JPS6223003B2 - - Google Patents

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Publication number
JPS6223003B2
JPS6223003B2 JP57175891A JP17589182A JPS6223003B2 JP S6223003 B2 JPS6223003 B2 JP S6223003B2 JP 57175891 A JP57175891 A JP 57175891A JP 17589182 A JP17589182 A JP 17589182A JP S6223003 B2 JPS6223003 B2 JP S6223003B2
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JP
Japan
Prior art keywords
weight
resin
parts
temperature
hours
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.)
Expired
Application number
JP57175891A
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Japanese (ja)
Other versions
JPS5964616A (en
Inventor
Naoya Kominami
Juji Shimanuki
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.)
Asahi Yukizai Corp
Original Assignee
Asahi Organic Chemicals Industry 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 Asahi Organic Chemicals Industry Co Ltd filed Critical Asahi Organic Chemicals Industry Co Ltd
Priority to JP17589182A priority Critical patent/JPS5964616A/en
Publication of JPS5964616A publication Critical patent/JPS5964616A/en
Publication of JPS6223003B2 publication Critical patent/JPS6223003B2/ja
Granted legal-status Critical Current

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  • Phenolic Resins Or Amino Resins (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は改善された性能を有する固形レゾール
樹脂の製造方法、特に従来のフエノール樹脂に比
べて顕著に優れた電気絶縁性、耐熱性及び耐湿性
を有するノーアンモニアベンジリツクエーテル型
固形レゾール樹脂の製造方法に関するものであ
る。 プラスチツクスの中で最も早くから開発された
フエノール樹脂は、耐熱性及び電気特性の良好な
プラスチツク材料として、長い間電気部品などに
使用されてきた。しかし、例えば不飽和ポリエス
テル樹脂、ジアリルフタレート樹脂、エポキシ樹
脂などの熱硬化性樹脂がつぎつぎと開発され、そ
のより優れた電気特性のためにフエノール樹脂に
替えて用いられるようになつた。特に電気技術の
進展に伴つて、いつそう優れた電気特性や物性を
有するプラスチツク成形材料が要求されるように
なり、フエノール樹脂の用途分野は縮少の一途を
たどつている。さらに、ある程度の耐熱性を有
し、電気特性の良好なエンジニアリングプラスチ
ツクスの出現により順次その用途が奪われ、その
需要はじり貧化している。このような状況に至つ
たフエノール樹脂の最大の弱点は、特に常態の体
積固有抵抗が低いことで、従来のフエノール樹脂
は高度な電気技術分野で要求される高い電気抵抗
よりもはるかに低い抵抗値のものであり、電気特
性の優れた上記熱硬化性樹脂類に比べて3〜4け
た低いものでしかない。 本発明者らは、工業的に安価に提供されるフエ
ノール樹脂の欠点を改善し、特に高度な電気技術
分野の部品に適用しうる高い常態体積固有抵抗及
び耐熱性を有し、かつ加工性の優れたフエノール
系樹脂を開発すべく研究を重ねた結果、樹脂中の
フリーフエノール量をできるだけ減少させ、樹脂
の架橋密度を可及的に高めたベンジリツクエーテ
ル型固形レゾール樹脂が目的を達成しうることを
見出し、本発明に至つた。 すなわち、本発明は、フエノール類と該フエノ
ール1モルに対し1〜2モルのアルデヒドとをフ
エノール類の重量の0.1〜2重量%の二価金属の
塩の存在下で、2〜6時間加熱縮合反応させ、次
いで温度110〜120℃及び減圧度700mmHg以上にお
いて脱水させることからなる、遊離フエノール含
有量2重量%以下、ゲルタイム180〜480秒を有す
る固形レゾール樹脂であつて、かつこの樹脂30重
量部に対し結晶シリカ65.5重量部、酸化マグネシ
ウム3重量部及びステアリン酸亜鉛1.5重量部を
加えて成形材料としたとき、常態、煮沸体積固有
抵抗値1014Ω以上、温度180℃における熱時体積
固有抵抗値1011Ω以上、温度120℃、相対湿度100
%における1000時間後の高温高湿時体積固有抵抗
値1011Ω以上、及び温度120℃、相対湿度100%に
おける1000時間後の吸水率1.0%以下の物性を示
すことを特徴とするノーアンモニアベンジリツク
エーテル型固形レゾール樹脂の製造方法を提供す
るものである。 本発明において、ノーアンモニアベンジリツク
エーテル型固形レゾール樹脂を形成させるための
フエノール類は、フエノール及びその該誘導体類
を包含し、特に好ましいものは、フエノール、ク
レゾール及びキシレノールである。 また、アルデヒドはホルマリンやパラホルムア
ルデヒドなどのホルムアルデヒドが好適で、とく
に好ましくはパラホルムアルデヒドを用いるのが
良い。アルデヒドは、本発明の望ましい樹脂を得
るには上記フエノール類1モル当たり1〜2モル
の割合で反応に供することが重要であり、この範
囲逸脱するときは本発明の目的を達成することが
できない。また触媒は、反応によつて形成される
樹脂の電気特性及び物性を阻害しない限り制限さ
れないが、好ましくは有機酸塩であり、特に酢酸
亜鉛、酢酸マンガン及びナフテン酸鉛が有利に用
いられる。これらは単独で又は2種以上を組み合
わせて使用することができる。この二価金属塩
は、フエノール類100重量部に対し、0.1〜2重量
部、の範囲量を反応系に存在させることが必要で
ある。この範囲を逸脱すると、所望の優れた諸性
質を有する樹脂を得ることができない。 本発明においては、上記のようなフエノール
類、アルデヒド及び二価金属塩を混合し、縮合反
応させる。反応温度は、特に制限されないが、通
常還流温度が有利に採用される。また反応時間は
温度、原料の相互の割合や濃度によつて多少異な
るが、2〜6時間の範囲である。縮合反応を行つ
たのち、反応系を110〜120℃の温度及び700mmHg
より高い減圧条件で脱水処理することにより、目
的の固形レゾール樹脂を取得できる。この脱水処
理条件は極めて重要であり、脱水の温度と減圧度
の組合せの範囲をいずれが逸脱しても所望の望ま
しい樹脂を得ることができない。さらに好ましい
範囲は、110〜115℃の脱水温度及び730mmHg以上
の高い減圧度である。 本発明方法により得られるレゾール樹脂は、メ
チロール基及びメチレン基よりも多いジメチレン
エーテル基をもつた結合構造を有し、フリーのフ
エノール含量が極めて少なく、約60〜70℃の融点
を有し、ゲルタイムはかなり長くかつ望ましくな
いアンモニアを発生しないベンジリツクエーテル
型の固形のものである。 本発明方法により得られる樹脂中に含有される
遊離のフエノール類の量は2重量%以下でなけれ
ばならず、好ましくは1重量%以下である。2重
量%を超えると、樹脂のゲルタイムが著るしく短
くなり、成形材料への加工に際してロール混練が
十分行えないので、得られる成形材料中に残存す
る揮発分が多く、そのため材料の体積固有抵抗値
が低くなり好ましくない。この観点から、本発明
の樹脂のゲルタイムは180秒以上であることが重
要であり、また実用上望ましい範囲は240〜480秒
である。480秒よりもゲルタイムが長くなるとロ
ール混練時間が長くなりすぎ、樹脂の硬化がおそ
くなつて生産性が著しく低下するので好ましくな
い。ここにゲルタイムはJIS K 6910に記載され
た方法により測定した値であり、また上記の遊離
フエノール類含有量は液体クロマドグラフイーに
より測定される値である。 また、本発明方法により得られる固形レゾール
樹脂は、フエノール系成形材料を評価する一般的
な方法、すなわち、樹脂30重量部、結晶シリカ
65.5重量部、酸化マグネシウム3重量部及びステ
アリン酸亜鉛1.5重量部から成る組成物を、例え
ば85℃に加熱したロールで18分間加熱混練し、例
えばシートに成形して冷却後これを粉砕した成形
材料が常態、煮沸体積固有抵抗値1014Ω以上で、
温度180℃の熱時の体積固有抵抗値1011Ω以上を
有し、かつ温度120℃及び相対湿度100%の雰囲気
条件下に1000時間さらすとき体積固有抵抗値1011
Ω以上を有し、吸水率1.0重量%以下の望ましい
ものである。上記成形材料の常態、煮沸および熱
時体積固有抵抗値はJISK6911に基づいて測定し
ものであり、高温高湿時体積固有抵抗値及び吸水
率は、エポキシ樹脂成形材料などの物性測定に使
用されるプレツシヤークツカー法における2気圧
の条件で測定したものである。 また、成形材料の基材として使用した結晶シリ
カは、本発明方法により得られる樹脂を使用した
成形材料の物性を表現するための一つの曲型的基
材であつて、他の基材、例えばケイ酸アルミ、焼
成クレー、ガラス、アスベスト、炭酸カルシウ
ム、マイカ、水酸化アルミニウム、アルミナなど
を用いても同様の物性値を確認することができ
る。 このような本発明方法により得られる固形レゾ
ール樹脂は、高い性能が要求される電気部品用プ
ラスチツクスとして使用することができ、従来の
フエノール系樹脂に比べて顕著に改善された電気
絶縁性、耐熱性及び耐湿性の成形材料を提供する
ことができる。例えば従来のフエノール樹脂を代
表する遊離フエノール2重量%以下を含有するノ
ボラツク樹脂を用いて、その30重量部を結晶シリ
カ基材65.5重量部ほかと同様に配合して得られた
成形材料と本発明の樹脂を用いて得られた同様組
成の成形材料とを比較すると、本発明方法により
得られる樹脂は次のような利点を有する。 (1) 常態、煮沸体積固有抵抗値は1014Ω以上であ
り2〜3オーダー(102〜103Ω)高い値を示
す。 (2) 高温時の体積固有抵抗値は180℃で1011Ω以
上あり、3オーダー(103Ω)高い値を示す。 (3) 耐湿性、とくに120℃,100%相対湿度下、
1000時間で、体積固有抵抗値が1011Ω以上あ
り、2オーダー(102Ω)高い値を示す。 (4) 吸水率は120℃,100%相対湿度下、1000時間
で比較材料が2重量%以下であるのに対し、1
重量%以下である。 (5) 耐熱性も高く、180℃における長期重量変化
を測定すると減少率が比較材料より小さい値を
示す。 以上のごとく、本発明方法により得られる樹脂
は、従来のフエノール樹脂を代表するノボラツク
樹脂にくらべ、耐熱性、耐湿性及び特に電気絶縁
性が大巾に優れており、前記の他の熱硬化性樹脂
にも匹敵する物性を備えているものである。 以下、実施例により本発明をさらに詳細に説明
するが本発明はこれに限定されるものではない。 なお、例中の%及び部は特に記載しない限り重
量によるものである。 実施例 1 5容の三つ口フラスコにフエノール3000g、
92%パラホルム1560g(モル比1.5)及び酢酸亜
鉛12gを加え、還流温度115〜103℃で4時間反応
後、脱水温度115℃、減圧度755mmHgで減圧脱水
を行い、反応物が脱水物粘度になつた時点で減圧
脱水を終了し、フラスコから脱水反応物を取り出
した。 得られた樹脂の特性は、フロー∞、ゲルタイム
270秒、融点61℃、遊離フエノール量1.2%であつ
た。 なお、フロー、ゲルタイムはJISK6910によ
り、また融点はキヤピラリー法によつて測定した
値である。(以下同じ) この樹脂30部に、結晶シリガ(MALVERN
MIN―ERALS CO製ノバサイト)65.5部,MgO3
部及びステアリン酸亜鉛1.5部を配合し、混合
後、85℃に加熱したロールで18分間混練してシー
トとなし、冷却後、粉砕して成形材料を得た。 この材料の各種物性は、後記第1表に後記各例
とともにまとめて示す。 実施例 2 5容の三つ口フラスコに、フエノール3000
g、92%パラホルム1250g(モル比1.2)及び酢
酸亜鉛12gを加え、還流温度114〜102℃で5時間
反応後、脱水温度117℃、減圧度755mmHgで減圧
脱水を行い、反応物が目的の脱水物粘度になつた
時点で、減圧脱水を終了し、フラスコから脱水反
応物を排出した。 得られた樹脂の特性は、フロー∞、ゲルタイム
350秒、融点64℃、遊離フエノール量0.9%であつ
た。 この樹脂を使用して、実施例1と同様にして成
形材料を得た。 比較例 1 5容の三つ口フラスコにフエノール3000g、
92%パラホルム1560g(モル比1.5)及び酢酸亜
鉛12gを加え、還流温度115〜103℃で4時間反応
後、脱水温度115℃、減圧度600mmHgで減圧脱水
を行い、反応物が目的の脱水物粘度になつた時点
で減圧脱水を終了し、フラスコから脱水反応物を
排出した。 得られた樹脂の特性は、フロー120mm、ゲルタ
イム51秒、融点49℃、遊離フエノール量4.6%で
あつた。 この樹脂を使用して、実施例1と同じ配合で85
℃に加熱したロールで3分間混練してシートとな
し、冷却後粉砕して成形材料を得た。 比較例 2 5容の三つ口フラスコにフエノール3000g、
92%パラホルム1560g(モル比1.5)及び酢酸亜
鉛12gを加え還流温度115〜103℃で4時間反応
後、脱水温度130℃、減圧度730mmHgで減圧脱水
を行い、反応物が目的の脱水粘度になつた時点で
減圧脱水を終了し、フラスコから脱出反応物を排
出した。 得られた樹脂の特性はフロー147mm、ゲルタイ
ム135秒、融点53℃、遊離フエノール量3.2%であ
つた。 この樹脂を使用して実施例1と同じ配合で85℃
に加熱したロールで4分間混練してシートとな
し、冷却後粉砕して成形材料を得た。 比較例 3 5容の三つ口フラスコにフエノール3000g、
37%ホルマリン2200g(モル比0.85)及びシユウ
酸18gを加え、102〜101℃の還流温度で3時間反
応後、脱水温度175℃、減圧度700mmHgで2時間
減圧脱水し、反応物を排出した。 得られた樹脂の特性はフロー86mm、ゲルタイム
48秒、融点74℃、(いずれもヘキサメチレンテト
ラアミン10%混合における値)フリーフエノール
量2.0%であつた。 この樹脂26部、ヘキサメチレンテトラアミン
4.5部、結晶シリカ(MALVERN MINERALS
CO製ノバサイト)65.5部、MgO2.5部及びステア
リン酸亜鉛1.5部を配合し、混合後85℃に加熱し
たロールで6分間混練してシートとなし、冷却後
粉砕して成形材料を得た。 比較例 4 不飽和ポリエステル樹脂(日本ユピカ製ユピカ
8542)21部,ジアリルオルソフタレート樹脂(大
阪曹達製DAP―K)9部、結晶シリカ(MAL―
VERN MINERALS CO.製ノバサイト)67.6部,
ジグミルパーオキシド1.2部及びステアリン酸亜
鉛1.2部を配合,混合後、95℃に加熱したロール
で12分間混練してシートとなし、冷却後粉砕して
成形材料を得た。 以上の実施例1〜2及び比較例1〜4で得られ
た成形材料の物性を次表に示す。
The present invention relates to a method for producing a solid resol resin having improved performance, particularly for producing a non-ammonia benzyl ether type solid resol resin having significantly superior electrical insulation, heat resistance, and moisture resistance compared to conventional phenolic resins. It is about the method. Phenol resin, which was developed among the earliest plastics, has long been used in electrical parts and the like as a plastic material with good heat resistance and electrical properties. However, thermosetting resins such as unsaturated polyester resins, diallyl phthalate resins, and epoxy resins have been developed one after another and have come to be used in place of phenolic resins due to their superior electrical properties. In particular, as electrical technology progresses, plastic molding materials with superior electrical and physical properties are increasingly required, and the fields of use for phenolic resins are shrinking. Furthermore, with the advent of engineering plastics that have a certain degree of heat resistance and good electrical properties, their uses are gradually being taken away, and the demand for them is gradually declining. The biggest weakness of phenolic resins that led to this situation is that they have particularly low normal volume resistivity, and conventional phenolic resins have much lower resistance values than the high electrical resistance required in advanced electrical technology fields. This is only 3 to 4 orders of magnitude lower than the above-mentioned thermosetting resins, which have excellent electrical properties. The present inventors have improved the drawbacks of phenolic resins, which are industrially available at low cost, and have high normal volume resistivity and heat resistance that can be applied to parts in the advanced electrical technology field, and have excellent processability. As a result of repeated research to develop an excellent phenolic resin, we found that a benzylic ether-type solid resol resin, which reduces the amount of free phenol in the resin as much as possible and increases the crosslinking density of the resin as much as possible, has achieved the goal. This discovery led to the present invention. That is, the present invention involves heating and condensing phenols and 1 to 2 moles of aldehyde per mole of the phenol in the presence of a divalent metal salt of 0.1 to 2% by weight based on the weight of the phenols for 2 to 6 hours. A solid resol resin having a free phenol content of 2% by weight or less and a gel time of 180 to 480 seconds, which is obtained by reacting and then dehydrating at a temperature of 110 to 120°C and a degree of vacuum of 700 mmHg or more, and 30 parts by weight of this resin. When 65.5 parts by weight of crystalline silica, 3 parts by weight of magnesium oxide, and 1.5 parts by weight of zinc stearate are added to the molding material, the volume resistivity under normal conditions and boiling is 10-14 Ω or more, and the volume resistivity when heated at a temperature of 180°C. Value 10 11 Ω or more, temperature 120℃, relative humidity 100
%, after 1000 hours at high temperature and high humidity, a volume resistivity of 10-11 Ω or more, and a water absorption rate of 1.0% or less after 1000 hours at a temperature of 120°C and a relative humidity of 100%. The present invention provides a method for producing a liquid ether type solid resol resin. In the present invention, phenols for forming a non-ammonia benzyl ether type solid resol resin include phenol and its derivatives, and particularly preferred are phenol, cresol and xylenol. Moreover, formaldehydes such as formalin and paraformaldehyde are suitable as the aldehyde, and it is particularly preferable to use paraformaldehyde. In order to obtain the desired resin of the present invention, it is important to use the aldehyde in the reaction at a ratio of 1 to 2 moles per mole of the above phenols; if it deviates from this range, the purpose of the present invention cannot be achieved. . Further, the catalyst is not limited as long as it does not impair the electrical properties and physical properties of the resin formed by the reaction, but organic acid salts are preferably used, and zinc acetate, manganese acetate, and lead naphthenate are particularly advantageously used. These can be used alone or in combination of two or more. The divalent metal salt needs to be present in the reaction system in an amount ranging from 0.1 to 2 parts by weight per 100 parts by weight of the phenol. If it deviates from this range, a resin having desired excellent properties cannot be obtained. In the present invention, the above phenols, aldehydes, and divalent metal salts are mixed and subjected to a condensation reaction. The reaction temperature is not particularly limited, but reflux temperature is usually advantageously employed. The reaction time varies somewhat depending on the temperature and the mutual ratio and concentration of raw materials, but is in the range of 2 to 6 hours. After the condensation reaction, the reaction system was heated to a temperature of 110-120℃ and 700mmHg.
The desired solid resol resin can be obtained by performing dehydration treatment under higher reduced pressure conditions. The conditions for this dehydration treatment are extremely important, and if the combination of dehydration temperature and degree of vacuum is out of range, the desired resin cannot be obtained. More preferred ranges are a dehydration temperature of 110 to 115°C and a high degree of vacuum of 730 mmHg or higher. The resol resin obtained by the method of the present invention has a bond structure with more dimethylene ether groups than methylol groups and methylene groups, has an extremely low free phenol content, and has a melting point of about 60 to 70 ° C. The gel time is fairly long and the benzyl ether type solids do not generate undesirable ammonia. The amount of free phenols contained in the resin obtained by the process of the invention must be less than 2% by weight, preferably less than 1% by weight. If it exceeds 2% by weight, the gel time of the resin will be significantly shortened and sufficient roll kneading will not be possible during processing into a molding material, resulting in a large amount of volatile matter remaining in the resulting molding material, resulting in a decrease in the volume resistivity of the material. The value becomes low, which is not desirable. From this point of view, it is important that the gel time of the resin of the present invention is 180 seconds or more, and the practically desirable range is 240 to 480 seconds. If the gel time is longer than 480 seconds, the roll kneading time becomes too long, which slows curing of the resin and significantly reduces productivity, which is not preferable. The gel time here is a value measured by the method described in JIS K 6910, and the above free phenol content is a value measured by liquid chromatography. In addition, the solid resol resin obtained by the method of the present invention was prepared using the general method for evaluating phenolic molding materials, that is, 30 parts by weight of resin, crystalline silica
A molding material obtained by heating and kneading a composition consisting of 65.5 parts by weight, 3 parts by weight of magnesium oxide, and 1.5 parts by weight of zinc stearate using rolls heated to, for example, 85°C for 18 minutes, forming it into a sheet, cooling it, and pulverizing it. is normal, when the boiling volume specific resistance value is 10-14 Ω or more,
It has a volume resistivity value of 10 11 Ω or more when heated at a temperature of 180°C, and a volume resistivity value of 10 11 when exposed for 1000 hours under atmospheric conditions of a temperature of 120°C and a relative humidity of 100%.
Ω or more and a water absorption rate of 1.0% by weight or less. The normal, boiling, and hot volume resistivity values of the above molding materials are measured based on JISK6911, and the volume resistivity values and water absorption rates at high temperature and high humidity are used to measure the physical properties of epoxy resin molding materials, etc. It was measured under the condition of 2 atmospheres according to the Plessia-Kutsker method. In addition, the crystalline silica used as the base material of the molding material is a curved base material for expressing the physical properties of the molding material using the resin obtained by the method of the present invention, and other base materials, such as Similar physical property values can be confirmed using aluminum silicate, calcined clay, glass, asbestos, calcium carbonate, mica, aluminum hydroxide, alumina, and the like. The solid resol resin obtained by the method of the present invention can be used as plastics for electrical parts that require high performance, and has significantly improved electrical insulation and heat resistance compared to conventional phenolic resins. It is possible to provide molding materials that are resistant to moisture and moisture. For example, a molding material obtained by using a novolak resin containing 2% by weight or less of free phenol, which is representative of conventional phenolic resins, and blending 30 parts by weight thereof with 65.5 parts by weight of a crystalline silica base material and the like, and the present invention. When compared with a molding material of similar composition obtained using the resin described above, the resin obtained by the method of the present invention has the following advantages. (1) Under normal conditions, the boiling volume resistivity value is 10 14 Ω or more, which is 2 to 3 orders of magnitude (10 2 to 10 3 Ω) higher. (2) The volume resistivity value at high temperatures is 10 11 Ω or more at 180°C, which is 3 orders of magnitude (10 3 Ω) higher. (3) Moisture resistance, especially at 120℃ and 100% relative humidity.
After 1000 hours, the volume resistivity value is 10 11 Ω or more, which is two orders of magnitude (10 2 Ω) higher. (4) The water absorption rate was 1% by weight or less for the comparative material in 1000 hours at 120°C and 100% relative humidity, whereas it was less than 2% by weight for the comparative material.
% by weight or less. (5) It also has high heat resistance, and when measuring long-term weight changes at 180°C, the reduction rate is smaller than that of comparative materials. As described above, the resin obtained by the method of the present invention has significantly superior heat resistance, moisture resistance, and especially electrical insulation properties compared to novolak resins that represent conventional phenolic resins, and has excellent heat resistance, moisture resistance, and especially electrical insulation properties. It has physical properties comparable to resins. EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto. Note that % and parts in the examples are by weight unless otherwise specified. Example 1 3000g of phenol in a 5-volume three-necked flask,
Add 1560 g of 92% paraform (molar ratio 1.5) and 12 g of zinc acetate, and after reacting for 4 hours at a reflux temperature of 115 to 103°C, dehydrate under reduced pressure at a dehydration temperature of 115°C and a degree of vacuum of 755 mmHg until the reaction product has the viscosity of a dehydrated product. At that point, the dehydration under reduced pressure was completed, and the dehydrated reaction product was taken out from the flask. The properties of the obtained resin are flow ∞, gel time
270 seconds, melting point 61°C, free phenol content 1.2%. Note that the flow and gel time are the values measured according to JISK6910, and the melting point is the value measured by the capillary method. (The same applies hereinafter) To 30 parts of this resin, crystal silica (MALVERN
MIN―ERALS CO Novasite) 65.5 parts, MgO3
After mixing, the mixture was mixed with 1.5 parts of zinc stearate, kneaded for 18 minutes using rolls heated to 85°C to form a sheet, cooled, and crushed to obtain a molding material. Various physical properties of this material are summarized in Table 1 below together with each example below. Example 2 Phenol 3000 in a 5-volume three-necked flask
g, 1250 g of 92% paraform (molar ratio 1.2) and 12 g of zinc acetate were added, and after reacting at a reflux temperature of 114 to 102 °C for 5 hours, dehydration was performed under reduced pressure at a dehydration temperature of 117 °C and a degree of vacuum of 755 mmHg, and the reaction product was dehydrated to the desired level. When the viscosity reached a solid level, the dehydration under reduced pressure was completed and the dehydrated reaction product was discharged from the flask. The properties of the obtained resin are flow ∞, gel time
350 seconds, the melting point was 64°C, and the amount of free phenol was 0.9%. A molding material was obtained in the same manner as in Example 1 using this resin. Comparative Example 1 3000g of phenol in a 5-volume three-necked flask,
Add 1560 g of 92% paraform (molar ratio 1.5) and 12 g of zinc acetate, and after reacting for 4 hours at a reflux temperature of 115 to 103°C, dehydration is performed under reduced pressure at a dehydration temperature of 115°C and a degree of vacuum of 600 mmHg, so that the reaction product reaches the desired viscosity of the dehydrated product. At the point at which the dehydration was completed, the dehydration under reduced pressure was completed, and the dehydration reaction product was discharged from the flask. The properties of the resulting resin were a flow of 120 mm, a gel time of 51 seconds, a melting point of 49° C., and a free phenol content of 4.6%. Using this resin, 85
The mixture was kneaded for 3 minutes using rolls heated to 0.degree. C. to form a sheet, and after cooling, it was crushed to obtain a molding material. Comparative Example 2 3000g of phenol in a 5-volume three-necked flask,
Add 1560 g of 92% paraform (molar ratio 1.5) and 12 g of zinc acetate and react at a reflux temperature of 115 to 103°C for 4 hours, then dehydrate under reduced pressure at a dehydration temperature of 130°C and a reduced pressure of 730 mmHg until the reactant reaches the desired dehydrated viscosity. At that point, the dehydration under reduced pressure was completed, and the escaped reaction product was discharged from the flask. The properties of the resulting resin were a flow of 147 mm, a gel time of 135 seconds, a melting point of 53° C., and a free phenol content of 3.2%. Using this resin, the same formulation as in Example 1 was used at 85°C.
The mixture was kneaded for 4 minutes using heated rolls to form a sheet, and after cooling, it was crushed to obtain a molding material. Comparative Example 3 3000g of phenol in a 5-volume three-necked flask,
2200 g of 37% formalin (molar ratio 0.85) and 18 g of oxalic acid were added, and after reacting for 3 hours at a reflux temperature of 102 to 101°C, dehydration was carried out under reduced pressure at a dehydration temperature of 175°C and a degree of vacuum of 700 mmHg for 2 hours, and the reaction product was discharged. The properties of the obtained resin are flow 86mm, gel time
The temperature was 48 seconds, the melting point was 74°C, and the amount of free phenol was 2.0% (all values for a 10% mixture of hexamethylenetetraamine). 26 parts of this resin, hexamethylenetetraamine
4.5 parts, crystalline silica (MALVERN MINERALS
After mixing, 65.5 parts of CO Novasite), 2.5 parts of MgO, and 1.5 parts of zinc stearate were mixed, kneaded for 6 minutes with rolls heated to 85°C to form a sheet, cooled, and then crushed to obtain a molding material. Comparative Example 4 Unsaturated polyester resin (Yupica manufactured by Nippon Upica)
8542) 21 parts, diallyl orthophthalate resin (Osaka Soda DAP-K) 9 parts, crystalline silica (MAL-
Novacyte manufactured by VERN MINERALS CO.) 67.6 copies,
1.2 parts of digyl peroxide and 1.2 parts of zinc stearate were blended and mixed, then kneaded for 12 minutes with rolls heated to 95°C to form a sheet, cooled and crushed to obtain a molding material. The physical properties of the molding materials obtained in Examples 1 to 2 and Comparative Examples 1 to 4 are shown in the following table.

【表】【table】

【表】 以上説明したごとく、本発明の固形レゾール樹
脂は、従来のフエノール樹脂を代表するノボラツ
ク樹脂にくらべ耐熱性、耐湿性およびとくに、電
気絶縁性が大巾に優れており、かつそれ自体の有
する熱時の機械的強度を組合せることにより、他
の熱硬化性樹脂にも匹敵する物性を備えることに
なり、今までに考えられなかつた分野への巾広い
展開が期待できる樹脂である。また本発明の固形
レゾール樹脂は成形材料のみならず、積層板シエ
ルモード用結合剤、塗料、接着剤などにも好適に
使用できる。
[Table] As explained above, the solid resol resin of the present invention has significantly superior heat resistance, moisture resistance, and especially electrical insulation properties compared to novolac resins that represent conventional phenolic resins, and also has its own properties. By combining the mechanical strength when heated, it has physical properties comparable to other thermosetting resins, making it a resin that can be expected to be widely used in fields that have not been considered before. Furthermore, the solid resol resin of the present invention can be suitably used not only as a molding material but also as a binder for shell mode laminates, paints, adhesives, and the like.

Claims (1)

【特許請求の範囲】[Claims] 1 フエノール類と該フエノール1モルに対し1
〜2モルのアルデヒドとをフエノール類の重量の
0.1〜2重量%の二価金属の塩の存在下で、2〜
6時間加熱縮合反応させ、次いで温度110〜120℃
及び減圧度700mmHg以上において脱水させること
からなる、遊離フエノール含有量2重量%以下、
ゲルタイム180〜480秒を有する固形レゾール樹脂
であつて、かつこの樹脂30重量部に対し結晶シリ
カ65.5重量部、酸化マグネシウム3重量部及びス
テアリン酸亜鉛1.5重量部を加えて成形材料とし
たとき、常態、煮沸体積固有抵抗値1014Ω以上、
温度180℃における熱時体積固有抵抗値1011Ω以
上、温度120℃、相対湿度100%における1000時間
後の高温高湿時体積固有抵抗値1011Ω以上、及び
温度120℃、相対湿度100%における1000時間後の
吸水率1.0%以下の物性を示すことを特徴とする
ノーアンモニアベンジリツクエーテル型固形レゾ
ール樹脂の製造方法。
1 phenols and 1 mole of the phenol
~2 moles of aldehyde and the weight of phenols
In the presence of 0.1-2% by weight of salts of divalent metals, 2-
Heat condensation reaction for 6 hours, then at a temperature of 110-120℃
and a free phenol content of 2% by weight or less, which consists of dehydration at a reduced pressure of 700 mmHg or more,
A solid resol resin having a gel time of 180 to 480 seconds, and when made into a molding material by adding 65.5 parts by weight of crystalline silica, 3 parts by weight of magnesium oxide, and 1.5 parts by weight of zinc stearate to 30 parts by weight of this resin, the normal state , boiling volume specific resistance value 10 14 Ω or more,
Volume resistivity at high temperatures of 10-11 Ω or higher at a temperature of 180°C, volume resistivity at high temperatures and humidity of 10-11 Ω or higher after 1000 hours at a temperature of 120°C and a relative humidity of 100%, and a temperature of 120°C and a relative humidity of 100%. 1. A method for producing a non-ammonia benzyl ether type solid resol resin, which exhibits physical properties of a water absorption rate of 1.0% or less after 1000 hours.
JP17589182A 1982-10-06 1982-10-06 Solid resol resin and its production Granted JPS5964616A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17589182A JPS5964616A (en) 1982-10-06 1982-10-06 Solid resol resin and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17589182A JPS5964616A (en) 1982-10-06 1982-10-06 Solid resol resin and its production

Publications (2)

Publication Number Publication Date
JPS5964616A JPS5964616A (en) 1984-04-12
JPS6223003B2 true JPS6223003B2 (en) 1987-05-21

Family

ID=16004027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17589182A Granted JPS5964616A (en) 1982-10-06 1982-10-06 Solid resol resin and its production

Country Status (1)

Country Link
JP (1) JPS5964616A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010038703A1 (en) * 2008-10-03 2010-04-08 住友ベークライト株式会社 Metal-clad phenolic-resin laminate
JP2010162737A (en) * 2009-01-14 2010-07-29 Sumitomo Bakelite Co Ltd Laminate plate

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB757392A (en) * 1953-06-16 1956-09-19 Distillers Co Yeast Ltd Preparation of novolak resins

Also Published As

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