロ)を29.69(−o
n 基で0.16モル相当)とフェノール79、 Of
 (0,84モル)とを仕込みンユウ酸1.0f、87
%ホルマリン水67.41 (0,88モル)を添加し
て以下実施例2と同様な操作を行ない、透明で淡黄上色
の固型樹脂102fを得た。この樹脂の軟化点は102
℃であった。
Example 8 The compound -(b) obtained in Reference Example 1 was converted to 29.69(-o
n group equivalent to 0.16 mol) and phenol 79, Of
(0.84 mol) and oxalic acid 1.0f, 87
After adding 67.41% (0.88 mol) of formalin water, the same operation as in Example 2 was carried out to obtain a transparent, pale yellow solid resin 102f. The softening point of this resin is 102
It was ℃.

実施例4 反応器に参考例1で得られた化合物−(イ)を84.6
F(0,10モル)、フェノール76.8F(0,80
モル)、87%ホルマリン水89,8F(1,10モル
)及び触媒としてアンモニア水(比重0.8814fを
仕込んで45分を要して沸点まで加熱し、さらに80分
間、還流Fで反応を行なった。反応終了後200TTt
の温水で2回デカノテーシぢン水洗し、反応生成物を加
熱、減圧脱水して、淡黄褐色の固型樹脂180fを得た
。この樹脂の軟化点は71°Cであった。
Example 4 84.6% of the compound-(a) obtained in Reference Example 1 was placed in a reactor.
F (0,10 mol), phenol 76.8F (0,80
mol), 87% formalin water 89.8F (1.10 mol), and aqueous ammonia (specific gravity 0.8814f) as a catalyst were charged and heated to the boiling point over 45 minutes, and the reaction was further carried out under reflux F for 80 minutes. 200TTt after the completion of the reaction
The reaction product was decanotated twice with warm water, and the reaction product was heated and dehydrated under reduced pressure to obtain a pale yellowish brown solid resin 180f. The softening point of this resin was 71°C.

実施例5 フェノールと1.4−ジ(2−ヒドロキシ−2−プロピ
ル)ベンゼンを用いて参考例1と同様な反応及び後処理
操作を行ない、1゜4−ジ(2−P−ヒドロキシフェニ
ル−2−プロピル)ベンゼンを88重量%含む化合物−
e場を得た。(但し、反応後の加熱減圧下で脱水、脱溶
媒、脱フェノールを行なった後の濃縮缶液をさす。) 、この化合物−ぐ1を21.6 f (−(Jll基で
0.12モル相当)とフェノール82.8F(0,88
モル)とを仕込み、シュウ酸1.Of、87%ホルマリ
ン水67.4F(0,88モル)を添加して以下実施例
2と同様な操作を行ない透明で淡黄上色の固型樹脂10
7fを得た。この樹脂の軟化点は、113°Cであった
Example 5 The same reaction and post-treatment as in Reference Example 1 were carried out using phenol and 1,4-di(2-hydroxy-2-propyl)benzene to produce 1°4-di(2-P-hydroxyphenyl- Compound containing 88% by weight of 2-propyl)benzene
I got an e field. (However, this refers to the concentrated distillate after dehydration, desolvation, and dephenolization under heating and reduced pressure after the reaction.) This compound equivalent) and phenol 82.8F (0,88
mol) and 1. mol of oxalic acid. Of, 67.4F (0.88 mol) of 87% formalin water was added and the same operation as in Example 2 was carried out to obtain a transparent, pale yellow solid resin 10.
I got 7f. The softening point of this resin was 113°C.

実施例6 p−クレゾール648.81(6,0モル)、1.8−
ジ(2−ヒドロキシ−2−プロピル)ベンゼン194.
8F(1,0モル)、溶媒としてトルエン1000−を
用いて、参考例1と同様な反応及び後処理操作を行ない
、1.3−ジ[2−(2−ヒドロキシ−5−メチルフェ
ニル)2−プロピル]ベノゼンを87M1L%含む化合
物−に)を得た。(但し、反応後の加熱減圧下で脱水、
脱溶媒、脱p−クレゾールを行なった後の濃縮缶液)さ
す。) 仁の化合物−に)を、28.41 (−0fi基で0.
12モル相当)とp−クレゾール95.1F(0,88
モル)とを仕込み、シュウ酸1.5f、87%ホルマリ
ン水67.49 (0,88モル)を添加して、以下実
施例2と同様な操作を行ない透明で淡黄上色の固型樹脂
96fを得た。
Example 6 p-cresol 648.81 (6.0 mol), 1.8-
Di(2-hydroxy-2-propyl)benzene 194.
Using 8F (1.0 mol) and toluene 1000 as a solvent, the same reaction and post-treatment operations as in Reference Example 1 were carried out to obtain 1,3-di[2-(2-hydroxy-5-methylphenyl)2 A compound containing 87M1L% of -propyl]benozene) was obtained. (However, dehydration under heating and reduced pressure after the reaction,
Concentrated can liquid after solvent removal and p-cresol removal). ) to 28.41 (-0fi group).
12 mole equivalent) and p-cresol 95.1F (0,88
After adding 1.5 f of oxalic acid and 67.49 (0.88 mol) of 87% formalin water, the same procedure as in Example 2 was carried out to obtain a transparent, pale yellow solid resin. I got 96f.

この樹脂の軟化点は109℃であった。The softening point of this resin was 109°C.

実施例7 レゾルシン880.1 F (8モル)、1,8−ジ(
2−ヒドロキシ−2−プロピル)−ベンセン194.8
F(1,0モル)、溶媒としてベンモノ10100O,
濃塩酸1000−を仕込み、5℃で15時間反応を行な
った。反応終了後黄土色の油層を分離し、熱炭酸ソーダ
水で中和した。中和後、油層中に含まれている未反応の
レゾルシンを熱水況浄で除去し、油層を氷水浴で冷却し
た。冷却により、淡黄上色の固体が析出し、口過分離で
淡黄上色の化合物−(ホ)を得た。
Example 7 Resorcinol 880.1 F (8 mol), 1,8-di(
2-Hydroxy-2-propyl)-benzene 194.8
F (1.0 mol), Benmono 10100O as a solvent,
1,000 ml of concentrated hydrochloric acid was charged and the reaction was carried out at 5°C for 15 hours. After the reaction was completed, the ocher oil layer was separated and neutralized with hot soda water. After neutralization, unreacted resorcin contained in the oil layer was removed by hot water purification, and the oil layer was cooled in an ice water bath. Upon cooling, a pale yellowish solid was precipitated, and by oral separation, a pale yellowish compound (e) was obtained.

この化合物−(ホ)は、1.3−ジ[2−(2゜4−ジ
ヒドロキシフェニル)−2−プロピル]ベンゼンを95
重重息含んでいた。
This compound (e) contains 1,3-di[2-(2゜4-dihydroxyphenyl)-2-propyl]benzene at 95%
He was breathing heavily.

この化合物−(ホ)を29.8 II (−OR基テ0
.8モル相当)とレゾルシン77、LfCo、7モル)
とを仕込み、シュウ酸1.of、37%ホルマリン水6
7.4F(0,88モル)を添加して以下実施例2と同
様な操作を行ない、淡黄褐色の固型樹脂110f得た。
This compound -(e) is 29.8 II (-OR group Te0
.. 8 mol equivalent) and resorcinol 77, LfCo, 7 mol)
and 1. oxalic acid. of, 37% formalin water 6
7.4F (0.88 mol) was added and the same operation as in Example 2 was carried out to obtain a pale yellowish brown solid resin 110f.

この樹脂の軟化点は101℃であった。The softening point of this resin was 101°C.

実施例8 参考例1で得られた化合物−(ロ)を44.4F(−0
H基で0.24モル相当)とフェノール□71.5F(
0,76モル)を仕込み、シュウ酸1、Of、87%ホ
ルマリン水67.410.88モル)を添加して以下実
施例2と同様な操作を行ない、透明で淡黄上色の固型樹
脂118fを得た。この樹脂の軟化点は104”Cであ
った。
Example 8 Compound -(b) obtained in Reference Example 1 was heated to 44.4F(-0
H group equivalent to 0.24 mol) and phenol □71.5F (
0.76 mol) of oxalic acid, 1 of oxalic acid, 67.410.88 mol of 87% formalin water) were added, and the same operation as in Example 2 was carried out to obtain a transparent, pale yellow solid resin. 118f was obtained. The softening point of this resin was 104''C.

この得られた樹脂を用いてノニルモールド用、及びフェ
ノール成形、材料用評価を行なった例を以下にホす。
Examples of evaluations for nonyl molding, phenol molding, and materials using the obtained resin are shown below.

くノニルモールド用の評価〉 この固型樹脂50M量部と市販のフェノールノボラック
樹脂50重患部を150℃に予熱した7号ケイ砂800
0重量部に混合した後、ヘキサメチレンテトラミンの2
0%水浴液60重量部を加えて更に混合し、砂の粒子が
ほぐれるようになったところでステアリン酸カルシウム
を8重量部を加えた。
Evaluation for nonyl mold> 50M parts of this solid resin and 50 parts of commercially available phenol novolac resin were mixed with No. 7 silica sand 800 preheated to 150°C.
After mixing to 0 parts by weight, 2 parts of hexamethylenetetramine
60 parts by weight of 0% water bath solution was added and further mixed, and when the sand particles became loose, 8 parts by weight of calcium stearate was added.

得られた樹脂被覆砂を使用してシェルモールドとしての
性能を250 ’Cの金型で。の熱処理時開とその25
0 ”G!に於ける熱間強度により調べた。同様にフェ
ノールノボラック樹脂とへキサメチレンテトラミンのみ
の場合と比較して本発明の固型樹脂を用いるとより少な
いへキサミン屋で強度が発現することが判明した。
The resulting resin-coated sand was used to perform as a shell mold in a mold at 250'C. Opening during heat treatment and Part 25
It was investigated by hot strength at 0 ”G!.Similarly, compared to the case of using only phenol novolac resin and hexamethylenetetramine, when the solid resin of the present invention is used, strength is developed with less hexamine. It has been found.

以Fに実験値を示す。Experimental values are shown below.

く成形材料用の呼側) この固型樹脂を用いフェノール樹脂成形材料の改質を行
なったところ以Fに示す結果のごとくとなり、耐熱性、
曲げ強さが改良されることが判明した。
When this solid resin was used to modify a phenolic resin molding material, the results shown in F were obtained, and the heat resistance,
It was found that the bending strength was improved.

以下に実験値を示す。Experimental values are shown below.

(1) 成形材料の作成と成形 表−2に示す配合処方のものを二本ロ ール(110〜120°C)で5分間混練した後、冷却
し粉砕して成形材料とした。
(1) Preparation of molding material and molding The formulation shown in Table 2 was kneaded for 5 minutes with two rolls (110 to 120°C), then cooled and pulverized to obtain a molding material.

これを170°Cで2分間 180 Kg/mGで圧縮
成形した。
This was compression molded at 170°C for 2 minutes at 180 Kg/mG.

表−2成形材料配合処方(N′kk部)(2) 成形物
物性 (1)で得られた成形物の物性を表−8に示す。
Table 2 Molding material formulation (N'kk part) (2) Physical properties of the molded product Table 8 shows the physical properties of the molded product obtained in (1).

Claims (1)

【特許請求の範囲】 一般式(4) (式中、R+lよH1炭素数1〜8のアルキル基、炭素
数1〜8のアルケニル基、 −OH基、を、R2はH1
炭素数1〜8のアルキル基または炭素数1〜8のアルケ
ニル基を示す。)で表わされるフェノール類と一般式向 を示す。R4の定義はR8と同じであり、 Reと同一
でも異っていてもよい。) で表わされる化合物とを酸性触媒の存在下に反応して得
られる化合物を 一般式(ト) 1 fl! (式中、R1はH1炭素数1〜8のアルキル基、炭素数
1〜8のアルケニル基、−OH基、基を、 RzはH1
炭素数1〜8のアルキル基または炭素数1〜8のアルケ
ニル基を示ス。)で表わされるフェノール類の存在下又
は実質的に非存在下に酸性〃触媒下又はアルカリ性触媒
ドでアルデヒド類と反応させることを特徴とする変性フ
ェノール系樹脂の製造法。
[Scope of Claims] General formula (4) (wherein R+l is H1 an alkyl group having 1 to 8 carbon atoms, an alkenyl group having 1 to 8 carbon atoms, -OH group, and R2 is H1
It represents an alkyl group having 1 to 8 carbon atoms or an alkenyl group having 1 to 8 carbon atoms. ) and the general formula direction are shown. The definition of R4 is the same as R8, and may be the same as or different from Re. ) in the presence of an acidic catalyst. (In the formula, R1 is H1 an alkyl group having 1 to 8 carbon atoms, an alkenyl group having 1 to 8 carbon atoms, an -OH group, and Rz is H1
Indicates an alkyl group having 1 to 8 carbon atoms or an alkenyl group having 1 to 8 carbon atoms. ) A method for producing a modified phenolic resin, which comprises reacting the modified phenolic resin with an aldehyde under an acidic catalyst or an alkaline catalyst in the presence or substantially absence of the phenol represented by the following formula.
JP24253583A 1983-05-18 1983-12-22 Production of modified phenolic resin Granted JPS60135418A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP24253583A JPS60135418A (en) 1983-12-22 1983-12-22 Production of modified phenolic resin
EP19840303352 EP0126625B1 (en) 1983-05-18 1984-05-17 Method for the production of phenolic compounds and resins
DE8484303352T DE3484994D1 (en) 1983-05-18 1984-05-17 METHOD FOR PRODUCING PHENOL COMPOUNDS AND RESINS.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24253583A JPS60135418A (en) 1983-12-22 1983-12-22 Production of modified phenolic resin

Publications (2)

Publication Number Publication Date
JPS60135418A true JPS60135418A (en) 1985-07-18
JPS635414B2 JPS635414B2 (en) 1988-02-03

Family

ID=17090555

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24253583A Granted JPS60135418A (en) 1983-05-18 1983-12-22 Production of modified phenolic resin

Country Status (1)

Country Link
JP (1) JPS60135418A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3236266U (en) * 2021-12-10 2022-02-07 株式会社ヒヨリジャパン Crack prevention reinforcement and crack prevention structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3236266U (en) * 2021-12-10 2022-02-07 株式会社ヒヨリジャパン Crack prevention reinforcement and crack prevention structure

Also Published As

Publication number Publication date
JPS635414B2 (en) 1988-02-03

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