JPS5912690B2 - resin composition - Google Patents

resin composition

Info

Publication number
JPS5912690B2
JPS5912690B2 JP49129344A JP12934474A JPS5912690B2 JP S5912690 B2 JPS5912690 B2 JP S5912690B2 JP 49129344 A JP49129344 A JP 49129344A JP 12934474 A JP12934474 A JP 12934474A JP S5912690 B2 JPS5912690 B2 JP S5912690B2
Authority
JP
Japan
Prior art keywords
parts
weight
resin
viscosity
unsaturated polyester
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
JP49129344A
Other languages
Japanese (ja)
Other versions
JPS5155364A (en
Inventor
勝利 高石
武 村上
京治 政元
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 JP49129344A priority Critical patent/JPS5912690B2/en
Publication of JPS5155364A publication Critical patent/JPS5155364A/ja
Publication of JPS5912690B2 publication Critical patent/JPS5912690B2/en
Expired legal-status Critical Current

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  • Macromonomer-Based Addition Polymer (AREA)
  • Reinforced Plastic Materials (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】 本発明は難燃化された不飽和ポ刃エステル樹脂組成物に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flame-retardant unsaturated polyester resin composition.

従来、不飽和ポリエステル樹脂を難燃化するために、水
和アルミナを配合する方法が採用されていた。し力化、
不飽和ポリエステル樹脂に水和アルミナを添加すると樹
脂粘度が大きくなり、シート状成形材料(SMC)や積
層板用のプリプレグ製造用に使用することはできなかつ
た。このためスチレンモノマの含有量を大きくし、全体
の粘度を低下させて用いる方法も考案されているが、ス
チレンモノマ量を増やすと性能が低下するので好ましく
ない。一方、樹脂粘度はその分子量を小さくして低下さ
せる方法も考えられるが、この場合はかえつて増粘効果
が得られず、さらに従来の製法では積層板(樹脂板)を
成形する場合厚み精度が得られず、スペーサなどを用い
て成形10していた。本発明は以上のような欠点を改良
した水和アルミナで難燃化された不飽和ポリエステル樹
脂組成物を提供するものである。
Conventionally, in order to make unsaturated polyester resin flame retardant, a method of blending hydrated alumina has been adopted. power,
When hydrated alumina was added to unsaturated polyester resin, the resin viscosity increased, making it impossible to use it for manufacturing sheet molding materials (SMC) or prepregs for laminates. For this reason, a method has been devised in which the styrene monomer content is increased to lower the overall viscosity, but increasing the styrene monomer content is not preferable because the performance deteriorates. On the other hand, it is possible to reduce the viscosity of the resin by reducing its molecular weight, but in this case, the viscosity increasing effect cannot be obtained, and furthermore, with the conventional manufacturing method, the thickness accuracy is poor when molding a laminate (resin board). However, it was not possible to obtain the desired shape, so it was molded using a spacer or the like. The present invention provides an unsaturated polyester resin composition made flame retardant with hydrated alumina, which improves the above-mentioned drawbacks.

しかして本発明は、不飽和ポリエステルを合成する場合
にグリコール/15二塩基酸のモル比が1.06以下、
好ましくは1.04以下で反応させ、得られた不飽和ポ
リエステルの液状架橋剤溶液の粘度が25℃において1
00センチポイズ以下で、かつこの溶液の液状架橋剤含
有量が50重量%以下である樹脂液に対して水和アルミ
ナと2価金属化合物と硬化剤を混合し、要すれば他の充
填剤、顔料、離型剤等を混合してスラリ状組成物となし
、これをガラス繊維基材と一体化させると共に加熱熟成
してなる点に特徴を有する。25本発明で用いる不飽和
ポリエステルは、無水マレイン酸、フマル酸等の不飽和
二塩基酸および要すれば無水フタル酸、イソフタル酸等
の飽和酸を併用し、これとエチレングリコール、プロピ
レングリコール、プロピレングリコール、ネオペンチ3
0ルグリコール、水添ビスフェノールA)ビスフェノー
ルAブロピレンオ午サイド付加物等のグリコール類を使
用し公知の手段で反応させる。
Therefore, in the present invention, when synthesizing an unsaturated polyester, the molar ratio of glycol/15 dibasic acid is 1.06 or less,
Preferably, the reaction temperature is 1.04 or less, and the viscosity of the obtained liquid crosslinking agent solution of unsaturated polyester is 1 at 25°C.
Hydrated alumina, a divalent metal compound, and a hardening agent are mixed with a resin liquid whose temperature is 00 centipoise or less and the liquid crosslinking agent content of this solution is 50% by weight or less, and if necessary, other fillers and pigments are added. It is characterized in that it is made by mixing a mold release agent and the like to form a slurry composition, which is integrated with a glass fiber base material and then heated and aged. 25 The unsaturated polyester used in the present invention is prepared by using in combination an unsaturated dibasic acid such as maleic anhydride or fumaric acid and, if necessary, a saturated acid such as phthalic anhydride or isophthalic acid, together with ethylene glycol, propylene glycol, or propylene. glycol, neopliers 3
The reaction is carried out using a known method using glycols such as hydrogenated bisphenol glycol, hydrogenated bisphenol A) and bisphenol A propylene acid adduct.

この場合のグリコール/二塩基酸のモル比が1.06以
下好ましくは1.04以下となるように使用比率を決3
5める。モル比がさきの数値を超えるとより増粘性が悪
くなる。以上のようにして得た不飽和ポリエステルをス
チレン等の液状架橋に溶解する。
In this case, the usage ratio is determined so that the molar ratio of glycol/dibasic acid is 1.06 or less, preferably 1.04 or less.
5 counts. If the molar ratio exceeds the above value, the thickening property will become worse. The unsaturated polyester obtained as described above is dissolved in a liquid crosslinking material such as styrene.

この場合の架橋剤の含有量は50重量%以下であり、好
ましくは45重量%以下である。これらの限界を越える
と製品の耐水性その他の性能が悪くなる。充填剤として
は、アルミナ、炭酸カルシウム、シリカ等の無機質粉末
を用いる。211ifi金属化合物としてはマグネシウ
ム、カルシウム、亜鉛等の酸化物、水酸化物等が用いら
れる。
In this case, the content of the crosslinking agent is 50% by weight or less, preferably 45% by weight or less. If these limits are exceeded, the water resistance and other performance of the product will deteriorate. As the filler, inorganic powder such as alumina, calcium carbonate, silica, etc. is used. As the 211ifi metal compound, oxides and hydroxides of magnesium, calcium, zinc, etc. are used.

これらは併用してもよい。以上のものの配合割合は樹脂
液100部(重量部以下同じ)に対して水和アルミナ1
50部以上、2価金属化合物は0.4〜2.0部、硬化
剤は0.5〜4部が好ましい。なお、充填剤、顔料、離
型剤その他の添加剤の混合量は任意である。このスラリ
状樹脂組成物をガラスマツト、ガラスチップトストラン
ドマットなどのガラス繊維基材に含浸させて一体化し、
二枚のブラスチツクフイルム(ポリエチレン、ポリプロ
ピレン等)間に挟んで適宜加熱して熟成をし、シート状
成形材料(SMC)とする。この操作は通常SMC製造
機を用いて、スラリ状組成物を、プラスチツクフイルム
上に塗布し、これで以つてガラス繊維基材を上下より挟
んでロールを用いて脱泡含浸させて製造する。あるいは
逆にガラス繊維基材上にスラリ状組成物をフイードし、
外側より2枚のプラスチツクスフイルムを当ててロール
で、脱泡含浸させる。得られたものを40〜50℃の温
度で24〜48時間熟成する。このようにして得られた
SMCはプラスチツクスフイルムを除いても指触乾燥状
態であり、付着性はない。以上のようにして得られたS
MCは難燃性を有すると共に樹脂の含浸状態、成形性の
すぐれたものである。
These may be used in combination. The mixing ratio of the above ingredients is 1 part of hydrated alumina to 100 parts of resin liquid (same parts below by weight).
Preferably, the amount is 50 parts or more, the divalent metal compound is preferably 0.4 to 2.0 parts, and the curing agent is 0.5 to 4 parts. Note that the amount of fillers, pigments, mold release agents, and other additives to be mixed is arbitrary. This slurry-like resin composition is impregnated into a glass fiber base material such as glass mat or glass chipped strand mat to integrate it.
It is sandwiched between two pieces of plastic film (polyethylene, polypropylene, etc.) and heated and aged to form a sheet-shaped molding material (SMC). This operation is usually carried out by applying a slurry composition onto a plastic film using an SMC manufacturing machine, and then sandwiching the glass fiber base material from above and below and using rolls to degas and impregnate it. Or, conversely, feed a slurry composition onto a glass fiber base material,
Apply two plastic films from the outside and roll to defoam and impregnate. The resultant is aged for 24-48 hours at a temperature of 40-50°C. The SMC thus obtained is dry to the touch even without the plastic film and has no adhesive properties. S obtained as above
MC has flame retardancy and is excellent in resin impregnation and moldability.

しかしてこれより得られる成形品の厚み精度もすぐれて
いる。実施例 1 先ずイソフタル酸332部、無水フタル酸296部、プ
ロプレングリコール797部の配合で第1段の反応を行
い、ついでフマル酸696部と反応物総量に対して20
0ppmのハイドロキノンを加えて第2段の反応を行わ
せ、酸価32の不飽和ポリエステルを得た。
However, the thickness accuracy of the molded product obtained from this method is also excellent. Example 1 First, the first stage reaction was carried out using a mixture of 332 parts of isophthalic acid, 296 parts of phthalic anhydride, and 797 parts of propene glycol, and then 696 parts of fumaric acid and 20 parts of the total amount of reactants.
A second stage reaction was carried out by adding 0 ppm of hydroquinone to obtain an unsaturated polyester having an acid value of 32.

これを不飽和ポリエステル濃度が55重量%になるよう
にスチレンモノマに溶解し、粘度90センチポイズ(2
5℃)の樹脂液〔A〕を得た。この場合のグリコール/
二塩基酸のモル比は1.05であつた。つぎに樹脂液〔
A〕の配合に対してプロピレングリコールを814部と
変更した以外はほぼ同様にして酸価32の不飽和ポリエ
ステルを得、同量のスチレンに溶かして粘度73センチ
ポイズの樹脂液〔B〕を得た。
This was dissolved in styrene monomer so that the unsaturated polyester concentration was 55% by weight, and the viscosity was 90 centipoise (2
5° C.) was obtained. Glycol in this case/
The molar ratio of dibasic acid was 1.05. Next, the resin liquid [
An unsaturated polyester with an acid value of 32 was obtained in almost the same manner except that propylene glycol was changed to 814 parts with respect to the formulation of [A], and it was dissolved in the same amount of styrene to obtain a resin liquid [B] with a viscosity of 73 centipoise. .

この場合のグリコール/二塩基酸のモル比は1.07で
あつた。以上とは別に、樹脂液〔A〕と同配合で、酸価
20であり、かつ粘度320センチポイズの樹脂液〔C
〕を得た。
The glycol/diacid molar ratio in this case was 1.07. Apart from the above, there is a resin liquid [C] which has the same composition as the resin liquid [A], has an acid value of 20, and has a viscosity of 320 centipoise.
] was obtained.

以上で得た樹脂液〔A〕、〔B〕、〔C〕を用い、各々
の樹脂液100部に対し、水和アルミナ150部、t−
ブチルパーベンゾエート1.2部を混合した後、さらに
酸化マグネシウム1.5部を添加してスラリ状の組成物
を得た。
Using the resin liquids [A], [B], and [C] obtained above, 150 parts of hydrated alumina and t-
After mixing 1.2 parts of butyl perbenzoate, 1.5 parts of magnesium oxide was further added to obtain a slurry composition.

これらを用いてガラス繊維含有量が3801)になるよ
うにガラス繊維マツトに含浸させ、両面をポリプロピレ
ンフイルムに挟み45℃で48時間加熱して熟成した。
この段階で樹脂液〔C〕を用いたものは増粘により粘度
が高くなり過ぎ、ガラス繊維マツトに含浸させることが
できなかつた。樹脂液〔A〕,〔B〕を用いたものは充
分含浸させることができた。しかし樹脂液〔B〕のもの
は含浸後も増粘が起らず指触乾燥状態にならなかつた。
樹脂液〔A〕をガラス繊維マツトに含浸させたものは指
触乾燥状態のSMCとなつた。このSMC2枚重ねて圧
力35kf!/d1温度140℃、時間30分の条件で
成形を行つたところ第1表のような性能の樹脂液が得ら
れた。なお、厚み精度はスペーサを用いなくても良好で
あつた。実施例 2無水マレイン酸539部、イソフタ
ル酸8301ネオペンチルグリコール208、プロピレ
ングリコール608部の配合で、実施例1と同様に2段
反応を行わせて酸価81の不飽和ポリエステルを得た。
These were used to impregnate a glass fiber mat so that the glass fiber content was 3801), and both sides were sandwiched between polypropylene films and heated at 45° C. for 48 hours to age.
At this stage, the resin liquid [C] used had an excessively high viscosity due to thickening, and could not be impregnated into the glass fiber mat. Those using resin liquids [A] and [B] were able to be sufficiently impregnated. However, the resin solution [B] did not increase in viscosity even after impregnation and did not become dry to the touch.
Glass fiber mat impregnated with resin liquid [A] resulted in SMC that was dry to the touch. Pressure is 35kf when these two SMCs are stacked! Molding was carried out under the conditions of /d1 temperature of 140° C. and time of 30 minutes, and a resin liquid having the performance as shown in Table 1 was obtained. Note that the thickness accuracy was good even without using a spacer. Example 2 A two-stage reaction was carried out in the same manner as in Example 1 using a blend of 539 parts of maleic anhydride, 8301 isophthalic acid, 208 parts of neopentyl glycol, and 608 parts of propylene glycol to obtain an unsaturated polyester with an acid value of 81.

これを用いて不飽和ポリエステル濃度が58%になるよ
うにスチレンモノマに溶解し、粘度23センチポイズ(
25℃)の樹脂液〔D〕を得た。このもののグリコール
/二塩基酸モル比は0.95であつた。なお、樹脂液〔
D〕と同配合で酸化が63になるまで反応させ、同濃度
で、粘度123センチポイズ(25℃)の樹脂液〔E〕
を得た。この樹脂液〔DLCE〕を用いて、樹脂液10
0部に対して、水和アルミナ170部、t−ブチルパー
ベンゾエート1.2部、酸化マグネシウム0.8部を混
合してスラリ状組成物とし、熱硬化性樹脂バインダで結
合したガラス繊維マツトに、ガラス繊維コンテシトが4
0%になるように含浸させた。樹脂液〔D〕の組成物は
粘度が7000センチポイズであり、上記ガラス繊維マ
ツトによく含浸した。しかし、樹脂液〔E〕の組成物は
粘度が70000センチポイズとなりガラス繊維マツト
に含浸させることができなかつた。樹脂液〔D〕を用い
た組成物のガラス繊維マツト含浸物を実施例1と同様に
加熱熟成してSMCとなした。これを2枚重ね、401
<g/C7lll38℃、30分の条件で成形した樹脂
板は表面状態は良好で、第2表に示すような性能を有し
ていた。なお、スペーサを用いなくても樹脂板の厚み精
度は良好であつた。
Using this, it was dissolved in styrene monomer so that the unsaturated polyester concentration was 58%, and the viscosity was 23 centipoise (
A resin liquid [D] was obtained at a temperature of 25°C. The glycol/diacid molar ratio of this product was 0.95. In addition, resin liquid [
Resin liquid [E] with the same concentration and viscosity of 123 centipoise (25°C) was reacted with the same formulation as [D] until the oxidation level reached 63.
I got it. Using this resin liquid [DLCE], resin liquid 10
0 parts, 170 parts of hydrated alumina, 1.2 parts of t-butyl perbenzoate, and 0.8 parts of magnesium oxide were mixed to form a slurry composition, and the slurry was mixed with glass fiber mat bonded with a thermosetting resin binder. , glass fiber content is 4
It was impregnated to a concentration of 0%. The resin liquid [D] composition had a viscosity of 7000 centipoise and was well impregnated into the glass fiber mat. However, the resin liquid [E] composition had a viscosity of 70,000 centipoise and could not be impregnated into glass fiber mat. A glass fiber mat impregnated product of the composition using the resin liquid [D] was heated and aged in the same manner as in Example 1 to obtain SMC. Stack two of these, 401
<g/C7lll The resin plate molded at 38° C. for 30 minutes had a good surface condition and had the performance shown in Table 2. Note that the thickness accuracy of the resin plate was good even without using a spacer.

実施例 3 イソフタル酸664部、エチレングリコール310部、
プロピレングリコール380部の配合で第1段反応を行
わせ、つぎにフマル酸812部を追加して第2段反応を
行わせて酸価92の不飽和ポリエステルを得た。
Example 3 664 parts of isophthalic acid, 310 parts of ethylene glycol,
The first stage reaction was carried out by adding 380 parts of propylene glycol, and then the second stage reaction was carried out by adding 812 parts of fumaric acid to obtain an unsaturated polyester having an acid value of 92.

この場合グリコール/二塩基酸のモル比は0.91であ
つた。この不飽和ポリエステルを二分し、一方を不飽和
ポリエステル分が50重量%になるようにスチレンに溶
解した粘度15センチボイズ(25スC)とした樹脂液
〔F〕とし、他方を不飽和ポリエステル分が45重量%
になるようにスチレン溶解し、粘度を8センチポイズ(
25℃)とした樹脂液〔G〕とした。以上の樹脂液を用
い、樹脂液100部、水和アルミナ200部の配合で混
合し、さらにt−ブチルパーベンゾエート1.0部、酸
化マグネシウム1.5部を添加して混合し、実施例2と
同様のガラス繊維マツトに含浸させて一体化し、2枚の
ポリプロピレンフイルムに挟んで48℃、45時間の条
件で加熱熟成して指触乾燥状態のSMCを得た。それぞ
れのガラス繊維コンテントは30重量%であつた。以上
の各SMCにつき、それぞれを2枚重ねてさらにその上
に銅箔(福田金属社製、商品名CF−TS)を重ね14
0℃、40kg/CTIIl25分の条件で成形して銅
張板を得た。
In this case the glycol/diacid molar ratio was 0.91. This unsaturated polyester was divided into two parts, one was dissolved in styrene so that the unsaturated polyester content was 50% by weight, and the resin liquid [F] had a viscosity of 15 centiboise (25 C). 45% by weight
Dissolve the styrene so that the viscosity is 8 centipoise (
Resin liquid [G] was prepared at a temperature of 25°C). Using the above resin liquid, 100 parts of the resin liquid and 200 parts of hydrated alumina were mixed, and 1.0 part of t-butyl perbenzoate and 1.5 parts of magnesium oxide were added and mixed. Example 2 The SMC was impregnated into a glass fiber mat similar to the above, and then sandwiched between two polypropylene films and heated and aged at 48° C. for 45 hours to obtain SMC that was dry to the touch. The glass fiber content of each was 30% by weight. For each of the above SMCs, two sheets of each are stacked, and then copper foil (manufactured by Fukuda Kinzoku Co., Ltd., product name CF-TS) is layered on top of that.14
A copper-clad board was obtained by molding at 0° C. and 40 kg/CTIIl for 25 minutes.

Claims (1)

【特許請求の範囲】[Claims] 1 グリコール/二塩基酸のモル比を1.06以下で反
応させて得られる不飽和ポリエステルを液状架橋剤に、
25℃における粘度が100センチポイズ以下で、かつ
液状架橋剤の濃度が50重量%以下となるように溶解し
た樹脂液100重量部に対して、水和アルミナ150重
量部以上、2価金属化合物0.4〜2.0重量部、硬化
剤0.5〜4重量部、要すれば充填剤、顔料、離型剤等
その他の添加剤を配合してなる組成物をガラス繊維基材
に含浸させ、熟成してなる樹脂組成物。
1 Unsaturated polyester obtained by reacting at a glycol/dibasic acid molar ratio of 1.06 or less as a liquid crosslinking agent,
150 parts by weight or more of hydrated alumina and 0.0 parts by weight of a divalent metal compound are added to 100 parts by weight of a resin solution dissolved so that the viscosity at 25° C. is 100 centipoise or less and the concentration of the liquid crosslinking agent is 50% by weight or less. Impregnating a glass fiber base material with a composition comprising 4 to 2.0 parts by weight, 0.5 to 4 parts by weight of a curing agent, and other additives such as fillers, pigments, and mold release agents if necessary, A resin composition obtained by aging.
JP49129344A 1974-11-09 1974-11-09 resin composition Expired JPS5912690B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49129344A JPS5912690B2 (en) 1974-11-09 1974-11-09 resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49129344A JPS5912690B2 (en) 1974-11-09 1974-11-09 resin composition

Publications (2)

Publication Number Publication Date
JPS5155364A JPS5155364A (en) 1976-05-15
JPS5912690B2 true JPS5912690B2 (en) 1984-03-24

Family

ID=15007277

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49129344A Expired JPS5912690B2 (en) 1974-11-09 1974-11-09 resin composition

Country Status (1)

Country Link
JP (1) JPS5912690B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0346734Y2 (en) * 1986-08-18 1991-10-03

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0346734Y2 (en) * 1986-08-18 1991-10-03

Also Published As

Publication number Publication date
JPS5155364A (en) 1976-05-15

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