JPS59127724A - Manufacture of laminate - Google Patents
Manufacture of laminateInfo
- Publication number
- JPS59127724A JPS59127724A JP58001477A JP147783A JPS59127724A JP S59127724 A JPS59127724 A JP S59127724A JP 58001477 A JP58001477 A JP 58001477A JP 147783 A JP147783 A JP 147783A JP S59127724 A JPS59127724 A JP S59127724A
- Authority
- JP
- Japan
- Prior art keywords
- laminate
- base material
- resin
- solvent
- phenolic
- 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
Links
Classifications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K3/00—Apparatus or processes for manufacturing printed circuits
- H05K3/02—Apparatus or processes for manufacturing printed circuits in which the conductive material is applied to the surface of the insulating support and is thereafter removed from such areas of the surface which are not intended for current conducting or shielding
- H05K3/022—Processes for manufacturing precursors of printed circuits, i.e. copper-clad substrates
Landscapes
- Reinforced Plastic Materials (AREA)
- Laminated Bodies (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
Description
【発明の詳細な説明】
不発明は無浴炸]で製造丁ゐ積層板あるいは銅張り積層
板の製造法に関す/)ものである。その目的とするとこ
ろは浴剤の不便用、グリグレグ作底の際の乾燥工程の不
用VCよる製造方法の効率化でるΦ0
従来、フェノール樹月盲積層板ヶ製造丁ゐ場合、フェス
=H造1−る除に多量の浴剤ン使用し、しかもスリグレ
グ7T:製造丁々際も一建倉塗布する為、ワニスの樹脂
分あるいは粘度に調節子ゐのf/(多量の浴剤を使用し
ていR1゜しかもこnらの浴剤は塗工工程で、外部より
熱牙加えて乾燥させ外部VC飛散させなりlしは、tb
、’rい。埃境珠全の観点からこnらの浴剤は燃焼芒せ
てから外気に放出している。このように浴剤に使用丁ゐ
ことで乾燥コスト2よび公害対米コストかかかるという
欠点r肩していた。しかも浴剤には火災の危険性ン南し
ており問題があっRO
不発明は上記欠点に改良するもので、基材f予め硬化剤
のみγ付層させておき、次いで浴剤【含1ないフェノー
ル側膚葡該基材C塗布してフリグレグ紮作成し、こn’
2所足枚数宣ねあるいにそ′t″Lvc銅箔ン厘ねて加
熱加圧成形子ゐことン%徴とする0加熱加圧成形する際
フェノール樹脂が流n出さないように凹みのある金型r
使用してもよい。DETAILED DESCRIPTION OF THE INVENTION The invention relates to a method for manufacturing laminates or copper-clad laminates without bathing. The purpose of this is to eliminate the inconvenience of bath salts, eliminate the drying process when making Grigregs, and improve the efficiency of the VC manufacturing method. - A large amount of bath agent is used, and since the coating is applied in one warehouse just before production, the resin content or viscosity of the varnish is adjusted to f/(R1゜). Moreover, in the coating process of these bath additives, heat is added from the outside to dry and external VC is scattered.
,'r. From the viewpoint of dust safety, these bath salts are burned and then released into the outside air. By using it in bath salts in this way, the disadvantages of increased drying costs and pollution costs were borne. In addition, bath additives have the problem of increasing fire hazards. Apply the base material C on the phenol side to create a frigleg ligature.
2. After determining the number of sheets, remove the Lvc copper foil and heat and press mold it. A certain mold r
May be used.
このようにすることで、溶剤を便わj“乾燥工程なし[
積層板ン製造丁ゐCと力S小米る。By doing this, the solvent is removed and there is no drying process [
Laminated board manufacturing machine C and force S Xiaomiru.
無浴剤でフェノール樹脂積層板r製造する方法としては
硬化剤と粉末状ノボ2ツク切脂r粉末で基材に与えたつ
硬化剤と樹力旨を一緒に与える方法かあ/)が02tら
の方法に成形条件の背坤巾が狭いという問題がある。本
発明は硬化剤と2工ノール側脂?分離して基材に付与丁
ゐため成形条件の管理中か広くなり製造しヤ丁いという
特長r市している。A method for manufacturing phenolic resin laminates without using bath additives is to apply a hardening agent and resin strength to the base material together with a hardening agent and powdered Nobo2tsuk resin powder. The problem with this method is that the molding conditions have a narrow range. Is the present invention a hardening agent and a 2-ethanol side fat? Because it is separated and applied to the base material, it has the advantage of being easy to manufacture and control while controlling the molding conditions.
不発明?さらに詳しく龜明する。不発明に使用する積層
板用基材に紙や本綿布蝉の天然繊維(以下余白)
布やホリアミド、ポリエステル、ポリビニルアルコール
、アクリル等の有機合成繊維布やガラス、アスベスト等
の無像繊維布あゐいはこ扛らの不織布マット等である。Uninvented? Let's take a closer look. The base materials for the laminates used in the invention include paper and cotton, natural fibers such as cicada (blank below), organic synthetic fibers such as cloth, holamide, polyester, polyvinyl alcohol, and acrylic, and non-imageable fibers such as glass and asbestos. These are non-woven mats and the like.
樹脂の基材への浸透 l性ン考えると基材か紙の
ノ易合廚度に0.3〜0.6強度が弱くなり積層数V(
L、た場合r(基拐切nヤ機械的強度の低下ケ引き起こ
丁。Considering the penetration of resin into the base material, the strength decreases by 0.3 to 0.6 depending on the degree of adhesion between the base material and paper, and the number of laminated layers V (
L, in case r (reduced cutting) causes a decrease in mechanical strength.
その他の基材はほとんど制限r受けることなく使用でき
る。ガラス繊維布、不織布、マットVC関しては表面処
理r施した基材?用いることが望ましい。Other substrates can be used with few limitations. Regarding glass fiber cloth, non-woven fabric, and matte VC, are the base materials subjected to surface treatment? It is desirable to use it.
更r(不発明V(用いる浴剤盆宮葦lいフェノール樹脂
とじては、ノボラック型フェノールホルムアルデヒド樹
脂、桐油、アマニ?’[+3寺の乾性油′とノポラック
ン反応σぜた乾性油変性ノボ2ツク樹脂あるいは必少に
応じてキシレン樹脂などの芳香族炭化水素樹脂で変性し
にノボラック型ンヱノール樹脂などかめる。ここで浴剤
2含11いとはグリプレグ製造時に樹脂の溶剤の乾燥工
程r必安としlいCと2意味丁ゐ。Furthermore, the phenolic resin used in the bath agent is a novolak-type phenol formaldehyde resin, tung oil, and linseed? Polyester resin or, if necessary, aromatic hydrocarbon resin such as xylene resin, is modified with novolak-type resin.Here, the bath agent 2 and 11 refers to the drying process of the resin solvent during the production of Gripreg. 1C and 2 meanings.
ノボラック型フェノール樹艙は通常行lゎ7しているよ
つ匠塩酸、修岐なとの酸触媒の存在下πフェノール、ク
レゾール類とホルムアルデヒドr反比、させて得らrt
、/S。フェノール類とホルり製造するのが難しい。Novolac-type phenol trees are usually obtained by inversely comparing π-phenol, cresols, and formaldehyde in the presence of acid catalysts such as Yotsutaku hydrochloric acid and Shukinato, which are carried out in the process.
,/S. Phenols are difficult to produce.
乾性油変性ノボランク樹脂は桐油あるいけアマニ油など
の乾性油と上記の方法で侍ら′nたノホラック樹脂ケバ
ラドルエンスルポン酸なとの酸触媒の存在下f(50〜
150℃で反応させ、未反応の乾性油がl(なっに時点
ケ終点としてトリエチルアミン、ジエチルアミン、ピリ
ジン等の塩基性物質で中和して、反応が加熱しても進行
しないよ′)V(丁^8こfLは塗布工程で反応が進み
、ゲル化すること2防ぐためでめゐ。キシレン樹脂など
の芳香族炭化水素樹脂で変性し女ノボラック型フェノー
ル側脂は、1丁キシレン樹脂、例えは二カノールH(三
菱瓦斯化学問品名)とフェノール、クレゾール類ケバラ
ドルエンスルホン等の敵性触媒上反応させその抜ホルム
アルデヒドケフェノール類1モルC対して0.4〜0.
85モル刀0えて反工6r疼洗竹しノボラッタ型キシレ
ン俯脂変性フェノール樹脂か得ら扛る。こnに、その1
1積層板用側廁として用いてもいいし、上述しkように
桐油等の乾性油と反応させてから用いてもよい。The drying oil-modified novolanc resin is prepared by combining a drying oil such as tung oil or linseed oil with a noholac resin obtained by the above method in the presence of an acid catalyst such as kevaradruene sulfonic acid.
The reaction is carried out at 150°C, and the unreacted drying oil is neutralized with a basic substance such as triethylamine, diethylamine, or pyridine to prevent the reaction from proceeding even if heated. ^8 This is to prevent the reaction from proceeding during the coating process and gelation.Novolak-type phenol resin modified with an aromatic hydrocarbon resin such as xylene resin can be used with a xylene resin, e.g. Dicanol H (product name of Mitsubishi Gas Chemical Co., Ltd.) is reacted with phenol, cresols, etc. over a hostile catalyst such as kevaradruene sulfone, and then the formaldehyde is removed.
An 85-mol knife was used, and a 6r-thickness was removed from the novolata-type xylene denatured phenolic resin. Today, part 1
It may be used as a side wall for a laminated board, or it may be used after reacting with a drying oil such as tung oil as described above.
更に従来の難燃性槓層叡π使わnていゐ娩燃剤r上記の
ノボラック型フェノール樹脂および変性ノボラック型フ
ェノール樹脂に混合して不発明の方法によ々難燃性!R
層板ケ製造することができろ。特にリン系の難燃剤例え
はトリフヱニルホスフエート、トリクレジルホス7z−
)、タレジルジフェニルホスフェート、キシレルジ2エ
ニルホス2エートzとはノボランク型フ工ノール樹脂の
粘度ン下けるのに効果があり、グリプレフ2作敢するの
VCs合かよい。In addition, conventional flame retardant additives are mixed with the above novolac type phenolic resin and modified novolac type phenol resin to achieve even greater flame retardancy! R
It should be possible to manufacture laminated plates. In particular, examples of phosphorus-based flame retardants include triphenyl phosphate and tricresyl phos-7z-
), talesyl diphenyl phosphate, and xylyl di-2-enyl phos-2ate z are effective in lowering the viscosity of novolank-type phenolic resins, and are suitable for use with VCs when used with Glypref 2.
でに粉体で基材f(供給するCとが可能なことから無機
化@物の難燃剤例えは三酸化アンチモンlとr使用丁ゐ
揚台従来の混練工程が省略できるの−cH造コノコスト
き下げVCC未来ある0基材π予め付N芒せゐ硬化剤と
してf”Iノホラソク型フェノール側脂の硬化剤として
用いらfLゐへキサメチレンテトラミンやトリオキザン
、レゾール型?エノールホルムアルデヒド&r 116
かあゐO
硬化剤とし又は熱的に安定で金属元素rもっていないヘ
キサメチレンテトラばンが好チしい。Since it is possible to supply the base material F (C) as a powder, the conventional kneading process can be omitted using a mineralized flame retardant such as antimony trioxide L and R. Lowered VCC future 0 base material π pre-applied as a curing agent f” I used as a curing agent for phenolic type phenol side fat fL hexamethylenetetramine, trioxane, resol type? enol formaldehyde &r 116
As a curing agent, hexamethylenetetraban, which is thermally stable and does not contain metal elements, is preferred.
硬化剤で飽加童としては後で塗布子ゐ無箔剤フェノール
樹脂100部VC対して2〜25部[72ゐよ′)に基
材に付涜させることが必倭でめゐ〇本発明のプリプレグ
の作成法の好逢しい?1lvcついて更に詳しく説明す
る01丁硬化剤の水浴液r@浸タンク方式、スグレ一方
式、キスコート方式などで光分vc基材に含浸さ一+!
:/1)01¥7.燥炉中で力DPPさせ水?蒸発させ
硬化沖jの与rか月に残留式せる。その俊該基材V(高
温(仙脂の軟化点よi、120℃〜50℃晶い温度)F
j設定した樹脂タンクからス’) −1’ f通して仙
脂r付与丁ゐその俊で熱ロールで表面に+滑げする。C
の時は、積層板の成形性r考慮して、熱ロール温度およ
びフェノール柾脂の軟化点で調節しなりnはならない。When using a curing agent, it is necessary to apply 2 to 25 parts [72 parts] per 100 parts VC of the non-foil agent phenolic resin to the base material afterwards.This invention Is there a good way to make prepreg? I will explain in more detail about 1lvc. 01 curing agent can be impregnated into the VC base material using the dipping tank method, the one-way method, the kiss coating method, etc.
:/1)01¥7. Power DPP water in a drying oven? It is allowed to evaporate and harden for several months to form a residual formula. The flexible base material V (high temperature (softening point of Senso, crystallization temperature of 120°C to 50°C) F
From the set resin tank, pass through the resin and apply resin, and then slide it onto the surface with a heated roll. C
In this case, the temperature of the hot roll and the softening point of the phenol resin must be adjusted in consideration of the formability of the laminate.
フェノール樹脂の軟化点に城形性ヶ考慮して一10°C
〜50℃か好ましい。軟化点か低いものV(に積層板の
低温打抜性に改良するためのノボラック型乾性油変性フ
ェノール樹脂がある。一方、軟化点の旨いノボラック型
フェノール便脂(軟化点50〜100℃)のもσノは、
常温で固形であるから、こn2微粉砕した粉末に硬化剤
2含んだ基材に散布丁ゐ。次いで熱ロール(軟化点以上
の尚い温度)でカロ熱してグリ7レグr作成丁ゐ。The softening point of phenolic resin is -10°C considering the castle shape.
~50°C is preferred. There are novolac-type drying oil-modified phenolic resins with low softening points (V) for improving the low-temperature punching properties of laminates. Moσノ is
Since it is solid at room temperature, this finely pulverized powder contains two hardening agents and is sprinkled on the substrate. Next, heat it with a hot roll (at a temperature above the softening point) to make 7 legs.
該グリスレフ1次足枚数厘ねて平板プレスで1’tU[
跳板に挾んで100〜15Clkg/醪の圧力1′15
0℃1時間力ロ熱丁ゐことで積層&r得ゐことか出来る
o′f、斤粉末フェノール樹脂r用いた場合、樹脂の流
n性?調節するのが難しい0jcQ、rL)IQは平板
プレスの代わりに周辺に突起のついた熱板に用いるCと
Vtよって樹脂流nが抑制できるので都合がよい。Lay down several sheets of the GrisLev primary foot and press 1'tU [
100-15 Clkg/pressure of moromi 1'15 between springboards
Lamination can be achieved by heating at 0°C for 1 hour, and when powdered phenolic resin is used, the flowability of the resin can be improved. 0jcQ, rL) IQ, which is difficult to adjust, is convenient because the resin flow n can be suppressed by using C and Vt, which are used on a hot plate with protrusions around the periphery instead of a flat plate press.
実施例1〜6
vEllliLo、6 g /cm’m重125 g
/m2であるコツトンリンター紙に’5wt%のヘキサ
メチレンテトラミン浴液ケ含浸させ乾燥させてヘキサメ
チレンテトラミン処理基材7作成しfr、(、ヘキサメ
チレンテトラミンの付m重12wt%(−As@に対し
て)であっ女ocnvc下記の台成汐りにボ丁ノボラッ
ク4111脂r粉宋散布後熔融あるいは熔融させて基材
に塗布してブリグレッツ作成したC該プリプレグに8教
皇ねて凹のめる金型に法んで成形圧力80kg/crr
P、 150℃60分間積層成形してフェノール樹脂
積層板を得た。Examples 1-6 vElliLo, 6 g/cm'm weight 125 g
A hexamethylenetetramine-treated base material 7 was prepared by impregnating 5wt% of hexamethylenetetramine bath solution on a cotton linter paper with a weight of /m2 and drying it. ) After spraying Boding Novolac 4111 powder on the table below, melt or melt it and apply it to the base material to create Brigretz. Molding pressure 80kg/crr in the mold
P. A phenol resin laminate was obtained by lamination molding at 150°C for 60 minutes.
合成例1
三ツ口の61のフラスコに2工ノール1000g、ホル
マリン560 g、蓚酸5gk加えて還流させ反応液が
乳化した後60分後から減圧上脱水濃縮して軟化点が7
0℃になっに時点で反応ン止め、金−パットに釜出しし
て冷却後ミキサーで粉砕し7.0この粉末?上記(1)
コツトンリンター紙に散布して80℃−1石ヒ加熱して
熔融させプリプレグン作成した(実施例1)側脂付層重
は77%(基材r(対して)であった。Synthesis Example 1 Into a three-necked 61 flask were added 1000 g of bispropylene, 560 g of formalin, and 5 g of oxalic acid and refluxed. After 60 minutes, the reaction solution was dehydrated and concentrated under reduced pressure to reach a softening point of 7.
Stop the reaction when the temperature reaches 0°C, take it out of the pot on a metal pad, cool it, and then crush it with a mixer.7.0 This powder? Above (1)
A prepreg gun was prepared by scattering it on cotton linter paper and heating it at 80° C. for 1 kettle to melt it (Example 1).The layer weight with side fat was 77% (relative to the base material r).
@底側2
三つ口の61のフラスコにm−p−タレゾール(m/p
比=6/4)1000g、ホルマリン525g、8%塩
酸水溶110gケ入n徐々に加熱した0反応液の発熱が
止1つ女時点で80℃1で温度r上は反応h1fjt、
けた0乳化した後60分後から減圧上脱水濃縮した。軟
化点か60℃に’fe−)た所で反応ン止め金属ノくッ
トに取り出して冷却し゛ミキサーで粉砕した002′L
k熔融して上記のコツ−トンリンター紙に塗布しに0(
実施例2)樹脂の付着量102%(基羽に対して)であ
った0
合取例6
61の三ツロフラスコに桐油200 g @ D19’
J2で@成したノボラック型フェノール街脂500g’
c入nパラトルエンスルホンm O,2g khDえて
80℃で1時間反応尽せた。反応終了後トリエチルアミ
ン’に0.2g加えて中和した。その11熔融して上記
のコツトンリンター紙に塗布した(拠施例6)樹脂の付
着量82%(基拐に対して)であった。@bottom side 2 m-p-talesol (m/p
Ratio = 6/4) 1000 g, formalin 525 g, 8% hydrochloric acid aqueous solution 110 g n Gradually heated 0 When the reaction solution stopped generating heat, it was 80℃ 1 and the temperature r was higher than the reaction h1fjt,
After 60 minutes of emulsification, the mixture was dehydrated and concentrated under reduced pressure. When the softening point reached 60°C, the 002'L was taken out into a metal knot to stop the reaction, cooled, and pulverized with a mixer.
Melt it and apply it on the above tip-ton linter paper.
Example 2) The amount of resin deposited was 102% (based on the base layer). Example 6 200 g of tung oil @ D19' was placed in a 61 Mitsuro flask.
Novolac type phenolic street fat made with J2 500g'
After adding 2 g of n-paratoluenesulfone (mO) and 2 g of khD, the reaction was completed at 80° C. for 1 hour. After the reaction was completed, 0.2 g of triethylamine was added to neutralize. No. 11 was melted and applied to the above-mentioned cotton linter paper (based on Example 6), and the adhesion amount of the resin was 82% (based on the substrate).
比較Vす1
61のフラスコにフェノール1000g、パラホルム5
10g、ホルマリン276g’K))Dえトリメチルア
ミン水浴液62gk加え70℃で反応させた160℃の
熱板上でのゲル化時…J2測足し180秒になった点を
終点とした。こrしにメタノール2刀りえa1月貸方が
48%にするよりに調整しフェスン作成しft、 0こ
のワニスに使って不実J!1i12で使用したコツトン
リンター紙に含浸させプリプレグに作成した俊、実施例
と同じ条件で加熱加圧して積層板に作成した。Comparison V1 1000 g of phenol and 5 paraform in a 61 flask
10g, formalin 276g'K)) 62gk of D-trimethylamine water bath solution was added and the reaction was carried out at 70°C. When gelling was performed on a hot plate at 160°C...J2 was added and the point at which it reached 180 seconds was taken as the end point. To do this, I adjusted the methanol 2 sword Rie a January credit to 48% and created a festoon, ft, 0 I used it for this varnish and it was dishonest J! A prepreg was made by impregnating the cotton linter paper used in 1i12, and a laminate was made by heating and pressing under the same conditions as in the example.
側脂付層員は85%(基材に対して)T″あった0 次f(傅ら′nk積層板の付性に表1に示す。The side fat layer was 85% (relative to the base material) T″0. The properties of the laminate are shown in Table 1 below.
表1 積層板の特性
*I Jr’s−c 6481に準Uて11JM
L*、。Table 1 Characteristics of laminate *I 11JM based on Jr's-c 6481
L*,.
実施例と比較例を比べると特性的V(はほとんど変化が
ない0即ち実施例のように無溶剤型σ)ノボランク型2
□ノールホルムアルデヒド樹脂に用いても従来から使わ
tているレゾール型フェノール駕脂r用いたのと同じ特
性τだ丁ことができる。従って不発明によ々方法か浴剤
r筐わない点、乾燥工程に必蒙kLn一点でコスト的に
人@な効果がある。Comparing Examples and Comparative Examples, characteristic V (has almost no change, 0, i.e., solvent-free type σ as in Example), Novolank type 2
□ Even when used in norformaldehyde resin, it can have the same characteristics as the conventionally used resol type phenol resin. Therefore, there is no need for an inventive method or bath additives, and the drying process is only required, which has a cost-effective effect.
Claims (1)
で溶剤に宮丑ないフェノール樹脂ン該基材に塗布してプ
リプレフッ詐取し、こn2)9r足aNねあるいはそn
に飼司箔牙■ねて刀1熱加圧して成形丁ゐこと’t’V
j激と丁ゐ2エノ−7し拉1月買槓層叛の製造法。 2、基材が紙であることr%徴とする特許請求範囲第1
項記載の積層板の製造法。 3、硬化剤がヘキサメチレンテトラミンで、64ことケ
特徴と丁ゐ%許請求第1項記載の積層板の製造法。 4、浴剤を含11い熱硬化性樹脂が乾性油変性ノボラッ
ク型フェノールホルムアルデヒド樹脂″′Cあることr
%徴とする特許請求範囲絹1項記載の積層板の製造法。[Scope of Claims] 1. A layer of curing agent is applied to the base material for the laminate in advance, and then a phenolic resin containing a solvent is applied to the base material to remove the pre-pre-fluid. aNne or son
Nikaishi Hakuga■ Lay down the sword 1 and mold it by heat and pressure. Also known as 't'V
The manufacturing method for the 2nd and 7th generation of the 1st month purchase. 2. Claim 1, which states that the base material is paper
Method for manufacturing the laminate described in Section 1. 3. The method for producing a laminate according to claim 1, wherein the curing agent is hexamethylenetetramine, and 64%. 4. The thermosetting resin containing the bath agent is a drying oil-modified novolak type phenol formaldehyde resin''C.
1. A method for producing a laminate according to claim 1, in which the percentage is expressed as silk.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58001477A JPS59127724A (en) | 1983-01-07 | 1983-01-07 | Manufacture of laminate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58001477A JPS59127724A (en) | 1983-01-07 | 1983-01-07 | Manufacture of laminate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59127724A true JPS59127724A (en) | 1984-07-23 |
Family
ID=11502528
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58001477A Pending JPS59127724A (en) | 1983-01-07 | 1983-01-07 | Manufacture of laminate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59127724A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573524A (en) * | 1978-11-30 | 1980-06-03 | Dainippon Ink & Chem Inc | Production of reinforced plastic |
JPS57176121A (en) * | 1981-04-23 | 1982-10-29 | Nippon Gakki Seizo Kk | Molding of frp |
-
1983
- 1983-01-07 JP JP58001477A patent/JPS59127724A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573524A (en) * | 1978-11-30 | 1980-06-03 | Dainippon Ink & Chem Inc | Production of reinforced plastic |
JPS57176121A (en) * | 1981-04-23 | 1982-10-29 | Nippon Gakki Seizo Kk | Molding of frp |
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