JPS591255A - Continuous manufacture of sandwich panel - Google Patents

Continuous manufacture of sandwich panel

Info

Publication number
JPS591255A
JPS591255A JP57110451A JP11045182A JPS591255A JP S591255 A JPS591255 A JP S591255A JP 57110451 A JP57110451 A JP 57110451A JP 11045182 A JP11045182 A JP 11045182A JP S591255 A JPS591255 A JP S591255A
Authority
JP
Japan
Prior art keywords
foaming
synthetic resin
stock solution
rolls
thickness
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
JP57110451A
Other languages
Japanese (ja)
Other versions
JPS621825B2 (en
Inventor
若林 尭
浜口 健太郎
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.)
Toyo Tire Corp
Original Assignee
Toyo Tire and Rubber 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 Toyo Tire and Rubber Co Ltd filed Critical Toyo Tire and Rubber Co Ltd
Priority to JP57110451A priority Critical patent/JPS591255A/en
Publication of JPS591255A publication Critical patent/JPS591255A/en
Publication of JPS621825B2 publication Critical patent/JPS621825B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)

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】 コイル状薄肉金属板を圧延ロールを用いて圧延又は凹凸
形状に成形し、該薄肉金属板間にポリウレタンフォーム
のような発泡性合成樹脂を吐出発泡させる方法や、塩化
ビニル樹脂薄肉基材」二に発泡性ポリウレタン樹脂原液
を注入した後、裏面シートを介してローラーで発泡性ポ
リウレタン樹脂原液が発泡する前に基材全面に上記ウレ
タン樹脂原液の中央部が厚肉となるように押し拡げ、次
いで整形ローラーで発泡し始めたウレタン樹脂原液の厚
みを均一化した後、上下ダブルコンベヤーを用いて発泡
ウレタン樹脂を平担に発泡成形させる連続的発泡断熱板
の製造方法(特開昭56−144937号)は公知であ
る。
Detailed Description of the Invention: A method in which a coiled thin metal plate is rolled or formed into an uneven shape using a rolling roll, and a foamable synthetic resin such as polyurethane foam is discharged and foamed between the thin metal plates, and vinyl chloride After injecting the foamable polyurethane resin stock solution into the thin resin base material 2, before the foamable polyurethane resin stock solution is foamed by a roller through the back sheet, the central part of the urethane resin stock solution becomes thick on the entire surface of the base material. A method for producing a continuous foam insulation board (special method) in which the thickness of the urethane resin stock solution that has begun to foam is made uniform using a shaping roller, and then the foamed urethane resin is foam-molded into a flat layer using an upper and lower double conveyor. 144937/1983) is publicly known.

しかしながら、上下面材に凹凸形状を賦形した場合や側
部において上下面材端縁部が相対するような曲げ加工を
施されてサンドイッチパネルを連続的に成形する場合に
は、上下部組が若干の蛇行を生じても合成樹脂発泡体が
発泡硬化完了後では修正が不可能となるので、品質管理
上、」二下面材の蛇行防止は極めて重要な技術である。
However, when the top and bottom panels are formed into an uneven shape, or when the edges of the top and bottom panels are bent so that they face each other at the sides and a sandwich panel is continuously formed, the top and bottom assemblies are Even if slight meandering occurs, it cannot be corrected after the synthetic resin foam has completed foaming and hardening, so preventing meandering of the bottom surface material is an extremely important technique from the standpoint of quality control.

特に合成樹脂発泡性原液の発泡時には、まだ合成樹脂原
液は流動状態にあり、発泡圧により上面面材を浮き上ら
せようとする力が働くと同時に、側面方向に流れようと
する力も働くので、単に上下ロールやダブルコンベヤー
で加圧挟持させるだけの従来法では、微妙な上下面材の
ずれの発生を防止することができず、コンスタントに良
品を得ることか困難であった。特に最近は、一般住宅用
断熱材又は防音材としての用途が増加してきて、その要
求寸法公差も高度化してきて、厚みのバラツキ及び上下
面材の両端部におけるずれは±0.5mm以内に規格化
されるようになってきているが、従来法では±1.5m
+n ′P1.度のバラツキの発生は避けられなかった
。この対策としてダブルコンベヤ一部に側面位置を規制
するガイド装置を設ける手段を試みたが、上下面材が金
属板のような剛体の場合ガイド装置の異常摩耗を起した
り、極端なケースでは破損を招くなど問題解決には至ら
なかった。
In particular, when a synthetic resin foaming stock solution is foamed, the synthetic resin stock solution is still in a fluid state, and at the same time a force that tries to lift the top material due to the foaming pressure is exerted, there is also a force that tries to flow in the side direction. However, with the conventional method of simply pressurizing and clamping using upper and lower rolls or double conveyors, it was not possible to prevent the occurrence of subtle misalignment of the upper and lower surface materials, making it difficult to consistently obtain good quality products. Particularly recently, the use of heat insulating materials or soundproofing materials for general housing has increased, and the required dimensional tolerances have also become more sophisticated. However, in the conventional method, ±1.5m
+n'P1. The occurrence of variation in degree was unavoidable. As a countermeasure to this problem, we attempted to install a guide device on a part of the double conveyor to regulate the side position, but if the upper and lower surfaces are rigid bodies such as metal plates, the guide device may become abnormally worn, or in extreme cases, break. The problem could not be resolved by inviting

本願発明者等は種々検討を重ねてきたが、本願のような
剛性の高い面材を用いる連続生産システムにおいては、
発泡性合成樹脂原液が吐出された後まだ充分な流動性を
有する反応初期の間から、徐々に上下面材位置並びに厚
みを調す:曾しない限り、到底市場要求寸法規格を満足
させ得ないとの結論に達し鋭意検討を進めた結果、本願
発明を完成するに至ったものである。
The inventors of this application have made various studies, but in a continuous production system using a highly rigid surface material like the one used in this application,
After the foamable synthetic resin stock solution has been discharged, the position and thickness of the upper and lower surfaces are gradually adjusted from the early stage of the reaction when it still has sufficient fluidity. As a result of reaching this conclusion and proceeding with intensive studies, we have completed the present invention.

本願発明を図面により詳細に説明する。第1図の(1)
及び(1′)はそれぞれコイル状に巻かれた上面面材(
11)及び下面面材(11’)を送り出す供給装置であ
る。駆動装置は図示していないが、(11)と(11’
)とは同速で送り出せるように調整されている。面材送
り出し速度は合成樹脂発泡体の硬化速度によって最適速
度を選ぶ必要があるが、通り;(3〜]Om/分の範囲
が適当である。(21)と(21″)は、−[二下それ
ぞれの面材にテンションを15えると共に次の工程へ面
材を供給するためのガイドロールである。
The present invention will be explained in detail with reference to the drawings. (1) in Figure 1
and (1') are the upper surface material (
11) and a lower surface material (11'). Although the driving device is not shown, (11) and (11'
) is adjusted so that it can be sent out at the same speed. It is necessary to select the optimal speed for feeding the face material depending on the curing speed of the synthetic resin foam, but a range of (3 to] Om/min is appropriate. (21) and (21'') are -[ This is a guide roll that applies tension to each of the two lower facing materials and supplies the facing materials to the next process.

本願で用いられる」二下面材(11)及び(11’)は
薄板鋼板の他、ステンレス薄板、アルミニウム又はアル
ミニウム合金板、銅又は銅合金板、戒はこれらの複合板
等を用いることができる。その厚みは0.1.−10m
m、巾は200−2000mmのものが好適で、予めメ
ッキや塗装、印刷或は合成樹脂フィルムをラミネートし
たり、真空蒸着処理や酸化被膜形成処理を行ったものを
用いてもよい。
In addition to thin steel plates, the second lower surface materials (11) and (11') used in the present application may be stainless steel plates, aluminum or aluminum alloy plates, copper or copper alloy plates, or composite plates thereof. Its thickness is 0.1. -10m
It is preferable to have a width of 200 to 2000 mm, and it is also possible to use one that has been plated, painted, printed, laminated with a synthetic resin film, vacuum-deposited, or oxidized film-formed in advance.

(2)は薄肉金属製−上下面材の冷開成形装置を示し、
凹凸成形用ロール(22)、(22’ )、(23)、
(23’ )を複数組設けられている。これらの成形ロ
ールにより薄肉金属板は所望形状に成形される。第1図
では冷開成形用ロールは各々2組ずつしか示されていな
いが、所望形状により適宜組数は増減すればよい。尚、
凹凸形状を面材に設ける必要がない場合にはIPに平ロ
ールを用いて一ヒ下面材を貼に圧延するだけでよい。
(2) shows a cold-open forming device for thin-walled metal top and bottom materials;
Rolls for unevenness forming (22), (22'), (23),
A plurality of sets of (23') are provided. These forming rolls form the thin metal plate into a desired shape. Although only two sets of cold-open forming rolls are shown in FIG. 1, the number of sets may be increased or decreased as appropriate depending on the desired shape. still,
If it is not necessary to provide the surface material with an uneven shape, it is sufficient to simply roll the bottom surface material into sheets using a flat roll for IP.

(3)は発泡性合成樹脂原液の吐出口である。図示して
いないが、原液供給タンクより発泡性合成樹脂原液がメ
ータリングされて所望社管送される設備に連結されてい
る。その混合機構は、合成樹脂の種類により公知のもの
が選択される。この吐出口(3)は1個だけ用いて、面
材幅だけ面材進行方向に直角方向に水平にトラバースさ
せてもよく、又、吐出口を複数個並列に設置して静止状
態で発泡性合成樹脂原液をスプレーさせるようにしても
よい。本願で用いられる発泡性合成樹脂としては、ポリ
ウレタンフォー11、フェノールフォー11、ポリイミ
ドフオーム、ユリアフォームのような原料が液体の熱硬
化性合成胡脂発泡体である。発泡体の厚みは特に制限は
ないが、5〜100 m / +nの範囲が望ましい。
(3) is a discharge port for the foamable synthetic resin stock solution. Although not shown, the stock solution supply tank is connected to equipment where the foamable synthetic resin stock solution is metered and piped to a desired company. A known mixing mechanism is selected depending on the type of synthetic resin. Only one outlet (3) may be used to horizontally traverse perpendicular to the advancing direction of the panel by the width of the panel, or multiple outlets may be installed in parallel to allow foaming in a stationary state. Alternatively, a synthetic resin stock solution may be sprayed. The foamable synthetic resin used in the present application is a thermosetting synthetic sesame foam whose raw material is liquid, such as polyurethane foam 11, phenol foam 11, polyimide foam, and urea foam. The thickness of the foam is not particularly limited, but is preferably in the range of 5 to 100 m/+n.

ロール(24)は上面面材をレギュレーター装置(5)
へ送るためのガイドロールである。(4)は上下面材の
蛇行を防止するための側端部位置調整用ガイドロールで
ある。第1図ではレギュレーター装置(5)の入口部に
設けているが、この位置はレギュレーター装置の中央部
又は出口部に設けてもよく、又1組だけでなく、適宜複
数組設置してもよい。
The roll (24) has a regulator device (5) for the upper surface material.
It is a guide roll for sending to. (4) is a guide roll for side edge position adjustment to prevent meandering of the upper and lower surface materials. Although it is provided at the inlet of the regulator device (5) in Fig. 1, it may be provided at the center or outlet of the regulator device, and it may be installed not only in one set but also in multiple sets as appropriate. .

又上下面材のいずれか一方、又は両方に長手方向に一定
幅の凹凸が設けられるような場合には、レギュレーター
装置(5)に入る手前で上下一対のロールを設置し、面
材の凹凸位置に対応する位置に凹形状の場合はこれに嵌
合可能な凸形状の、又凸形状の場合は、これに嵌合可能
な凹形状のガイド用リングを設けて側端部ガイドロール
と共働するよう、にしてもよい。この場合の上下部ガイ
ド用リングは面材に形成された凹凸帳より0.’5m/
+n程度の余裕をもたせるようにするのが望ましい。
In addition, if unevenness of a certain width is provided in the longitudinal direction on one or both of the upper and lower surface materials, a pair of upper and lower rolls is installed before entering the regulator device (5), and the uneven position of the surface material is adjusted. In the case of a concave shape, a convex guide ring that can be fitted into the concave shape is provided at a position corresponding to the concave shape, and in the case of a convex shape, a concave guide ring that can be fitted to the guide ring is provided to cooperate with the side end guide roll. You may choose to do so. In this case, the upper and lower guide rings are 0.0 mm from the uneven surface formed on the surface material. '5m/
It is desirable to have a margin of about +n.

しちヤーター装置(5)は、下面面材上に吐出された発
泡性合成樹脂原液が泡化反応の進行によって厚みが次第
に増大していくのに対応して、上下ロール間隔が広くす
るように配設されている複数対のロールからなっている
。図示していないが、複数対の各ロール間隙は、可変で
きる調整機構がとりつけられている。複数対のそれぞれ
のロール間隙は、用いる合成樹脂発泡体の発泡時の立上
り速度とコンベヤー速度とによって求められる発泡曲線
によって定められるが、通常この発泡曲線の最も厚い部
位と最も薄い部位との中間厚み近傍に設定されるのが望
ましい。この発泡初期段階で泡化物質を余り加圧しすぎ
ると形成される泡が偏平状になり、最終発泡成形体の耐
圧強度等の特性に余り良い結果を与えないので注意する
必要がある。
The Shichiyater device (5) is designed to widen the gap between the upper and lower rolls in response to the gradual increase in thickness of the foamable synthetic resin stock solution discharged onto the lower surface material as the foaming reaction progresses. It consists of multiple pairs of rolls arranged. Although not shown, each of the plurality of pairs of roll gaps is equipped with an adjustment mechanism that can vary the gap. The gap between each of the plurality of pairs of rolls is determined by a foaming curve determined from the rise speed of the synthetic resin foam used and the conveyor speed, and is usually determined by the intermediate thickness between the thickest and thinnest regions of this foaming curve. It is desirable to set it nearby. Care must be taken because if the foamed material is pressurized too much at this initial stage of foaming, the foam formed will become flat, which will not give very good results to the properties such as pressure resistance of the final foamed molded product.

レギュレーター装置部の長さは、前記発泡性合成樹脂の
発泡初期から発泡反応が終って最高高さになる迄の間と
するのが望ましく、硬質ポリウレタンフォームの場合反
応の早い系では2m、遅い系では10m程度である。レ
ギューターロールの組数は第1図では7組の例を示した
が、反応速度に応じて適宜増減すればよい。一般に反応
速度が早い程前後のロール設置間隔は小さくすることが
望ましいが通常30〜300mm間隔の範囲が選択され
る。レギュレーターロールの径も特に制限はないが、2
5〜250n+n+ψ の範囲が適当である。このレギ
ュレーターロール間を発泡性合成樹脂と上下面材が通過
する間に強固に互いに接着される。
The length of the regulator unit is preferably from the initial stage of foaming of the foamable synthetic resin until the maximum height is reached after the foaming reaction is completed; in the case of rigid polyurethane foam, it is 2 m for fast reaction systems, and 2 m for slow reaction systems. It is about 10m. Although seven sets of regulator rolls are shown as an example in FIG. 1, the number of regulator rolls may be increased or decreased as appropriate depending on the reaction rate. Generally, it is desirable that the faster the reaction speed is, the smaller the distance between the front and rear rolls is, and usually a range of 30 to 300 mm is selected. There is no particular limit to the diameter of the regulator roll, but 2
A range of 5 to 250n+n+ψ is appropriate. While the foamable synthetic resin and the upper and lower surface materials pass between the regulator rolls, they are firmly adhered to each other.

(6)は上下−組の等速で作動するコンベアーで、はぼ
発泡反応の完了した面材付き合成樹脂発泡体を加熱硬化
室(7)へ搬送すると共に、最終的に製品厚みを調整す
るための加圧の役目をもっている。
(6) is a set of upper and lower conveyors that operate at a constant speed, and conveys the synthetic resin foam with face material that has undergone the foaming reaction to the heat curing chamber (7), and finally adjusts the thickness of the product. It has the role of pressurizing.

この上下のダブルコンベヤーも上下間隔を適宜調節する
ための補助装置を備えている。(図示していない)コン
ベアーの材質はスチール製のスチールコンベヤーが用い
られているが、加圧できる機能があれば、ゴム又はスチ
ールベルトコンベヤーであってもよい。スチールコンベ
ヤーの場合、騒音と摩耗を防止するため、ゴム又はウレ
タンのような樹脂ライニングを施して用いるのが望まし
N。
This upper and lower double conveyor is also equipped with an auxiliary device to appropriately adjust the upper and lower distances. As for the material of the conveyor (not shown), a steel conveyor is used, but a rubber or steel belt conveyor may be used as long as it has a function of pressurizing. In the case of steel conveyors, it is desirable to use a rubber or resin lining such as urethane to prevent noise and wear.

厚みを最終的に調整された面材付き合成樹脂発泡体は、
ダブルコンベヤーに近接して設けられた加熱硬化室(7
)へ導かれる。この加熱硬化室内で合成樹脂発泡成形体
は50〜150℃好ましくは60〜100℃で2〜3分
間加熱されて合成樹脂発泡体の硬化反応を実質的に完了
させる。硬化が完了した長尺サンドイッチ状の合成樹脂
発泡成形体は、加熱硬化室に続いて設けられた裁断機(
8)によって所望長さに切断されて最終製品であるサン
ドインチパネル(12)に仕上げられる。
The synthetic resin foam with a face material whose thickness has been finally adjusted is
Heat curing chamber (7) installed near the double conveyor
). In this heat curing chamber, the synthetic resin foam molding is heated at 50 to 150°C, preferably 60 to 100°C, for 2 to 3 minutes to substantially complete the curing reaction of the synthetic resin foam. After curing, the long sandwich-shaped synthetic resin foam molded product is cut into a cutting machine (
8) is cut to a desired length to produce a final product, a sand inch panel (12).

実施例 コイル状に巻かれた厚さ0.27mm、中1.000m
mの鋼板を上面面材とし、厚さ0.27m/+n、 I
ll 930m/mの鋼板を下面面材にして上下法り出
し装置より、それぞれ5m/分の速度で送り出し、第2
図及び第3図に示したように上面面材は2条の凹みと端
部折り曲げ形成できるよう上面面材冷開成形用ロールを
、又下面面材は単に平板状に圧延しながら端部のみ祈り
曲げ成形し得るよう下面面材成形用ロールを配設して上
下面材加工を行った。次いで第1表に示した配合処方の
硬質ポリウレタンフォーム用原液を混合撹拌と同時に下
面面材上に1.500g/分の吐出量で吐出させた。こ
の場合、吐出用ノズルは成形幅900mm間を往復させ
るようにした。又、側端部位置調整用ガイドロールはレ
ギュレーター装置入口部のみに設けるようにした。
Example: coiled, thickness 0.27mm, medium 1.000m
m steel plate is used as the top surface material, thickness 0.27 m/+n, I
ll A 930 m/m steel plate is used as the bottom surface material and is sent out from the upper and lower bending devices at a speed of 5 m/min, respectively.
As shown in the figure and Fig. 3, the upper surface material is formed by cold-open forming rolls so that the upper surface material can be formed with two recesses and the edges are bent, and the lower surface material is simply rolled into a flat plate and only the ends are formed. The upper and lower surfaces were processed by installing rolls for forming the lower surfaces so that they could be bent and formed. Next, a stock solution for rigid polyurethane foam having the formulation shown in Table 1 was mixed and stirred and simultaneously discharged onto the lower surface material at a discharge rate of 1.500 g/min. In this case, the discharge nozzle was made to reciprocate over a molding width of 900 mm. Further, the guide roll for adjusting the side end position is provided only at the inlet of the regulator device.

第1表に示したライズタイム45秒と、サンドイッチパ
ネルの最終厚み18n+n+、コンベヤー速度5n1/
分より計算して、発泡開始から最終厚みに達する迄にコ
ンベヤーは3.75m進行することとなることから25
m/mψの鋼製レギュレーターロールの発泡初期部分に
おける上下ロール間隙を7 m / mに発泡最終段階
で18m/u+間隙とし1合計上下それぞれ12組のロ
ールを1mrnずつロール間隙を広げるよ1うにして配
設した。加熱硬化室の温度は60℃に調節し、実質的に
硬化完了したサンドインチ状発泡成形体は1 ’380
 m m長さに裁断機で切断された。得られたサンドイ
ンチパネルは厚さ18.]m/m、rll 9 ] 8
+n/ m、長さ1083m/mのもので、上下面材の
端縁部は僅かに±0.2m/mの段差が生じたのみで目
標許容差±0.5m / mに対して充分合致するもの
であった。
The rise time shown in Table 1 is 45 seconds, the final thickness of the sandwich panel is 18n+n+, and the conveyor speed is 5n1/
The conveyor will travel 3.75m from the start of foaming to the final thickness, calculated from 25 minutes.
The gap between the upper and lower rolls of the m/mψ steel regulator roll at the initial stage of foaming is set to 7 m/m, and the gap between the upper and lower rolls is increased to 18 m/u+ at the final stage of foaming. It was arranged as follows. The temperature of the heat curing chamber was adjusted to 60°C, and the sandwich-shaped foam molded product that had been substantially cured had a temperature of 1'380.
It was cut into lengths of mm using a cutting machine. The resulting sandwich panel has a thickness of 18. ] m/m, rll 9 ] 8
+n/m, length 1083m/m, there was only a slight step difference of ±0.2m/m at the edge of the upper and lower surface materials, which fully matched the target tolerance of ±0.5m/m. It was something to do.

実施例の結果にみられるように、本願発明は発泡性合成
樹脂原液の発泡開始直後から発泡立上り完了迄の間1発
泡立上り速度とコンベヤー進行速度及び最終厚みとより
得られる発泡曲線に基づいて発泡状混合物の最大厚み部
と最小厚み部とのほぼ中間の厚みとなるよう小きざみに
ロール間隙を漸増連設することによって発泡圧に対して
相対的に微弱な圧をかけて厚みの調整を図ると共に、側
端部位置調整用ガイドロールを発泡段階のまだ流動状態
にある段階において併用することにより。
As can be seen in the results of the examples, the present invention performs foaming from immediately after the start of foaming of the foamable synthetic resin stock solution until the completion of foaming based on the foaming curve obtained from the foaming rise speed, conveyor advancement speed, and final thickness. The thickness is adjusted by gradually increasing the gap between the rolls in small increments so that the thickness is approximately halfway between the maximum thickness and minimum thickness of the mixture, thereby applying a weak pressure relative to the foaming pressure. At the same time, a guide roll for side edge position adjustment is used in combination at the foaming stage, which is still in a fluid state.

極めて簡単な装置で寸法調整が可能となり、且っ側端部
上下面材のずれによる段差を著しく小さくし得たもので
ある。側端部段差が大きくなった場合、家屋や工場建屋
の断熱・防音材のような取付相手との寸法精度が要求さ
れる用途では不良品として廃棄する以外使用できなくな
るが、本願発明の方法により製造することによって著し
く寸法精度が向上し、収率向上に大きな効果が得ること
ができる極めて有用な技術である。
Dimensions can be adjusted with an extremely simple device, and the difference in level caused by misalignment of the upper and lower surface materials at the side ends can be significantly reduced. If the side edge level difference becomes large, the product cannot be used other than being discarded as a defective product in applications that require dimensional accuracy with respect to the mounting partner, such as insulation and soundproofing materials for houses and factory buildings. However, the method of the present invention This is an extremely useful technique that can significantly improve dimensional accuracy and greatly improve yield.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本願発明の製造方法の一連の流れを示す側面図
、第2図は本願発明によって得られたサンドインチパネ
ルの一実施例の斜視図、第3図はそのx−x’断面図、
第4図は本願発明の他の実施例を示す断面図である。 (3)−−−一発泡性合成樹脂原液吐出口(4)−−−
一側端部位置調整用ガイドロール(5)−−−−レギュ
レーターロール (6)−−−−ダブルコンベヤー (7)−−−一加熱硬化室 (8)−−−一裁断機 (11) 、 (11’)−−−一上下面材・、  (
12’)−−−−サンドイッチパネル(22)、(22
’)、(23)、(23’)−−−一冷間成形用ロール
特許出願人 東洋ゴム工業株式会社
Fig. 1 is a side view showing a series of steps in the manufacturing method of the present invention, Fig. 2 is a perspective view of an embodiment of the sandwich panel obtained by the present invention, and Fig. 3 is a cross-sectional view taken along line xx'. ,
FIG. 4 is a sectional view showing another embodiment of the present invention. (3) --- Monofoaming synthetic resin stock solution outlet (4) ---
One side end position adjustment guide roll (5)---Regulator roll (6)---Double conveyor (7)---One heating curing chamber (8)---One cutting machine (11), (11') --- Upper and lower surface materials・, (
12') ---- Sandwich panel (22), (22
'), (23), (23') --- Cold forming roll patent applicant Toyo Rubber Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] 上下2組の冷間加工可能な面材を圧延しながら所望形状
に成形し、上下面材間に発泡性合成樹脂原液を吐出させ
て連続的にサンドイッチパネルを製造する方法において
吐出された発泡性合成樹脂原液の発泡開始直後から発泡
反応が終了する迄の間を上下複数対からなるレギュレー
ターロール及び少くとも1組の側部部蛇行防止用ロール
を併用することにより厚み並びに側端部寸法を調整する
ことを特徴とするサンドインチパネルの連続製造方法
The foaming property discharged in a method of continuously manufacturing sandwich panels by forming two sets of upper and lower cold-workable face materials into a desired shape while rolling, and discharging a foamable synthetic resin stock solution between the upper and lower face materials. The thickness and side edge dimensions are adjusted by using regulator rolls consisting of multiple upper and lower pairs and at least one set of side meandering prevention rolls from immediately after the foaming of the synthetic resin stock solution starts until the foaming reaction ends. A continuous manufacturing method for sand inch panels characterized by:
JP57110451A 1982-06-25 1982-06-25 Continuous manufacture of sandwich panel Granted JPS591255A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57110451A JPS591255A (en) 1982-06-25 1982-06-25 Continuous manufacture of sandwich panel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57110451A JPS591255A (en) 1982-06-25 1982-06-25 Continuous manufacture of sandwich panel

Publications (2)

Publication Number Publication Date
JPS591255A true JPS591255A (en) 1984-01-06
JPS621825B2 JPS621825B2 (en) 1987-01-16

Family

ID=14536046

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57110451A Granted JPS591255A (en) 1982-06-25 1982-06-25 Continuous manufacture of sandwich panel

Country Status (1)

Country Link
JP (1) JPS591255A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6030559A (en) * 1997-02-14 2000-02-29 Celotex Corporation Method for the continuous manufacture of plastic foam

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5226779A (en) * 1975-08-25 1977-02-28 Nomura Seiichi Dust incinerator
JPS5366969A (en) * 1976-11-27 1978-06-14 Kurashiki Boseki Kk Production of sandwich panel
JPS55164132A (en) * 1979-06-08 1980-12-20 Kanto Chiyuuo:Kk Method and apparatus for producing lightweight foamed polyurethane panel

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5226779A (en) * 1975-08-25 1977-02-28 Nomura Seiichi Dust incinerator
JPS5366969A (en) * 1976-11-27 1978-06-14 Kurashiki Boseki Kk Production of sandwich panel
JPS55164132A (en) * 1979-06-08 1980-12-20 Kanto Chiyuuo:Kk Method and apparatus for producing lightweight foamed polyurethane panel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6030559A (en) * 1997-02-14 2000-02-29 Celotex Corporation Method for the continuous manufacture of plastic foam

Also Published As

Publication number Publication date
JPS621825B2 (en) 1987-01-16

Similar Documents

Publication Publication Date Title
EP0032624A1 (en) Apparatus and method for the continuous manufacture of foam board
KR20130133829A (en) Method and device for applying liquid reaction mixtures to a cover layer
US4255105A (en) Equipment for the continuous production of foam boards
US7842151B2 (en) Method and device for forming a layered product having a bent over edge
JPS591255A (en) Continuous manufacture of sandwich panel
US3644606A (en) Process for the manufacture of foam slabs
DK169836B1 (en) Process and production equipment for the manufacture of phenolic foam plastic laminates
US5817260A (en) Method of using a heated metering device for foam production
EP0021564B1 (en) Apparatus for the continuous manufacture of foam board
KR20190012375A (en) Urethane foam board manufacturing apparatus
KR102438331B1 (en) Foaming application apparatus in continuous building assembly pannel prodution line
JPH01120314A (en) Apparatus for preparing composite panel
JP2717284B2 (en) Insulation panel manufacturing method
JPH0796277B2 (en) Continuous manufacturing method and device for composite building panel
JPS63199618A (en) Manufacturing device for composite plate of phenolic resin foam
JP2561576B2 (en) Thermosetting resin foam board manufacturing equipment
JP2008238553A (en) Sandwich panel manufacturing equipment and sandwich panel manufacturing process
JP2008265022A (en) Production equipment for rigid polyurethane slab and production method thereof
JPH0357452Y2 (en)
JP6406669B2 (en) Sandwich panel manufacturing method and sandwich panel
JP2577057B2 (en) Manufacturing method of composite board
KR900004786B1 (en) A device for the preparing complex sheet
JPH1024431A (en) Rigid urethane pouring method for continuous production
JPH01204739A (en) Production of composite panel
JPH0216037A (en) Manufacture of resin-impregnated mat laminated foam