JPS6234775B2 - - Google Patents
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- Publication number
- JPS6234775B2 JPS6234775B2 JP53153662A JP15366278A JPS6234775B2 JP S6234775 B2 JPS6234775 B2 JP S6234775B2 JP 53153662 A JP53153662 A JP 53153662A JP 15366278 A JP15366278 A JP 15366278A JP S6234775 B2 JPS6234775 B2 JP S6234775B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- prepreg
- diallyl phthalate
- moles
- 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
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Description
【発明の詳細な説明】
本発明は複合材料の物性を低下させることなく
プリプレグのタツクを調整でき且つ一方向プリプ
レグの貯蔵中における割れ目の発生を防止できる
ところの樹脂組成物、及びこの樹脂組成物を含浸
してなる炭素繊維プリプレグ、並びにその製造方
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a resin composition that can adjust the tack of prepreg without reducing the physical properties of the composite material and can prevent the occurrence of cracks during storage of unidirectional prepreg, and this resin composition. The present invention relates to a carbon fiber prepreg impregnated with carbon fiber prepreg and a method for manufacturing the same.
炭素繊維は合成樹脂との複合材料用強化材とし
て優れたものであることが知られ、その一成形方
法として未硬化樹脂を含浸させたいわゆるプリプ
レグを経て成形硬化し製品とする方法がある。 Carbon fiber is known to be excellent as a reinforcing material for composite materials with synthetic resins, and one molding method is to form a so-called prepreg impregnated with uncured resin and then mold and harden it into a product.
この炭素繊維のプリプレグは炭素繊維との接着
力及びマトリツクスの安定性からくるプリプレグ
の保存性の面から主としてエポキシ樹脂を主体と
するものが使用されてきた。 This carbon fiber prepreg has mainly been made of epoxy resin from the viewpoint of the preservability of the prepreg due to its adhesive strength with carbon fibers and the stability of the matrix.
又本発明者らは先に速硬化性および不飽和ポリ
エステル樹脂をマトリツクスとしたガラス繊維複
合材料とのハイブリツド化が可能等不飽和ポリエ
ステル樹脂をマトリツクスとする炭素繊維プリプ
レグの有効性に鑑み不飽和ポリエステル樹脂をマ
トリツクスとする炭素繊維プリプレグをホツトメ
ルト法により製造する方法を開発した。即ちその
構成単位がイソフタール酸20〜60モル、フマール
酸80〜40モル、プロピレングリコール100モルか
らなる不飽和ポリエステルプレポリマーとジアリ
ルフタレート又はジアセトンアクリルアミド10〜
50重量%及び硬化触媒からなる樹脂組成物を用い
て優れた複合材料物性を有する炭素繊維プリプレ
グをホツトメルト法によつてつくるものである。 In addition, the present inventors have previously discovered the effectiveness of carbon fiber prepregs having an unsaturated polyester resin matrix, which are fast-curing and capable of being hybridized with glass fiber composite materials having an unsaturated polyester resin matrix. We have developed a method for producing carbon fiber prepreg using a resin matrix using the hot melt method. That is, an unsaturated polyester prepolymer whose constituent units are 20 to 60 moles of isophthalic acid, 80 to 40 moles of fumaric acid, and 100 moles of propylene glycol, and 10 to 10 moles of diallylphthalate or diacetone acrylamide.
A carbon fiber prepreg having excellent composite material properties is produced by a hot melt method using a resin composition consisting of 50% by weight and a curing catalyst.
一方プリプレグに要求される品質としては複合
材料物性が優れていることはもちろんであるが作
業性、取扱い性の点からタツクも重要な品質の一
つである。同一の不飽和ポリエステルプレポリマ
ーを用いた場合タツクの調整は架橋用モノマーの
量によつて行なわざるを得ない。 On the other hand, as for the quality required for prepreg, it goes without saying that the physical properties of the composite material are excellent, but one of the important qualities is tack from the viewpoint of workability and handling. When using the same unsaturated polyester prepolymer, the tack must be adjusted by adjusting the amount of crosslinking monomer.
しかしこの場合架橋用モノマーの量を変えるこ
とによつて複合材料物性を犠牲にしたりまたプリ
プレグのタツクを弱くしようとすればジアリルフ
タレートモノマーの量を減らすことになり必然的
に溶融粘度が上昇しホツトメルト法によるプリプ
レグ製造の場合樹脂の混練、炭素繊維への樹脂含
浸が困難となるなどの欠点を有している。 However, in this case, if the physical properties of the composite material are sacrificed or the tack of the prepreg is weakened by changing the amount of crosslinking monomer, the amount of diallyl phthalate monomer will be reduced, which will inevitably increase the melt viscosity and cause the hot melt to deteriorate. Prepreg production by this method has drawbacks such as difficulty in kneading the resin and impregnating carbon fibers with the resin.
従つて樹脂混合物の溶融粘度を上げずにタツク
を弱めることができ且つ複合材料物性の低下をき
たさない手段があればホツトメルト法による不飽
和ポリエステル樹脂をマトリツクスとする炭素繊
維プリプレグにとつて極めて有効である。さらに
また不飽和ポリエステル樹脂をマトリツクスとす
る一方向のシート状炭素繊維プリプレグはエポキ
シ樹脂系プリプレグに比較しその貯蔵中に割れ目
が発生しやすく品質上問題となる場合が多かつ
た。 Therefore, if there were a means to weaken the tack without increasing the melt viscosity of the resin mixture and without deteriorating the physical properties of the composite material, it would be extremely effective for carbon fiber prepregs using unsaturated polyester resin as a matrix by hot melting. be. Furthermore, unidirectional sheet-like carbon fiber prepregs using unsaturated polyester resin as a matrix are more likely to crack during storage than epoxy resin prepregs, which often poses quality problems.
本発明者らは鋭意検討の結果ジアリルフタレー
トのプレポリマーを加えることによつて複合材料
物性を低下させずにタツクを弱めることができ且
つホツトメルト法によつて製造可能であり、しか
も驚くべきことに一方向プリプレグの場合、貯蔵
品の割れ目の発生が著しく減少することを見い出
し本発明に到達した。 As a result of intensive studies, the present inventors found that by adding a prepolymer of diallyl phthalate, it was possible to weaken the tack without reducing the physical properties of the composite material, and it was possible to manufacture the composite material by the hot melt method. The inventors have discovered that the occurrence of cracks in stored products is significantly reduced in the case of unidirectional prepreg, and have arrived at the present invention.
即ち二塩基酸成分としてイソフタール酸20〜60
モルとエチレン性不飽和二塩基酸としてフマール
酸80〜40モル、グリコール成分としてプロピレン
グリコール100モルとからなる固体の不飽和ポリ
エステルプレポリマー100重量部と15〜30重量部
のジアリルフタレート、3〜15重量部のジアリル
フタレートプレポリマーを用いることによりホツ
トメルト法によるプリプレグ製造工程に支障をき
たさずまた複合材料物性を低下させることなくプ
リプレグのタツクを弱め且つ一方向プリプレグの
貯蔵中の割れ目の発生を防止することができるこ
とを見出した。 That is, isophthalic acid 20 to 60 as the dibasic acid component.
100 parts by weight of a solid unsaturated polyester prepolymer consisting of 80 to 40 moles of fumaric acid as ethylenically unsaturated dibasic acid and 100 moles of propylene glycol as the glycol component and 15 to 30 parts by weight of diallyl phthalate, 3 to 15 By using parts by weight of diallyl phthalate prepolymer, the tack of the prepreg is weakened without interfering with the prepreg manufacturing process by the hot melt method or deteriorating the physical properties of the composite material, and the occurrence of cracks during storage of the unidirectional prepreg can be prevented. I found out that it is possible.
ジアリルフタレートモノマーの添加量を減らし
てプリプレグのタツクを弱めようとすれば前述し
た如く物性の低下とホツトメルト方式によるプリ
プレグ製造上のトラブルが避けられないのに対し
ジアリルフタレートプレポリマーを添加すること
により複合材料物性が低下せず且つホツトメルト
法によるプリプレグ製造上も問題なくプリプレグ
のタツクを弱めることができるのである。ここで
用いるジアリルフタレートプレポリマーとはジア
リルフタレートモノマーを初期重合して得られる
ところの分子内に重合し得る二重結合をもつた比
較的線状の重合物で熱可塑性を有するものであ
り、また本発明の目的のためには軟化点が15〜70
℃、特に20〜60℃のものが好ましい。軟化点が15
℃以下ではタツクを弱める効果が小さくまた70℃
以上のものは樹脂の溶融粘度が上昇してプリプレ
グ製造工程上樹脂の混練や炭素繊維への樹脂の含
浸が困難となり好ましくない。 If we try to weaken the toughness of the prepreg by reducing the amount of diallyl phthalate monomer added, the deterioration of physical properties and troubles in producing prepreg using the hot melt method will be unavoidable, as described above, but by adding diallyl phthalate prepolymer, The tack of the prepreg can be weakened without deteriorating the physical properties of the material and without causing any problems in producing the prepreg by the hot melt method. The diallyl phthalate prepolymer used here is a relatively linear polymer having polymerizable double bonds in the molecule obtained by initial polymerization of diallyl phthalate monomers, and is thermoplastic. For the purposes of this invention, the softening point is between 15 and 70.
℃, especially preferably 20 to 60℃. Softening point is 15
The effect of weakening the tack is small below 70℃.
The above materials are not preferred because the melt viscosity of the resin increases, making it difficult to knead the resin and impregnate carbon fibers with the resin during the prepreg manufacturing process.
ジアリルフタレートモノマー量は本発明に用い
る不飽和ポリエステル樹脂プレポリマー100重量
部に対し15重量部以下では樹脂の溶融粘度が高く
ホツトメルト法によるプリプレグ製造が困難とな
るばかりでなく複合材料物性が低下して好ましく
ない。また30重量部以上ではプリプレグのタツク
が強すぎもはやジアリルフタレートプレポリマー
を加えても希望するタツクに弱めることができな
くなる。 If the amount of diallyl phthalate monomer is less than 15 parts by weight per 100 parts by weight of the unsaturated polyester resin prepolymer used in the present invention, the melt viscosity of the resin will be high, not only making it difficult to produce prepreg by the hot melt method, but also decreasing the physical properties of the composite material. Undesirable. Moreover, if it exceeds 30 parts by weight, the tack of the prepreg will be too strong and it will no longer be possible to weaken it to the desired tack even by adding diallyl phthalate prepolymer.
ジアリルフタレートプレポリマーの添加量は3
〜15重量部が適当である。3重量部以下ではタツ
クを弱め且つプリプレグの割れ目発生の防止効果
が小さく、15重量部以上ではプリプレグのタツク
が弱まりすぎるだけでなくホツトメルト式プリプ
レグ製造上炭素繊維への樹脂含浸が困難となる。 The amount of diallyl phthalate prepolymer added is 3
~15 parts by weight is suitable. If it is less than 3 parts by weight, the effect of weakening the tack and preventing the occurrence of cracks in the prepreg is small, and if it is more than 15 parts by weight, not only the tack of the prepreg becomes too weak, but also it becomes difficult to impregnate carbon fiber with resin in hot melt prepreg production.
本発明の範囲でジアリルフタレートプレポリマ
ーを加えても本発明不飽和ポリエステル樹脂マト
リツクスを炭素繊維との接着力は全く変化なく層
間せん断強度(ILSS)は9Kg/mm2以上示すとい
う事実とあいまつて本発明樹脂組成物は不飽和ポ
リエステル樹脂をマトリツクスとする炭素繊維プ
リプレグの品質向上と商品価値を著しく高めその
意義は極めて大きいものである。 Coupled with the fact that even if diallyl phthalate prepolymer is added within the scope of the present invention, the adhesion strength of the unsaturated polyester resin matrix of the present invention to carbon fibers does not change at all, and the interlaminar shear strength (ILSS) shows 9 kg/mm 2 or more. The resin composition of the invention is of great significance as it significantly improves the quality and commercial value of carbon fiber prepregs using unsaturated polyester resin as a matrix.
次に本発明プリプレグの製造法について説明す
る。 Next, a method for manufacturing the prepreg of the present invention will be explained.
所定量の不飽和ポリエステルプレポリマー、ジ
アリルフタレート、ジアリルフタレートプレポリ
マーをニーダーにて70〜110℃の温度で溶解混練
する。該樹脂混合物を3本ロールミルにて所定量
の硬化触媒と混練し次いでフイルムコーターにて
離型紙上にフイルム状にコーテイングする。この
樹脂をコーテイングした離型紙上に炭素繊維集合
体を配し、さらにその上に離型紙を導入して80〜
140℃に加熱された加熱板を通した後60〜160℃に
加熱されたホツトローラーにて0.1〜100Kg/cmの
線圧で加圧して炭素繊維を押し広げてシート状に
すると同時に炭素繊維に樹脂を含浸させる。炭素
繊維集合体としては一方向又はランダムウエブ等
任意の形態で利用できる。 A predetermined amount of unsaturated polyester prepolymer, diallyl phthalate, and diallyl phthalate prepolymer are melt-kneaded in a kneader at a temperature of 70 to 110°C. The resin mixture is kneaded with a predetermined amount of curing catalyst using a three-roll mill, and then coated onto a release paper in the form of a film using a film coater. Carbon fiber aggregates are placed on the release paper coated with this resin, and the release paper is further introduced on top of the release paper.
After passing through a heating plate heated to 140°C, the carbon fibers are pressed with a linear pressure of 0.1 to 100 kg/cm using a hot roller heated to 60 to 160°C to spread them out and form them into a sheet. Impregnate with resin. The carbon fiber aggregate can be used in any form such as unidirectional or random web.
硬化触媒はt−ブチルパーオキシベンゾエート
の如く定温で安定で高温で分解速度の大きいもの
が好ましい。 The curing catalyst is preferably one that is stable at a constant temperature and has a high decomposition rate at high temperatures, such as t-butyl peroxybenzoate.
以下実施例によつて説明する。 This will be explained below using examples.
実施例 1
イソフタール酸40モル、フマール酸60モル、プ
ロピレングリコール100モルよりなる固体の不飽
和ポリエステルプレポリマー(武田薬品工業製ポ
リマールX381)100重量部と23重量部のジアリル
フタレートモノマー、および8重量部のジアリル
フタレートプレポリマー(大阪曹達製ダイソーダ
ツプL、軟化点40℃)をニーダーにて90℃で混練
均一化しさらにこれをロールミル上に移してt−
ブチルパーオキシベンゾエート6重量部と混練し
た。該樹脂組成物をフイルムコーターにて離型紙
上にコーテイングしこの上に炭素繊維(東邦ベス
ロン製ベスフアイト7−6K)を一方向に且つ等
間隔に導入し、さらにその上に離型紙を導入して
120℃に加熱された加熱板上を30秒間通す。さら
に130℃に加熱されたホツトローラーに30Kg/cm
の線圧で加圧して炭素繊維に押し広げてシート状
にすると同時に炭素繊維に樹脂を含浸させて一方
向のシート状プリプレグを製造した。Example 1 100 parts by weight of a solid unsaturated polyester prepolymer (Polymer X381 manufactured by Takeda Pharmaceutical Co., Ltd.) consisting of 40 moles of isophthalic acid, 60 moles of fumaric acid, and 100 moles of propylene glycol, 23 parts by weight of diallyl phthalate monomer, and 8 parts by weight Diaryl phthalate prepolymer (Daiso Tap L manufactured by Osaka Soda, softening point 40°C) was homogenized by kneading at 90°C in a kneader, and then transferred to a roll mill to make a t-
The mixture was kneaded with 6 parts by weight of butyl peroxybenzoate. The resin composition was coated on a release paper using a film coater, carbon fibers (Beshuite 7-6K manufactured by Toho Veslon) were introduced in one direction and at equal intervals, and a release paper was further introduced on top of this.
Pass it over a heating plate heated to 120°C for 30 seconds. Furthermore, 30Kg/cm is placed on a hot roller heated to 130℃.
A unidirectional sheet-like prepreg was manufactured by pressing the carbon fibers with a linear pressure of 100 mL to form a sheet, and at the same time impregnating the carbon fibers with a resin.
このプリプレグは25℃で互いに貼り合わせても
簡単にはがれる程度にタツクが弱くまた室温に数
日間放置しても割れ目の発生はほとんどなかつ
た。またこのプリプレグを一方向に積層し150℃
で30分、7Kg/cm2の硬化条件で成形した成形物の
物性は次の如くであつた。 This prepreg had such a weak tack that it could be easily peeled off even when attached to each other at 25°C, and almost no cracking occurred even when left at room temperature for several days. In addition, this prepreg is laminated in one direction and heated to 150°C.
The physical properties of the molded product molded under curing conditions of 7 kg/cm 2 for 30 minutes were as follows.
曲げ強度 162Kg/mm2
曲げ弾性率 12.9T/mm2
層間せん断強度(ILSS) 9.2Kg/mm2
繊維体積含有率(V) 60%
比較例 1
イソフタール酸40モル、フマール酸60モル、プ
ロピレングリコール100モルよりなる固体の不飽
和ポリエステルプレポリマー(武田薬品工業製ポ
リマールX381)100重量部と18重量部のジアリル
フタレートモノマーおよび6重量部のt−ブチル
パーオキシベンゾエートを用いて実施例1と同様
にして一方向の炭素繊維プリプレグを製造したが
実施例1に比較し樹脂組成物の溶融粘度が高く樹
脂の混練および炭素繊維への樹脂含浸が困難であ
つた。又得られたプリプレグのタツクは実施例1
と同等に弱かつたが、室温に1日放置すると割れ
目が多数発生した。このプリプレグを一方向に積
層し実施例1と同一条件で成形した成形物の物性
は次の如くであつた。 Bending strength 162Kg/mm 2 Flexural modulus 12.9T / mm Interlaminar shear strength (ILSS) 9.2Kg/mm 2 Fiber volume content (V) 60% Comparative example 1 Isophthalic acid 40 mol, fumaric acid 60 mol, propylene glycol 100 Example 1 was repeated using 100 parts by weight of a solid unsaturated polyester prepolymer (Polymer X381, manufactured by Takeda Pharmaceutical Co., Ltd.), 18 parts by weight of diallyl phthalate monomer and 6 parts by weight of t-butyl peroxybenzoate. Although a unidirectional carbon fiber prepreg was produced, the melt viscosity of the resin composition was higher than in Example 1, making it difficult to knead the resin and impregnate the carbon fibers with the resin. Moreover, the tack of the obtained prepreg is as shown in Example 1.
However, many cracks appeared when left at room temperature for one day. This prepreg was laminated in one direction and molded under the same conditions as in Example 1. The properties of the molded product were as follows.
曲げ強度 159Kg/mm2 曲げ弾性率 13.0T/mm2 ILSS 8.3Kg/mm2 V 60% 実施例1に比較しILSSが低下している。 Bending strength 159Kg/mm 2 Bending modulus 13.0T/mm 2 ILSS 8.3Kg/mm 2 V 60% Compared to Example 1, ILSS is lower.
Claims (1)
40モルとプロピレングリコール100モルとからな
る固体の不飽和ポリエステルプレポリマー100重
量部と、ジアリルフタレート15〜30重量部、ジア
リルフタレートプレポリマー3〜15重量部及び硬
化触媒とからなる樹脂組成物。 2 イソフタール酸20〜60モル、フマール酸80〜
40モルとプロピレングリコール100モルとからな
る固体の不飽和ポリエステルプレポリマー100重
量部と、ジアリルフタレート15〜30重量部、ジア
リルフタレートプレポリマー3〜15重量部及び硬
化触媒とからなる樹脂組成物を含浸してなる炭素
繊維プリプレグ。 3 イソフタール酸20〜60モル、フマール酸80〜
40モルとプロピレングリコール100モルとからな
る固体の不飽和ポリエステルプレポリマー100重
量部と、ジアリルフタレート15〜30重量部、ジア
リルフタレートプレポリマー3〜15重量部及び硬
化触媒とからなる樹脂組成物を離型紙上に展延し
てフイルム状となし、この上に炭素繊維集合体を
配し、60〜160℃にて加熱圧着して当該樹脂組成
物を炭素繊維集合体に含浸させることを特徴とす
る不飽和ポリエステルをマトリツクスとする炭素
繊維プリプレグの製造方法。[Claims] 1. 20 to 60 mol of isophthalic acid, 80 to 60 mol of fumaric acid
A resin composition comprising 100 parts by weight of a solid unsaturated polyester prepolymer consisting of 40 moles of polypropylene glycol and 100 moles of propylene glycol, 15 to 30 parts by weight of diallyl phthalate, 3 to 15 parts by weight of diallyl phthalate prepolymer, and a curing catalyst. 2 Isophthalic acid 20~60mol, fumaric acid 80~
Impregnated with a resin composition consisting of 100 parts by weight of a solid unsaturated polyester prepolymer consisting of 40 moles and 100 moles of propylene glycol, 15 to 30 parts by weight of diallyl phthalate, 3 to 15 parts by weight of diallyl phthalate prepolymer, and a curing catalyst. Carbon fiber prepreg. 3 Isophthalic acid 20~60mol, fumaric acid 80~
A resin composition consisting of 100 parts by weight of a solid unsaturated polyester prepolymer consisting of 40 moles and 100 moles of propylene glycol, 15 to 30 parts by weight of diallyl phthalate, 3 to 15 parts by weight of diallyl phthalate prepolymer, and a curing catalyst is separated. It is characterized in that it is spread on a paper pattern to form a film, a carbon fiber aggregate is placed on top of this, and the resin composition is impregnated into the carbon fiber aggregate by heat-pressing at 60 to 160°C. A method for producing carbon fiber prepreg using unsaturated polyester as a matrix.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15366278A JPS5580531A (en) | 1978-12-14 | 1978-12-14 | Carbon fiber prepreg and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15366278A JPS5580531A (en) | 1978-12-14 | 1978-12-14 | Carbon fiber prepreg and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5580531A JPS5580531A (en) | 1980-06-17 |
| JPS6234775B2 true JPS6234775B2 (en) | 1987-07-29 |
Family
ID=15567432
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15366278A Granted JPS5580531A (en) | 1978-12-14 | 1978-12-14 | Carbon fiber prepreg and method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5580531A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6117551A (en) * | 1996-12-18 | 2000-09-12 | Toray Industries, Inc. | Carbon fiber prepreg, and a production process thereof |
| WO2025113789A1 (en) * | 2023-11-29 | 2025-06-05 | Ithaka Institute For Carbon Strategies | Prepreg, prepreg body and a method to produce a prepreg |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1260409A (en) * | 1969-03-10 | 1972-01-19 | Sec Dep For Defence Formerly M | Carbon fibre reinforced resin plastics sheet |
| JPS4921492A (en) * | 1972-06-19 | 1974-02-25 | ||
| JPS5569612A (en) * | 1978-11-16 | 1980-05-26 | Toray Ind Inc | Resin composition for fiber-reinforcement |
-
1978
- 1978-12-14 JP JP15366278A patent/JPS5580531A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5580531A (en) | 1980-06-17 |
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