JPS6259039A - Method and device for manufacturing phenol resin foam composite board - Google Patents

Method and device for manufacturing phenol resin foam composite board

Info

Publication number
JPS6259039A
JPS6259039A JP60200084A JP20008485A JPS6259039A JP S6259039 A JPS6259039 A JP S6259039A JP 60200084 A JP60200084 A JP 60200084A JP 20008485 A JP20008485 A JP 20008485A JP S6259039 A JPS6259039 A JP S6259039A
Authority
JP
Japan
Prior art keywords
foaming
phenolic resin
foam
curing
resin mixture
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.)
Granted
Application number
JP60200084A
Other languages
Japanese (ja)
Other versions
JPH0225786B2 (en
Inventor
勉 中村
三好 剛一
伏見 邦夫
富宇賀 順一
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 JP60200084A priority Critical patent/JPS6259039A/en
Publication of JPS6259039A publication Critical patent/JPS6259039A/en
Publication of JPH0225786B2 publication Critical patent/JPH0225786B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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
造方法、およびこの方法を実施するために用いる製造装
置に関するものでおる。
[Detailed Description of the Invention] <Industrial Application Field> The present invention provides a method for manufacturing a composite plate having a laminated structure in which a core material of phenolic resin foam is sandwiched between a bottom material and a top material, and This article relates to the manufacturing equipment used to carry out the process.

〈従来の技術〉 従来からウレタンフオーム、ポリスチレンフオーム、フ
ェノールフオーム等の樹脂発泡体を芯材とし、これをア
スベス1〜紙、ガラスペーパー、アルミ箔2石青ボード
、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 foams such as urethane foam, polystyrene foam, and phenol foam have been used as a core material, and this has been used as a material between asbestos (1), paper, glass paper, aluminum foil (2), and various surface materials such as stone blue board and steel plate. Composite plates having a laminated structure sandwiched between two are 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 common method for continuously manufacturing such composite boards is to discharge a resin mixture onto the bottom material that is being continuously transported.
A top material is further laminated and supplied on top of this resin mixture to form a continuous laminated body. Next, this laminated continuum is passed through a curing furnace and heated while being pressed from the top and bottom surfaces, thereby foaming and hardening the layer of the resin mixture to a predetermined thickness, and the laminated continuum coming out of the curing furnace to a predetermined size. A resin foam composite board 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 resin foams that serve as core materials, phenolic resin foams have excellent properties such as heat resistance, flame retardance, and low smoke emission, but compared to other resin foams, phenolic resin foams have very low performance. It was difficult to use because it was brittle.

フェノール樹脂発泡体のもつかような欠点を解潤するも
のとして、本願と同一出願人によりvIr規な発泡性フ
ェノール樹脂混合液が提案されている(特願昭59−4
3866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。
In order to eliminate the drawbacks of phenolic resin foam, a vIr foamable phenolic resin mixture has been proposed by the same applicant as the present application (Japanese Patent Application No. 59-4).
No. 3866). This foamable phenolic resin mixture is a benzylic ether type phenolic resin and a polyisocyanate compound.

芳香族スルホン酸化合物、水2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。
It consists of an aromatic sulfonic acid compound, water, a blowing agent, and a foam stabilizer, and by foaming and curing this mixture, a phenolic resin foam having good mechanical properties can be 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 phenolic resin foam composite board using the above-mentioned foamable phenolic resin mixture. For this production, the general method as described above was employed, and the temperature of the curing furnace was set at 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おることがわかった。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。
When the composite board thus obtained was examined, it was found that the phenolic resin foam layer had good mechanical properties, but there were some areas where the foam was not uniformly foamed, and the uniformity of density was poor. I found out that there were some problems. Further, although the above-mentioned foamable phenol resin mixture has good self-adhesive strength with various face materials, the adhesive strength of the face material with the foam may not necessarily be sufficient depending on the conditions.

そこで本発明の目的は、発泡体層が均一発泡し、密度の
均一性に優れ、ざらには面材との十分な接着力を有する
フェノール樹脂発泡体複合板を生産性よく製造すること
ができる方法と装置を提供することである。
Therefore, an object of the present invention is to be able to produce with high productivity a phenolic resin foam composite board in which the foam layer is uniformly foamed, has excellent density uniformity, and has sufficient adhesion to the surface material. An object of the present invention is to provide a method and apparatus.

〈問題点を解決するための手段〉 本発明者等は、前)ホしたごとき従来の連続的な複合板
の製造方法において採用されているキュア炉での発泡硬
化工程を発泡工程と硬化工程の2段階に完全に分離し、
各々の工程に最適な条件を与えることによって、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 present inventors have developed a method of combining the foaming process and the curing process in the curing furnace, which is employed in the conventional continuous composite plate manufacturing method as described above. Completely separated into two stages,
This invention was completed by discovering that the above object can be achieved by providing optimal conditions to each step.

すなわち第1の発明であるフェノール樹脂発泡体複合板
の製造方法は、従来から採用されていた発泡性フェノー
ル樹脂混合液層の1段階での発泡硬化工程を、温度20
〜80°Cでこの(か]脂混合液層を発泡させる工程と
、発泡した樹脂混合液層を温度50〜100℃で硬化さ
せる工程とに分けて行なう。
That is, the method for manufacturing a phenolic resin foam composite board, which is the first invention, replaces the conventional one-stage foaming and curing process of the foamable phenolic resin mixed liquid layer with a temperature of 20°C.
The process is divided into a step of foaming the resin mixed liquid layer at ~80°C and a step of curing the foamed resin mixed liquid layer at a temperature of 50 to 100°C.

また第2の発明でおる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づる吐出機と、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ベルト
コンベアまたはローラを備え、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用法に切断して複合体製品とする
切断機とを順次配列してなる装置において、前記キュア
炉を、温度20〜80℃に積層連続体を加熱して樹脂混
合液層を発泡せしめる発泡室と、この発泡室から出た積
層連続体を温度50〜100℃に加熱して樹脂混合液の
発泡層を硬化せしめる硬化室とから構成したことを特徴
とするものでおる。
Further, the second invention provides an apparatus for manufacturing a phenolic resin foam composite board, which includes: a continuous supply device for a bottom material; a discharge machine for discharging a foamable phenolic resin mixture onto the bottom material; a top material lamination supply device that continuously laminates and supplies the top material on top of the resin mixture to form a continuous layered body; and a belt conveyor or rollers arranged vertically facing each other with a predetermined interval. , a curing furnace in which the layer of the resin mixture is heated and foamed and hardened to a predetermined thickness by continuously passing the layered layer between them; In an apparatus comprising a cutting machine for producing a composite product and sequentially arranged, the curing furnace is connected to a foaming chamber that heats the laminated continuous body to a temperature of 20 to 80°C to foam a resin mixed liquid layer, and a foaming chamber that foams a resin mixed liquid layer. It is characterized by comprising a curing chamber for heating the resulting laminated continuous body to a temperature of 50 to 100°C to cure the foamed layer of the resin mixture.

この発明においては、樹脂混合液層の発泡温度より硬化
温度の方が高い温度となるように設定することが必要で
あり、これによって発泡工程とそれに引続く硬化工程と
を明確に2段階に分けて行なうのである。
In this invention, it is necessary to set the curing temperature to be higher than the foaming temperature of the resin mixed liquid layer, thereby clearly dividing the foaming process and the subsequent curing process into two stages. That's what we do.

く作 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
発泡工程と硬化工程とに完全に分離したため、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工程で与えることができる。そ
のため、温度20〜80℃の範囲内の発泡最適温度でラ
イスタイム(発泡体が最高の高さに到達するに要する時
間)直前まで効率よく発泡工程または発泡室にて発泡さ
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工程または硬化室にて
効率よく硬化させることが可能となる。
Effects> The quality of this type of composite board product is mainly influenced by the quality of foaming of the resin foam that is the core material, but according to the present invention, the foaming process and curing process are completely separated, so The optimum temperature for foaming the foamable phenolic resin mixture and the optimum temperature for curing after foaming can be provided in each step. Therefore, the phenolic resin foam is efficiently foamed in the foaming process or foaming chamber at the optimal foaming temperature within the temperature range of 20 to 80°C until just before the rice time (the time required for the foam to reach its maximum height). The layer can be efficiently cured in a curing process or curing chamber with an optimum curing temperature within the range of 50 to 100<0>C.

発泡温度が20℃より低いと、ライスタイムが非常に長
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ずる傾向がみられる。
If the foaming temperature is lower than 20°C, the rice time will be very long, and if it is higher than 80°C, the foaming speed cannot be controlled, uniform foaming will not be achieved, and the uniformity of density will deteriorate. On the other hand, if the curing temperature is lower than 50°C, curing will not be sufficient and the mechanical properties of the foam will be poor. Furthermore, if the temperature is higher than 100°C, there is a tendency for cracks to occur in the foam.

〈実施例〉 以下にこの発明の好ましい実施例を挙げてざらに詳J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、
発泡室4、硬化室5、切断機6がこの順で配列されてな
る。
<Examples> Preferred examples of the present invention will be listed below and will be described in detail. The attached drawing shows an example of the composite plate manufacturing apparatus of the present invention, which includes a continuous supply device 1 for bottom material, a discharge device 2 for foaming phenolic resin mixture, a layered supply device 3 for top material,
A foaming chamber 4, a curing chamber 5, and a cutting machine 6 are arranged in this order.

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
The bottom material supply device 1 includes an uncoiler 11 wrapped with the bottom material.
and pinch rollers 12, whereby the underside material is continuously supplied from left to right in the drawing. The discharge machine 2 is a device that discharges a predetermined amount of the foamable phenolic resin mixture onto the lower surface material, and includes one or more discharge nozzles.

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。発泡
室4は、ベルトコンベア41と複数日−ラ42とを所定
間隙をもたせて上下に対向配置せしめた抑圧搬送装置を
有しており、硬化室5は所定間隙をもたせてベルトコン
ベア51.52を上下に対向配置した二軸ベル1〜コン
ベアからなる抑圧搬送装置を有している。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。
The top material lamination supply device 3 has an uncoiler 31 wrapped with the top material and a guide roller 32, and thereby continuously laminates the top material on top of the resin mixture discharged onto the bottom material.
This is a device for supplying and forming a laminated continuous body. The foaming chamber 4 has a suppression conveyor device in which a belt conveyor 41 and a plurality of rollers 42 are disposed vertically facing each other with a predetermined gap, and the curing chamber 5 has a belt conveyor 51, 52 with a predetermined gap between them. It has a suppression conveyance device consisting of a two-shaft bell 1 and a conveyor arranged vertically opposite each other. In the illustrated example, a preheater 7 is installed in front of the discharge machine 2 to preheat the lower surface material. In addition, if a steel plate or the like is used as the bottom material, the pinch roller 12 may be used as necessary.
An embossing roll and a molding machine can be installed between the preheater 7 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
熱されたのら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
液の所定間を連続的に吐出し、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されて所定の厚さを保持されな
がら発泡室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、ベル1〜コンベア41およびローラ42を介
して20〜80℃に加熱されて、発泡室4出口付近でラ
イスタイム直前に達して所定の厚みに到達せしめる。発
泡室4を出た発泡汎の積層連続体は次に硬化室5へ送ら
れ、ここで二輪ベルトコンベア51.52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
室5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6によって所定寸法に切断されて複合板製品と
なる。
To explain the operation of this device, the bottom material that is continuously supplied from the bottom material supply device 1 is preheated through a preheater 7, and then continuously fed into the line. Next, a predetermined amount of the foamable phenolic resin mixture is continuously discharged from the dispensing machine 2 onto the bottom material, and the top material, which is continuously supplied from the top material supplying device 3, is further applied onto this resin mixture. By overlapping, a laminated continuous body is formed in which a layer of the resin mixture is sandwiched between the upper surface material and the lower surface material. The laminated continuous body is conveyed through the foaming chamber 4 while being pressed from its upper and lower surfaces to maintain a predetermined thickness. During this time, the resin mixture in the laminated continuous body is spread uniformly between the bottom material and the top material, and is heated to 20 to 80°C via the bell 1 to the conveyor 41 and rollers 42, and near the exit of the foaming chamber 4. The rice is heated just before the rice time to reach a predetermined thickness. The foamed laminate continuous body leaving the foaming chamber 4 is then sent to the curing chamber 5, where it is conveyed via a two-wheeled belt conveyor 51, 52.
Curing is completed by heating to ~100°C. The foamed and cured laminated continuous body continuously sent out from the curing chamber 5 is cut into a predetermined size by a cutter 6 to produce 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、これらは接着剤
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, which can be self-adhesive to the face material without using an adhesive.

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1石高ボード、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 boards, metal surface materials, and the like can be used as appropriate.

以下にこの発明方法を実施例および比較例によって更に
詳細に説明する。
The method of the present invention will be explained in more detail below with reference to Examples and Comparative Examples.

実施例 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 357Q1パラホルムアルデヒド174g、ナフ
テン酸亜鉛1.5g 、ナフテン酸亜鉛3.0gを攪拌
混合し、110〜114°Cにて3時間反応せしめた俊
速やかに減圧下に脱水し、粘度30、000cps  
(at 25°C)のベンジリックエーテル型フェノー
ル樹脂を得た。
Example Synthesis of benzylic ether type phenolic resin: 174 g of phenol 357Q1 paraformaldehyde, 1.5 g of zinc naphthenate, and 3.0 g of zinc naphthenate were stirred and mixed, and reacted rapidly at 110 to 114°C for 3 hours. Dehydrated under reduced pressure, viscosity 30,000 cps
A benzylic ether type phenol resin (at 25°C) was obtained.

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 88.5重量部−ル樹
脂(上記で合成したもの) 発泡剤″フレオンR−11”    8.8@伍部(三
井フロロケミカル社製) 整泡剤”TWeen−4Q”      2.7重聞部
(花王アトラス社製) B成分 硬化剤       30重狙八へ (p−1〜ル工ンスルホン酸70%水溶液)C成分 粗製ジフェニルメタンジイソシ 1o  !1アネー(
・(“ミリオネート MR−200”、日本ポリウレタ
ン礼装) 上記A、B、C成分をミキサー(東邦機械拘I P−3
06型)で混合し、発泡性フェノール樹l)混合液を調
製した。
Preparation of foamable phenolic resin mixture: A component: 88.5 parts by weight of benzylic ether type phenol resin (synthesized above) Foaming agent "Freon R-11" 8.8@Gobe (Mitsui Fluorochemical Co., Ltd.) ) Foam stabilizer "TWeen-4Q" 2.7 layers (manufactured by Kao Atlas Co., Ltd.) B component curing agent 30 layers (p-1 ~ 70% aqueous solution of polysulfonic acid) C component crude diphenylmethane diisopropylene 1o! 1 anne (
・(“Millionate MR-200”, Japan Polyurethane Formal Attire) The above A, B, and C components are mixed in a mixer (Toho Machinery Co., Ltd. I P-3
06 type) to prepare a foamable phenolic resin l) mixture.

複合板の装造: 添付図面のごとき装置により、下面材とじlカラー鋼板
、上面材としてアルミ箔張りクラじ1・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
樹脂混合液の仕込ノ帛は39kMm”、ラインスピード
は15m/min 、発泡室の長さは11.3m 、硬
化室の長さG222.3mとした。複合板寸法と製造条
件を第17にまとめて示す。
Composite board construction: Composite boards of various sizes were manufactured using the equipment shown in the attached drawings using bound color steel plates as the bottom material and aluminum foil-covered paper as the top material. At this time, the charging rate of the foamable phenolic resin mixture was 39 km, the line speed was 15 m/min, the length of the foaming chamber was 11.3 m, and the length of the curing chamber was 222.3 m. Dimensions and manufacturing of the composite plate. The conditions are summarized in No. 17.

]1 し ;[− 寸 *2 プレヒーターから出てくる上面材温度*3 コン
ベア温度 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、  34〜35 kM m
s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1qる接
着力をもっていた。
]1 [- size *2 Temperature of the top material coming out of the preheater *3 Conveyor temperature The phenolic resin foam layer of the obtained composite board all has a small skin layer, and the cross section of the foam has a layered part. Without,
It is uniformly foamed, and the density is 34-35 kmM.
It was s. In addition, the obtained composite plywood can be used with a jigsaw,
It was able to withstand cutting with a circular saw, etc., and machining inside and outside corners, and had an adhesive strength of 1q.

比較例 添付図面の装置における発泡室の温度と硬化室の温度を
ともに80°Cとした以外は、上記実施例と同じ操作に
よってフェノール樹脂発泡体造した。
Comparative Example A phenolic resin foam was produced by the same procedure as in the above example except that the temperature of the foaming chamber and the temperature of the curing chamber in the apparatus shown in the attached drawings were both 80°C.

1qられた複合板のフェノール樹脂発泡体は、粗密部が
多く、かつ断面には層状部分ができていた。密度も、部
位によっては20k(]/m3から40k(]/m3ま
での場合があった。また、この複合板内の一部には、ジ
グソー、丸ノコ等の切断入隅出隅加工に不適当なものが
あった。
The phenolic resin foam of the composite plate prepared in 1q had many dense and dense parts, and a layered part was formed in the cross section. The density also ranged from 20k(]/m3 to 40k(]/m3 depending on the area.In addition, some parts of this composite board were difficult to cut with jigsaws, circular saws, etc.). There was something suitable.

〈発明の効果〉 以上説明したようにこの発明によれば、従来は1段階で
行なっていた発泡硬化工程を、発泡に最適な温度を与え
る発泡工程と、発泡後の硬化に最適な温度を与える硬化
工程との2段階に分けて行なうことによって、フェノー
ル樹脂発泡体層での効果的かつ均一な発泡がなされるた
め密度の均一性に優れ、ざらには面材と発泡体層との接
着力も良好ケフェノール樹脂発泡体複合板を得ることが
できる。
<Effects of the Invention> As explained above, according to the present invention, the foaming and curing process, which was conventionally performed in one step, can be replaced with a foaming process that provides an optimal temperature for foaming, and a foaming process that provides an optimal temperature for curing after foaming. By performing the process in two stages, including the curing process, effective and uniform foaming is achieved in the phenolic resin foam layer, resulting in excellent density uniformity and improved adhesion between the face material and the foam layer. A good kephenol resin foam composite board can be obtained.

【図面の簡単な説明】 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・・・発泡室、5・・・硬化
室、6・・・切断殿。
BRIEF DESCRIPTION OF THE DRAWINGS The accompanying drawings are explanatory views showing embodiments of the apparatus of the present invention. 1... Bottom material continuous supply device, 2... Discharge machine, 3...
・Top material lamination supply device, 4... Foaming chamber, 5... Curing chamber, 6... Cutting hall.

Claims (1)

【特許請求の範囲】 1、連続的に移送されている下面材上に発泡性フェノー
ル樹脂混合液を吐出し、該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し、該積層
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該樹脂混合液の層を所定厚さに発泡
硬化せしめたのち、該積層連続体を所定寸法に切断する
ことからなるフェノール樹脂発泡体複合板の製造方法に
おいて、前記発泡硬化工程を、温度20〜80℃で前記
樹脂混合液層を発泡させる工程と発泡した前記樹脂混合
液層を温度50〜100℃で硬化させる工程とに分けて
行なうことを特徴とするフェノール樹脂発泡体複合板の
製造方法。 2、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ベルトコンベ
アまたはローラを備え、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、前記キュア炉を、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
める発泡室と、該発泡室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
める硬化室とから構成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。
[Claims] 1. A foamable phenolic resin mixture is discharged onto the bottom material that is being continuously transported, and the top material is continuously supplied on top of the resin mixture to form a continuous layered material. The layer of the resin mixture is foamed and cured to a predetermined thickness by heating the laminated continuum to a predetermined thickness by pressing the laminated continuum from its upper and lower surfaces, and then the laminated continuum is cut into a predetermined size. In the method for producing a phenolic resin foam composite board, the foaming and curing step is performed by foaming the resin mixed liquid layer at a temperature of 20 to 80°C, and foaming the foamed resin mixed liquid layer to a temperature of 50 to 100°C. A method for producing a phenolic resin foam composite board, characterized by carrying out the step of curing at °C. 2. A continuous supply device for the bottom material; a discharge machine that discharges the foamable phenolic resin mixture onto the bottom material; and a top material that is continuously laminated on top of the resin mixture discharged onto the bottom material. , a top material laminate supply device that feeds to form a laminate continuous body; and a belt conveyor or rollers arranged vertically facing each other with a predetermined interval, and by continuously passing the laminate continuous body between them. A phenolic resin formed by sequentially arranging a curing furnace that heats a layer of the resin mixture to foam and harden it to a predetermined thickness; and a cutting machine that cuts the foam-hardened laminated continuous body into a predetermined size to produce a composite plate product. In an apparatus for producing a foam composite board, the curing furnace includes a foaming chamber that heats the laminated continuum to a temperature of 20 to 80°C to foam the resin mixed liquid layer, and a laminated continuum that comes out of the foaming chamber. temperature 50
1. An apparatus for manufacturing a phenolic resin foam composite board, comprising a curing chamber for heating to ~100[deg.] C. to harden a foamed layer of the resin mixture.
JP60200084A 1985-09-10 1985-09-10 Method and device for manufacturing phenol resin foam composite board Granted JPS6259039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60200084A JPS6259039A (en) 1985-09-10 1985-09-10 Method and device for manufacturing phenol resin foam composite board

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60200084A JPS6259039A (en) 1985-09-10 1985-09-10 Method and device for manufacturing phenol resin foam composite board

Publications (2)

Publication Number Publication Date
JPS6259039A true JPS6259039A (en) 1987-03-14
JPH0225786B2 JPH0225786B2 (en) 1990-06-05

Family

ID=16418586

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60200084A Granted JPS6259039A (en) 1985-09-10 1985-09-10 Method and device for manufacturing phenol resin foam composite board

Country Status (1)

Country Link
JP (1) JPS6259039A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014124789A (en) * 2012-12-25 2014-07-07 Asahi Kasei Construction Materials Co Ltd Phenol resin foam laminate sheet and method for manufacturing the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6411783B2 (en) * 2014-06-18 2018-10-24 ケイミュー株式会社 Metal siding manufacturing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014124789A (en) * 2012-12-25 2014-07-07 Asahi Kasei Construction Materials Co Ltd Phenol resin foam laminate sheet and method for manufacturing the same

Also Published As

Publication number Publication date
JPH0225786B2 (en) 1990-06-05

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