JPS58173656A - Continuous manufacture of foamed body packed panel - Google Patents

Continuous manufacture of foamed body packed panel

Info

Publication number
JPS58173656A
JPS58173656A JP57056328A JP5632882A JPS58173656A JP S58173656 A JPS58173656 A JP S58173656A JP 57056328 A JP57056328 A JP 57056328A JP 5632882 A JP5632882 A JP 5632882A JP S58173656 A JPS58173656 A JP S58173656A
Authority
JP
Japan
Prior art keywords
foam
panel
filled
surface treatment
injection
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
JP57056328A
Other languages
Japanese (ja)
Other versions
JPH0372462B2 (en
Inventor
北原 幹夫
藤井 幸成
石岡 忠司
長岡 宗男
泉田 正市
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP57056328A priority Critical patent/JPS58173656A/en
Publication of JPS58173656A publication Critical patent/JPS58173656A/en
Publication of JPH0372462B2 publication Critical patent/JPH0372462B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Laminated Bodies (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (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】 本発明は発泡機より吐出後は殆んど体積膨張のない発泡
体を充填したパネルの連続的な製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for continuously manufacturing panels filled with a foam that exhibits almost no volumetric expansion after being discharged from a foaming machine.

従来、発泡体を充填したパネルとしては合成樹脂、たと
えばウレタン、イソシアヌレート、ユリア、フェノール
等に加熱又は減圧により気体となり体積膨張を起こす液
状発泡剤、代表的にはフレオンやブタン等を使用した発
泡体を充填したパネルが断熱性、防音性にすぐれること
から建築物、冷蔵庫等に広く利用されてきた。
Conventionally, foam-filled panels have been made using synthetic resins such as urethane, isocyanurate, urea, phenol, etc., and liquid foaming agents that turn into gas and expand in volume when heated or under reduced pressure, typically freon or butane. The panels filled with the body have excellent heat insulation and soundproofing properties, so they have been widely used in buildings, refrigerators, etc.

これらのパネルは発泡体原料をパネルに注入後発泡させ
るため、開放方式は困難であり、はぼ密閉されたパネル
に注入する方式が取られているが。
Since these panels are made by injecting the foam raw material into the panel and then foaming it, it is difficult to use an open method, so a method is used in which the material is injected into a nearly sealed panel.

かかる方法では、パネル温度により発泡倍率が異なって
くる為に、未充填部分を発生し易く、しかもパネルがほ
ぼ密閉されている為未充填部分の発見がしに<<、後で
は補修がむずかしい為、不完全なる充填、即ち、未充填
部分のある断熱パネルが製造される結果を生じる。たと
えば、図−2の如くパネル内部が中枠により、升目状に
分割されている構造のパネルに発泡体を注入する方法は
、外枠に上下面材が接着された状態で外枠に設けられた
注入口より発泡体原料を注入して発泡、固化される。ま
たは、上下面材のどちらか一方が接着されていない場合
においても、面材に代わる押え蓋を取シつけ、外枠ない
しは押え蓋に設けられた注入口より注入するものである
が、発泡圧によるパネル面材のフクレを防止するために
パネル上下面を押える必要がある。またこの発泡圧を除
去するために空気抜きのための穴を設けることと、注入
終了後、注入口より、発泡体の逆流漏出を防ぐための治
具が必要である。又、注入された発泡体で順次、升目が
充填されてゆく様に中枠に適当な大きさ及び配列で切り
欠きを設ける必要がある等、生産性の低下につながる欠
点がある。更に、この升目は、その空間容積がパネルに
よって、また一枚のパネルの中でも異なるため、発泡体
の注入量、密度のコントロールが非常に困難であり、未
充填部分が発生し易い。しかも発泡体充填状態の確認が
、上下面材、或いは押さえ蓋がある為に、充填作業中に
おいては不可能でおり、未充填部が発生した場合の補修
が不可能、或いは困難であり実用上生産に供しにくい。
With this method, the expansion ratio varies depending on the panel temperature, which tends to cause unfilled areas, and since the panel is almost sealed, it is difficult to discover unfilled areas, and it is difficult to repair them later. , resulting in incomplete filling, ie, insulation panels being produced with unfilled areas. For example, a method of injecting foam into a panel with a structure in which the interior of the panel is divided into squares by an inner frame as shown in Figure 2 is to inject foam into a panel with upper and lower panels adhered to the outer frame. The foam raw material is injected through the injection port, and is foamed and solidified. Alternatively, even if either the upper or lower surface materials are not bonded, a presser cover may be installed in place of the surface material, and the injection can be made from the injection port provided on the outer frame or the presser cover, but the foaming pressure It is necessary to press the top and bottom of the panel to prevent the panel surface material from blistering. In addition, it is necessary to provide a hole for air vent to remove this foaming pressure, and to provide a jig to prevent the foam from leaking back through the injection port after injection is completed. In addition, there are drawbacks that lead to a decrease in productivity, such as the need to provide cutouts of appropriate size and arrangement in the inner frame so that the cells are sequentially filled with the injected foam. Furthermore, since the spatial volume of these squares varies from panel to panel and even within a single panel, it is very difficult to control the injection amount and density of the foam, and unfilled portions are likely to occur. Moreover, it is impossible to check the foam filling state during the filling process because of the upper and lower surface materials or the holding lid, and if an unfilled area occurs, it is impossible or difficult to repair it, which is impractical. Difficult to use in production.

本発明者は、かかる従来法の欠点を解消する方法として
発泡機より吐出後は殆んど体積膨張の無い発泡体による
パネルの充填方法について、鋭意検討して来たが、密閉
方式では従来法の持つ、低生産性、不良パネルの発生等
の欠点を完全には解消出来ない。又発泡機より吐出後光
んど体積膨張のない発泡体は、発泡が安定し一定の密度
の発泡体が得られる迄に時間が掛かり、断続的注入では
、管理が煩雑で密度等の品質管理がむずかしく、従って
片方の面材を取り付は閉蓋する前の段階、すなわちパネ
ルの片面が開放状態で発泡体を充填することにより連続
的に生産することで従来法の欠点を解消することが出来
ることを発見し、本発明を完成した。
The present inventor has intensively studied a method of filling panels with foam that hardly expands in volume after being discharged from a foaming machine as a way to overcome the drawbacks of the conventional method. It is not possible to completely eliminate the disadvantages of low productivity, generation of defective panels, etc. In addition, for foams that do not expand in volume after being discharged from a foaming machine, it takes time to stabilize the foaming and obtain a foam with a constant density, and with intermittent injection, management is complicated and quality control such as density is difficult. Therefore, it is possible to solve the drawbacks of the conventional method by continuously producing one side of the panel by filling it with foam while one side of the panel is open, before the panel is closed. He discovered what could be done and completed the present invention.

すなわち、本発明は生産性が向上し、品質のよい発泡体
充填パネルの連続生産方法で、発泡機より吐出後は、殆
んど体積膨張のない発泡体に適用できるものであり、そ
の代表的なものは、発泡剤として空気を用い、通常メカ
ニカルフロス発泡機又はオークス型連続ミキサー等と呼
ばれる混合機(特願昭56−138604号、特公昭4
0−17143号)に発泡体主剤と硬化剤と空気を混合
し、空気を樹脂中に均一に分散して含泡状態となし、メ
カニカルクロス発泡機キリ吐出せしめて、その後硬化が
進み発泡体が形成されるごときものである。
That is, the present invention is a method for continuous production of foam-filled panels with improved productivity and high quality, and can be applied to foams with almost no volumetric expansion after being discharged from a foaming machine. This type uses air as a foaming agent and is usually manufactured by a mixing machine called a mechanical floss foaming machine or an Oaks type continuous mixer (Japanese Patent Application No. 138604/1986, Japanese Patent Publication No. 4
No. 0-17143), the foam main agent, curing agent, and air are mixed, the air is uniformly dispersed in the resin to form a foamed state, and the foam is discharged through a mechanical cloth foaming machine. It is like being formed.

発泡体主剤としては、尿素樹脂原料の他、フェノール樹
脂等の樹脂原料がちり、硬化剤としては樹脂の種類によ
っても異るが、尿素樹脂原料の場合には、酸性水溶液、
たとえば塩酸、硫酸、シん酸、しゆう酸、パラトルエン
スルホン酸、それらの塩、酸無水物の水溶液などがある
In addition to the urea resin raw material, the foam main agent includes dust from resin raw materials such as phenol resin, and the hardening agent varies depending on the type of resin, but in the case of the urea resin raw material, acidic aqueous solution,
Examples include aqueous solutions of hydrochloric acid, sulfuric acid, cynic acid, oxalic acid, para-toluenesulfonic acid, salts thereof, and acid anhydrides.

発泡体主剤又は硬化剤には、この他に界面活性剤、気泡
安定剤、粘度調整剤などの通常使用される添加剤の含ま
れることがある。
The foam base agent or curing agent may also contain commonly used additives such as surfactants, foam stabilizers, and viscosity modifiers.

このような発泡体主剤の例としては、粘度550センチ
ボイズ、不揮発分68%の尿素樹脂初期縮合物100重
量部に対して水35重量部、アルキルジフェニルエーテ
ルジスルフォン酸ソーダ2重i部を加えて粘度50セン
チボイズとした樹脂液がある。
An example of such a foam base agent is to add 35 parts by weight of water and 2 parts by weight of sodium alkyl diphenyl ether disulfonate to 100 parts by weight of a urea resin initial condensate having a viscosity of 550 centiboise and a non-volatile content of 68%. There is a resin liquid with a 50 centimeter void.

この樹脂液と硬化液とを重量比100738の流量で前
記メカニカルフロス発泡機(たとえば東邦機械工業■製
、東邦TM−302型)に注入し、また、圧縮空気を注
入口より注入し、内圧を3.5〜4.5Kp/cm2に
保ち、発泡機の回転子は450rpmの回転数で回転す
る。得られた含泡状混合物を発泡機吐出ノズルよりパネ
ルに充填する。
This resin liquid and curing liquid were injected into the mechanical floss foaming machine (for example, Toho TM-302 model manufactured by Toho Kikai Kogyo ■) at a flow rate of 100,738 by weight, and compressed air was injected from the injection port to reduce the internal pressure. It is maintained at 3.5 to 4.5 Kp/cm2, and the rotor of the foaming machine rotates at a rotation speed of 450 rpm. The obtained foam-containing mixture is filled into a panel through a foaming machine discharge nozzle.

本発明における発泡体充填パネルは連続製造により生産
される。この工程を第1図に示し説明する。
The foam-filled panels of the present invention are produced by continuous manufacturing. This process is shown and explained in FIG.

まず、パネルlが、ベルトコンベア2の上に整列され、
矢印Aの方向に搬送される。パネルlu第2図に示すご
とき木製枠組の下片面に面材を接着剤で貼合わせ、スタ
ッカー等で仮止めしたもので、充填に供されるために、
ベルト上に整列される。ついでパネル1には、発泡体注
入装置3の注入ノズル4から吐出された発泡体が充填さ
れる。
First, the panels l are arranged on the belt conveyor 2,
It is transported in the direction of arrow A. A panel lu is a wooden frame shown in Figure 2 with a panel pasted on one side of the bottom with adhesive and temporarily fixed with a stacker, etc. In order to be used for filling,
aligned on the belt. The panel 1 is then filled with foam discharged from the injection nozzle 4 of the foam injection device 3.

発泡体は図外のメカニカルフロス発泡機で製造され注入
ノズル4に至る。パネル1内部に発泡体未充填がないよ
う、吐出ノズル4はエアシリンダ5を用いて上下、前後
、に移動可能なものとなっている。中枠8及び外枠9の
位置は光電センサー、リミノトスインチ等で検出される
。充填をより完全にするため、ベルトコンベア2の搬送
速度を変化させてもよい。このような吐出ノズル4を用
いることにより、パネルの形状が変化しても正確な注入
が可能である。
The foam is manufactured by a mechanical floss foaming machine (not shown) and reaches the injection nozzle 4. The discharge nozzle 4 is movable up and down and back and forth using an air cylinder 5 so that the inside of the panel 1 is not filled with foam. The positions of the inner frame 8 and outer frame 9 are detected by a photoelectric sensor, a riminotoschi, or the like. To achieve more complete filling, the conveying speed of the belt conveyor 2 may be varied. By using such a discharge nozzle 4, accurate injection is possible even if the shape of the panel changes.

ついでパネル1は、発泡体ならしベルト11と表面処理
ブラシ12からなる表面処理装置13により処理される
。発泡体はパネルに105〜115%程度過剰に注入さ
れ、この余剰発泡体を排除するため、スチールあるいは
プラスチックのエンドレスの発泡体ならしベル)11を
比較的低速、たとえば1〜3m/分でパネル上を矢印C
の方向(左回転)に走行させる。発泡体ならしベルト1
1とパネル1との位置関係は、次の要件を満足させるこ
とが望ましい。すなわち第3図におけるθ□−50〜8
00、好ましくは60〜70°であり、80°超では発
泡体の枠外排出がスムーズに行われず、50°未満では
装置が大きくなり好ましくない。又第4図におけるθ。
The panel 1 is then treated by a surface treatment device 13 comprising a foam leveling belt 11 and a surface treatment brush 12. The foam is over-injected into the panel by about 105-115%, and to remove this excess foam, the panel is heated with an endless steel or plastic foam leveling bell (11) at a relatively slow speed, e.g. 1-3 m/min. Up arrow C
Run in the direction of (clockwise rotation). Foam leveling belt 1
It is desirable that the positional relationship between the panel 1 and the panel 1 satisfies the following requirements. That is, θ□-50 to 8 in Fig. 3
00°, preferably 60 to 70°; if it exceeds 80°, the foam cannot be discharged out of the frame smoothly, and if it is less than 50°, the device becomes large, which is not preferable. Also, θ in FIG.

=40〜80°、好ましくは50〜70°であり、50
0未満では、余剰発泡体の押えかきとりが円滑に行われ
ず、80°超では、ベルトのリターン側7、特に内部に
発泡体が付着し、ベルトが蛇行するなど、操業トラブル
の原因となる。なお、発泡体ならしベルトに発泡体を残
さないため、高速回転するプラスチック製の一対の除去
ブラシ14で、発泡体ならしベルトを挟設する。
=40 to 80°, preferably 50 to 70°, and 50
If the angle is less than 0, excess foam will not be smoothly scraped off, and if it exceeds 80 degrees, the foam will adhere to the return side 7 of the belt, especially the inside, causing operational troubles such as meandering of the belt. In order to avoid leaving any foam on the foam leveling belt, the foam leveling belt is sandwiched between a pair of plastic removal brushes 14 that rotate at high speed.

ついで表面処理のため高速回転するプラスチック製処理
ブラシ12にょシ発泡体をパネル表面から1 % 4 
mの深さまでかきとり、又枠上面に付着した発泡体を除
去する。この処理工程は閉蓋する際には、接着剤中への
発泡体混入による接着性低下を防止する効果もある。処
理ブラシ12の好ましい仕様は、ブラシ芯径60〜80
MLφ、植毛材はナイロンあるいはポリプロピレンで太
すo、4〜0.7mφ、植毛材長30〜40%、又ブラ
シの外周速度は200〜800 m 7分の範囲である
。ブラシによるがきとり処理に先立ち、かき取りを円滑
に糾うため発泡体の表面を深さ3〜10111程度固化
するため表面固化装置16、たとえば遠赤外線ランプ、
熱風エヤーナイフ、あるいはマイクロ波発生装置をパネ
ル上に配設し通過させてもよい。又、パネル押えロール
17はパネルの上下への変動を止め、処理ブラシ12と
パネルlとの間隔を一定に保つ様にする。
Next, for surface treatment, a plastic treatment brush 12 that rotates at high speed removes 1% of the foam from the panel surface.
Scrape to a depth of m and remove foam adhered to the top surface of the frame. This treatment step also has the effect of preventing deterioration of adhesiveness due to foam mixed into the adhesive when the lid is closed. The preferred specifications for the treated brush 12 are a brush core diameter of 60 to 80 mm.
MLφ, the flocking material is made of nylon or polypropylene, the diameter is 4 to 0.7 mφ, the length of the flocking material is 30 to 40%, and the peripheral speed of the brush is in the range of 200 to 800 m 7 minutes. Prior to the scraping process using a brush, a surface hardening device 16, such as a far-infrared lamp, is used to harden the surface of the foam to a depth of about 3 to 10111 mm to ensure smooth scraping.
A hot air knife or microwave generator may be placed on and passed through the panel. Further, the panel presser roll 17 stops the panel from moving up and down, and keeps the distance between the processing brush 12 and the panel l constant.

なお、発泡体注入装置3と発泡体ならしベルト11下方
に余剰発泡体回収装置20を設置することが望ましい。
Note that it is desirable to install an excess foam recovery device 20 below the foam injection device 3 and the foam leveling belt 11.

該回収装置20Fi発泡体ならしベルト11により排除
された発泡体及び注入スタート前の発泡体調整時、ある
いはストップ後の発泡機からノズル間の洗浄時、又はパ
ネルが一時的に供給されない時等に発泡体を効率よく回
収する。該装置の概略図を第5図に示すが、上部には発
泡体21を水とともに流出させるための給水配管22、
下部底面には給水された水を排出させるたとえば全鋼製
の水排出部23を有する。給水された水24を除去した
発泡体21は、たとえば高速攪拌機で破壊するかプレス
で押圧して破壊することができる。ついでパネル1に閉
蓋する場合には常法に従い、上部に接着剤を塗布し、上
蓋を貼合せ、仮止め、プレス等の後工程30を経て、閉
蓋する。尚、パネルの用途によっては上面材を省略して
も良い。
The foam removed by the recovery device 20Fi foam leveling belt 11 and when adjusting the foam before starting injection, when cleaning between the nozzles from the foaming machine after stopping, or when the panel is temporarily not supplied. To efficiently collect foam. A schematic diagram of the device is shown in FIG. 5, and the upper part includes a water supply pipe 22 for discharging the foam 21 together with water;
The lower bottom surface has a water discharge part 23 made of all steel, for example, for discharging the supplied water. The foamed body 21 from which the supplied water 24 has been removed can be destroyed, for example, by using a high-speed stirrer or by being pressed with a press. Next, when the panel 1 is to be closed, an adhesive is applied to the upper part of the panel 1, a top cover is pasted, a post process 30 such as temporary fixing, pressing, etc. is carried out, and then the cover is closed. Note that the top material may be omitted depending on the use of the panel.

以上の方法を用いることによって発泡体の充填状態を目
視により確認しながら生産する為、未充填部分の無い、
良好な発泡体充填パネルの連続生産が極めて順調、かつ
能率的に行うことができた。
By using the above method, the filling state of the foam can be visually confirmed during production, so there is no unfilled part.
Continuous production of foam-filled panels of good quality was achieved in an extremely smooth and efficient manner.

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

第1図は発泡体充填パネル連続製造方法の工程図、第2
図はパネルの斜視図、第3図は発泡体ならしベルトの平
面図、第4図は第3図のB−B断面図、第5図は余剰発
泡体回収装置の正面図、第6図は余剰発泡体回収装置の
左側面図である。 1・・・・パネル、2・・・・ベルトコンベア、3・・
・・発泡体注入装置、4・・・・注入ノズル、5・・・
・エアシリンダ、7・・・・ベルトのリターン側、8・
・・・中枠、9・・・・外枠、11・・・・発泡体なら
しベルト、12・・・・処理ブラシ、13・・・・表面
処理装置、14・・・除去ブラン、16・・・・表面固
化装置、17・・・・押えロール、20・・・・回収装
置、21・・・・発泡体、22・・・・給水装置、23
・・・・金鋼、24・・・・水。 特許出願人 三井東圧化学株式会社 代理人 弁理士 井 上 雅 生 第3図 第4図 第6rXj
Figure 1 is a process diagram of the continuous manufacturing method for foam-filled panels, Figure 2
The figure is a perspective view of the panel, Figure 3 is a plan view of the foam leveling belt, Figure 4 is a sectional view taken along line B-B in Figure 3, Figure 5 is a front view of the excess foam recovery device, and Figure 6. is a left side view of the surplus foam recovery device. 1...Panel, 2...Belt conveyor, 3...
... Foam injection device, 4... Injection nozzle, 5...
・Air cylinder, 7... Belt return side, 8.
... Middle frame, 9 ... Outer frame, 11 ... Foam leveling belt, 12 ... Treatment brush, 13 ... Surface treatment device, 14 ... Removal blanket, 16 ... Surface solidification device, 17 ... Presser roll, 20 ... Recovery device, 21 ... Foam, 22 ... Water supply device, 23
...Golden steel, 24...Water. Patent applicant Mitsui Toatsu Chemical Co., Ltd. Agent Patent attorney Masaru Inoue Figure 3 Figure 4 Figure 6rXj

Claims (1)

【特許請求の範囲】 1、 注入後殆んど体積膨張のない発泡体を、搬送され
た開蓋パネルに注入し、発泡体充填パネルを製造する連
続製造方法において、 (1)発泡体注入工程と (2)表面処理工程と (3)余剰発泡体回収工程とを有することを特徴とする
発泡体充填パネル連続製造方法。 2、発泡体注入工程が、移動可能な注入ノズルで発泡体
を注入することを含む特許請求の範囲第1項記載の発泡
体充填パネル連続製造方法。 3 表面処理工程が、発泡体ならしベルトと表面処理ブ
ラシで表面処理を行う工程からなる特許請求の範囲第1
項記載の発泡体充填パネル連続製造方法。 4、 余剰発泡体回収工程が、上部に発泡体を流出させ
る給水配管と、下部床面に給水された水を排出させる排
出部を有する装置を使用することを含む特許請求の範囲
第1項記載の発泡体充填パネル連続製造方法。 5、発泡体ならしベルトがパネル進行方向に対し60〜
7o0の角度を有し、且つ水平方向に対し50〜70°
の角度をもって傾斜したものである特許請求の範囲第3
項記載の発泡体充填パネル連続製造方法。 6、 表面処理ブラシが芯径が60〜SOWφ、植毛材
の太さが0,4〜0.7Wφ、植毛材の長さが30〜4
0mのものであり、該ブラシは、外周速度200〜80
0m/分で回転し、発泡体をならし表面から1〜4謬の
深さまでかき取り、且つパネル枠面の発泡体を除去する
ものである特許請求の範囲第3項記載の発泡体充填パネ
ル連続製造方法。
[Claims] 1. In a continuous manufacturing method for producing a foam-filled panel by injecting a foam with almost no volumetric expansion after injection into a conveyed open-lid panel, (1) a foam injection step; (2) a surface treatment step; and (3) a surplus foam recovery step. 2. The method for continuously manufacturing a foam-filled panel according to claim 1, wherein the foam injection step includes injecting the foam with a movable injection nozzle. 3. Claim 1, wherein the surface treatment step comprises a step of performing surface treatment with a foam leveling belt and a surface treatment brush.
A method for continuously manufacturing a foam-filled panel as described in Section 1. 4. The surplus foam recovery step includes the use of a device having a water supply pipe for discharging the foam at the upper part and a discharge part for discharging the water supplied to the lower floor surface. Continuous manufacturing method for foam-filled panels. 5. The foam leveling belt is 60~
Has an angle of 7o0 and 50 to 70 degrees to the horizontal direction
Claim 3 is inclined at an angle of
A method for continuously manufacturing a foam-filled panel as described in Section 1. 6. The surface treatment brush has a core diameter of 60~SOWφ, the thickness of the flocked material is 0.4~0.7Wφ, and the length of the flocked material is 30~4.
0 m, and the brush has an outer peripheral speed of 200 to 80
The foam-filled panel according to claim 3, which rotates at 0 m/min to scrape the foam from the smoothed surface to a depth of 1 to 4 ft, and remove the foam from the panel frame surface. Continuous manufacturing method.
JP57056328A 1982-04-05 1982-04-05 Continuous manufacture of foamed body packed panel Granted JPS58173656A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57056328A JPS58173656A (en) 1982-04-05 1982-04-05 Continuous manufacture of foamed body packed panel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57056328A JPS58173656A (en) 1982-04-05 1982-04-05 Continuous manufacture of foamed body packed panel

Publications (2)

Publication Number Publication Date
JPS58173656A true JPS58173656A (en) 1983-10-12
JPH0372462B2 JPH0372462B2 (en) 1991-11-18

Family

ID=13024112

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57056328A Granted JPS58173656A (en) 1982-04-05 1982-04-05 Continuous manufacture of foamed body packed panel

Country Status (1)

Country Link
JP (1) JPS58173656A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5462405B1 (en) * 2013-10-02 2014-04-02 則之 加納 Sandwich panel manufacturing equipment
JP2018096199A (en) * 2016-12-10 2018-06-21 積水化学工業株式会社 Phenol resin foam and manufacturing method for the same, external adiabatic wall

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS512957A (en) * 1974-06-28 1976-01-12 Sanyo Electric Co INSATSUTEIKO CHOSEIHO
JPS54941A (en) * 1977-06-06 1979-01-06 Okuma Machinery Works Ltd Microcomputer control system
JPS57157737A (en) * 1981-03-25 1982-09-29 Mitsui Toatsu Chem Inc Manufacture of heat-insulating panel

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS512957A (en) * 1974-06-28 1976-01-12 Sanyo Electric Co INSATSUTEIKO CHOSEIHO
JPS54941A (en) * 1977-06-06 1979-01-06 Okuma Machinery Works Ltd Microcomputer control system
JPS57157737A (en) * 1981-03-25 1982-09-29 Mitsui Toatsu Chem Inc Manufacture of heat-insulating panel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5462405B1 (en) * 2013-10-02 2014-04-02 則之 加納 Sandwich panel manufacturing equipment
JP2018096199A (en) * 2016-12-10 2018-06-21 積水化学工業株式会社 Phenol resin foam and manufacturing method for the same, external adiabatic wall

Also Published As

Publication number Publication date
JPH0372462B2 (en) 1991-11-18

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