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JPS6017413B2 - Manufacturing method of thermosetting resin - Google Patents
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JPS6017413B2 - Manufacturing method of thermosetting resin - Google Patents

Manufacturing method of thermosetting resin

Info

Publication number
JPS6017413B2
JPS6017413B2 JP14897980A JP14897980A JPS6017413B2 JP S6017413 B2 JPS6017413 B2 JP S6017413B2 JP 14897980 A JP14897980 A JP 14897980A JP 14897980 A JP14897980 A JP 14897980A JP S6017413 B2 JPS6017413 B2 JP S6017413B2
Authority
JP
Japan
Prior art keywords
formaldehyde
reaction
nonylphenol
added
melamine
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
JP14897980A
Other languages
Japanese (ja)
Other versions
JPS5773018A (en
Inventor
一紀 光橋
繁 伊藤
満利 鎌田
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.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery 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 Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP14897980A priority Critical patent/JPS6017413B2/en
Publication of JPS5773018A publication Critical patent/JPS5773018A/en
Publication of JPS6017413B2 publication Critical patent/JPS6017413B2/en
Expired legal-status Critical Current

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

Description

【発明の詳細な説明】 本発明は、打抜き加工性、難燃性、耐アーク性、耐薬品
性、耐熱性の各特性を高度に必要とする積層板の製造に
有効な熱硬化性樹脂の製造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a thermosetting resin that is effective for manufacturing laminates that require high properties such as punching workability, flame retardance, arc resistance, chemical resistance, and heat resistance. Regarding manufacturing.

従釆、上記護持性を高度に与える方法として、フェノー
ル樹脂とメラミンの様なトリアジン環を含むァミノ化合
物を共縮合した樹脂に可塑剤を添加する技術が採用され
るされている。
As a method for imparting the above-mentioned protective properties to a high degree, a technique has been adopted in which a plasticizer is added to a resin obtained by co-condensing a phenol resin with an amino compound containing a triazine ring such as melamine.

しかし、この従来法は、共縮合性に問題があり樹脂製造
時に厳密なPH管理を必要とし、縮合物の貯蔵安定性が
なく未反応のアミノ化合物の沈澱がじやすく、且基材に
合浸し積層板とした時の特性が前記の諸特性を満足しな
い。即ち、トリアジン系化合物を使用すれば難燃性、耐
アーク性は向上するも硬くなる頃向がある。従って、適
正な温度範囲での打抜き加工性を得るためには多量の可
塑剤が必要となり、耐薬品性、耐熱性が著しく低下する
欠点がある。また、この様な加工性と耐薬品性、耐熱性
を兼ね合わせる必要があるとの函馬点からアルキルフェ
ノール、例えばノニルフェノールーホルムアルデヒド反
応物を従釆の可塑剤に代えて使用する方法も考えられる
が、メラミンの如きトリアジン化合物との安定した共縮
合やメラミンーホルムアルデヒドとの相溶が充分出釆ず
、樹脂ワニスの貯蔵安定性がなく積層板にした場合前記
の諸特性を充分に満足できるものではなかった。本発明
は、以下に記述する方法で/ニルフェノール、フエノー
ル、メラミンーホルムアルデ十ヒド初期縮合物の三者を
同一反応系の中で反応せしめ、安定した樹脂ワニスを提
供し、前記の積層板とした時の諸特性を保持出来る熱硬
化性樹脂を提供することを目的とし、特にノエルフェノ
ールの可蓬性による打抜き加工性、フェノールを併用す
ることによるメラミンーホルムアルデヒド初期縮合物の
樹脂ワニス中での安定化と積層板にした時の耐薬品性、
更にメラミン樹脂の併用による耐ァーク性、難燃性を付
加して最近の電子分野で要望される積層板を提供せんと
するものである。
However, this conventional method has problems with co-condensation, requires strict pH control during resin production, lacks storage stability of the condensate, tends to precipitate unreacted amino compounds, and is difficult to co-dip into the base material. The properties when made into a laminate do not satisfy the above properties. That is, if a triazine compound is used, flame retardancy and arc resistance are improved, but there is a tendency for the material to become hard. Therefore, in order to obtain punching workability in an appropriate temperature range, a large amount of plasticizer is required, which has the drawback of significantly lowering chemical resistance and heat resistance. In addition, considering the need to combine such processability with chemical resistance and heat resistance, it is also possible to use an alkylphenol, such as a nonylphenol-formaldehyde reaction product, in place of the conventional plasticizer. However, stable co-condensation with triazine compounds such as melamine and compatibility between melamine and formaldehyde do not occur sufficiently, and the storage stability of the resin varnish is poor, so when made into a laminate, the above-mentioned properties cannot be fully satisfied. There wasn't. The present invention provides a stable resin varnish by reacting nylphenol, phenol, and melamine-formaldedehyde initial condensate in the same reaction system by the method described below. The aim is to provide a thermosetting resin that can maintain various properties when molded, especially the flexibility of Noel phenol to improve punching processability, and the combined use of phenol to improve the melamine-formaldehyde initial condensate in resin varnish. Stabilization and chemical resistance when laminated,
Further, by adding arc resistance and flame retardance by using a melamine resin in combination, the present invention aims to provide a laminate that is required in the recent electronic field.

タ 即ち、本発明は、ノニルフェノールとホルムアルデ
ヒドをアルカリ触媒存在下に反応させた後、この反応系
に前記ノニルフェノールに対して50〜20の重量%の
フェノールを添加、反応せしめ、反応生成物中の高分子
量物(分子量400〜800)が該生成物中の5〜2の
重量%の範囲内になるように反応を制御する。次いで、
メラミンーホルムアルデヒド初期縮合物を前記ノニルフ
ヱノールに対して20〜100重量%添加反応させたも
のを減圧脱水すれば目的の熱硬化性樹脂が得られる。本
発明を実施するに当り、ノニルフェノールとホルムアル
デヒドの反応は、周知の如く酸性、アルカリ触媒のいず
れでも行なえるが、メラミン−ホルムァルデヒド初期縮
合物を併用する場合は樹脂ワニスの安定性の点よりアル
カリ性が適当であり、触媒の種類としてはエチレンジア
ミン、ジェチルアミン、トリメチルアミン等が適当であ
る。
That is, in the present invention, after nonylphenol and formaldehyde are reacted in the presence of an alkali catalyst, phenol is added in an amount of 50 to 20% by weight based on the nonylphenol to this reaction system, and the reaction is caused to occur. The reaction is controlled such that the molecular weight product (molecular weight 400-800) is in the range of 5-2% by weight in the product. Then,
The desired thermosetting resin can be obtained by adding 20 to 100% by weight of a melamine-formaldehyde initial condensate to the nonylphenol and dehydrating it under reduced pressure. In carrying out the present invention, the reaction between nonylphenol and formaldehyde can be carried out using either acidic or alkaline catalysts, as is well known, but when a melamine-formaldehyde initial condensate is used in combination, it is preferable from the viewpoint of stability of the resin varnish. Alkalinity is suitable, and suitable catalysts include ethylenediamine, diethylamine, trimethylamine, etc.

また、ノニルフェノールとホルムアルデヒドを反応させ
る第1段階に於て、ノニルフェノールと縮合するホルム
ァルデヒドと後で添加するフェ/ールと縮合するに必要
なホルムアルデヒドをも含めたホルムアルデヒド量を使
用するのが望ましい。モル比としては一般的にレゾール
を生成するモル比、即ちノニルフェノール及びフェノー
ル各1モルに対して各々1.1〜1.5モルの範囲であ
れば良い。ノニルフェノールはフェノールより反応性が
劣り、フェノール添加前にノニルフェノールとホルムア
ルデヒドを縮合する必要がある。ホルムアルデヒドとに
はパラホルムアルデヒド、37%ホルマリンが使用出来
る。ノニルフェノールとホルムアルデヒドの反応の程度
は、環流温度下でホルムアルデヒド消費量が平衡になる
まで進める。ノニルフェノールとホルムアルデヒドの反
応物に直接メラミンーホルムアルデヒド初期縮合物を添
加反応せしめると樹脂ワニスの相溶性不充分による貯蔵
不安定を起こしゲル状物の沈澱や反応系でのゲル化現象
を起こす。従って、フェノールを併用することにより、
メラミンーホルムアルデヒド初期縮合物を安定させてゲ
ル化を起こすことなく反応に関与させることが出釆る。
使用するフェノール量はノニルフェ/−ルに対して5の
重量%禾満の場合は前記の効果はなく且、積層板にした
場合の耐薬品性が劣る。一方、20の重量%を越えると
積層板の硬さが増加し、打抜き加工性が低下する。更に
、ノニルフェノールとホルムアルデヒドの反応系にフェ
ノールを添加して反応せしめる場合、反応生成物中の高
分子量物(分子量400〜800)が該生成物中の5〜
2の重量%の範囲内になるよう制御する必要がある。尚
、反応制御を容易にするため、フェノールの反応は80
〜90qoの低温で行なうのが好ましい。前記生成物中
の高分子量物が5重量%未満の場合は未反応のフェノー
ルが多く。積層板にした場合耐薬品性の低下をきたす。
一方、2の重量%を越えると、特にメラミン−ホルムア
ルデヒド初期縮合物を添加した時反応系の安定性が保持
されず、ゲル化物が生成するかまたは得られた樹脂ワニ
スに濁りが生じる。メラミンーホルムアルデヒド初期縮
合物は、メラミンとホルムアルデヒドをPH8〜10で
縮合させたトリメチロールメラミンを主成分とする統合
物であり、市販のもの、例えば商品名ニカレジンS−3
05 S−260(日本カーバィド工業■製)が使用で
きる。
In addition, in the first step of reacting nonylphenol and formaldehyde, it is desirable to use an amount of formaldehyde that includes the formaldehyde that is condensed with nonylphenol and the formaldehyde necessary for condensation with phenol that is added later. . The molar ratio may generally be in the range of 1.1 to 1.5 moles for each mole of nonylphenol and phenol, which is the molar ratio that produces resol. Nonylphenol is less reactive than phenol, and it is necessary to condense nonylphenol and formaldehyde before adding phenol. Paraformaldehyde and 37% formalin can be used as formaldehyde. The extent of the reaction between nonylphenol and formaldehyde is allowed to proceed until formaldehyde consumption reaches equilibrium at reflux temperature. When a melamine-formaldehyde initial condensate is directly added to a reaction product of nonylphenol and formaldehyde to cause a reaction, storage instability occurs due to insufficient compatibility of the resin varnish, resulting in precipitation of a gel-like substance and a gelation phenomenon in the reaction system. Therefore, by using phenol together,
It is possible to stabilize the melamine-formaldehyde initial condensate and allow it to participate in the reaction without causing gelation.
If the amount of phenol used is less than 5% by weight based on nonyl phenol, the above-mentioned effect will not be obtained and the chemical resistance will be poor when made into a laminate. On the other hand, if it exceeds 20% by weight, the hardness of the laminate increases and the punching workability decreases. Furthermore, when phenol is added to the reaction system of nonylphenol and formaldehyde to cause a reaction, the high molecular weight substances (molecular weight 400 to 800) in the reaction product are
It is necessary to control the amount within a range of 2% by weight. In addition, in order to facilitate reaction control, the reaction of phenol was carried out at 80%
It is preferable to carry out at a low temperature of ~90 qo. When the amount of high molecular weight substances in the product is less than 5% by weight, there is a large amount of unreacted phenol. When made into a laminate, chemical resistance decreases.
On the other hand, if the amount exceeds 2% by weight, the stability of the reaction system will not be maintained, especially when the melamine-formaldehyde initial condensate is added, and a gelled product will be formed or the resulting resin varnish will become cloudy. The melamine-formaldehyde initial condensate is an integrated product whose main component is trimethylolmelamine, which is obtained by condensing melamine and formaldehyde at pH 8 to 10, and is commercially available, for example, under the trade name Nicaresin S-3.
05 S-260 (manufactured by Nippon Carbide Kogyo ■) can be used.

該初期縮合物を反応系に添加する場合、pHは6.8〜
7.5程度が相溶性の点から好ましい。前記初期縮合物
の添加量はノニルフェノールに対して20〜10の重量
%が適当である。2の重量%未満の場合、目的とする耐
アーク性、難燃性を得ることが出来ない。
When the initial condensate is added to the reaction system, the pH is 6.8~
A value of about 7.5 is preferable from the viewpoint of compatibility. The amount of the initial condensate added is suitably 20 to 10% by weight based on nonylphenol. If the amount is less than 2% by weight, the desired arc resistance and flame retardance cannot be obtained.

また、10の重量%を越えると樹脂ワニスの安定性の低
下と共に積層板にした場合硬く、打抜き加工が低下する
。また、反応の程度は、ゲル化時間を測定して塗工に適
する程度にまで調整する。最終的に、減圧脱れし溶剤と
してメタノール、アセトン等を添加して樹脂ワニスとす
る。このようにして得られた熱硬化性樹脂は、適当量の
鍵燃補助剤、例えばリン酸ェステル化合物やハ。
Moreover, if it exceeds 10% by weight, the stability of the resin varnish decreases, and when it is made into a laminate, it becomes hard and the punching process deteriorates. Further, the degree of reaction is adjusted to a degree suitable for coating by measuring gelation time. Finally, methanol, acetone, etc. are added as a solvent to be removed under reduced pressure to obtain a resin varnish. The thermosetting resin thus obtained is treated with a suitable amount of a key fuel additive, such as a phosphate ester compound or the like.

ゲン化ェポキシ化合物等を加えて常法により紙基材に合
浸し加熱乾燥してプリプレグとした後、該ブリプレグを
所定枚数重ね、要すれば銅箔等を重ねて加熱加圧により
積層成形する。以下実施例を述べる。
After adding a genified epoxy compound and the like and dipping it into a paper base material by a conventional method and heating and drying to obtain a prepreg, a predetermined number of sheets of the prepreg are stacked, and if necessary, copper foil or the like is stacked and laminated by heating and pressing. Examples will be described below.

実施例 1 /ニルフェノール(純度99.5%)500部(以下「
部」は重量部を示す)、85%パラホルムアルデヒド3
3碇部、37%ホルマリン8疎部、エチレンジアミン3
部を鷹洋装道、逆流冷却器及び温度計付反応容器に入れ
環流温度で4時間反応させた。
Example 1 / 500 parts of nylphenol (purity 99.5%) (hereinafter referred to as “
"parts" indicate parts by weight), 85% paraformaldehyde 3
3 anchor parts, 37% formalin 8 loose parts, ethylenediamine 3 parts
The mixture was placed in a reaction vessel equipped with a Takayoso-do, a counterflow condenser, and a thermometer, and reacted at reflux temperature for 4 hours.

この段階でフェノールを50の都添加し温度80qoに
て反応を進め数平均分子量400〜800の高分子量物
が反応物中の1の重量%の時点(ガスクロマトグフィー
分析)でpH7.1を確認後メラミンーホルムアルデヒ
ド初期縮合物(ニカレジンS−305)を25碇部添加
混合し、環流温度で反応を進め、反応生成物のゲル化時
間が3分3栃鱗こなった時点で減圧脱水を行ない、メタ
ノール80碇部を加えて固形分50%の樹脂ワニスを得
た。該ワニスは1ケ自室温にて放置しても濁りや沈澱は
生成せず安定性の良好なものであった。尚、ゲル化時間
は樹脂10夕を50ccビーカーにとり160qoの温
度下に燈拝し、樹脂がゲル状を程する迄の時間で表わし
たものである。
At this stage, 50% of phenol was added and the reaction proceeded at a temperature of 80qo, and when the high molecular weight substance with a number average molecular weight of 400 to 800 was 1% by weight in the reactant (gas chromatography analysis), the pH was confirmed to be 7.1. After that, 25 parts of melamine-formaldehyde initial condensate (Nicaresin S-305) were added and mixed, the reaction was allowed to proceed at reflux temperature, and when the gelation time of the reaction product reached 3 minutes, dehydration was performed under reduced pressure. , 80 parts of methanol was added to obtain a resin varnish with a solid content of 50%. The varnish had good stability without forming turbidity or precipitate even when left alone at room temperature. The gelation time is expressed as the time it takes for the resin to change into a gel after 10 minutes of the resin is placed in a 50cc beaker and heated at a temperature of 160 quarts.

上記ワニスに難燃性肋剤としてリン酸ェステルを第1表
に示す固形分比率(部)で配合して塗工用ワニスとし、
厚さ10ミルスのリンター紙に含浸、乾燥して樹脂量5
0%のプリプレグとし、該プリプレグを9枚重ねて積層
プレスに挿入し、温度16び0、圧力100k9/地、
時間60分の条件で加熱加圧して、1.6の/肌厚の積
層板を得た。
A coating varnish is prepared by blending phosphate ester as a flame retardant additive into the above varnish at the solid content ratio (parts) shown in Table 1,
Impregnated into linter paper with a thickness of 10 mils and dried to a resin amount of 5
0% prepreg, 9 sheets of the prepreg were stacked and inserted into a lamination press, temperature 16 to 0, pressure 100k9/ground,
Heat and pressure was applied for 60 minutes to obtain a laminate with a skin thickness of 1.6.

該積層板の特性は第2表の通りであった。実施例 2ノ
ニルフエノール35碇部、85%パラホルムアルデヒド
337部、37%ホルマリン8碇郡、エチレンジアミン
3部を還流温度で4時間反応させた。
The properties of the laminate were as shown in Table 2. Example 2 35 parts of nonylphenol, 337 parts of 85% paraformaldehyde, 8 parts of 37% formalin, and 3 parts of ethylenediamine were reacted at reflux temperature for 4 hours.

この階段でフェノールを65$部加え、実施例1と同様
に反応させ、数平均分子量400〜800の高分子量物
が反応生成物中の15重量%になった点でメラミンーホ
ルムアルデヒド初期縮合物(ニカレジンS−305)を
25碇部添加、反応させ、反応生成物のゲル化時間3分
2硯砂・で減圧脱水に入り、脱水終了後、メタノール8
0戊郡を加えて固形分50%の樹脂ワニスを得た。該ワ
ニスは1ケ月間室温に放置しても濁りや固形分の沈澱は
なかった。上記ワニスを第1表に示す配合にて塗工用ワ
ニスとし、実施例1と同様にして1.6の/仇厚の積層
板を得た。
In this step, 65 parts of phenol was added, and the reaction was carried out in the same manner as in Example 1. When the amount of high molecular weight substances with a number average molecular weight of 400 to 800 was 15% by weight in the reaction product, the melamine-formaldehyde initial condensate ( 25 parts of Nikaresin S-305) was added and reacted, gelling time of the reaction product was 3 minutes, dehydration was started under reduced pressure with 2 silica sand, and after completion of dehydration, 8 parts of methanol was added.
A resin varnish with a solid content of 50% was obtained by adding 0.05%. Even when the varnish was left at room temperature for one month, there was no turbidity or precipitation of solid content. The above-mentioned varnish was used as a coating varnish in the formulation shown in Table 1, and a laminate having a thickness of 1.6 mm was obtained in the same manner as in Example 1.

該積層板の特性は第2表の通りであつた。比較例 1 実施例1に於けるノニルフェノールーホルムァルデヒド
反応物にフェノールを用いず直接メラミンーホルムアル
デヒド初期縮合物を添加すると反応系は濁りを生じ、ゲ
ル状物が沈澱し、積層板に提供出来る樹脂ワニスは製造
できなかった。
The properties of the laminate were as shown in Table 2. Comparative Example 1 When the melamine-formaldehyde initial condensate was directly added to the nonylphenol-formaldehyde reaction product in Example 1 without using phenol, the reaction system became cloudy and a gel-like substance precipitated, which could be provided to the laminate. Resin varnish could not be manufactured.

比較例 2実施例1に於て、メラミンーホルムアルデヒ
ド初期縮合物(ニカレジンS−305)を使用せず、/
ニルフェノールーホルムアルデヒド反応系にフェノール
を添加するのみで反応を進めた樹脂ワニスを用いて第1
表に示す配合にて塗工用ワニスとし、他は実施例1と同
様にして1.6の/仇厚の積層板を得た。
Comparative Example 2 In Example 1, the melamine-formaldehyde initial condensate (Nicaresin S-305) was not used;
The first experiment was carried out using a resin varnish in which the reaction proceeded only by adding phenol to the nylphenol-formaldehyde reaction system.
A coating varnish was prepared using the formulation shown in the table, and a laminate having a thickness of 1.6 mm was obtained in the same manner as in Example 1 except for the following.

該積層板の特性は第2表の通りであつた。比較例 3 実施例2に於てメラミンーホルムアルデヒド初期縮合物
(ニカレジンS一305)を40碇部添加し、反応を進
め、反応生成物のゲル化時間3分で減圧脱水に入り脱水
終了後メタノールを950部加え、固形分50%の樹脂
ワニスを得た。
The properties of the laminate were as shown in Table 2. Comparative Example 3 In Example 2, 40 parts of melamine-formaldehyde initial condensate (Nicaresin S-305) was added to proceed with the reaction, and after 3 minutes of gelation time of the reaction product, dehydration began under reduced pressure and methanol was added after completion of dehydration. 950 parts of were added to obtain a resin varnish with a solid content of 50%.

該ワニスは室温にて2小時間後には濁りを生じ、3日後
には沈澱物を生成した。該ワニスを使用した積層板の特
性を第2表に示す。第1表 (注)C.D.P:クレジルジフェニルフオスフェート
(リン酸ェステル化合物)一般に難燃性向上 剤として使用される。
The varnish became cloudy after 2 hours at room temperature and formed a precipitate after 3 days. Table 2 shows the properties of the laminate using this varnish. Table 1 (Note) C. D. P: Cresyl diphenyl phosphate (phosphate ester compound) Generally used as a flame retardancy improver.

第2表 上記特性試験の方法は次の通りである。Table 2 The method for the above characteristic test is as follows.

‘1}最適打抜き加工温度:ASTM法によるVeり鰍
odの評点の得られる温度(60qo以下を目標){2
)難燃性:UL製法による(V−○を目標)(V−0平
均5秒以下、最大1の砂以下)【3}耐ァーク性:AS
TM法による(10の母以上を目標){4)耐薬品性:
外観にて判断(斑点が生成するとout)第2表から明
らかなように、本発明の方法による熱硬化性樹脂を使用
した積層板は、打抜き加工性、難燃性、耐アーク性、耐
薬品性、耐熱性の各特性を兼ね合わせ保持している。
'1} Optimum punching temperature: Temperature at which a Ve od rating can be obtained according to the ASTM method (targeting 60 qo or less) {2
) Flame retardancy: By UL manufacturing method (targeting V-○) (V-0 average 5 seconds or less, maximum 1 sand or less) [3} Arc resistance: AS
By TM method (targeting 10 or higher) {4) Chemical resistance:
Judging by appearance (out if spots are formed) As is clear from Table 2, the laminate using the thermosetting resin produced by the method of the present invention has excellent punching workability, flame retardancy, arc resistance, and chemical resistance. It maintains both properties of heat resistance and heat resistance.

Claims (1)

【特許請求の範囲】[Claims] 1 ノニルフエノールとホルムアルデヒドをアルカリ触
媒存在下に反応させた後この反応系に前記ノニルフエノ
ールに対して50〜200重量%のフエノールを添加し
て反応生成物中の高分子量物(分子量400〜800)
が該生成物中の5〜20重量%を占めるまで反応を進め
、次いでメラミン−ホルムアルデヒド初期縮合物を前記
ノニルフエノールに対して20〜100重量%添加して
反応させることを特徴とする熱硬化性樹脂の製造法。
1. After reacting nonylphenol and formaldehyde in the presence of an alkali catalyst, 50 to 200% by weight of phenol based on the nonylphenol is added to the reaction system to remove high molecular weight substances (molecular weight 400 to 800) in the reaction product.
The reaction is allowed to proceed until it accounts for 5 to 20% by weight in the product, and then 20 to 100% by weight of the melamine-formaldehyde initial condensate is added to the nonylphenol and reacted. Method of manufacturing resin.
JP14897980A 1980-10-24 1980-10-24 Manufacturing method of thermosetting resin Expired JPS6017413B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14897980A JPS6017413B2 (en) 1980-10-24 1980-10-24 Manufacturing method of thermosetting resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14897980A JPS6017413B2 (en) 1980-10-24 1980-10-24 Manufacturing method of thermosetting resin

Publications (2)

Publication Number Publication Date
JPS5773018A JPS5773018A (en) 1982-05-07
JPS6017413B2 true JPS6017413B2 (en) 1985-05-02

Family

ID=15464960

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14897980A Expired JPS6017413B2 (en) 1980-10-24 1980-10-24 Manufacturing method of thermosetting resin

Country Status (1)

Country Link
JP (1) JPS6017413B2 (en)

Also Published As

Publication number Publication date
JPS5773018A (en) 1982-05-07

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