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JPS6042566B2 - Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates - Google Patents
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JPS6042566B2 - Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates - Google Patents

Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates

Info

Publication number
JPS6042566B2
JPS6042566B2 JP53077668A JP7766878A JPS6042566B2 JP S6042566 B2 JPS6042566 B2 JP S6042566B2 JP 53077668 A JP53077668 A JP 53077668A JP 7766878 A JP7766878 A JP 7766878A JP S6042566 B2 JPS6042566 B2 JP S6042566B2
Authority
JP
Japan
Prior art keywords
continuously
laminate
metal foil
impregnated
coated
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
JP53077668A
Other languages
Japanese (ja)
Other versions
JPS554838A (en
Inventor
正征 大泉
正名 後藤
実 一色
八洲男 伏木
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP53077668A priority Critical patent/JPS6042566B2/en
Publication of JPS554838A publication Critical patent/JPS554838A/en
Publication of JPS6042566B2 publication Critical patent/JPS6042566B2/en
Expired legal-status Critical Current

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  • Laminated Bodies (AREA)
  • Insulating Bodies (AREA)

Description

【発明の詳細な説明】 本発明は電気用積層板または金属箔張り積層板の新規
な製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for manufacturing electrical laminates or metal foil laminates.

従来、電気部品用あるいは電子部品用積層絶縁板、あ
るいは印刷回路板用金属箔張り積層板は、主にフェノー
ル樹脂と紙を基材として製造されている。
Conventionally, laminated insulating boards for electrical or electronic parts, or metal foil-clad laminates for printed circuit boards have been manufactured mainly using phenolic resin and paper as base materials.

この従来品は、溶剤によつて常温で液体とした樹脂ワニ
スを紙に含浸し、溶剤を乾燥していわゆるBステージと
なし常温で粘着性を有しないプリプレグを形成し、しか
る後切断積層し、加熱加圧ブレスによつて製造されてい
る。かかる従来法においては、近年生産性や製品コスト
が限界に達し、より生産性の高い新規な製造方法が期待
されているのが実情である。従来品の中にはエポキシ樹
脂と紙を基材としたものがあるが、これも上記従来法を
踏襲するものであ、また常温で固体であるような不飽和
ポリエステルと溶剤からなる樹脂ワニスを用いる提案も
なされているが、これも前記従来法を前提としたもので
ありコスト高等から実用化されていない。
This conventional product impregnates paper with a resin varnish made liquid at room temperature by using a solvent, then dries the solvent to form a so-called B stage, which forms a prepreg that does not have adhesiveness at room temperature, and then cuts and laminates the paper. Manufactured using a heated and pressurized press. The reality is that the productivity and product cost of such conventional methods have reached their limits in recent years, and new manufacturing methods with higher productivity are expected. Some conventional products are based on epoxy resin and paper, but this also follows the above conventional method, and also uses a resin varnish made of unsaturated polyester, which is solid at room temperature, and a solvent. Although some proposals have been made to use this method, this method is also based on the above-mentioned conventional method and has not been put into practical use due to the high cost.

また、特開昭52−103(社)号公報には印刷回路板
の一種の連続的製造方法が開示されている。この方法は
進行方向に向かつて幅が狭くなつて行く開口を有するダ
イスを通し、樹脂液含浸基材と被覆物との複合体を引き
抜き、同時にダイスを通過する複合体を加熱て成形硬化
する方法であるが、複合体がダイス内部を通過する際の
抵抗に打ち勝つて複合体を引き抜き成形するものである
から、基材はそのための大きな張力に耐えられるもの、
例えばガラスクロス等に自ら限定される。加えて、複合
体はその成形時単一方向へ強力に引つ張られるため、製
品積層板は方向性を帯び、極めて高い均質性が要求され
る印刷回路基板や絶縁板等に使用される電気用積層板に
は向かないので、未だ工業的に実用化されていない。本
発明者はかかる現状に鑑み、鋭意研究を行つた結果架橋
用モノマーが例えばスチレンのごとき室温において液状
である不飽和ポリエステル樹脂を、なんらの溶剤を用い
るとなく直接基材に連続的に含浸し、そのまま積層し、
続いて硬化することによつて性状に優れた電気用絶縁板
また金属箔張り積層板を効率的に製造できることを見い
出し、本発明に到達した。
Furthermore, Japanese Patent Laid-Open No. 103/1983 discloses a type of continuous manufacturing method for printed circuit boards. In this method, a composite of a resin liquid-impregnated base material and a coating is pulled out through a die having an opening that becomes narrower in the direction of travel, and at the same time the composite passing through the die is heated to form and harden. However, since the composite is pultruded and molded by overcoming the resistance when the composite passes through the inside of the die, the base material must be able to withstand the large tension required for this purpose.
For example, it is limited to glass cloth. In addition, because the composite is strongly pulled in a single direction during molding, the product laminate becomes directional, making it ideal for electrical applications such as printed circuit boards and insulating boards that require extremely high homogeneity. It is not suitable for industrial laminates, so it has not yet been put into practical use industrially. In view of the current situation, the inventors of the present invention conducted intensive research and found that the crosslinking monomer, for example, styrene, is a liquid unsaturated polyester resin that is liquid at room temperature, and is directly impregnated into the base material without using any solvent. , stack them as is,
It was discovered that electrical insulating plates or metal foil-clad laminates with excellent properties could be efficiently produced by subsequent curing, and the present invention was achieved.

本発明は、架橋用ビニルモノマーを含み、揮発性副生成
物を生成することなく硬化し得る常温で液状の不飽和ポ
リエステル樹脂液を並行して連続的に供給される複数枚
の基材に対し個別に連続的に含浸させ、該含浸基材を連
続的に積層し、該積層体の両面にフィルム状空気遮断体
および/または金属箔を連続的に被覆し、その状態で該
積層体を連続的に実質無圧の状態で、少なくとも切断可
能な状態まで硬化することを特徴とする電気用積層絶縁
板または金属箔張り積層板を連続的に製造する方法を要
旨とす。
The present invention is applied to a plurality of substrates to which an unsaturated polyester resin solution containing a crosslinking vinyl monomer and which is liquid at room temperature and can be cured without producing volatile by-products is continuously supplied in parallel. The impregnated base materials are continuously impregnated individually, the impregnated base materials are continuously laminated, both sides of the laminate are continuously coated with a film air barrier and/or metal foil, and the laminate is continuously impregnated in this state. The gist of the present invention is a method for continuously manufacturing an electrical laminated insulating plate or a metal foil-clad laminated plate, which is characterized by being cured to a state where it can be cut at least under substantially no pressure.

第1図に本発明の代表的な実施形態を示す工程説明図を
示してある。
FIG. 1 is a process explanatory diagram showing a typical embodiment of the present invention.

n個のリール1−1〜1−nから巻き出されたn枚の長
尺なセルロース繊維紙10−1〜10−n必要に応じて
乾燥器2を通り乾燥される。
N sheets of long cellulose fiber paper 10-1 to 10-n unwound from n reels 1-1 to 1-n are dried by passing through a dryer 2 as necessary.

紙に含まれる必要以上の吸着水は電気用積層絶縁板や金
属箔張り積層板に要求される高い耐熱性、たとえば26
0℃×6囲2、あるいは200℃×3紛等の条件下にお
いて、しばしば、゛ふくれ゛を発生せしめ望ましくない
。大気中に貯蔵された紙はたとえば110℃×1紛の如
き乾燥条件で乾燥状態とするのでが望ましく、“ふくれ
゛を発生させない条件で乾燥させねばならない。紙は1
枚ごとに分離され、樹脂液供給装置5によつて樹脂液1
1が片面より含浸される。
The excess adsorbed water contained in the paper will reduce the high heat resistance required for electrical laminated insulating boards and metal foil laminates, such as 26
Under conditions such as 0°C x 6x2 or 200°C x 3x, ``swelling'' often occurs, which is undesirable. It is preferable that paper stored in the atmosphere be dried under dry conditions such as 110°C x 1 powder, and must be dried under conditions that do not cause blistering.
The resin liquid 1 is separated into sheets by the resin liquid supply device 5.
1 is impregnated from one side.

ここにおいて、良好な含浸及び含浸速度を達成するため
には、樹脂液の粘度と紙の密度を適度に選択することが
重要である。一般に樹脂液の粘度が小さい程、含浸性は
高まり、樹脂液における液状モノマーの比率の増大、あ
るいは不飽和ポリエステル鎖の分子量の減少によつて粘
度を低下できるが、必要以上の粘度の低下は本発明にお
いては得られる製品の耐熱性や機械的特性を阻害し好ま
しくない。密度の小さい紙を使用することも含浸性を高
めるが、必要以上の密度の低下は製品の機拡的特性や加
工性を阻害する。本発明においては、樹脂液の25℃に
おける粘度が0.5〜15ポイズであつて、紙の密度が
0.3〜0.7g/dである時望ましい結果を得る。
Here, in order to achieve good impregnation and impregnation speed, it is important to appropriately select the viscosity of the resin liquid and the density of the paper. In general, the lower the viscosity of the resin liquid, the higher the impregnating property, and the viscosity can be lowered by increasing the proportion of liquid monomer in the resin liquid or decreasing the molecular weight of the unsaturated polyester chain, but it is important to avoid lowering the viscosity more than necessary. In the invention, it is undesirable because it impairs the heat resistance and mechanical properties of the resulting product. Using paper with a low density also improves impregnability, but lowering the density more than necessary impedes the product's expandability and processability. In the present invention, desirable results are obtained when the viscosity of the resin liquid at 25 DEG C. is 0.5 to 15 poise and the paper density is 0.3 to 0.7 g/d.

より好ましくは樹脂液の粘度が1〜10ポイズてあり、
紙の密度が0.4〜0.6g/c!iである。また、本
発明においては樹脂液を紙の片面より含浸せしめること
が肝要であつて、通常の樹脂液中に紙を浸漬する等の方
法によつては良好な含浸状態を確保することが困難てあ
る。
More preferably, the viscosity of the resin liquid is 1 to 10 poise,
Paper density is 0.4-0.6g/c! It is i. In addition, in the present invention, it is important to impregnate the paper with the resin liquid from one side, and it is difficult to ensure a good impregnated state using ordinary methods such as dipping the paper in the resin liquid. be.

本発明のように含浸した樹脂が未だ液状である間に含浸
基材のレイアツプを連続的に行い、次いで実質無圧の状
態で連続硬化させる方法では、まず第1に基材に樹脂液
を内部まで十分に含浸させることが大前提であつて、基
材中に樹脂液の含浸されていない部分や、気泡を形成し
た部分が存在すると製品の電気的および機械的特性に悪
影響を及ぼす。
In the method of the present invention, in which the impregnated base material is continuously laid up while the impregnated resin is still in a liquid state, and then continuously cured under virtually no pressure, first of all, the resin liquid is applied internally to the base material. The main premise is that the base material is sufficiently impregnated with the resin liquid, and if there are any areas in the base material that are not impregnated with the resin liquid or where air bubbles are formed, it will adversely affect the electrical and mechanical properties of the product.

そのため基材の見掛け密度、樹脂液の粘度、含浸方法等
に十分注意するとは勿論であるが、基材を重ねたまま同
時に含浸するのでは十分な含浸効果が得難いので、一枚
毎に含浸し、好ましくは含浸基材を積層するまでの間、
できるだけ十分な時間基材を独立して搬送し、しかるの
ち積層するのがよい。本発明に用いる不飽和ポリエステ
ル鎖は、例えばマレイン酸、無水マレイン酸、フマル酸
等の不飽和二塩基酸類、コハク酸、アジピン酸、無水フ
タル酸、イソフタル酸、テレフタル酸等の飽和二基酸類
、及びエチレングリコール、ジエチレングリコール、プ
ロピレングリコール等のグリコール類を原料として合成
される。
For this reason, it goes without saying that careful attention should be paid to the apparent density of the substrate, the viscosity of the resin liquid, the impregnation method, etc., but it is difficult to obtain a sufficient impregnation effect if the substrates are piled up and impregnated at the same time, so it is important to impregnate each sheet one by one. , preferably before laminating the impregnated base material,
The substrates are preferably conveyed independently for as long as possible and then laminated. The unsaturated polyester chains used in the present invention include, for example, unsaturated dibasic acids such as maleic acid, maleic anhydride, and fumaric acid; saturated dibasic acids such as succinic acid, adipic acid, phthalic anhydride, isophthalic acid, and terephthalic acid; It is synthesized using glycols such as ethylene glycol, diethylene glycol, and propylene glycol as raw materials.

本発明においては架橋用ビニルモノマーは液状であるこ
とが望ましく、スチレンが硬化速度、製品の均質性、製
品コストの点で本発明の連続生産法において最適である
In the present invention, the vinyl monomer for crosslinking is preferably liquid, and styrene is most suitable for the continuous production method of the present invention in terms of curing speed, product homogeneity, and product cost.

若干の不都合さを排除すればビニルトルエン、ジアリル
フタレート、酢酸ビニルも良好な結果を示す。このよう
な不飽和ポリエステル樹脂液は常温で液状であり、硬化
に際して水や炭酸ガスなどの揮発性副生成物を生成しな
い。
Vinyltoluene, diallyl phthalate, and vinyl acetate also show good results if some inconveniences are eliminated. Such an unsaturated polyester resin liquid is liquid at room temperature, and does not produce volatile byproducts such as water or carbon dioxide upon curing.

更に一般に認められ−ているように硬化反応の段階で三
次元的な架橋がおこり、不溶不融の状態に硬化する樹脂
がい\、必ずしも硬化に熱を必要とするとの趣旨ではな
く、常温硬化型や、光または放射線硬化型の樹脂をも含
む。樹脂含浸紙14は連続的にロール6とたとえばブレ
ード状物7の間にもうけられたクリアランスによつてラ
ミネートされ、同時にリール3及び4から巻き出された
フィルム状物がラミネートされる。
Furthermore, as is generally accepted, there are resins that undergo three-dimensional crosslinking during the curing reaction and harden to an insoluble and infusible state. This does not necessarily mean that heat is required for curing, but rather that resins that harden at room temperature. It also includes light- or radiation-curable resins. The resin-impregnated paper 14 is continuously laminated by the clearance provided between the roll 6 and, for example, the blade-like material 7, and at the same time, the film-like material unwound from the reels 3 and 4 is laminated.

ここにおいて、上記クリアランスは製品の厚!みを実質
的に決定する。従つて、このクリアランスに対応して、
使用する紙の厚みとラミネートされる樹脂含浸紙の枚数
が設定される。本発明にいては、たとえば0.25Tr
$Lの厚みの紙を用いることによつて、厚さが約0.2
5?から順次紙の枚数をふやクすことによつて、厚さが
数?である製品まで容易に製造できる。また、空気遮断
体としてラミネートされるフィルム状物12,13は積
層絶縁板の製造においては、製品性能上表面平滑性を有
するフィルム、たとえばセロハンやポリエステルフィル
ムが好ましい。必要に応じ、特にセロハンを用いる場合
は、ラミネート前にあらかじめ、乾燥することが望まし
い。本発明において含浸紙及びフィルム状物または金属
箔のラミネートの後、紙に含浸付着した過剰樹脂分を絞
り出すと同時に樹脂中の気泡を排除するに際し、ブレー
ド状物を用いてもよく、また必要に応じてロール状物を
用いても良く、また両者)を併用しても良い。
Here, the above clearance is the thickness of the product! substantively determines the Therefore, in response to this clearance,
The thickness of the paper to be used and the number of sheets of resin-impregnated paper to be laminated are set. In the present invention, for example, 0.25Tr
By using paper with a thickness of $L, the thickness is approximately 0.2
5? By sequentially increasing the number of sheets of paper, the thickness can be determined by increasing the number of sheets. It is possible to easily manufacture products that are Furthermore, in the production of laminated insulating plates, the film-like materials 12 and 13 to be laminated as air barriers are preferably films having surface smoothness, such as cellophane or polyester films, from the viewpoint of product performance. If necessary, especially when using cellophane, it is desirable to dry it before laminating. In the present invention, after laminating the impregnated paper and the film-like material or metal foil, a blade-like material may be used to squeeze out the excess resin impregnated onto the paper and at the same time eliminate air bubbles in the resin. Depending on the situation, a roll-shaped material may be used, or both may be used in combination.

硬化は例えば加熱炉8によつて行われる。Curing is performed, for example, in a heating furnace 8.

加熱炉8は常50℃〜100℃に加熱することが好まし
い。硬化の条件は、用いる触媒や助剤の種類や量によつ
て異なり、この種類や量は樹脂液のポツトライフや製品
の性状を考慮して設定されねばならない。低すぎる硬化
温度は樹脂液のポツトライフを犠性にし、高すぎる温度
はビニルモノマーの気化に起因する気泡の発生、あるい
は架橋密度の低下、ビニルモノマーの酸化をうながす。
本発明に″おいては、数ある有機過酸化物の内、特に、
クメンハイドロパーオキサイドまたはtーブチルパーオ
キシー2−エチルヘキサノエートを0.5〜3部、およ
びたとえばナフテン酸コバルトの如き助剤を0.005
〜0.02部配合し、前記硬化温度にて硬化時間を1吟
〜9紛とした時、電気用積層絶縁板または銅張り板とし
て性状のすぐれたものを得ることが出来る。硬化の状態
は製品の性状に大きな影響をもつ。
It is preferable that the heating furnace 8 is always heated to 50°C to 100°C. Curing conditions vary depending on the type and amount of the catalyst and auxiliary agent used, and the type and amount must be set in consideration of the pot life of the resin liquid and the properties of the product. Too low a curing temperature will sacrifice the pot life of the resin solution, while too high a temperature will promote the generation of bubbles due to vaporization of the vinyl monomer, a decrease in crosslinking density, and oxidation of the vinyl monomer.
In the present invention, among the many organic peroxides, in particular,
0.5 to 3 parts of cumene hydroperoxide or t-butylperoxy-2-ethylhexanoate and 0.005 parts of auxiliary agent such as cobalt naphthenate.
When ~0.02 part is blended and the curing time is 1 to 9 times at the above curing temperature, an electrical laminated insulating board or a copper-clad board with excellent properties can be obtained. The state of curing has a large effect on the properties of the product.

本発明においては、飽和二塩基酸類によつて、あらかじ
め不飽和ポリエステル鎖の不飽和度を制御することが重
要であつて、樹脂単独の硬度が、ロックウェル硬度で9
0〜120であるようなものを使用することが特に製品
の機械的特性、加工特性において好ましい。飽和二塩基
酸類として、フタル酸が一般的だが、本発明においては
イソフタル酸、テレフタル酸がより望ましい。硬化した
積層板17は引き取り機9によつて連続的に引き取られ
る。
In the present invention, it is important to control the degree of unsaturation of the unsaturated polyester chain in advance using saturated dibasic acids, and the hardness of the resin alone is 9 on the Rockwell hardness scale.
It is preferable to use one having a molecular weight of 0 to 120, especially in view of the mechanical properties and processing properties of the product. Phthalic acid is common as the saturated dibasic acid, but isophthalic acid and terephthalic acid are more preferred in the present invention. The cured laminate 17 is continuously taken off by a take-off machine 9.

この段階で硬化を完了させても良いが、少なくとも切断
可能な状態、すなわち切断しても変形したり、金属箔が
ごくわずかでも移動してしわを発生したりしない、すな
わち自己形態保持性を有する状態までかつ少なくとも該
遮断体を剥離して切断できる状態まで連続硬化させ、し
かる後、例えば架橋用ビニルモノマーの臭気の低減等の
目的のため適当時間アフターキユアしても良い。また、
加熱炉内に設置したロール状物15のクリアランスの調
整により厚み精度の微調整が可能である。連続硬化後の
両面のフィルム状空気遮断体を連一続的に剥離すれば電
気用積層絶縁板が得られる。片面のみフィルム状空気遮
断体他面に金属箔を使用した場合には、硬化後フィルム
状空気遮断体を剥離すれば片面金属箔張り積層体となる
。図示するように、積層物16は硬化反応進行中ブレス
等により側面からの加圧を受けることなしに、積層物の
自重による軽微の圧力を除いて実質的に無圧の状態で硬
化される。
Although curing may be completed at this stage, it is at least in a cuttable state, that is, it does not deform when cut, and the metal foil does not move even slightly and cause wrinkles, that is, it has self-shape retention. After curing continuously to a state where the barrier can be peeled off and cut, it may be after-cured for a suitable period of time, for example, for the purpose of reducing the odor of the crosslinking vinyl monomer. Also,
The thickness accuracy can be finely adjusted by adjusting the clearance of the roll-shaped material 15 installed in the heating furnace. After continuous curing, the film-like air barrier on both sides is continuously peeled off to obtain an electrical laminated insulating board. When a film-like air barrier is used on one side and a metal foil is used on the other surface, a single-sided metal foil-covered laminate is obtained by peeling off the film-like air barrier after curing. As shown in the figure, the laminate 16 is cured under substantially no pressure, except for a slight pressure due to the weight of the laminate, without being subjected to side pressure by a press or the like during the curing reaction.

そのため樹脂液は溶剤を含まず常温で液状であり、かつ
揮発性副生物を生成することなく硬化し得ることが必要
である。電気用積層絶縁板や金属箔張り積層板において
は、一般用波板等と異なり、1260℃あるいは200
℃における耐熱性、2低い加熱収縮率、3高い厚み精度
、4表面平滑性、5低い吸湿特性、6良好な打ち抜き加
工性、7高い電気絶縁特性、等の高度な特性が要求され
る。
Therefore, it is necessary that the resin liquid does not contain a solvent and is liquid at room temperature, and that it can be cured without producing volatile by-products. Unlike general-use corrugated boards, electrical laminated insulation boards and metal foil laminates can be heated to 1260°C or 200°C.
It is required to have advanced properties such as heat resistance at ℃, 2. low heat shrinkage, 3. high thickness accuracy, 4. surface smoothness, 5. low moisture absorption properties, 6. good punching workability, and 7. high electrical insulation properties.

これら諸特性を満足するためには、以上述べたごとき製
造方法を注意深く実行するとにより、可能であることを
見い出したことは、従来、加圧ブレス方式によつてにみ
しか製造できなかつたことを考えるなら驚くべきことで
ある。以上、基材としてセルロース繊維紙を用いる場合
について述べたが、基材としてたとえばガラス繊維布を
用いることによつて、ガラスクロスと不飽和ポリエステ
ル樹脂からなる電気用積層絶縁板または金属箔張り積層
板を同様に製造できる。
We have discovered that it is possible to satisfy these characteristics by carefully implementing the manufacturing method described above, which was previously only possible using the pressurized press method. It's amazing if you think about it. The case where cellulose fiber paper is used as the base material has been described above, but by using, for example, glass fiber cloth as the base material, it is possible to create an electrical laminated insulating board or a metal foil-clad laminate made of glass cloth and unsaturated polyester resin. can be manufactured similarly.

本発明においても、通常積層板に混入される添加剤等は
全て用いることが出来る。例えば難燃剤、難燃助剤、充
填剤、着色剤等が適宜使用され得る。以下実施例により
本発明をさらに詳しく説明する。実施例1 マレイン酸、イソフタル酸及びエチレングリコールを原
料として不飽和ポリエステル鎖を合成し、スチレンを配
合して得られる不飽和ポリエステル樹脂100部に対し
、さらにクメンハイドロパーオキサイド2部及びナフテ
ン酸コバルト0.01部を添加し、樹脂単独で硬化させ
た時の注形物のロックウェル硬度が106であり、曲げ
弾性率が283k9/n!tであり、25℃における粘
度が5ポイズである不飽和ポリエステル樹脂液を得た。
Also in the present invention, all additives and the like that are normally mixed into laminates can be used. For example, flame retardants, flame retardant aids, fillers, colorants, etc. may be used as appropriate. The present invention will be explained in more detail with reference to Examples below. Example 1 An unsaturated polyester chain was synthesized using maleic acid, isophthalic acid, and ethylene glycol as raw materials, and styrene was blended to form an unsaturated polyester resin. To 100 parts of an unsaturated polyester resin, 2 parts of cumene hydroperoxide and 0 cobalt naphthenate were added. When 0.01 part was added and the resin was cured alone, the Rockwell hardness of the cast product was 106, and the flexural modulus was 283k9/n! An unsaturated polyester resin liquid having a viscosity of 5 poise at 25° C. was obtained.

このものを、65%RH下で、風乾時の密度が0.53
g/Cjlであつて厚さが0.25?あり、巾が500
瓢の長尺セルロース繊維紙の片面に含浸し、2枚の樹脂
含浸紙を積層し、両面をセロファンで被覆した状態で、
70℃の温度で3紛間加熱できるラインスピードで連続
的に硬化せしめ、セロファンを連続的に剥離した後50
D71rmごとに切断しついで60゜Cで6紛間アフタ
ーキユアを行い、厚さが0.5?であつて50077!
77!角のの積層絶縁板を得た。このものは、1260
℃×w秒、あるいは200℃×3紛間においてふくれ、
層間剥離、発泡、ヒビワレ、変色等に異常のない耐熱性
を有し、2180℃×10分における加熱収縮率は0.
3%以下であつて、331100の厚み精度であり、4
すぐれた表面平滑性を有した。また、5吸湿特性は、実
に紙一フェノール従来品に比して112〜113であつ
た。6打抜き加工性は常温打ち抜き可能てあり、7JI
S一C−6481に規定する表面電気抵抗は3×101
4Ωである等、各種の特性にすぐれたものであつた。
This material has a density of 0.53 when air-dried under 65% RH.
g/Cjl and thickness 0.25? Yes, width is 500
One side of long cellulose fiber paper of gourd is impregnated, two sheets of resin-impregnated paper are laminated, and both sides are covered with cellophane.
After curing continuously at a line speed that allows 3-powder heating at a temperature of 70°C and continuously peeling off the cellophane,
After cutting every D71rm, after-curing with 6 pieces at 60°C, the thickness was 0.5mm. And it’s 50077!
77! A square laminated insulation board was obtained. This one is 1260
Blisters at ℃×w seconds or 200℃×3 times,
It has heat resistance with no abnormalities such as delamination, foaming, cracking, and discoloration, and the heat shrinkage rate at 2180°C for 10 minutes is 0.
3% or less, thickness accuracy of 331100, 4
It had excellent surface smoothness. In addition, the moisture absorption properties of the paper were actually 112 to 113 compared to the conventional paper-phenol product. 6. Punching workability: room temperature punching is possible, 7JI
The surface electrical resistance specified in S-C-6481 is 3 x 101
It had excellent properties such as 4Ω.

実施例2実施例1において、ラミネートする樹脂含浸紙
を6枚とし、厚さが1.6?である積層絶縁板を得た。
Example 2 In Example 1, six sheets of resin-impregnated paper are laminated, and the thickness is 1.6? A laminated insulating board was obtained.

このものは打ち抜き加工において、50℃〜70℃での
加温打ち抜きにより良好な加工性を示し、他ノの特性は
実施例1と同等であつた。
This material showed good workability by heating punching at 50 DEG C. to 70 DEG C., and other properties were the same as in Example 1.

実施例3 実施例2においては空気遮断体フ2イルム状物として両
面にセロハンを用いたが、実施例2において下面を長尺
な厚さが35)Pmである接着剤の塗布5されていない
電解銅箔(福田金属製CF−T3)とし剥離しないて、
厚さが1.6TfUTLある印刷回路板用銅張り積層板
を得た。
Example 3 In Example 2, cellophane was used on both sides of the air barrier film, but in Example 2, the bottom surface was not coated with an adhesive having a long thickness of 35) Pm. Electrolytic copper foil (Fukuda Metals CF-T3) is used to prevent peeling.
A copper-clad laminate for printed circuit boards having a thickness of 1.6 TfUTL was obtained.

JIS−C−6481に規定する銅の引きはがし強度は
1.1k9/Clnであつた。
The peel strength of copper specified in JIS-C-6481 was 1.1k9/Cln.

従来の紙一フェノール銅ク張り板の引きはがし強度に比
して、若干劣るが、実用上問題はなかつた。従来法と異
なり、銅箔がラミネートされる時点で樹脂が液状である
ため、樹脂液と銅箔表面の繊細な接合が実現し、従来法
のごとく特別な接着剤を必要としなかつた。
Although the peel strength was slightly inferior to that of the conventional paper-phenolic copper board, there was no problem in practical use. Unlike conventional methods, the resin is in a liquid state when the copper foil is laminated, so a delicate bond between the resin liquid and the surface of the copper foil is achieved, and no special adhesive is required as in conventional methods.

この為に、特にウェットな状況下での表面電気抵抗特性
にすぐれ、JIS−C−6481に規定する吸湿時の表
面電気抵抗は実に1013Ω以上の値を示した。実施例
4 実施例3において、空気遮断体フィルム状物として、両
面に電解銅箔を連続的にラミネートして、両面銅張り積
層板を得た。
For this reason, it has excellent surface electrical resistance characteristics especially under wet conditions, and the surface electrical resistance during moisture absorption specified in JIS-C-6481 actually showed a value of 1013Ω or more. Example 4 In Example 3, electrolytic copper foil was continuously laminated on both sides to obtain a double-sided copper-clad laminate as an air barrier film.

このものの特性は実施例3に示したものと同等であつた
。以上述べたごとく、本発明は従来方法においては加圧
工程を必須とする為に、不可能であつた連続生産方法を
フェノール樹脂と異なり、硬化に際してなんら揮発性副
生物を生じない典型的な無圧成形用樹脂である常温で液
状の不飽和ポリエステル樹脂液をたくみに応用して効率
的な連続生産法を可能としたものであり、その工業的価
値は極めて高い。
The properties of this product were similar to those shown in Example 3. As described above, the present invention enables continuous production, which was impossible in conventional methods due to the necessity of a pressurizing process, to be achieved using typical non-containing resins that do not produce any volatile by-products during curing, unlike phenolic resins. This method makes efficient continuous production possible by cleverly applying unsaturated polyester resin liquid, which is a pressure molding resin, and is liquid at room temperature, and its industrial value is extremely high.

すなわち、リジツトタイプの積層板の連続生産法ではブ
レスを使用できないから、例えば硬化に際し水を副生物
として発生するフェノール樹脂を使用すると内部に空胴
を生じ、到底満足な製品は得られない。
That is, since a press cannot be used in the continuous production method of rigid-type laminates, for example, if a phenolic resin is used that generates water as a byproduct during curing, a cavity will be created inside the resin, making it impossible to obtain a completely satisfactory product.

不飽和ポリエステル樹脂は硬化に際し揮発性副生物を発
生せす、しかも電気的特性にもすぐれたいるから本発明
の目的にかなつている。また、合浸後基材層内部に気泡
が残存すると圧縮成形法と異なつてそれらが排除されな
いから、合浸によつて基材層内部の空隙は実質上すべて
樹脂液で満たされなければならない。
Unsaturated polyester resins are suitable for the purpose of the present invention because they generate volatile byproducts during curing and also have excellent electrical properties. Furthermore, if air bubbles remain inside the base material layer after co-immersion, they cannot be removed unlike compression molding, so substantially all the voids inside the base material layer must be filled with the resin liquid by co-immersion.

そのためには、各基材に対し、個別的に樹脂液を供給し
、基材層内部の空隙の実質上すべてを含浸樹脂液で満た
す個別的な片面含浸方法が適している。さらに、空気中
の酸素は不飽和ポリエステル樹脂に対して重合禁止剤と
して作用するとが知られている。
For this purpose, an individual one-sided impregnation method is suitable, in which a resin liquid is individually supplied to each base material and substantially all of the voids inside the base material layer are filled with the impregnating resin liquid. Furthermore, it is known that oxygen in the air acts as a polymerization inhibitor on unsaturated polyester resins.

従つて硬化に際し未硬化積層板を空気との接触から遮断
しなければならない。金属箔張り積層板の金属箔はこの
ような空気遮断体でもあるが、片面金属箔張り積層板や
アンクラッド積層板・の場合は、樹脂を含浸した基材の
露出面をフィルム状空気遮断体で被覆し、硬化終了後剥
離する必要がある。またこのようなフィルム状空気遮断
体は、未硬化状態の樹脂液が硬化装置に付着し、汚染す
ることを防止するキャリアシートとしても役立つ。本発
明は、少なくともこれらの要件を組合せることにより、
リジッドタイプの電気用積層板および金属箔張り積層板
の工業的連続生産を実用化可能としたものである。
Therefore, during curing, the uncured laminate must be shielded from contact with air. The metal foil of metal foil-clad laminates is also an air barrier, but in the case of single-sided metal foil-clad laminates and unclad laminates, the exposed surface of the resin-impregnated base material is used as a film-like air barrier. It needs to be coated with and peeled off after curing. Such a film-like air barrier also serves as a carrier sheet to prevent uncured resin liquid from adhering to and contaminating the curing device. The present invention, by combining at least these requirements,
This makes it possible to commercialize continuous industrial production of rigid-type electrical laminates and metal foil-clad laminates.

図面の簡単な説明第1図は本発明製造方法実施の1例の
工程説明図である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a process explanatory diagram of one example of implementing the manufacturing method of the present invention.

2は乾燥器、5は樹脂液供給装置、6はロール、7はブ
レード状物、8は加熱炉、9は引き取り機、10−1〜
10−nはセルロース繊維紙、11は樹脂液、12,1
3はフィルム状物、14は樹脂含浸紙、15はロール、
16は未硬化積層物、17は硬化積層板である。
2 is a dryer, 5 is a resin liquid supply device, 6 is a roll, 7 is a blade-like object, 8 is a heating furnace, 9 is a take-up machine, 10-1~
10-n is cellulose fiber paper, 11 is resin liquid, 12,1
3 is a film-like material, 14 is resin-impregnated paper, 15 is a roll,
16 is an uncured laminate, and 17 is a cured laminate.

Claims (1)

【特許請求の範囲】 1 架橋用ビニルモノマーを含み、揮発性副生成物を生
成することなく硬化し得る常温で液状の不飽和ポリエス
テル樹脂液を、並行して連続的に供給される複数枚の基
材に対し個別に連続的に含浸させ、該含浸基材を連続的
に積層し、該積層体の両面にフィルム状空気遮断体およ
び/または金属箔を連続的に被覆し、その状態で該積層
体を連続的に実質無圧の状態で、少なくとも切断可能な
状態まで硬化することを特徴とする電気用積層絶縁板ま
たは金属箔張り積層板を連続的に製造する方法。 2 該被覆積層体の厚みをクリアランスにより決定し、
実質無圧で移送、硬化させる特許請求の範囲第1項記載
の方法。 3 積層体の両面をフィルム状空気遮断体で連続的に被
覆し、連続硬化の後、該遮断体を連続的に剥離する特許
請求の範囲第1項または第2項のいずれかの方法。 4 被覆積層体の片面が該遮断体、他の片面が金属箔で
あつて、連続硬化の後該片面の遮断体を連続的に剥離す
る特許請求の範囲第1項または第2項のいずれかの方法
。 5 被覆積層体の両面が金属箔で被覆されており、連続
硬化の後、断続的に適宜長さに切断する特許請求の範囲
第1項または第2項のいずれかの方法。 6 基材が、風乾時の密度が0.3〜0.7g/cm^
2であるようなセルロース繊維紙である特許請求の範囲
第1項ないし第5項のいずれかの方法。 7 不飽和ポリエステル樹脂液の25℃における粘度が
0.5〜15ポイズである特許請求の範囲第1項ないし
第6項のいずれかの方法。 8 不飽和ポリエステル樹脂液が不飽和二塩基酸、飽和
二塩基酸およびグリコールを主原料とした不飽和ポリエ
ステル鎖と架橋用ビニルモノマーとを主成分とする特許
請求の範囲第1項ないし7項のいずれかの方法。
[Claims] 1. A plurality of sheets of unsaturated polyester resin containing a crosslinking vinyl monomer and which is liquid at room temperature and can be cured without producing volatile by-products are continuously supplied in parallel. Substrates are individually and continuously impregnated, the impregnated substrates are continuously laminated, both sides of the laminate are continuously coated with a film-like air barrier and/or metal foil, and in that state, the impregnated substrates are continuously impregnated. A method for continuously manufacturing an electrical laminated insulating board or a metal foil-clad laminate, comprising curing the laminate continuously under substantially no pressure to at least a state in which it can be cut. 2 Determining the thickness of the covering laminate by the clearance,
The method according to claim 1, wherein the method is transferred and cured under substantially no pressure. 3. The method according to claim 1 or 2, wherein both sides of the laminate are continuously coated with a film-like air barrier, and after continuous curing, the barrier is continuously peeled off. 4. Either one of claims 1 or 2, wherein one side of the coated laminate is the barrier and the other side is a metal foil, and after continuous curing, the barrier on one side is continuously peeled off. the method of. 5. The method according to claim 1 or 2, wherein both sides of the coated laminate are coated with metal foil, and after continuous curing, the coated laminate is intermittently cut into appropriate lengths. 6 The density of the base material when air-dried is 0.3 to 0.7 g/cm^
The method according to any one of claims 1 to 5, wherein the cellulose fiber paper is a cellulose fiber paper as in claim 2. 7. The method according to any one of claims 1 to 6, wherein the unsaturated polyester resin liquid has a viscosity of 0.5 to 15 poise at 25°C. 8. Claims 1 to 7, in which the unsaturated polyester resin liquid is mainly composed of an unsaturated polyester chain made of an unsaturated dibasic acid, a saturated dibasic acid, and a glycol, and a crosslinking vinyl monomer. Either way.
JP53077668A 1978-06-26 1978-06-26 Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates Expired JPS6042566B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53077668A JPS6042566B2 (en) 1978-06-26 1978-06-26 Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53077668A JPS6042566B2 (en) 1978-06-26 1978-06-26 Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates

Publications (2)

Publication Number Publication Date
JPS554838A JPS554838A (en) 1980-01-14
JPS6042566B2 true JPS6042566B2 (en) 1985-09-24

Family

ID=13640255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53077668A Expired JPS6042566B2 (en) 1978-06-26 1978-06-26 Method for continuously manufacturing electrical laminated insulation boards or metal foil clad laminates

Country Status (1)

Country Link
JP (1) JPS6042566B2 (en)

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JPS641536A (en) * 1988-03-12 1989-01-05 Kanegafuchi Chem Ind Co Ltd Continuous preparation of hard laminated body for electric application
JPH01264797A (en) * 1988-04-15 1989-10-23 Kanegafuchi Chem Ind Co Ltd Cutting of laminated plate

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GB1169193A (en) * 1966-07-07 1969-10-29 Micanite & Insulators Co Ltd Improvements in and relating to Electrical Insulation
JPS5085688A (en) * 1973-11-30 1975-07-10
JPS5422471B2 (en) * 1974-03-30 1979-08-07
JPS5548696B2 (en) * 1974-04-15 1980-12-08
JPS555992B2 (en) * 1974-05-28 1980-02-12
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