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JPS60199014A - Production of tung oil-modified phenolic resin - Google Patents

Production of tung oil-modified phenolic resin

Info

Publication number
JPS60199014A
JPS60199014A JP5683384A JP5683384A JPS60199014A JP S60199014 A JPS60199014 A JP S60199014A JP 5683384 A JP5683384 A JP 5683384A JP 5683384 A JP5683384 A JP 5683384A JP S60199014 A JPS60199014 A JP S60199014A
Authority
JP
Japan
Prior art keywords
tung oil
reaction
phenols
phenolic resin
reaction product
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
JP5683384A
Other languages
Japanese (ja)
Inventor
Atsuhiro Nakamoto
中本 篤宏
Akitsugu Miwa
晃嗣 三輪
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP5683384A priority Critical patent/JPS60199014A/en
Publication of JPS60199014A publication Critical patent/JPS60199014A/en
Pending legal-status Critical Current

Links

Classifications

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

Landscapes

  • Phenolic Resins Or Amino Resins (AREA)

Abstract

PURPOSE:To produce the titled resin having high trasparency without lowering electrical properties and plasticity, by mixing a reaction product of a phenolic compound and tung oil with a reaction product of methyl eleostearate and a phenolic compound at a specific ratio, and reacting the mixture with formaldehyde. CONSTITUTION:The reaction product (TP) prepared by the reaction of a phenolic compound with tung oil in the presence of p-toluene-sulfonic acid, triethanolamine, etc. is mixed with the reaction product (EP) prepared by the reacton of methyl eleostearate with a phenolic compound, at a weight ratio [EP/(TP+EP)] of 30-60. The mixture is made to react with formaldehyde in the presence of ammonia water, triethylamine, etc. to obtain the objective resin.

Description

【発明の詳細な説明】 [技術分野] こ発明は、フェノール樹脂の可塑化技術の分野に属する
。また一方では積層板の製造技術の分野にも属する。さ
らに詳しくはフェノール樹脂積層板の桐油変性による可
塑化の技術分野に属する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention belongs to the field of phenolic resin plasticization technology. On the other hand, it also belongs to the field of manufacturing technology for laminates. More specifically, it belongs to the technical field of plasticizing phenolic resin laminates by modifying them with tung oil.

[背景技術] 可塑化されたフェノール樹脂積層板を製造する場合、桐
油により樹脂を変性することが一般的に行われている。
[Background Art] When producing a plasticized phenolic resin laminate, it is common practice to modify the resin with tung oil.

桐油とフェノール類を反応させる際に、付加反応を安定
的に進行せさるために水を添加することが常法的になさ
れている。
When reacting tung oil with phenols, it is a common practice to add water in order to make the addition reaction proceed stably.

水を添加すれば、水による桐油の加水分解が生じるが、
加水分解生成物(主としてカルボン酸類であると思われ
る)が多量に混在すると得られる積層板の電気特性およ
び打ち抜き加工性が悪くなる。これを回避するためには
加水分解生成物の量を5%以下に留めるのが望ましい。
If water is added, hydrolysis of tung oil by water will occur,
If a large amount of hydrolysis products (which are thought to be mainly carboxylic acids) are present, the electrical properties and punching processability of the resulting laminate will deteriorate. In order to avoid this, it is desirable to keep the amount of hydrolysis products below 5%.

なおここで加水分解物の%は、桐油とフェノール類との
付加反応により生成した物から未反応のフェノール類を
除いた物の体積中に、桐油より低分子の物の占める体積
の比率で算出する値であり、GPC測定によるデータを
使用して算出する。
Note that the percentage of hydrolyzate here is calculated as the ratio of the volume of substances with lower molecular weight than tung oil to the volume of the product produced by the addition reaction between tung oil and phenols, excluding unreacted phenols. This value is calculated using data from GPC measurements.

しかし加水分解生成物を減少させると、得られる樹脂硬
化物が不透明となる。樹脂が不透明になると言うことは
積層板の性能あるいは外観も悪くなり商品価値が低下す
るので好ましくない、樹脂硬化物が不透明となる理由は
、長鎖の脂肪族(親油性)とフェノール類(親水性)と
の相溶性が悪くなるためで、相溶性が悪くなる結果、各
種の性能が悪化するのである。このように加水分解生成
物を減少させつつ、一方で透明性をも改良することは困
難であり、これを解決することが従来から要望されてい
た。
However, when the hydrolysis products are reduced, the resulting cured resin becomes opaque. If the resin becomes opaque, the performance or appearance of the laminate will deteriorate and the commercial value will decrease, which is undesirable. This is due to poor compatibility with the chemical properties), and as a result of poor compatibility, various performances deteriorate. It is difficult to improve transparency while reducing hydrolysis products as described above, and there has been a desire for a solution to this problem.

[発明の目的] 桐油変性フェノール樹脂を製造するに際して、電気的性
能、可塑性(打ち抜き加工性で評価する)を悪化させず
に、透明性の良好な桐油変性フェノール樹脂を製造する
方法を提供することを目的とする。
[Objective of the invention] To provide a method for producing a tung oil-modified phenolic resin with good transparency without deteriorating electrical performance and plasticity (evaluated by punching workability). With the goal.

[発明の開示] フェノール樹脂の桐油変性はすでに実用化されている。[Disclosure of invention] Tung oil modification of phenolic resin has already been put into practical use.

変性を行うにはまず、フェノール類と桐油を強酸の存在
下で付加反応させ、この付加反応生成物を変性剤として
使用することを特徴とする。すなわち、付加反応生成物
と未反応のフェノール類(場合によってはフェノール類
を追加してもよい)とホルムアルデヒドを、アルカリ触
媒の存在下で縮合反応させることを内容とする。ここで
桐油と付加反応させるためのフェノール類としては、フ
ェノール、クレゾールなど通常フェノール樹脂類の製造
原料とされるフェノール類であって、桐油と付加反応す
る性質のあるものが使用される。この場合バラ位が空い
ているフェノール類が反応性が優れているとされている
The modification is characterized in that phenols and tung oil are first subjected to an addition reaction in the presence of a strong acid, and the addition reaction product is used as a modifier. That is, the content is that the addition reaction product, unreacted phenols (phenols may be added depending on the case), and formaldehyde are subjected to a condensation reaction in the presence of an alkali catalyst. As the phenols for the addition reaction with tung oil, there are used phenols such as phenol and cresol which are usually used as raw materials for producing phenolic resins and which have the property of undergoing an addition reaction with tung oil. In this case, phenols with vacant positions are said to have excellent reactivity.

さて、この発明では桐油変性フェノール樹脂を製造する
に際して、フェノール類と桐油を反応させてて得られる
生成物(TP)と、エレオステアリン酸メチルエステル
とフェノール類を反応させて得られる生成物(E P)
を、EP/(TP+EP)の重量比が30〜60の範囲
で配合して、これをホルムアルデヒドと反応させること
を特徴とする。
Now, in this invention, when producing a tung oil-modified phenolic resin, a product (TP) obtained by reacting phenols and tung oil, and a product (TP) obtained by reacting eleostearic acid methyl ester and phenols. EP)
are blended in a weight ratio of EP/(TP+EP) in the range of 30 to 60, and this is reacted with formaldehyde.

なお、以上においてフェノール類と桐油あるいはエレオ
ステアリン酸メチルエステルとの反応は主として付加反
応と言われる反応が支配的であるが、ここで反応生成物
と称し、あるいはホルムアルデヒドとの反応に使用する
ものは未反応のフェノール類を含むものである。
In addition, in the above, the reaction between phenols and tung oil or eleostearic acid methyl ester is mainly a reaction called an addition reaction. contains unreacted phenols.

以下詳細に説明する。This will be explained in detail below.

[11桐油とフェノール類との反応 桐油、フェノール類、触媒(パラトルエンスルホン酸な
どの強酸)、水を反応容器中で攪拌しながら加熱して付
加反応物(TPと称する)を得る。この付加反応では加
水分解生成物が5重量%(以下%と略す)以下となる。
[11 Reaction between tung oil and phenols Tung oil, phenols, a catalyst (strong acid such as para-toluenesulfonic acid), and water are heated in a reaction vessel with stirring to obtain an addition reaction product (referred to as TP). In this addition reaction, the amount of the hydrolysis product is 5% by weight or less (hereinafter abbreviated as %).

なお、この際添加する水の量を減らす程加水分解生成物
の量は減少する。しかし水が少な過ぎるとゲル化を起こ
すため、ある程度の水の量は必要である。付加反応の条
件は限定はしない。
Note that the amount of hydrolyzed products decreases as the amount of water added at this time is reduced. However, too little water causes gelation, so a certain amount of water is necessary. The conditions for the addition reaction are not limited.

以上の付加反応に際しての桐油/フェノール類の配合重
量比は限定する趣旨ではないが、377〜7/3の範囲
が好ましい、水の好ましい添加量は反応系全体に対して
0.2〜2.5%相当量でアリ、パラトルエンスルホン
酸は50%水溶液で反応系全体に対して0.2〜1.0
%相当量が好ましい。反応時間は30〜250分、反応
温度は70〜90℃が好ましい。
Although the weight ratio of tung oil/phenols in the above addition reaction is not intended to be limited, it is preferably in the range of 377 to 7/3, and the preferable amount of water added is 0.2 to 2.0% relative to the entire reaction system. In a 5% equivalent amount, para-toluenesulfonic acid is 0.2 to 1.0 in a 50% aqueous solution to the entire reaction system.
% equivalent amount is preferred. The reaction time is preferably 30 to 250 minutes, and the reaction temperature is preferably 70 to 90°C.

反応終了後にトリエタノールアミンを添加する。これは
水溶液として添加するのが好ましい。添加量は反応系全
体に対して、50%の水溶液換算で0.2〜0.8%相
当量が好ましい。
Triethanolamine is added after the reaction is complete. Preferably, this is added as an aqueous solution. The amount added is preferably 0.2 to 0.8% equivalent in terms of 50% aqueous solution based on the entire reaction system.

[11]エレオステアリン酸メチルエステルとフェノー
ル類との反応 前記[I]における桐油を、エレオステアリン酸メチル
エステルに置き換えて同様の条件で反応させて付加反応
物(EPと称する)を得る。ただし、必ずしも水を添加
する必要はない。
[11] Reaction between methyl eleostearate and phenols The tung oil in [I] above is replaced with methyl eleostearate and the reaction is carried out under the same conditions to obtain an addition reaction product (referred to as EP). However, it is not always necessary to add water.

[11変性剤の調整 前記[11で得た付加反応(TP)と[+1]で得た付
加反応(B P)を重量比: EP/ (TP+EP)
が30〜70となるように混合する。
[11 Preparation of modifier Weight ratio of the addition reaction (TP) obtained in [11] and the addition reaction (B P) obtained in [+1]: EP/ (TP+EP)
Mix so that the ratio is 30 to 70.

[IV]桐油変性フェノール樹脂の製造以上で得た変性
剤にホルマリン、触媒を加えて変性フェノール樹脂を得
る。反応条件は限定するものではないが、通常は以下の
条件で反応させる。すなわち、 反応モル比がホルムアルデヒド/未反応フヱノ−ル類の
モル比が1.0〜1.5となるようにホルムアルデヒド
、大抵はホルマリンを添加する。
[IV] Production of tung oil modified phenolic resin Formalin and a catalyst are added to the modifier obtained above to obtain a modified phenolic resin. Although the reaction conditions are not limited, the reaction is usually carried out under the following conditions. That is, formaldehyde, usually formalin, is added so that the reaction molar ratio of formaldehyde/unreacted phenols is 1.0 to 1.5.

触媒を添加して縮合反応を行わせて変性フェノール樹脂
を得る。ここで使用する触媒としては、たとえばアンモ
ニア、ジエチルアミン、トリメチルアミンなど、あるい
はこれらの混合物が使用される。反応温度は60〜11
0℃、反応時間は40〜240分が好ましい。
A catalyst is added to carry out a condensation reaction to obtain a modified phenol resin. The catalyst used here is, for example, ammonia, diethylamine, trimethylamine, or a mixture thereof. The reaction temperature is 60-11
Preferably, the temperature is 0°C and the reaction time is 40 to 240 minutes.

反応後は減圧下で脱水し、溶剤を添加して希釈する。こ
こで使用される溶剤としてはアセトン、メタノール、T
HFなどが使用される。
After the reaction, the mixture is dehydrated under reduced pressure and diluted by adding a solvent. Solvents used here include acetone, methanol, T
HF etc. are used.

以上で得た桐油変性フェノール樹脂は、特に用途を限定
するものではないが、特に積層板用に好都合に利用され
る。そして積層板をこの変性樹脂を使用して製造した場
合には、加水分解生成物であるカルボン酸成分の混在が
少なく、電気的性能が優れ、かつ打ち抜き加工性で評価
されるところの可塑性が優れた積層板が製造できるので
ある。
The tung oil-modified phenolic resin obtained above is not particularly limited in its uses, but is particularly conveniently used for laminated boards. When a laminate is manufactured using this modified resin, it contains less carboxylic acid component, which is a hydrolysis product, and has excellent electrical performance and excellent plasticity as evaluated by punching workability. This makes it possible to produce laminates with different laminates.

透明性も良好である。この透明性が良好となる理由は明
らかではないが、エレオステアリン酸メチルエステルと
フェノール類との付加反応生成物が桐油の反応物および
フェノール樹脂との相溶性が、共に優れているためと考
えられる。
Transparency is also good. The reason for this good transparency is not clear, but it is thought to be because the addition reaction product of methyl eleostearate and phenols has excellent compatibility with both the reactant of tung oil and the phenol resin. It will be done.

実施例 (1)桐油とフェノール類との反応を以下の条件で行っ
た。
Example (1) A reaction between tung oil and phenols was carried out under the following conditions.

フェノール 61.4重量部 桐油 38.6重量部 パラトルエン スルホン酸 0.7重W部 水 1.3重量部 トリエタノール アミン(反応後) 0.6重量部 反応温度 80℃ 反応時間 60分 以上で得られた付加反応生成物中の加水分解生成物は4
.5%であった。
Phenol 61.4 parts by weight Tung oil 38.6 parts by weight Para-toluenesulfonic acid 0.7 parts by weight Water 1.3 parts by weight Triethanolamine (after reaction) 0.6 parts by weight Reaction temperature 80°C Reaction time 60 minutes or more The hydrolysis product in the obtained addition reaction product is 4
.. It was 5%.

なお、加水分解物の測定はGPCを使用した分析により
行った。そして加水分解生成物の量は、桐油とフェノー
ル類との反応生成物から未反応のフェノール類を除いた
物の体積中に、桐油メリ(琢分子の物の占める体積の比
率で算出した。
Note that the hydrolyzate was measured by analysis using GPC. The amount of the hydrolyzed product was calculated as the ratio of the volume of tung oil molecules to the volume of the reaction product between tung oil and phenols, excluding unreacted phenols.

(2)つぎにエレオステアリン酸メチルエステルとフェ
ノールの反応を以下の通り行った。
(2) Next, methyl eleostearate and phenol were reacted as follows.

フェノール 61.4重量部 エレオステアリン酸 メチルエステル 38.6重量部 パラトルエン スルホン酸 0. 7重量部 トリエタノール アミン(反応t&) 0.6重量部 反応温度 80℃ 反応時間 60分 (3)以上で得な付加反応生成物(TPおよびEP)の
混合比率を変え(混合物中のBP含有重量%で30.4
0.50,60.70%)、かつ次のような基本配合で
変性フェノール樹脂の合成を行った。
Phenol 61.4 parts by weight Eleostearic acid methyl ester 38.6 parts by weight Para-toluenesulfonic acid 0. 7 parts by weight Triethanolamine (reaction t&) 0.6 parts by weight Reaction temperature 80°C Reaction time 60 minutes 30.4 in weight%
(0.50%, 60.70%), and a modified phenolic resin was synthesized using the following basic formulation.

TP、BP混合物 74.4重量部 ホルマリン(37%) 1.0重量部 25%アンモニア水 1.0重量部 トリエチルアミン 2.4重量部 反応時間は150分、反応温度は80℃であった。反応
後減圧脱水した。得られた樹脂100重量部に対し、4
0M量部のメタノールを添加しワニスを得た。
TP, BP mixture 74.4 parts by weight Formalin (37%) 1.0 parts by weight 25% aqueous ammonia 1.0 parts by weight Triethylamine 2.4 parts by weight The reaction time was 150 minutes, and the reaction temperature was 80°C. After the reaction, the mixture was dehydrated under reduced pressure. For 100 parts by weight of the obtained resin, 4
A 0M part of methanol was added to obtain a varnish.

(4)以上で得た桐油変性フェノール樹脂の性能を評価
するために、紙基材のフェノール樹脂積層板を製造した
。すなわち、以上のワニスを厚さ10ミルスのクラフト
紙に含浸させ、乾燥してプリプレグを調整し、プリプレ
グ8枚を重ねて接着剤つきの銅箔を載置し、加圧成形し
て積層板を得た。
(4) In order to evaluate the performance of the tung oil-modified phenolic resin obtained above, a paper-based phenolic resin laminate was manufactured. That is, kraft paper with a thickness of 10 mils was impregnated with the above varnish, dried to prepare a prepreg, 8 sheets of prepreg were stacked, copper foil with adhesive was placed on top, and a laminate was obtained by pressure forming. Ta.

得られた積層板の性能を調べたところ第1表のようであ
った。
When the performance of the obtained laminate was examined, it was as shown in Table 1.

比較例 実施例と同様な条件で比較実験を行った。性能評価の結
果は第2表に示した。
Comparative Example A comparative experiment was conducted under the same conditions as in the example. The results of the performance evaluation are shown in Table 2.

ただし比較例5のTPは次の反応の条件で行った。However, TP in Comparative Example 5 was conducted under the following reaction conditions.

フェノール 61.4重量部 桐油 38.6重量部 パラトルエン スルホン酸 0.7重量部 水 4.31量部 トリエタノール アミン(反応後)0.6重量部 反応温度 80℃ 反応時間 120分 E以下余白] 第1表 第2表 注二 来煮沸後の絶縁抵抗 未来表面温度50での性能 [発明の効果] この発明は、桐油変性フェノール樹脂の製法において、
フェノール類と桐油の付加反応物(TP)と、エレオス
テアリン酸メチルエステルとフェノールの付加反応物(
EP)を、EP/(TP+EP)の重量比が30〜60
の範囲の割合で変性剤として使用することを特徴とする
ので、電気的特性および透明性の優れた変性フェノール
樹脂を得ることができた。
Phenol 61.4 parts Tung oil 38.6 parts Para-toluenesulfonic acid 0.7 parts Water 4.31 parts Triethanolamine (after reaction) 0.6 parts Reaction temperature 80°C Reaction time 120 minutes Margin below E ] Table 1 Table 2 Note 2 Insulation resistance after boiling Performance at future surface temperature 50 [Effects of the invention] This invention provides a method for producing a tung oil-modified phenolic resin.
Addition reaction product of phenols and tung oil (TP), and addition reaction product of eleostearic acid methyl ester and phenol (TP).
EP), the weight ratio of EP/(TP+EP) is 30 to 60
Since it is characterized in that it is used as a modifier in a proportion within the range of , it was possible to obtain a modified phenol resin with excellent electrical properties and transparency.

特許出願人 松下電工株式会社 代理人弁理士 竹元敏丸(ほか2名)Patent applicant: Matsushita Electric Works Co., Ltd. Representative Patent Attorney Toshimaru Takemoto (and 2 others)

Claims (1)

【特許請求の範囲】[Claims] (1)桐油変性フェノール樹脂の製法において、フェノ
ール類と桐油を反応させて得られる生成物(TP)およ
びエレオステアリン酸メチルエステルとフェノール類を
反応させて得られる生成物(EP)を、BP/ (TP
+BP)の重量比が30〜60の範囲になるように混合
し、これをホルムアルデヒドと反応させることを特徴と
する桐油変性フェノール樹脂の製法。
(1) In the method for producing tung oil-modified phenolic resin, a product obtained by reacting phenols with tung oil (TP) and a product obtained by reacting eleostearic acid methyl ester with phenols (EP) are converted into BP. / (TP
+BP) in a weight ratio of 30 to 60, and reacting the mixture with formaldehyde.
JP5683384A 1984-03-24 1984-03-24 Production of tung oil-modified phenolic resin Pending JPS60199014A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5683384A JPS60199014A (en) 1984-03-24 1984-03-24 Production of tung oil-modified phenolic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5683384A JPS60199014A (en) 1984-03-24 1984-03-24 Production of tung oil-modified phenolic resin

Publications (1)

Publication Number Publication Date
JPS60199014A true JPS60199014A (en) 1985-10-08

Family

ID=13038385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5683384A Pending JPS60199014A (en) 1984-03-24 1984-03-24 Production of tung oil-modified phenolic resin

Country Status (1)

Country Link
JP (1) JPS60199014A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03188118A (en) * 1989-12-15 1991-08-16 Matsushita Electric Works Ltd Production of oil-modified phenolic resin
CN103601703A (en) * 2013-07-11 2014-02-26 中南林业科技大学 Method for preparing epoxy methyl eleostearate from tung oil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03188118A (en) * 1989-12-15 1991-08-16 Matsushita Electric Works Ltd Production of oil-modified phenolic resin
CN103601703A (en) * 2013-07-11 2014-02-26 中南林业科技大学 Method for preparing epoxy methyl eleostearate from tung oil

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