JPH0688268B2 - Equipment for manufacturing phenol resin foam composite plates - Google Patents

Equipment for manufacturing phenol resin foam composite plates

Info

Publication number
JPH0688268B2
JPH0688268B2 JP62031261A JP3126187A JPH0688268B2 JP H0688268 B2 JPH0688268 B2 JP H0688268B2 JP 62031261 A JP62031261 A JP 62031261A JP 3126187 A JP3126187 A JP 3126187A JP H0688268 B2 JPH0688268 B2 JP H0688268B2
Authority
JP
Japan
Prior art keywords
surface material
foaming
phenol resin
curing
foam
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 - Lifetime
Application number
JP62031261A
Other languages
Japanese (ja)
Other versions
JPS63199618A (en
Inventor
中村  勉
哲夫 佐々木
邦夫 伏見
順一 富宇賀
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.)
Hodogaya Chemical Co Ltd
Original Assignee
Hodogaya Chemical 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 Hodogaya Chemical Co Ltd filed Critical Hodogaya Chemical Co Ltd
Priority to JP62031261A priority Critical patent/JPH0688268B2/en
Publication of JPS63199618A publication Critical patent/JPS63199618A/en
Publication of JPH0688268B2 publication Critical patent/JPH0688268B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 〈産業上の利用分野〉 この発明は、下面材および上面材の間にフェノール樹脂
発泡体の芯材を挟み込んだ積層構造を有する複合板の製
造装置に関するものである。
Description: TECHNICAL FIELD The present invention relates to a composite plate manufacturing apparatus having a laminated structure in which a core material of a phenol resin foam is sandwiched between a lower surface material and an upper surface material.

〈従来の技術〉 従来からウレタンフォーム,ポリスチレンフォーム,フ
ェノールフォーム等の樹脂発泡体を芯材とし、これをア
スベスト紙,ガラスペーパー,アルミ箔,石膏ボード,
鋼板等の各種面材の間に挟み込んだ積層構造を有する複
合板が知られている。
<Conventional technology> Conventionally, resin foam such as urethane foam, polystyrene foam, and phenol foam has been used as a core material, and asbestos paper, glass paper, aluminum foil, gypsum board,
A composite plate having a laminated structure sandwiched between various face materials such as steel plates is known.

かような複合板を連続的に製造する一般的方法は、連続
的に移送されている下面材の上に樹脂混合液を吐出し、
この樹脂混合液の上にさらに上面材を連続的に積層供給
して積層連続体を形成する。次いでこの積層連続体をそ
の上下面から押圧しながらキュア炉に通して加熱するこ
とにより、樹脂混合液の層を所定厚さに発泡硬化せし
め、キュア炉から出てくる積層連続体を所定寸法に切断
することによって樹脂発泡体複合板が得られる。
A general method for continuously manufacturing such a composite plate is to discharge the resin mixture onto the lower surface material that is continuously transferred,
An upper surface material is further continuously layered and supplied onto the resin mixed solution to form a layered continuous body. Next, the laminated continuous body is heated while being passed through a curing furnace while being pressed from the upper and lower surfaces thereof, whereby the layer of the resin mixed liquid is foamed and cured to a predetermined thickness, and the laminated continuous body coming out of the curing furnace is set to a predetermined size. A resin foam composite plate is obtained by cutting.

しかしながら、芯材となる樹脂発泡体のうちフェノール
樹脂発泡体は、耐熱性,難燃性,低発煙性等の優れた性
能を有するにも拘らず、他の樹脂発泡体に比較して非常
に脆いために使用方法が難しかった。
However, among the resin foams as the core material, the phenolic resin foams have excellent performances such as heat resistance, flame retardancy, and low smoke generation, but are extremely superior to other resin foams. It was brittle and difficult to use.

フェノール樹脂発泡体のもつかような欠点を解消するも
のとして、本願と同一出願人により新規な発泡性フェノ
ール樹脂混合液が提案されている(特開昭60-11520
号)。この発泡性フェノール樹脂混合液は、ベンジリッ
クエーテル型フェノール樹脂、ポリイソシアネート化合
物,芳香族スルホン酸化合物,水,発泡剤および整泡剤
からなり、この混合液を発泡硬化させることにより良好
な機械的物性を有するフェノール樹脂発泡体が得られ
る。
As a solution to the disadvantages of the phenol resin foam, a new foamable phenol resin mixture has been proposed by the same applicant as the present application (Japanese Patent Laid-Open No. 60-11520).
issue). This foamable phenol resin mixed liquid comprises a benzylic ether type phenol resin, a polyisocyanate compound, an aromatic sulfonic acid compound, water, a foaming agent and a foam stabilizer, and the mixture liquid is foamed and cured to obtain good mechanical properties. A phenol resin foam having physical properties is obtained.

〈発明が解決しようとする問題点〉 本発明者等は、上記の発泡性フェノール樹脂混合液を用
いてフェノール樹脂発泡体複合板を製造した。この製造
に際しては前述したような一般的方法を採用し、キュア
炉の温度を60〜80℃として行なった。
<Problems to be Solved by the Invention> The present inventors manufactured a phenol resin foam composite plate using the above-mentioned foamable phenol resin mixture. In this manufacturing, the general method as described above was adopted and the temperature of the curing furnace was set to 60 to 80 ° C.

かくして得られた複合板を調べたところ、フェノール樹
脂発泡体層は良好な機械的物性を有していたが、発泡体
中で均一な発泡がなされていない部分があり、密度の均
一性の点で若干問題のあることがわかった。また、上記
の発泡性フェノール樹脂混合液は各種面材との自己接着
力が良好であるが、条件によっては面材は発泡体との接
着力が必ずしも十分でないものもあった。
Examination of the composite plate thus obtained showed that the phenolic resin foam layer had good mechanical properties, but there was a portion where uniform foaming was not made in the foam, and the density uniformity Turned out to be a little problem. Further, although the above-mentioned foamable phenol resin mixed liquid has a good self-adhesive strength with various face materials, the face material may not always have a sufficient adhesive strength with the foam depending on the conditions.

そこで本発明者等は、従来の製造装置を改良し、樹脂混
合液層の発泡と硬化の両方を行なう従来のキュア炉を、
樹脂混合液層を発泡せしめる発泡室と、得られた発泡層
を硬化せしめる硬化室との2つの室に完全に分離し、発
泡室では発泡に最適な条件を、硬化室では硬化に最適な
条件を各々与えることによって、発泡体層が均一発泡
し、密度の均一性に優れ、さらには面材と発泡体との十
分な接着性を有するフェノール樹脂発泡体複合板が製造
できることを見出し、既に特許出願を行なった(特願昭
60-200084号)。
Therefore, the inventors of the present invention have improved the conventional manufacturing apparatus and installed a conventional curing furnace for performing both foaming and curing of the resin mixed liquid layer,
Completely separates into two chambers, a foaming chamber for foaming the resin mixture layer and a curing chamber for curing the resulting foamed layer. Optimal conditions for foaming in the foaming chamber and optimal conditions for curing in the curing chamber. It was found that a phenol resin foam composite plate having uniform foaming of the foam layer, excellent in density uniformity, and having sufficient adhesiveness between the face material and the foam can be produced by giving Filed an application
60-200084).

しかしながら上記した先願に係る改良装置においては、
例えば温度条件については発泡室および硬化室の各々に
最適な温度に保持することができるが、発泡室と硬化室
は各々一定寸法として並置されているため、各室での発
泡時間および硬化時間は積層連続体を各室に通して搬送
させるラインスピードによって各々一義的に決定され
る。その結果、発泡室内で確実にライズタイム(発泡体
が最高の高さに到達するに要する時間)付近まで発泡さ
せるようにするための生産管理が煩雑になる不利があっ
た。特に発泡室と硬化室との間に隔りをもたせてあるよ
うな場合には、この隔り部分で発泡が起ると発泡体自身
が面材から剥離してしまう現象もみられる。
However, in the improved device according to the above-mentioned prior application,
For example, regarding the temperature conditions, it is possible to maintain the optimum temperature in each of the foaming chamber and the curing chamber, but since the foaming chamber and the curing chamber are arranged side by side with a certain size, the foaming time and curing time in each chamber are It is uniquely determined by the line speed at which the laminated continuous body is conveyed through each chamber. As a result, there has been a disadvantage that the production control for surely performing the foaming in the foaming chamber to the vicinity of the rise time (the time required for the foam to reach the maximum height) becomes complicated. In particular, when there is a gap between the foaming chamber and the curing chamber, when foaming occurs in this gap, the foam itself may peel from the face material.

それ故この発明は、上記の先願に係る装置をさらに改良
し、より一層適切な条件を発泡室および硬化室に各々与
えることができ、これによって、均一発泡,均一密度の
発泡体層をもたらすとともに、面材と発泡体との接着性
の良好なフェノール樹脂発泡体複合板をより一層生産性
よく製造することができる装置を提供することを目的と
してなされたものである。
Therefore, the present invention further improves the apparatus according to the above-mentioned prior application, and can provide more appropriate conditions to the foaming chamber and the curing chamber, respectively, thereby providing a foam layer of uniform foaming and uniform density. At the same time, it is an object of the present invention to provide an apparatus capable of producing a phenol resin foam composite plate having good adhesion between the face material and the foam with even higher productivity.

〈問題点を解決するための手段〉 本発明者等は、積層連続体の樹脂混合液層を発泡硬化さ
せるキュア炉を、前述の先願装置におけるように完全に
独立,分離させて並置した発泡室と硬化室とから構成さ
せずに、キュア炉内を水平方向に移動可能な仕切りによ
って発泡域と硬化域とに区分することによって、上記の
目的を達成できることを見出しこの発明を完成させたも
のである。
<Means for Solving the Problems> The inventors of the present invention have completely configured the curing furnace for foaming and hardening the resin mixture layer of the continuous laminate, which is completely independent, separated and juxtaposed as in the above-mentioned prior application device. The present invention has been completed by finding out that the above object can be achieved by dividing the inside of the curing furnace into a foaming zone and a curing zone by a partition that can move in the horizontal direction without forming a curing chamber and a curing chamber. Is.

すなわちこの発明のフェノール樹脂発泡体複合板の製造
装置は、下面材の連続供給装置と;該下面材上に発泡性
フェノール樹脂混合液を吐出する吐出機と;該下面材上
に吐出された該樹脂混合液の上に上面材を連続的に積
層,供給して積層連続体を形成する上面材積層供給装置
と;所定間隔をもたせて上下に対向配置せしめた押圧搬
送装置を備え、これらの間に該積層連続体を連続的に通
すことによって該樹脂混合液の層を加熱し所定厚さに発
泡硬化せしめるキュア炉と;発泡硬化した該積層連続体
を所定寸法に切断して複合板製品とする切断機とを順次
配列してなるフェノール樹脂発泡体複合板の製造装置に
おいて、前記キュア炉内を、水平方向に移動可能な仕切
りによって温度20〜80℃に前記積層連続体を加熱して前
記樹脂混合液層を発泡せしめる発泡域と、該発泡域から
出た積層連続体を温度50〜100℃に加熱して該樹脂混合
液の発泡層を硬化せしめる硬化域とに区分したことを特
徴とするものである。
That is, the apparatus for producing a phenol resin foam composite plate according to the present invention comprises a continuous supply device for a lower surface material; an ejector for ejecting a foamable phenol resin mixture onto the lower surface material; An upper surface material laminating and supplying device for continuously laminating and supplying an upper surface material on the resin mixed liquid to form a continuous laminated body; and a pressing and conveying device vertically opposed to each other with a predetermined interval provided between them. A curing furnace for heating the layer of the resin mixed solution to foam and harden it to a predetermined thickness by continuously passing the laminated continuous body through a sheet; and a composite plate product obtained by cutting the foamed and hardened layered continuous body into a predetermined size. In a manufacturing apparatus of a phenol resin foam composite plate which is sequentially arranged with a cutting machine, in the curing furnace, the laminated continuous body is heated to a temperature of 20 to 80 ° C. by a partition that can be moved in the horizontal direction. Foam resin mixture layer It is characterized in that it is divided into a foaming zone for hardening and a hardening zone for hardening the foamed layer of the resin mixture by heating the laminated continuum emerging from the foaming zone to a temperature of 50 to 100 ° C.

〈作用〉 この種の複合板の製品の良否は、主として芯材である樹
脂発泡体の発泡の良否に影響されるが、本発明によれば
キュア炉内を仕切りによって発泡域と硬化域とに区分し
たため、発泡性フェノール樹脂混合液の発泡に最適な温
度と、発泡後の硬化に最適な温度を各々の区域で与える
ことができるだけでなく、仕切りを水平方向に移動させ
ることによって発泡域および硬化域の長さを変えること
ができるため、ラインスピードを変えずとも発泡時間お
よび硬化時間を調節することができる。そのため、温度
20〜80℃の範囲内の発泡最適温度でライズタイム直前に
至るまでの最適な時間だけ発泡域にて発泡させることが
でき、かくして発泡させたフェノール樹脂発泡体層を、
温度50〜100℃の範囲内の硬化最適温度をもつ硬化域に
て効率よく硬化させることが可能となる。
<Function> Although the quality of the product of this type of composite plate is mainly affected by the quality of the foaming of the resin foam as the core material, according to the present invention, the inside of the cure furnace is partitioned into a foaming zone and a curing zone. Since it is divided, not only can the optimum temperature for foaming of the foamable phenol resin mixture and the optimum temperature for curing after foaming be given in each area, but the partition can be moved horizontally to expand and cure the foamed area. Since the length of the zone can be changed, the foaming time and the curing time can be adjusted without changing the line speed. Therefore, the temperature
At the optimum foaming temperature within the range of 20 to 80 ° C, it is possible to foam in the foaming zone for the optimum time up to just before the rise time, and thus the foamed phenolic resin foam layer,
It becomes possible to cure efficiently in a curing zone having an optimal curing temperature within the range of 50 to 100 ° C.

発泡温度が20℃より低いと、ライズタイムが非常に長く
なり、80℃より高いと発泡速度をコントロールできなく
なり、均一な発泡がなされなく、密度の均一性が悪くな
る。一方、硬化温度が50℃より低いと硬化が十分でな
く、発泡体の機械的物性が劣る。また、100℃より高い
と発泡体中に亀裂を発生する傾向がみられる。
If the foaming temperature is lower than 20 ° C, the rise time becomes extremely long, and if it is higher than 80 ° C, the foaming rate cannot be controlled, uniform foaming is not performed, and the uniformity of density is deteriorated. On the other hand, if the curing temperature is lower than 50 ° C., the curing will be insufficient and the mechanical properties of the foam will be poor. If the temperature is higher than 100 ° C, the foam tends to crack.

〈実施例〉 以下にこの発明の好ましい実施例を挙げてさらに詳述す
る。添付図面は、この発明の複合板製造装置の一例を示
すものであって、下面材の連続供給装置1、発泡性フェ
ノール樹脂混合液の吐出機2、上面材積層供給装置3、
キュア炉4、切断機5がこの順で配列されてなる。下面
材供給装置1は、下面材を巻装したアンコイラ11とピン
チローラ12からなり、これによって下面材は図面の左か
ら右へ連続的に供給される。吐出機2は発泡性フェノー
ル樹脂混合液の所定量を下面材上に吐出する装置であ
り、1本または複数本の吐出ノズルを備えている。上面
材積層供給装置3は、上面材を巻装したアンコイラ31と
ガイドローラ32を有し、これによって下面材上に吐出さ
れた樹脂混合液の上に上面材を連続的に積層,供給して
積層連続体を形成するための装置である。キュア炉4の
内部は、水平方向に移動可能な仕切り6によって発泡域
41と硬化域42とに区分されており、仕切り6を水平方向
に移動することによって発泡域41の長さと硬化域42に長
さの割合を変えられるようになっている。発泡域41は、
複数ローラ43と44とを所定間隙をもたせて上下に対向配
置せしめた押圧搬送装置を有している。この複数ローラ
からなる押圧搬送装置は硬化域42の一部へも延設されて
いるが、硬化域42の出口近傍では、所定間隙をもたせて
ベルトコンベア45,46を上下に対向配置した二軸ベルト
コンベアからなる押圧搬送装置となっている。なお図示
の例では、吐出機2の前にプレヒーター7を設置して下
面材を予熱するようになっている。また、下面材として
鋼板等を使用する場合には、必要に応じてピンチローラ
12とプレヒーター7の間にエンボスロールおよび成形機
を設置することができる。
<Examples> Hereinafter, the present invention will be described in more detail with reference to preferred examples. The attached drawings show an example of the composite plate manufacturing apparatus of the present invention, which comprises a lower surface material continuous supply device 1, a foamable phenol resin mixed liquid discharger 2, an upper surface material stacking supply device 3,
The curing furnace 4 and the cutting machine 5 are arranged in this order. The lower surface material supply device 1 includes an uncoiler 11 around which a lower surface material is wound and a pinch roller 12, whereby the lower surface material is continuously supplied from left to right in the drawing. The discharger 2 is a device that discharges a predetermined amount of the foamable phenol resin mixed liquid onto the lower surface material, and includes one or a plurality of discharge nozzles. The upper surface material stacking and feeding device 3 has an uncoiler 31 around which the upper surface material is wound and a guide roller 32, whereby the upper surface material is continuously stacked and supplied on the resin mixed liquid discharged onto the lower surface material. It is an apparatus for forming a laminated continuous body. The inside of the curing furnace 4 is formed by a partition 6 that can move in the horizontal direction.
It is divided into 41 and a curing area 42, and the length ratio of the foaming area 41 to the curing area 42 can be changed by moving the partition 6 in the horizontal direction. The foam area 41 is
It has a pressing and conveying device in which a plurality of rollers 43 and 44 are vertically opposed to each other with a predetermined gap. The pressing and conveying device composed of a plurality of rollers is extended to a part of the curing area 42, but in the vicinity of the outlet of the curing area 42, the belt conveyors 45 and 46 are vertically opposed to each other with a predetermined gap. It is a pressing and conveying device composed of a belt conveyor. In the illustrated example, a pre-heater 7 is installed in front of the discharger 2 to preheat the lower surface material. When using a steel plate etc. as the bottom surface material, if necessary, use a pinch roller.
An embossing roll and a molding machine can be installed between 12 and the preheater 7.

この装置の動作を説明すると、下面材供給装置1から連
続的に供給される下面材は、プレヒーター7を通って予
熱されたのち連続的にラインに送り込まれる。次いでこ
の下面材の上に吐出機2から発泡性フェノール樹脂混合
液の所定量を連続的に吐出し、この樹脂混合液の上にさ
らに上面材供給装置3から連続的に供給される上面材を
被せることによって、樹脂混合液の層が上面材と下面材
の間に挟み込まれた積層連続体が形成される。積層連続
体はその上下面から押圧搬送装置によって押圧されて所
定の厚さを保持されながらキュア炉4内を通って運ばれ
る。この間、積層連続体の樹脂混合液は下面材と上面材
の間で均一に拡げられるとともに、複数ローラ43および
44を介して20〜80℃に加熱されて、発泡域41出口付近で
ライズタイム直前に達して所定の厚みに到達せしめる。
発泡域41を出た発泡済の積層連続体は次に硬化域42へ送
られ、ここで複数ローラ43,44および二軸ベルトコンベ
ア45,46を介して50〜100℃に加熱することにより硬化が
完了する。硬化域42から連続的に送り出される発泡硬化
済の積層連続体は切断機5によって所定寸法に切断され
て複合板製品となる。
The operation of this apparatus will be described. The lower surface material continuously supplied from the lower surface material supply device 1 is preheated through the preheater 7 and then continuously fed into the line. Then, a predetermined amount of the foamable phenol resin mixed liquid is continuously discharged from the discharger 2 onto the lower surface material, and the upper surface material continuously supplied from the upper surface material supply device 3 onto the resin mixed solution. By covering, a layered continuous body in which the layer of the resin mixed liquid is sandwiched between the upper surface material and the lower surface material is formed. The layered continuous body is conveyed from inside the curing furnace 4 while being pressed from above and below by a pressing and conveying device to maintain a predetermined thickness. During this time, the resin mixed liquid of the laminated continuous body is uniformly spread between the lower surface material and the upper surface material, and the plurality of rollers 43 and
It is heated to 20 to 80 ° C. via 44 and reaches a predetermined thickness near the exit of the foaming zone 41 just before the rise time.
The foamed laminated continuum exiting the foaming zone 41 is then sent to a curing zone 42, where it is cured by heating it to 50-100 ° C via multiple rollers 43,44 and biaxial belt conveyors 45,46. Is completed. The foamed and cured laminated continuous body continuously sent out from the curing area 42 is cut into a predetermined size by the cutting machine 5 to form a composite board product.

この発明において好ましく使用できるフェノール樹脂と
しては、ベンジリックエーテル型フェノール樹脂および
レゾール型フェノール樹脂が挙げられ、これら接着剤を
使用せずに面材との自己接着が可能である。
Phenolic resins that can be preferably used in the present invention include benzylic ether type phenolic resins and resol type phenolic resins, and self-adhesion with a face material is possible without using these adhesives.

面材としては、アスベスト紙,ガラスペーパー,アルミ
箔,各種の耐熱,耐炎性ラミネート紙,石膏ボード,金
属面材等を適宜使用することができる。
As the surface material, asbestos paper, glass paper, aluminum foil, various heat resistant and flame resistant laminated paper, gypsum board, metal surface material and the like can be appropriately used.

以下にこの実施例の装置の使用例を挙げてこの発明を更
に説明する。
The present invention will be further described below with reference to usage examples of the apparatus of this embodiment.

使用例 ベンジリックエーテル型フェノール樹脂の合成: フェノール 357g、パラホルムアルデヒド 174g、ナフ
テン酸鉛 1.5g、ナフテン酸亜鉛 3.0gを攪拌混合し、
110〜114℃にて3時間反応せしめた後速やかに減圧下に
脱水し、粘度30,000cps(at25℃)のベンジリックエー
テル型フェノール樹脂を得た。
Example of use Synthesis of benzylic ether type phenol resin: Phenol 357g, paraformaldehyde 174g, lead naphthenate 1.5g, zinc naphthenate 3.0g are mixed with stirring,
After reacting at 110 to 114 ° C. for 3 hours, it was immediately dehydrated under reduced pressure to obtain a benzylic ether type phenol resin having a viscosity of 30,000 cps (at 25 ° C.).

発泡性フェノール樹脂混合液の調製: A成分 ベンジリックエーテル型フェノ−ル樹脂(上記で合成し
たもの) 88.5重量部 発泡剤“フレオンR-11"(三井フロロケミカル社製)8.8
重量部 整泡剤“Tween-40"(花王アトラス社製) 2.7重量部 B成分 硬化剤(p−トルエンスルホン酸70%水溶液)30重量部 C成分 粗製ジフェニルメタンジイソシアネート(“ミリオネー
ト MR-200"、日本ポリウレタン社製) 10重量部 上記A,B,C成分をミキサー(東邦機械社製 P-306号)で
混合し、発泡性フェノール樹脂混合液を調製した。
Preparation of Effervescent Phenolic Resin Mixture: Component A Benzylic ether type phenolic resin (synthesized above) 88.5 parts by weight Foaming agent "Freon R-11" (Mitsui Fluorochemicals) 8.8
Parts by weight Foam stabilizer "Tween-40" (manufactured by Kao Atlas) 2.7 parts by weight B component curing agent (70% aqueous solution of p-toluenesulfonic acid) 30 parts by weight C component crude diphenylmethane diisocyanate ("Millionate MR-200", Japan Polyurethane Co., Ltd.) 10 parts by weight The above components A, B and C were mixed with a mixer (P-306 manufactured by Toho Machinery Co., Ltd.) to prepare a foamable phenol resin mixture.

複合板の製造: 添付図面のごとき装置により、下面材としてカラー鋼
板、上面材としてアルミ箔張りクラフト紙を用いて各種
寸法の複合板を製造した。このときの発泡性フェノール
樹脂混合液の仕込み量は39kg/m3、ラインスピードは15m
/min、キュア炉の全長は35m、キュア炉内の押圧搬送装
置は複数ローラ部31mおよびベルトコンベア部4mとし
た。また、キュア炉内の仕切りを水平方向に移動させる
ことによって、複合板寸法に応じた最適な発泡域長さ、
すなわち発泡所定時間を与えるように調節した。複合板
寸法と製造条件を第1表にまとめて示す。
Manufacture of Composite Plates: Composite plates of various sizes were manufactured using a color steel plate as the lower surface material and aluminum foil-clad kraft paper as the upper surface material using a device such as the attached drawings. At this time, the charging amount of the foamable phenol resin mixed liquid was 39 kg / m 3 , and the line speed was 15 m.
/ min, the total length of the curing furnace was 35 m, and the pressing and conveying device in the curing furnace was a plurality of roller parts 31 m and a belt conveyor part 4 m. Also, by moving the partition in the curing furnace horizontally, the optimal foaming zone length according to the composite plate dimensions,
That is, the foaming was adjusted to give a predetermined time. The composite plate dimensions and manufacturing conditions are summarized in Table 1.

得られた複合板のフェノール樹脂発泡体層はいずれもス
キン層が少なく、かつ発泡体断面には層状部分がなく、
均一発泡しており、密度は34〜35kg/m3であった。ま
た、得られた複合板はジグソー,丸ノコ等による切断,
入隅出隅加工に十分耐え得る接着力をもっていた。
Each of the phenolic resin foam layers of the obtained composite plate had few skin layers, and the foam cross section did not have a layered portion,
It was uniformly foamed and had a density of 34 to 35 kg / m 3 . Also, the obtained composite board is cut with a jigsaw, a circular saw, etc.
It had sufficient adhesive strength to withstand the processing of the inside and outside corners.

〈発明の効果〉 以上説明したようにこの発明によれば、キュア炉内を移
動可能な仕切りによって発泡域と硬化域とに区分したた
め、各々の区域において発泡最適温度および硬化最適温
度を与えることができるとともに、ラインスピードを変
えることなく単に仕切りを移動させるだけで発泡体の種
類や製品寸法の種類に応じた最適な発泡時間および硬化
時間に調節することができ、品質良好な複合板製品を生
産性よく製造することができる。
<Effects of the Invention> As described above, according to the present invention, since the inside of the curing furnace is divided into the foaming zone and the curing zone by the movable partition, it is possible to provide the optimal foaming temperature and the optimal curing temperature in each zone. At the same time, it is possible to adjust the optimal foaming time and curing time according to the type of foam and product size by simply moving the partition without changing the line speed, producing a good quality composite board product. It can be manufactured with good properties.

【図面の簡単な説明】[Brief description of drawings]

添付図面はこの発明の装置の実施例を示す説明図であ
る。 1……下面材連続供給装置、2……吐出機、3……上面
材積層供給装置、4……キュア炉、5……切断機、6…
…仕切り、41……発泡域、42……硬化域。
The attached drawings are explanatory views showing an embodiment of the apparatus of the present invention. 1 ... Lower surface material continuous supply device, 2 ... Discharging machine, 3 ... Upper surface material stacking supply device, 4 ... Cure furnace, 5 ... Cutting machine, 6 ...
… Partitions, 41… Foaming areas, 42… Curing areas.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B29L 9:00 4F (72)発明者 富宇賀 順一 神奈川県横浜市鶴見区大黒町7番43号 保 土谷化学工業株式会社中央研究所鶴見分室 内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical display location B29L 9:00 4F (72) Inventor Junichi Tomiuga 7-43 Daikokucho, Tsurumi-ku, Yokohama-shi, Kanagawa Hodogaya Chemical Co., Ltd. Central Research Laboratory Tsurumi Branch Office

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】下面材の連続供給装置と;該下面材上に発
泡性フェノール樹脂混合液を吐出する吐出機と;該下面
材上に吐出された該樹脂混合液の上に上面材を連続的に
積層,供給して積層連続体を形成する上面材積層供給装
置と;所定間隔をもたせて上下に対向配置せしめた押圧
搬送装置を備え、これらの間に該積層連続体を連続的に
通すことによって該樹脂混合液の層を加熱し所定厚さに
発泡硬化せしめるキュア炉と;発泡硬化した該積層連続
体を所定寸法に切断して複合板製品とする切断機とを順
次配列してなるフェノール樹脂発泡体複合板の製造装置
において、前記キュア炉内を、水平方向に移動可能な仕
切りによって温度20〜80℃に前記積層連続体を加熱して
前記樹脂混合液層を発泡せしめる発泡域と、該発泡域か
ら出た積層連続体を温度50〜100℃に加熱して該樹脂混
合液の発泡層を硬化せしめる硬化域とに区分したことを
特徴とするフェノール樹脂発泡体複合板の製造装置。
1. A continuous supply device for a lower surface material; a discharger for discharging a foamable phenol resin mixed liquid onto the lower surface material; a continuous upper surface material on the resin mixed liquid discharged onto the lower surface material. A stacking and feeding device for the upper surface material that stacks and feeds the film continuously to form a continuous stacked body; and a pressing and conveying device that is vertically opposed to each other at a predetermined interval, and continuously passes the continuous stacked body between them. A curing furnace for heating the layer of the resin mixed liquid to foam and harden it to a predetermined thickness, and a cutting machine for cutting the foamed and hardened laminated continuous body into a predetermined size to obtain a composite plate product are sequentially arranged. In the manufacturing apparatus of a phenol resin foam composite plate, in the curing furnace, a foaming zone for foaming the resin mixture layer by heating the laminated continuous body to a temperature of 20 to 80 ° C. by a partition that can move in the horizontal direction. , The laminated continuum from the foamed area An apparatus for producing a phenol resin foam composite plate, characterized in that it is divided into a hardening zone for heating the foamed layer of the resin mixture by heating at a temperature of 50 to 100 ° C.
JP62031261A 1987-02-13 1987-02-13 Equipment for manufacturing phenol resin foam composite plates Expired - Lifetime JPH0688268B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62031261A JPH0688268B2 (en) 1987-02-13 1987-02-13 Equipment for manufacturing phenol resin foam composite plates

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62031261A JPH0688268B2 (en) 1987-02-13 1987-02-13 Equipment for manufacturing phenol resin foam composite plates

Publications (2)

Publication Number Publication Date
JPS63199618A JPS63199618A (en) 1988-08-18
JPH0688268B2 true JPH0688268B2 (en) 1994-11-09

Family

ID=12326405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62031261A Expired - Lifetime JPH0688268B2 (en) 1987-02-13 1987-02-13 Equipment for manufacturing phenol resin foam composite plates

Country Status (1)

Country Link
JP (1) JPH0688268B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5430875B2 (en) * 2008-04-28 2014-03-05 旭化成建材株式会社 Method for producing phenolic resin foam laminate
JP5691970B2 (en) * 2011-09-27 2015-04-01 豊田合成株式会社 Method and apparatus for trimming surplus film of decorative film molded product
JP7027078B2 (en) * 2017-03-28 2022-03-01 旭化成建材株式会社 Phenol resin foam laminated board and its manufacturing method

Also Published As

Publication number Publication date
JPS63199618A (en) 1988-08-18

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