JP3183748B2 - Method for producing flame-retardant laminate - Google Patents
Method for producing flame-retardant laminateInfo
- Publication number
- JP3183748B2 JP3183748B2 JP9095793A JP9095793A JP3183748B2 JP 3183748 B2 JP3183748 B2 JP 3183748B2 JP 9095793 A JP9095793 A JP 9095793A JP 9095793 A JP9095793 A JP 9095793A JP 3183748 B2 JP3183748 B2 JP 3183748B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- phenol
- acid
- drying oil
- added
- 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 - Fee Related
Links
Landscapes
- Reinforced Plastic Materials (AREA)
- Laminated Bodies (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、低温打ち抜き加工性に
優れた難燃性積層板の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a flame-retardant laminate excellent in low-temperature punching workability.
【0002】[0002]
【従来の技術】紙−フェノール樹脂積層板は、穴あけ又
は外形加工を、金型による打ち抜き加工によって行って
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、室温で打ち抜き加工するようになっている。フェ
ノール樹脂単独では可撓性がなく、打ち抜き加工性が悪
いので、フェノール樹脂を変性して可撓化している。そ
して、難燃化するために、リン系難燃剤、窒素系難燃剤
や三酸化アンチモンに代表される無機系難燃剤、エポキ
シ基含有難燃剤を適宜配合している。2. Description of the Related Art Paper-phenol resin laminates are punched or contoured by punching with a die. In recent years, punching has been performed at room temperature in order to reduce the dimensional change of printed wiring boards. The phenol resin alone is not flexible and has poor punching workability, so the phenol resin is modified to be flexible. In order to achieve flame retardancy, a phosphorus-based flame retardant, a nitrogen-based flame retardant, an inorganic flame retardant represented by antimony trioxide, and an epoxy group-containing flame retardant are appropriately blended.
【0003】フェノール樹脂を可撓化するために、一般
的に、エリオステアリン酸を主成分とする反応性に富む
桐油でフェノール樹脂を変性する。しかし、桐油は、価
格変動が激しく、また、入手困難になる場合も多々あっ
て、供給安定性に難点があるので、入手が容易で、安価
で供給、価格ともに安定しているリノール酸、リノレン
酸を主成分とする乾性油、半乾性油を用いることが検討
されている。このような植物油としては、アマニ油、大
豆油、サフラワー油などがあるが、フェノール類との反
応性に乏しい。そこで、ルイス酸触媒を多量に用いるな
ど反応条件を厳しくしてフェノール類と反応させること
が提案されている(特開昭55−3903号公報及び特
開昭55−108414号公報参照)。[0003] In order to make the phenolic resin flexible, the phenolic resin is generally modified with a highly reactive tung oil containing eryostearic acid as a main component. However, tung oil is subject to severe price fluctuations and difficulties in obtaining it in many cases, and there are difficulties in supply stability, so linoleic acid and linolenic are easy to obtain, inexpensive to supply, and both prices are stable. Use of a drying oil or a semi-drying oil containing an acid as a main component has been studied. Such vegetable oils include linseed oil, soybean oil, safflower oil and the like, but have poor reactivity with phenols. Therefore, it has been proposed to react with phenols under severe reaction conditions such as using a large amount of a Lewis acid catalyst (see JP-A-55-3903 and JP-A-55-108414).
【0004】[0004]
【発明が解決しようとする課題】ところが、ルイス酸触
媒を多量に用いると、植物油の加水分解も同時に起こり
低分子量成分が増加する。このため、積層板にした場
合、表面にこれらの低分子量成分や未反応植物油がにじ
みだすようになるほか、多量の触媒を使用するため、積
層板の電気特性が低下するといった問題を生じ、実用に
耐える積層板を得ることができない。すなわち、積層板
にしたときに、架橋密度が上がらず、硬化度が不足し、
層間接着力が弱く、打ち抜き加工時にバルジが発生す
る。また、耐溶剤性も低く、実用上問題があった。However, when a large amount of Lewis acid catalyst is used, hydrolysis of vegetable oil occurs at the same time and low molecular weight components increase. For this reason, when a laminated board is used, these low molecular weight components and unreacted vegetable oil ooze out on the surface, and the use of a large amount of catalyst causes a problem that the electrical properties of the laminated board are deteriorated. It is not possible to obtain a laminate that can withstand the heat. That is, when made into a laminate, the crosslinking density does not increase, the curing degree is insufficient,
The interlayer adhesion is weak, and bulges occur during punching. Further, the solvent resistance was low, and there was a problem in practical use.
【0005】本発明は、このような課題を解決して、リ
ノール酸、リノレン酸を主成分とする乾性油、半乾性油
をフェノール樹脂の変性剤とし、安価で低温打ち抜き加
工性に優れた難燃性積層板の製造方法を提供することを
目的とするものである。The present invention solves the above-mentioned problems, and uses a drying oil or a semi-drying oil containing linoleic acid or linolenic acid as a main component as a modifier for a phenol resin, and is inexpensive and excellent in low-temperature punching workability. It is an object of the present invention to provide a method for manufacturing a flammable laminate.
【0006】[0006]
【課題を解決するための手段】本発明は、リノール酸又
はリノレン酸のいずれか又は両方を主成分とする乾性油
又は半乾性油に、パーフルオロアルカンスルホン酸など
の超強酸を触媒としてフェノール類を付加させ、これを
レゾール化して得られた植物油変性フェノール樹脂と、
エポキシ系反応型難燃剤を必須成分とする樹脂ワニス
を、繊維質基材に含浸乾燥して得られたプリプレグを所
定枚数重ねて加熱加圧することを特徴とする難燃性積層
板の製造方法である。SUMMARY OF THE INVENTION The present invention relates to a drying oil or semi-drying oil containing linoleic acid and / or linolenic acid as a main component, and using a phenol as a catalyst with a super strong acid such as perfluoroalkanesulfonic acid as a catalyst. And a vegetable oil-modified phenolic resin obtained by resolving the same,
A method for producing a flame-retardant laminate, characterized in that a predetermined number of prepregs obtained by impregnating and drying a fibrous base material with a resin varnish containing an epoxy-based reactive flame retardant as an essential component are heated and pressed. is there.
【0007】本発明に用いられるリノール酸、リノレン
酸を主成分とする植物油には、アマニ油、サフラワー
油、大豆油、ゴマ油、エノ油、アサミ油、菜種油、綿実
油、脱水ヒマシ油などがあり、特に不飽和度が高くしか
も価格が安価で供給量が安定しているアマニ油が好まし
い。[0007] Vegetable oils containing linoleic acid and linolenic acid as main components used in the present invention include linseed oil, safflower oil, soybean oil, sesame oil, eno oil, asami oil, rapeseed oil, cottonseed oil, dehydrated castor oil and the like. In particular, linseed oil having a high degree of unsaturation, a low price, and a stable supply is preferred.
【0008】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。[0008] Phenols include phenol, ortho-cresol, meta-cresol, para-cresol, xylenol, catechol, resorcinol, hydroquinone,
Octyl phenol, tert-butyl phenol, nonyl phenol, bisphenol-A and the like can be mentioned.
【0009】植物油とフェノール類との反応触媒に用い
られるパーフルオロアルカンスルホン酸としては、トリ
フルオロメタンスルホン酸、ペンタフルオロメタンスル
ホン酸、ヘプタフルオロメタンスルホン酸、ノナフルオ
ロメタンスルホン酸、ウンデカフルオロメタンスルホン
酸などが挙げられる。特に、トリフルオロメタンスルホ
ン酸が好ましい。The perfluoroalkanesulfonic acid used as a catalyst for the reaction between vegetable oil and phenols includes trifluoromethanesulfonic acid, pentafluoromethanesulfonic acid, heptafluoromethanesulfonic acid, nonafluoromethanesulfonic acid, undecafluoromethanesulfonic acid. Acids and the like. Particularly, trifluoromethanesulfonic acid is preferred.
【0010】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ち抜き加
工性が満足出来ない。The mixing ratio of vegetable oil to phenols is not particularly limited, but vegetable oil: phenols = 2: 8 to 6: 4, preferably 3: 7 to 4: 6, from the characteristics of the laminated board.
When the blending ratio of the vegetable oil is larger than 6: 4, the curability of the laminate decreases, and defects such as sticky surfaces appear.
On the other hand, when the ratio is smaller than 2: 8, the low-temperature punching workability of the laminate cannot be satisfied.
【0011】また、触媒の添加量も特に限定されない
が、植物油100重量部に対して、3〜0.001重量
部、特に、0.01〜0.05重量部が好ましい。3重
量部以上になると積層板の電気的特性が低下し、0.0
01重量部以下では反応が遅くなり、工業的生産性が低
下する。The amount of the catalyst to be added is not particularly limited, but is preferably 3 to 0.001 part by weight, particularly preferably 0.01 to 0.05 part by weight, per 100 parts by weight of the vegetable oil. If the amount is more than 3 parts by weight, the electrical properties of the laminated board deteriorate, and
If the amount is less than 01 parts by weight, the reaction will be slow and the industrial productivity will decrease.
【0012】植物油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、つぎ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、加水分解反応が頻発し低分
子量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 reaction between the vegetable oil and the phenol can be carried out in the absence of a solvent or in a solvent. However, considering the following reaction with formaldehyde, the reaction is preferably carried out without a solvent. The reaction temperature is preferably from 50 to 250C, particularly preferably 100C or lower. When the temperature is 100 ° C. or higher, a hydrolysis reaction frequently occurs, and a low molecular weight is likely to occur.
【0013】植物油とフェノール樹脂の相溶性をよくす
るために、植物油とフェノール類を反応させる前に、フ
ェノール類と芳香族炭化水素ホルムアルデヒド樹脂を酸
性触媒の存在下に反応させるとよい。In order to improve the compatibility between the vegetable oil and the phenol resin, the phenol and the aromatic hydrocarbon formaldehyde resin may be reacted in the presence of an acidic catalyst before the reaction between the vegetable oil and the phenol.
【0014】酸性触媒としては、パラトルエンスルホン
酸、ベンゼンスルホン酸なども挙げられるが、植物油と
の反応に用いられるパーフルオロアルカンスルホン酸い
わゆる超強酸が好ましい。芳香族炭化水素ホルムアルデ
ヒド樹脂としては、キシレン樹脂、トルエン樹脂などが
挙げられる。Examples of the acidic catalyst include p-toluenesulfonic acid, benzenesulfonic acid and the like, and a perfluoroalkanesulfonic acid used in the reaction with vegetable oil, a so-called super strong acid, is preferred. Examples of the aromatic hydrocarbon formaldehyde resin include a xylene resin and a toluene resin.
【0015】植物油とフェノール類の反応が終了したあ
と、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を行
い、積層板用樹脂を合成する。After the reaction between the vegetable oil and the phenols is completed, phenol is optionally added, and formaldehyde and a basic catalyst are added to carry out a usual resolving reaction to synthesize a resin for a laminate.
【0016】このようにして合成した変性フェノール樹
脂にエポキシ樹脂系反応型難燃剤を配合する。エポキシ
樹脂系反応型難燃剤としては、テトラブロモビスフェノ
ール−Aとエピクロルヒドリンとの反応生成物、ポリブ
ロモフェノール類のエピクロルヒドリン付加物、臭素化
ノボラック型エポキシ樹脂などが挙げられる。An epoxy resin-based reactive flame retardant is blended with the modified phenolic resin thus synthesized. Examples of the epoxy resin-based reactive flame retardant include a reaction product of tetrabromobisphenol-A with epichlorohydrin, an epichlorohydrin adduct of polybromophenols, and a brominated novolak epoxy resin.
【0017】これらの臭素含有エポキシ系難燃剤と、他
の難燃剤、例えば、リン系難燃剤、窒素系難燃剤や三酸
化アンチモンに代表される無機系難燃剤を併用してもよ
い。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、接着剤付き銅はくを重ねて、所定の圧力、温度で
所定時間加圧加熱して難燃性銅張り積層板とする。These bromine-containing epoxy flame retardants may be used in combination with other flame retardants, for example, inorganic flame retardants such as phosphorus flame retardants, nitrogen flame retardants and antimony trioxide. The varnish thus obtained is impregnated into a paper substrate and dried by heating to prepare a prepreg. A predetermined number of these sheets are stacked, copper foil with an adhesive is stacked, and pressurized and heated at a predetermined pressure and temperature for a predetermined time to obtain a flame-retardant copper-clad laminate.
【0018】フェノール類を付加した乾性油又は半乾性
油に、共役二重結合を分子中に含む脂肪酸を主成分とす
る乾性油又は半乾性油を反応させると、フェノール類を
付加したリノール酸又はリノレン酸と共役二重結合を分
子中に含む脂肪酸、例えば、二重結合を共役化したリノ
ール酸又はリノレン酸とがフェノール類を介して結合し
て分子量が大きくなり、樹脂の耐熱性が一層よくなる。
共役二重結合を分子中に含む脂肪酸を主成分とする乾性
油又は半乾性油としては、桐油、異性化アマニ油が挙げ
られる。この場合、リノール酸又はリノレン酸を主成分
とする乾性油又は半乾性油と、共役二重結合を分子中に
含む脂肪酸を主成分とする乾性油又は半乾性油との割合
は、重量比で、前者が95〜30に対して、後者が5〜
70とするのが好ましい。When a drying oil or a semidrying oil containing a conjugated double bond in a molecule as a main component is reacted with a drying oil or a semidrying oil to which a phenol is added, linoleic acid or linoleic acid added with a phenol is added. Linolenic acid and a fatty acid containing a conjugated double bond in the molecule, such as linoleic acid or linolenic acid having a conjugated double bond, are bonded via phenols to increase the molecular weight, thereby further improving the heat resistance of the resin. .
Examples of the drying oil or semi-drying oil mainly containing a fatty acid containing a conjugated double bond in the molecule include tung oil and isomerized linseed oil. In this case, the ratio of the drying oil or semi-dry oil containing linoleic acid or linolenic acid as a main component and the drying oil or semi-dry oil containing a fatty acid containing a conjugated double bond in the molecule as a main component is expressed by weight. The former is 95-30, while the latter is 5-30
It is preferably 70.
【0019】[0019]
【作用】リノール酸、リノレン酸を主成分とするアマニ
油などは、フェノール類を十分に付加させることができ
るが、アマニ油などの植物油同士を重合させることが困
難であるのに対し、アマニ油の二重結合を共役化した異
性化アマニ油は超強酸のような触媒下では異性化アマニ
油同士の重合が極めて容易に生ずる。すなわち、特殊な
触媒を選択すれば、リノール酸、リノレン酸を主成分と
する植物油でも低分子量化を抑制しながらフェノール類
と反応させることが可能で、しかも異性化アマニ油とフ
ェノール類の反応が一段と早まり、異性化アマニ油同士
の重合が促進され植物油フェノール類付加物が得られ
る。[Function] Linseic acid and linolenic acid as a main component can add phenols sufficiently, but it is difficult to polymerize linseed oil and other vegetable oils. Isomerized linseed oil in which the double bond is conjugated, polymerization of the isomerized linseed oil extremely easily occurs under a catalyst such as super strong acid. In other words, if a special catalyst is selected, linoleic acid and vegetable oils containing linolenic acid as a main component can be reacted with phenols while suppressing the reduction of molecular weight. Further, the polymerization of isomerized linseed oil is accelerated, and a phenol adduct of vegetable oil is obtained.
【0020】[0020]
実施例1 温度計、冷却管を備えた21の三つロフラスコに、アマ
ニ油200g、フェノール200g、トリフルオロメタ
ンスルホン酸0.3gを仕込み、80℃で3時間反応さ
せた。反応終了後フェノール180g、パラホルム25
5g、メタノール80g、アンモニア水38gを加えて
80℃でさらに反応させた。Example 1 200 g of linseed oil, 200 g of phenol, and 0.3 g of trifluoromethanesulfonic acid were charged into a 21-neck flask equipped with a thermometer and a condenser, and reacted at 80 ° C. for 3 hours. After completion of the reaction, phenol 180 g, paraform 25
5 g, 80 g of methanol and 38 g of aqueous ammonia were added, and further reacted at 80 ° C.
【0021】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、テトラブロモビスフェ
ノール−Aとエピクロルヒドリンとの反応生成物(YD
B−400 東都化成株式会社商品名)150g及びト
リフェニルホスフェート150gを撹拌しながら溶解し
てワニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time became 3 minutes, the reaction was terminated.
g of methanol and 200 g of methanol, and the reaction product of tetrabromobisphenol-A with epichlorohydrin (YD
B-400 150 g of Toto Kasei Co., Ltd. and 150 g of triphenyl phosphate were dissolved with stirring to form a varnish.
【0022】実施例2 温度計、冷却管を備えた21の三つロフラスコに、キシ
レン樹脂(ニカノール−H 三菱瓦斯化学株式会社 商
品名)50g、m,p−クレゾール250g、フルオロ
スルホン酸1.0gを仕込み、90℃で1時間反応さ
せ、さらに、アマニ油200gを加えて、同じ温度で2
時間反応させた。次に、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℃で反応させた。Example 2 In a 21 three-necked flask equipped with a thermometer and a cooling tube, 50 g of xylene resin (trade name of Nicanol-H, Mitsubishi Gas Chemical Co., Ltd.), 250 g of m, p-cresol, 1.0 g of fluorosulfonic acid And reacted at 90 ° C. for 1 hour. Further, 200 g of linseed oil was added thereto.
Allowed to react for hours. Next, 100 g of phenol, 177 g of paraform, 60 g of methanol, and 21.6 of aqueous ammonia.
g was added and reacted at 80 ° C.
【0023】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、テトラブロモビスフェ
ノール−Aとエピクロルヒドリンとの反応生成物(ES
B−400 住友化学工業株式会社商品名)150g及
びトリフェニルホスフェート150gを、撹拌しながら
溶解してワニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time became 3 minutes, the reaction was terminated.
g of methanol and 200 g of methanol, and a reaction product of tetrabromobisphenol-A with epichlorohydrin (ES
B-400 150 g of Sumitomo Chemical Co., Ltd. and 150 g of triphenyl phosphate were dissolved with stirring to form a varnish.
【0024】実施例3 温度計、冷却管を備えた21の三つロフラスコに、フェ
ノール200g、キシレン樹脂(ニカノール−H 三菱
瓦斯化学株式会社 商品名)50g、トリフルオロメタ
ンスルホン酸1.0gを仕込み、100℃で1時間反応
させ、さらに、大豆油200gを加え、同じ温度で5時
間反応させた。次に、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℃で反応させた。Example 3 200 g of phenol, 50 g of xylene resin (trade name of Nicanol-H, Mitsubishi Gas Chemical Co., Ltd.), and 1.0 g of trifluoromethanesulfonic acid were placed in a 21-neck flask equipped with a thermometer and a cooling tube. The reaction was carried out at 100 ° C. for 1 hour, and 200 g of soybean oil was further added, followed by a reaction at the same temperature for 5 hours. Next, 180 g of phenol, 255 g of paraform, 80 g of methanol and 38 g of aqueous ammonia were added and reacted at 80 ° C.
【0025】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、テトラブロモビスフェ
ノール−Aとエピクロルヒドリンとの反応生成物(YD
B−400 東都化成株式会社商品名)100g、ポリ
ブロモフェノール類のエピクロルヒドリン付加物(BR
−200 日本化薬株式会社商品名)50g及びトリフ
ェニルホスフェート150gを撹拌しながら溶解してワ
ニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time became 3 minutes, the reaction was terminated.
g of methanol and 200 g of methanol, and the reaction product of tetrabromobisphenol-A with epichlorohydrin (YD
B-400 100 g of Tohto Kasei Co., Ltd., epichlorohydrin adduct of a polybromophenol (BR)
-200 50 g of Nippon Kayaku Co., Ltd.) and 150 g of triphenyl phosphate were dissolved with stirring to form a varnish.
【0026】実施例4 温度計、冷却管を備えた21の三つロフラスコに、キシ
レン樹脂(ニカノール−H 三菱瓦斯化学株式会社 商
品名)80g、m,p−クレゾール250g、トリフル
オロメタンスルホン酸0.5gを仕込み、80℃で1時
間反応させ、さらに、アマニ油200gを加えて、10
0℃で2時間反応させた。その反応液に桐油50gを追
加して同じ温度で1時間反応させた。反応終了後、フェ
ノール170g、パラホルム190g、メタノール80
g、アンモニア水27gを加えて80℃で反応させた。Example 4 In a 21 three-necked flask equipped with a thermometer and a cooling tube, 80 g of xylene resin (trade name of Nicanol-H, Mitsubishi Gas Chemical Co., Ltd.), 250 g of m, p-cresol, and 0.1 g of trifluoromethanesulfonic acid were added. 5 g was charged and reacted at 80 ° C. for 1 hour.
The reaction was performed at 0 ° C. for 2 hours. 50 g of tung oil was added to the reaction solution and reacted at the same temperature for 1 hour. After completion of the reaction, 170 g of phenol, 190 g of paraform, and 80 g of methanol
g and 27 g of aqueous ammonia were added and reacted at 80 ° C.
【0027】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、臭素化ノボラック型エ
ポキシ樹脂(BREN 日本化薬株式会社 商品名)2
00g及びトリフェニルホスフェート150gを、撹拌
しながら溶解してワニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and dehydrated and concentrated. When the gelation time became 3 minutes, the reaction was terminated.
g, methanol 200 g, and brominated novolak type epoxy resin (BREN Nippon Kayaku Co., Ltd.) 2
00 g and 150 g of triphenyl phosphate were dissolved with stirring to form a varnish.
【0028】比較例1 温度計、冷却管を備えた2lの三つ口フラスコに、キシ
レン樹脂(ニカノール−H 三菱瓦斯化学株式会社 商
品名)50g、m,p−クレゾール250g、トリフル
オロメタンスルホン酸1.0gを仕込み、90℃で1時
間反応させ、さらに、アマニ油200gを加えて、同じ
温度で2時間反応させた。次に、フェノール100g、
パラホルム177g、メタノール60g、アンモニア水
21.6gを加えて80℃で反応させた。Comparative Example 1 A 2-liter three-necked flask equipped with a thermometer and a condenser was charged with 50 g of xylene resin (trade name of Nicanol-H, Mitsubishi Gas Chemical Co., Ltd.), 250 g of m, p-cresol, and trifluoromethanesulfonic acid 1 0.0 g, and reacted at 90 ° C. for 1 hour. Further, 200 g of linseed oil was added and reacted at the same temperature for 2 hours. Next, 100 g of phenol,
177 g of paraform, 60 g of methanol and 21.6 g of aqueous ammonia were added and reacted at 80 ° C.
【0029】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、テトラブロモビスフェ
ノール−A(添加型臭素系難燃剤として知られている)
135g及びトリフェニルホスフェート50gを添加し
てワニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and concentrated by dehydration. When the gelation time became 3 minutes, the reaction was terminated.
g, methanol 200 g, and tetrabromobisphenol-A (known as an addition-type brominated flame retardant)
135 g and 50 g of triphenyl phosphate were added to form a varnish.
【0030】比較例2 温度計、冷却管を備えた2lの三つ口フラスコに、キシ
レン樹脂(ニカノール−H 三菱瓦斯化学株式会社 商
品名)50g、m,p−クレゾール250g、トリフル
オロメタンスルホン酸1.0gを仕込み、90℃で1時
間反応させ、さらに、アマニ油200gを加えて、同じ
温度で2時間反応させた。次に、フェノール100g、
パラホルム177g、メタノール60g、アンモニア水
21.6gを加えて80℃で反応させた。Comparative Example 2 50 g of xylene resin (trade name of Nicanol-H, Mitsubishi Gas Chemical Co., Ltd.), 250 g of m, p-cresol, and trifluoromethanesulfonic acid 1 were placed in a two-liter three-necked flask equipped with a thermometer and a condenser. Then, the mixture was reacted at 90 ° C. for 1 hour, and further, 200 g of linseed oil was added and reacted at the same temperature for 2 hours. Next, 100 g of phenol,
177 g of paraform, 60 g of methanol and 21.6 g of aqueous ammonia were added and reacted at 80 ° C.
【0031】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、ゲル化時間
が3分になったところで反応を終了し、トルエン200
g、メタノール200gを加え、ポリブロモジフェニル
エーテル(添加型臭素系難燃剤として知られている)1
30g及びトリフェニルホスフェート150gを添加し
てワニスとした。When the gelation time at 160 ° C. became 6 minutes, the mixture was heated under reduced pressure and concentrated by dehydration. When the gelation time became 3 minutes, the reaction was terminated.
g, methanol 200 g, and polybromodiphenyl ether (known as an addition-type brominated flame retardant) 1
30 g and 150 g of triphenyl phosphate were added to make a varnish.
【0032】以上のようにして得られたワニスを、樹脂
分48%に調整した。水溶性フェノール樹脂を含浸乾燥
したクラフト紙を用意し、これに、上記のワニスを含
浸、乾燥させ、プリプレグとした。このプリプレグ所定
枚数重ね、片側に接着剤付銅はくを重ねて、10MP
a、160℃、1時間加熱加圧して銅張り積層板を製造
した。得られた銅張り積層板の特性をJIS−6481
に準拠して測定した。その結果を表1から表5に示す。The varnish obtained as described above was adjusted to a resin content of 48%. A kraft paper impregnated and dried with a water-soluble phenol resin was prepared, impregnated with the varnish described above, and dried to obtain a prepreg. A predetermined number of the prepregs are stacked, and a copper foil with an adhesive is stacked on one side, and 10MP
a, Heating and pressing at 160 ° C. for 1 hour to produce a copper-clad laminate. The characteristics of the obtained copper-clad laminate were measured in accordance with JIS-6481.
It measured according to. The results are shown in Tables 1 to 5.
【0033】[0033]
【表1】 ─────────────────────────────────── 絶縁抵抗(単位:Ω);処理条件、上段:受理状態、下段:D−2/100 ─────────────────────────────────── 実施例1 実施例2 実施例3 実施例4 比較例1 比較例2 2.7×1012 1.4×1012 0.9×1012 6.7×1012 1.8×1012 1.1×1012 2.8×108 1.6×108 2.3×108 4.3×108 1.6×106 1.9×108 ───────────────────────────────────[Table 1] ─────────────────────────────────── Insulation resistance (unit: Ω); Upper: receiving state, lower: D-2 / 100 ─────────────────────────────────── Example 1 Example 2 Example 3 Example 4 Comparative Example 1 Comparative Example 2 2.7 × 10 12 1.4 × 10 12 0.9 × 10 12 6.7 × 10 12 1.8 × 10 12 1.1 × 10 12 2.8 × 10 8 1.6 × 10 8 2.3 × 10 8 4.3 × 10 8 1.6 × 10 6 1.9 × 10 8 ───────────────────────────────────
【0034】[0034]
【表2】 ─────────────────────────────────── はんだ耐熱性(単位:秒) ─────────────────────────────────── 実施例1 実施例2 実施例3 実施例4 比較例1 比較例2 33 31 28 39 6 5 ───────────────────────────────────[Table 2] 耐熱 Solder heat resistance (unit: seconds) ─── ──────────────────────────────── Example 1 Example 2 Example 3 Example 4 Example 4 Comparative Example 1 Comparative Example 2 33 31 28 39 65 ───────────────────────────────────
【0035】[0035]
【表3】 ─────────────────────────────────── 耐トリクロールエチレン性(沸騰トリクロールエチレンに浸漬) ─────────────────────────────────── 実施例1 実施例2 実施例3 実施例4 比較例1 比較例2 30分 30分 30分 30分 1分で 1分で 異常なし 異常なし 異常なし 異常なし 表面白化 表面白化 ───────────────────────────────────[Table 3] ト リ Trichlorethylene resistance (to boiling trichlorethylene) (Immersion) ─────────────────────────────────── Example 1 Example 2 Example 3 Example 4 Comparison Example 1 Comparative Example 2 30 minutes 30 minutes 30 minutes 30 minutes 1 minute 1 minute No abnormality No abnormality No abnormality No abnormality No surface whitening Surface whitening ─────────────────── ────────────────
【0036】[0036]
【表4】 ─────────────────────────────────── 打ち抜き加工性 ─────────────────────────────────── 実施例1 実施例2 実施例3 実施例4 比較例1 比較例2 40〜100℃ 40〜110℃ 40〜90℃ 40〜110℃ バルジ発生 バルジ発生 良好 良好 良好 良好 ───────────────────────────────────[Table 4] 性 Punching workability ──────── ─────────────────────────── Example 1 Example 2 Example 3 Example 4 Comparative Example 1 Comparative Example 2 40 to 100 ° C. 40 ~ 110 ℃ 40 ~ 90 ℃ 40 ~ 110 ℃ Bulge occurrence Bulge occurrence Good Good Good Good ─────────────────────────────── ────
【0037】[0037]
【表5】 ─────────────────────────────────── 難燃性(UL−94);処理条件、上段:受理状態、下段:E−3/130 ─────────────────────────────────── 実施例1 実施例2 実施例3 実施例4 比較例1 比較例2 V−0 V−0 V−0 V−0 V−0 V−0 V−0 V−0 V−0 V−0 V−0 V−0 ───────────────────────────────────[Table 5] 燃 Flame retardant (UL-94); Processing conditions , Upper: receiving state, lower: E-3 / 130 1 Example 2 Example 3 Example 4 Comparative Example 1 Comparative Example 2 V-0 V-0 V-0 V-0 V-0 V-0 V-0 V-0 V-0 V-0 V-0 V −0 ───────────────────────────────────
【0038】[0038]
【発明の効果】アマニ油のように、安価で供給が安定し
ている乾性油又は半乾性油を、難燃性積層板用フェノー
ル樹脂の変性剤として、しかも特性が、桐油を変性剤と
した難燃性フェノール樹脂積層板と同等の難燃性フェノ
ール樹脂積層板を得ることができる。According to the present invention, dry oil or semi-dry oil which is inexpensive and has a stable supply, such as linseed oil, is used as a modifier for phenolic resins for flame-retardant laminates, and furthermore, tung oil is used as a modifier. A flame-retardant phenol resin laminate equivalent to the flame-retardant phenol resin laminate can be obtained.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 堀内 猛 茨城県下館市大字小川1500番地 日立化 成工業株式会社下館研究所内 (72)発明者 池田 謙一 茨城県下館市大字小川1500番地 日立化 成工業株式会社下館工場内 (72)発明者 奈良部 嘉行 茨城県下館市大字小川1500番地 日立化 成工業株式会社下館工場内 (72)発明者 中村 吉宏 茨城県下館市大字小川1500番地 日立化 成工業株式会社下館工場内 (56)参考文献 特開 昭63−83141(JP,A) 特開 昭63−83140(JP,A) 特開 昭54−129087(JP,A) 特開 平5−5022(JP,A) 特開 平4−168122(JP,A) (58)調査した分野(Int.Cl.7,DB名) B32B 1/00 - 35/00 B29B 11/16 B29B 15/08 - 15/14 C08J 5/04 - 5/10 C08J 5/24 H05K 1/03 ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Takeshi Horiuchi 1500 Oji Ogawa, Shimodate City, Ibaraki Prefecture Hitachi Chemical Industry Co., Ltd.Shimodate Research Laboratory (72) Inventor Kenichi Ikeda 1500 Oji Ogawa Shimodate City, Ibaraki Prefecture Hitachi Chemical Inside Shimodate Plant Co., Ltd. (72) Inventor Yoshiyuki Narabe 1500, Oji Ogawa, Shimodate City, Ibaraki Prefecture Hitachi Chemical Co., Ltd.Shitadate Plant Co., Ltd. (72) Yoshihiro Nakamura 1500 Ogawa Ogawa, Shimodate City, Ibaraki Prefecture Hitachi Chemical (56) References JP-A-63-83141 (JP, A) JP-A-63-83140 (JP, A) JP-A-54-129087 (JP, A) JP-A-5-5022 ( JP, A) JP-A-4-168122 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B32B 1/00-35/00 B29B 11/16 B29B 15/08-15 / 14 C08J 5/04-5/10 C08J 5/24 H05K 1/03
Claims (3)
は両方を主成分とする乾性油又は半乾性油に、パーフル
オロアルカンスルホン酸を触媒としてフェノール類を付
加させ、これをレゾール化して得られた植物油変性フェ
ノール樹脂と、エポキシ樹脂系反応型難燃剤を必須成分
とする樹脂ワニスを、繊維質基材に含浸乾燥して得られ
たプリプレグを所定枚数重ねて加熱加圧することを特徴
とする難燃性積層板の製造方法。1. A phenol compound is added to a drying oil or a semi-dry oil containing linoleic acid and / or linolenic acid as a main component, using perfluoroalkanesulfonic acid as a catalyst, and resolving the phenol. A prepreg obtained by impregnating and drying a fibrous base material with a resin varnish containing a vegetable oil-modified phenolic resin and an epoxy resin-based reactive flame retardant as essential components is stacked and heated and pressurized. Of manufacturing a functional laminate.
芳香族炭化水素ホルムアルデヒド樹脂の存在下に付加さ
せることを特徴とする請求項1記載の難燃性積層板の製
造方法。2. The method for producing a flame-retardant laminate according to claim 1, wherein a phenol is added to the drying oil or the semi-drying oil in the presence of an aromatic hydrocarbon formaldehyde resin.
性油に、共役二重結合を分子内に含む脂肪酸を主成分と
する乾性油又は半乾性油を反応させることを特徴とする
請求項1又は2記載の難燃性積層板の製造方法。3. The drying oil or the semi-drying oil containing a conjugated double bond in the molecule is reacted with the drying oil or the semi-drying oil to which phenols are added. Or the method for producing a flame-retardant laminate according to 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9095793A JP3183748B2 (en) | 1993-04-19 | 1993-04-19 | Method for producing flame-retardant laminate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9095793A JP3183748B2 (en) | 1993-04-19 | 1993-04-19 | Method for producing flame-retardant laminate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06297627A JPH06297627A (en) | 1994-10-25 |
JP3183748B2 true JP3183748B2 (en) | 2001-07-09 |
Family
ID=14012976
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JP9095793A Expired - Fee Related JP3183748B2 (en) | 1993-04-19 | 1993-04-19 | Method for producing flame-retardant laminate |
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JP (1) | JP3183748B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101547425B1 (en) | 2014-04-07 | 2015-08-25 | 주식회사 그루아이 | Toys play house which used young |
-
1993
- 1993-04-19 JP JP9095793A patent/JP3183748B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101547425B1 (en) | 2014-04-07 | 2015-08-25 | 주식회사 그루아이 | Toys play house which used young |
Also Published As
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JPH06297627A (en) | 1994-10-25 |
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