JPH06107756A - Production of modified phenol resin - Google Patents

Production of modified phenol resin

Info

Publication number
JPH06107756A
JPH06107756A JP4254598A JP25459892A JPH06107756A JP H06107756 A JPH06107756 A JP H06107756A JP 4254598 A JP4254598 A JP 4254598A JP 25459892 A JP25459892 A JP 25459892A JP H06107756 A JPH06107756 A JP H06107756A
Authority
JP
Japan
Prior art keywords
reaction
phenol
resin
catalyst
solid acid
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
JP4254598A
Other languages
Japanese (ja)
Inventor
Ken Nanaumi
憲 七海
Takeshi Horiuchi
猛 堀内
Masahiro Nomoto
雅弘 野本
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.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP4254598A priority Critical patent/JPH06107756A/en
Publication of JPH06107756A publication Critical patent/JPH06107756A/en
Pending legal-status Critical Current

Links

Classifications

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

Abstract

PURPOSE:To obtain a modified phenol resin having excellent low-temperature punchability, electrical insulating properties and electrolytic corrosion. CONSTITUTION:A tung oil is reacted with a phenol in the presence of a solid acid catalyst to synthesize a vegetable oil to which the phenol is added and after the reaction is completed, the solid acid catalyst is removed by filtration. The reaction solution from which the catalyst is removed is reacted with a phenol and an aldehyde in the presence of a basic catalyst into a resole.

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、低温打抜加工性、電気
的特性に優れた紙−フェノール積層板および銅張り積層
板(以下、両者を積層板と総称する)に用いられる植物
油変性フェノール樹脂の製造法に関する。
FIELD OF THE INVENTION The present invention relates to a vegetable oil-modified phenol used for paper-phenol laminates and copper-clad laminates (both are collectively referred to as laminates) having excellent low-temperature punchability and electrical characteristics. The present invention relates to a method for producing a resin.

【0002】[0002]

【従来の技術】従来より、紙−フェノール積層板は金型
による打抜加工によって、孔あけあるいは外形加工が行
われている。近年はプリント配線板の寸法変化を小さく
するため、打抜加工を加温せずに室温で打ち抜く傾向に
ある。したがって、積層板の打抜加工性を良くするた
め、可撓化したフェノール樹脂が用いられてきた。さら
に、電子機器の発展に伴い、印刷配線板は高密度化する
傾向にある。フェノール樹脂積層板もその流れに沿い、
銀スルーホールを適用した両面プリント配線板の需要の
伸びが著しい。したがって、最近では打抜加工性ととも
に高度な電気的特性が要求されるようになってきた。フ
ェノール樹脂を可撓化する方法としては、一般的に、エ
レオステアリン酸を主成分とする反応性に富む桐油やト
リフェニルホスフェートなどのリン酸エステル類が重用
されている。しかし、桐油はそのままで用いられること
はなく、桐油とフェノール類を強酸性触媒の存在下反応
させて、フェノール類を付加した変性桐油の形で使用し
ている。また、リン酸エステル類などによる可撓化は、
積層板の耐溶剤性や電気特性などに問題があり、リン酸
エステル類のみで低温打抜加工性を実現することは困難
であった。
2. Description of the Related Art Conventionally, a paper-phenol laminated plate has been punched or contoured by punching with a die. In recent years, in order to reduce the dimensional change of printed wiring boards, there is a tendency to punch at room temperature without heating. Therefore, a flexible phenol resin has been used in order to improve the punching workability of the laminated plate. Furthermore, with the development of electronic devices, printed wiring boards tend to have higher densities. Phenolic resin laminated board is also following the flow,
Demand for double-sided printed wiring boards using silver through-holes is growing rapidly. Therefore, recently, punching workability and high electrical characteristics have been required. As a method for making the phenol resin flexible, generally, phosphoric acid esters mainly containing eleostearic acid and having a high reactivity, such as tung oil and triphenyl phosphate, are heavily used. However, tung oil is not used as it is, and tung oil is reacted with phenols in the presence of a strongly acidic catalyst to use modified tung oil in which phenols are added. In addition, the flexibility of phosphoric acid esters, etc.
There is a problem with the solvent resistance and electrical characteristics of the laminate, and it has been difficult to achieve low-temperature punching workability only with phosphoric acid esters.

【0003】[0003]

【発明が解決しようとする課題】桐油やカシュー油とフ
ェノール類との反応は、パラトルエンスルホン酸などの
強酸性物質を触媒に用いて、植物油にフェノール類を付
加させた反応生成物をフェノール樹脂の変性剤として用
いることが一般的に行われているが、この反応に用いて
いる強酸性触媒は、ワニスの中に残存しできた積層板の
電気的特性を低下させる方向に作用する。本発明はかか
る状況に鑑みなされたもので、電気的特性並びに低温打
抜加工性にすぐれた変性フェノール樹脂の製造法を提供
することを目的とする。
The reaction of tung oil or cashew oil with phenols uses a reaction product obtained by adding phenols to vegetable oil with a phenol resin by using a strongly acidic substance such as paratoluenesulfonic acid as a catalyst. Although it is generally used as a modifier for the above, the strongly acidic catalyst used in this reaction acts to reduce the electrical characteristics of the laminated plate that could remain in the varnish. The present invention has been made in view of such circumstances, and an object of the present invention is to provide a method for producing a modified phenolic resin having excellent electrical characteristics and low-temperature punching processability.

【0004】[0004]

【課題を解決するための手段】前述したように、パラト
ルエンスルホン酸などの強酸性触媒は、桐油変性フェノ
ール樹脂中にレゾール化触媒の塩基性物質と塩を形成
し、塩の形で残存していると考えられる。これらの塩
は、印刷配線板とした時に、電気絶縁性や耐電食性の低
下の原因となっている。そこで、フェノールとエレオス
テアリン酸を多く含む桐油など反応性に富む植物油との
反応に、反応液に溶解しない触媒すなわち固体酸を用い
て反応させ、反応終了後、濾過することにより固体酸触
媒を系外に除去することによって植物油変性フェノール
樹脂の不純物を少なくすることが出来る。
[Means for Solving the Problems] As described above, a strongly acidic catalyst such as paratoluenesulfonic acid forms a salt with the basic substance of the resolization catalyst in the tung oil-modified phenolic resin and remains in the form of a salt. It is thought that These salts cause the deterioration of electrical insulation and electrolytic corrosion resistance when used as a printed wiring board. Therefore, in the reaction with highly reactive vegetable oil such as tung oil containing a large amount of phenol and eleostearic acid, a solid acid catalyst is reacted by using a catalyst that does not dissolve in the reaction solution, that is, a solid acid, and a solid acid catalyst is obtained by filtering after completion of the reaction. By removing it outside the system, impurities in the vegetable oil-modified phenol resin can be reduced.

【0005】桐油をはじめとする植物油変性フェノール
樹脂は、上述した桐油類とフェノール類を反応させたも
のに、さらにフェノール類を追加してまたは追加しない
ものに、ホルムアルデヒド類、塩基性触媒を加えてレゾ
ール化反応を行うことにより合成できる。この桐油変性
フェノール樹脂を紙基材に含浸させ、圧縮成形して積層
板にした場合電気特性、耐電食性の低下もなく従来の積
層板の電気的性能を一段と向上出来ることが分かった。
Vegetable oil-modified phenolic resins such as tung oil are obtained by reacting tung oils with phenols as described above, with or without addition of phenols, and by adding formaldehyde and a basic catalyst. It can be synthesized by performing a resolization reaction. It has been found that when a wood base material is impregnated with this tung oil-modified phenolic resin and compression-molded into a laminate, the electrical performance of the conventional laminate can be further improved without lowering the electrical characteristics and electrolytic corrosion resistance.

【0006】本発明に用いられる反応性に富む植物油に
は、桐油、カシュー油などがあり、特に不飽和度が高い
桐油が好ましい。またフェノール類としては、フェノー
ル、オルトクレゾール、メタクレゾール、パラクレゾー
ル、キシレノール、カテコール、レゾルシン、ハイドロ
キノン、オクチルフェノール、tert-ブチルフェノー
ル、ノニルフェノール、ビスフェノール−Aなどが挙げ
られる。植物油とフェノール類との反応触媒に用いられ
る固体酸としては、パーフルオロアルカンスルホン酸型
イオン交換樹脂、ベンゼンスルホン酸型イオン交換樹脂
や合成ゼオライトなどがある。取り扱いが易しく、価格
が比較的安いベンゼンスルホン酸型イオン交換樹脂が好
ましい。
The highly reactive vegetable oils used in the present invention include tung oil and cashew oil, and tung oil having a high degree of unsaturation is particularly preferable. Examples of phenols include phenol, orthocresol, metacresol, paracresol, xylenol, catechol, resorcin, hydroquinone, octylphenol, tert-butylphenol, nonylphenol and bisphenol-A. Examples of solid acids used as catalysts for the reaction of vegetable oils with phenols include perfluoroalkanesulfonic acid type ion exchange resins, benzenesulfonic acid type ion exchange resins and synthetic zeolites. A benzenesulfonic acid type ion exchange resin that is easy to handle and relatively inexpensive is preferable.

【0007】植物油とフェノール類の配合比は、特に限
定されないが積層板の特性から、植物油:フェノール類
=2:8〜6:4特に3:7〜4:6が好ましい。植物
油の配合比が6:4より大きくなると、積層板の硬化性
が低下し、表面がべとつくなどの欠点が現われる。ま
た、2:8より小さくなると積層板の低温打抜加工性が
満足できない。また、固体酸触媒の添加量も特に限定さ
れないが、固体酸の表面積及び官能基密度によってその
添加量は決められるべき性質のものであるが、粒径2m
mのペレット状で官能基密度(3.7meq/g−乾燥
樹脂)のイオン交換樹脂であるならば植物油100重量
部に対して、0.1〜30部で特に1〜10部が好まし
い。0.1部以下では反応が遅くなり、工業的生産性が
低下する。30部以上では、反応系の粘度が上昇し攪拌
効率が低下するため実用的でない。桐油類とフェノール
類の反応は、無溶剤でも溶剤中でも可能であるが、次の
ホルムアルデヒドとの反応を考えると無溶剤で反応させ
るのが好ましい。反応温度は、50〜250℃、特に、
100℃以下が好ましい。100℃以上になると、加水
分解反応も頻発し、低分子量化が起こりやすくなり、ひ
いては積層板の特性低下を引き起こす。
The blending ratio of vegetable oil and phenols is not particularly limited, but from the characteristics of the laminated plate, vegetable oil: phenols = 2: 8 to 6: 4, particularly 3: 7 to 4: 6 is preferable. When the blending ratio of vegetable oil is more than 6: 4, the curability of the laminated plate is lowered and defects such as sticky surface appear. On the other hand, if it is less than 2: 8, the low temperature punching workability of the laminated sheet cannot be satisfied. Further, the addition amount of the solid acid catalyst is not particularly limited, but the addition amount is a property which should be decided depending on the surface area and the functional group density of the solid acid, but the particle size is 2 m.
If the ion-exchange resin is a pellet of m and has a functional group density (3.7 meq / g-dry resin), it is preferably 0.1 to 30 parts, especially 1 to 10 parts per 100 parts by weight of vegetable oil. If it is less than 0.1 part, the reaction becomes slow and the industrial productivity is lowered. When it is 30 parts or more, the viscosity of the reaction system increases and the stirring efficiency decreases, which is not practical. The reaction of tung oils with phenols can be carried out without solvent or in solvent, but it is preferable to carry out the reaction without solvent in consideration of the following reaction with formaldehyde. The reaction temperature is 50 to 250 ° C., especially
It is preferably 100 ° C or lower. When the temperature is 100 ° C. or higher, hydrolysis reaction frequently occurs, lowering the molecular weight is apt to occur, and eventually the characteristics of the laminated plate are deteriorated.

【0008】桐油類とフェノール類の反応が終了したあ
と、反応に用いた固体酸触媒を除去するわけだがその方
法は特に限定されない。通常の化学工業で用いられてい
る方法であれば適用可能である。たとえば、メッシュの
細かいステンレス製、ナイロン製、テフロン製、ポリエ
ステル製織布や綿布などを反応釜の排出口に堅く結ん
で、常圧下濾過する方法や、濾紙やガラス製濾紙を用い
て、加圧あるいは減圧下濾過する方法などがある。この
ようにして得た反応液に場合によってはフェノールを追
加し、ホルムアルデヒド、塩基性触媒を添加して通常の
レゾール化反応させ積層板用樹脂を合成する。場合によ
っては、難燃剤を添加して、難燃性積層板用樹脂にする
こともできる。こうして得たワニスを紙基材に含浸し
て、加熱乾燥してプリプレグを作製する。これを、所定
枚数重ね合わせて、片面に接着剤付き銅箔を重ねて、所
定の圧力、温度で所定時間加圧加熱して銅張り積層板を
作製する。以下、実施例を示して具体的に説明する。
After the reaction of tung oils and phenols is completed, the solid acid catalyst used in the reaction is removed, but the method is not particularly limited. Any method used in ordinary chemical industries can be applied. For example, fine mesh mesh made of stainless steel, nylon, Teflon, polyester woven cloth or cotton cloth is tightly tied to the outlet of the reaction kettle and filtered under normal pressure, or by using filter paper or glass filter paper. Alternatively, there is a method of filtering under reduced pressure. In some cases, phenol is added to the reaction solution thus obtained, formaldehyde and a basic catalyst are added, and a usual resolization reaction is performed to synthesize a resin for a laminate. In some cases, a flame retardant may be added to give a flame-retardant laminate resin. A paper base material is impregnated with the varnish thus obtained, and dried by heating to prepare a prepreg. A predetermined number of these are stacked, a copper foil with an adhesive is stacked on one surface, and pressure-heated at a predetermined pressure and temperature for a predetermined time to produce a copper-clad laminate. Hereinafter, the present invention will be specifically described with reference to examples.

【0009】[0009]

【実施例】【Example】

実施例1 (積層板用ワニスの合成例1)温度計、冷却管を備えた
21の三つ口フラスコに桐油200g、フェノール20
0g、スルホン化スチレン型イオン交換樹脂(オルガノ
社製商品名:アンバーリスト200(交換容量4.3m
eq/g−乾燥樹脂)20gを加えて、120℃で3時
間反応させた。反応終了後100メッシュの綿布で常圧
下で濾過してイオン交換樹脂を除去した。この反応液に
さらに、フェノール180g、パラホルム255g、メ
タノール80g、アンモニア水38gを加えて80℃で
レゾール化反応をした。160℃におけるゲル化時間が
6分になったところで、減圧下に加熱して脱水濃縮し
た。ゲル化時間が3分になったところで反応終了にして
トルエン200g、メタノール200gを加えてワニス
1とした。
Example 1 (Synthesis example 1 of varnish for laminated board) 200 g of tung oil and 20 phenol in a three-necked flask of 21 equipped with a thermometer and a cooling tube.
0 g, sulfonated styrene type ion exchange resin (Organo brand name: Amberlyst 200 (exchange capacity 4.3 m
eq / g-dry resin) was added and reacted at 120 ° C for 3 hours. After completion of the reaction, the ion exchange resin was removed by filtration with a 100-mesh cotton cloth under normal pressure. Further, 180 g of phenol, 255 g of paraform, 80 g of methanol and 38 g of aqueous ammonia were added to this reaction solution, and a resolization reaction was carried out at 80 ° C. When the gelation time at 160 ° C. reached 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelling time reached 3 minutes, the reaction was terminated and 200 g of toluene and 200 g of methanol were added to form a varnish 1.

【0010】実施例2 (積層板用ワニスの合成例2)実施例1と同様のフラス
コに桐油200g、m,p−クレゾール250g、実施
例1で用いたイオン交換樹脂を洗浄して乾燥後、硝酸で
処理して再生したイオン交換樹脂を20gを加えて、1
00℃で2時間反応させた。さらに、キシレン樹脂(三
菱瓦斯化学社商品名:ニカノール−H)50gを加え
て、同じ温度で1時間反応させた。反応終了後、ガラス
フィルタを用いて、減圧下で濾過した。濾液を再びフラ
スコの戻して、さらに、フェノール100g、パラホル
ム177g、メタノール60g、アンモニア水21.6
gを加えて80℃でレゾール化反応をした。160℃に
おけるゲル化時間が6分になったところで、減圧下に加
熱して脱水濃縮した。ゲル化時間が3分になったところ
で反応終了にしてトルエン200g、メタノール200
gを加えてワニス2とした。
Example 2 (Synthesis example 2 of varnish for laminated plate) 200 g of tung oil, 250 g of m, p-cresol and the ion exchange resin used in Example 1 were washed in the same flask as in Example 1, washed and dried, Add 20 g of ion exchange resin regenerated by treatment with nitric acid,
The reaction was carried out at 00 ° C for 2 hours. Further, 50 g of xylene resin (trade name: Nikanol-H, manufactured by Mitsubishi Gas Chemical Co., Inc.) was added and reacted at the same temperature for 1 hour. After the reaction was completed, it was filtered under reduced pressure using a glass filter. The filtrate was returned to the flask again, and 100 g of phenol, 177 g of paraform, 60 g of methanol, 21.6 ammonia water were further added.
g was added and a resolization reaction was carried out at 80 ° C. When the gelation time at 160 ° C. reached 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time reached 3 minutes, the reaction was terminated and 200 g of toluene and 200 g of methanol were added.
Varnish 2 was prepared by adding g.

【0011】実施例3 (積層板用ワニスの合成例3)実施例1と同様のフラス
コにフェノール200gとキシレン樹脂(三菱瓦斯化学
社商品名:ニカノール−H)50g、粒径2mmのパー
フルオロアルカンスルホン酸型イオン交換樹脂50gを
仕込み、100℃で1時間反応させた。それに、桐油2
00gを追加して同じ温度で5時間反応させた。反応終
了後、イオン交換樹脂を濾過してフラスコから系外に除
去した。濾液にフェノール180g、パラホルム255
g、メタノール80g、アンモニア水38gを加えて8
0℃でレゾール化反応をした。160℃におけるゲル化
時間が6分になったところで、減圧下に加熱して脱水濃
縮した。ゲル化時間が3分になったところで反応終了に
してトルエン200g、メタノール200gを加えてワ
ニス3とした。
Example 3 (Synthesis example 3 of varnish for laminated plate) In a flask similar to that of Example 1, 200 g of phenol, 50 g of xylene resin (trade name: Nikanol-H, manufactured by Mitsubishi Gas Chemical Co., Inc.), and perfluoroalkane having a particle diameter of 2 mm were used. 50 g of a sulfonic acid type ion exchange resin was charged and reacted at 100 ° C. for 1 hour. And tung oil 2
00 g was added and the reaction was carried out at the same temperature for 5 hours. After the reaction was completed, the ion exchange resin was filtered and removed from the flask out of the system. 180g phenol and 255 paraform in the filtrate
g, 80 g of methanol, 38 g of ammonia water were added to obtain 8
A resolization reaction was performed at 0 ° C. When the gelation time at 160 ° C. reached 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time reached 3 minutes, the reaction was terminated and 200 g of toluene and 200 g of methanol were added to form a varnish 3.

【0012】比較例1 (桐油変性フェノール樹脂の合成)実施例1と同様のフ
ラスコにフェノール200gとキシレン樹脂(三菱瓦斯
化学社商品名:ニカノール−H)50g、パラトルエン
スルホン酸0.3gを仕込み、100℃で1時間反応さ
せた。それに、桐油200gを追加して同じ温度で2時
間反応させた。反応終了後、フェノール180g、パラ
ホルム255g、メタノール80g、アンモニア水38
gを加えて80℃でレゾール化反応をした。160℃に
おけるゲル化時間が6分になったところで、減圧下に加
熱して脱水濃縮した。ゲル化時間が3分になったところ
で反応終了にしてトルエン200g、メタノール200
gを加えて比較ワニス1とした。
Comparative Example 1 (Synthesis of tung oil-modified phenolic resin) A flask similar to that of Example 1 was charged with 200 g of phenol, 50 g of xylene resin (trade name: Nikanol-H, manufactured by Mitsubishi Gas Chemical Co., Inc.), and 0.3 g of paratoluenesulfonic acid. And reacted at 100 ° C. for 1 hour. To this, 200 g of tung oil was added and reacted at the same temperature for 2 hours. After completion of the reaction, phenol 180 g, paraform 255 g, methanol 80 g, ammonia water 38
g was added and a resolization reaction was carried out at 80 ° C. When the gelation time at 160 ° C. reached 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time reached 3 minutes, the reaction was terminated and 200 g of toluene and 200 g of methanol were added.
Comparative varnish 1 was prepared by adding g.

【0013】以上、合成したワニス4種類を樹脂分48
%に調整して、水溶液フェノール樹脂で第一次含浸した
クラフト紙に含浸、乾燥させ植物油変性フェノール樹脂
プリプレグを作製した。該プリプレグを所定枚数重ね
て、片側に接着剤付銅箔を重ねて、100kg/c
2、160℃、1時間加熱して銅張り積層板を製造し
た。該積層板の特性をJIS−6481に準拠して測定
した。その結果を表1に示す。
As described above, 4 kinds of the synthesized varnishes are used as resin components.
%, The kraft paper which was first impregnated with the aqueous solution phenol resin was impregnated and dried to prepare a vegetable oil modified phenol resin prepreg. A predetermined number of the prepregs are stacked, and a copper foil with an adhesive is stacked on one side to obtain 100 kg / c.
A copper-clad laminate was manufactured by heating at m 2 at 160 ° C. for 1 hour. The characteristics of the laminated plate were measured according to JIS-6481. The results are shown in Table 1.

【0014】[0014]

【表1】 [Table 1]

【0015】[0015]

【発明の効果】表1から明らかなように、従来の方法で
合成した桐油変性フェノール樹脂に比べて、本発明によ
れば、沸騰した水に浸漬して吸湿した後の絶縁抵抗が大
幅に向上し、さらに、耐電食性も1000時間でもデン
トライトの発生がみられず、大幅に改良された。
As is apparent from Table 1, according to the present invention, the insulation resistance after immersion in boiling water and absorption of moisture is significantly improved, as compared with the tung oil-modified phenol resin synthesized by the conventional method. Further, the electrolytic corrosion resistance was also greatly improved without the occurrence of dentrite even after 1000 hours.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】エレオステアリン酸を主成分とする乾性油
とフェノール類を固体酸触媒に用いて反応させ、反応終
了後に固体酸を濾別して除去した反応生成物に、塩基性
触媒の存在下にアルデヒド類を添加してレゾール化する
ことを特徴とする変性フェノール樹脂の製造法。
1. A reaction product obtained by reacting a drying oil containing eleostearic acid as a main component with a phenol as a solid acid catalyst and removing the solid acid by filtration after the reaction is completed in the presence of a basic catalyst. A process for producing a modified phenolic resin, which comprises adding an aldehyde to a resin to form a resole.
【請求項2】固体酸がパーフルオロアルカンスルホン酸
型イオン交換樹脂またはスルホン型強酸性イオン交換樹
脂または合成ゼオライトである請求項1に記載の変性フ
ェノール樹脂の製造法。
2. The method for producing a modified phenolic resin according to claim 1, wherein the solid acid is a perfluoroalkanesulfonic acid type ion exchange resin, a sulfone type strongly acidic ion exchange resin or a synthetic zeolite.
JP4254598A 1992-09-24 1992-09-24 Production of modified phenol resin Pending JPH06107756A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4254598A JPH06107756A (en) 1992-09-24 1992-09-24 Production of modified phenol resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4254598A JPH06107756A (en) 1992-09-24 1992-09-24 Production of modified phenol resin

Publications (1)

Publication Number Publication Date
JPH06107756A true JPH06107756A (en) 1994-04-19

Family

ID=17267266

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4254598A Pending JPH06107756A (en) 1992-09-24 1992-09-24 Production of modified phenol resin

Country Status (1)

Country Link
JP (1) JPH06107756A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008514769A (en) * 2004-10-01 2008-05-08 アクゾ ノーベル ナムローゼ フェンノートシャップ Process for the preparation of polymeric hydroxyalkyl-terminated polysulfides
CN108383962A (en) * 2018-03-06 2018-08-10 苏州兴业材料科技股份有限公司 A kind of preparation method of electronic material modified by alkyl phenol phenolic resin

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008514769A (en) * 2004-10-01 2008-05-08 アクゾ ノーベル ナムローゼ フェンノートシャップ Process for the preparation of polymeric hydroxyalkyl-terminated polysulfides
CN108383962A (en) * 2018-03-06 2018-08-10 苏州兴业材料科技股份有限公司 A kind of preparation method of electronic material modified by alkyl phenol phenolic resin
CN108383962B (en) * 2018-03-06 2020-06-02 苏州兴业材料科技股份有限公司 Preparation method of alkylphenol modified phenolic resin for electronic material

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