JPH1024431A - Rigid urethane pouring method for continuous production - Google Patents

Rigid urethane pouring method for continuous production

Info

Publication number
JPH1024431A
JPH1024431A JP8198258A JP19825896A JPH1024431A JP H1024431 A JPH1024431 A JP H1024431A JP 8198258 A JP8198258 A JP 8198258A JP 19825896 A JP19825896 A JP 19825896A JP H1024431 A JPH1024431 A JP H1024431A
Authority
JP
Japan
Prior art keywords
raw material
pair
injection
surface material
mixing heads
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
JP8198258A
Other languages
Japanese (ja)
Other versions
JP3659531B2 (en
Inventor
Shigeru Fujiike
滋 藤池
Takashi Oga
隆史 大賀
Hiroyuki Kamise
博幸 神瀬
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 JP19825896A priority Critical patent/JP3659531B2/en
Publication of JPH1024431A publication Critical patent/JPH1024431A/en
Application granted granted Critical
Publication of JP3659531B2 publication Critical patent/JP3659531B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To realize continuous production by a method wherein a plurality of mixing heads are arranged close to each other in the neighborhood of the inlet of double- conveyors at both the sides of the conveyors so as to direct the stock pouring height and angle of each nozzle or of a pair of nozzles vertically and horizontally in order to pour stock from an opposing pair of the nozzles and change the other pair of the nozzles over depending on stock situation. SOLUTION: Rigid urethane stock liquid 9 is poured to the central position of a lower surface part 5, for example, from the nozzle parts 7 and 7' of an opposing pair of mixing heads A and B, which are arranged on both the sides of conveyors 1. When abnormality appears in the filling properties of the spread stock liquid 9 and consequently a pair of the mixing heads A and B are changed over to a pair of mixing heads C and D, the stock liquid 9 is discharged from nozzle parts 8 and 8' before the stopping of the pouring through the nozzle parts 7 and 7' so as to stop the pouring through the nozzle parts 7 and 7' simultaneously with the arrival of the spread pattern formed by the stock liquid 9. The angles of the mixing heads A, B and C, D can be changed back and forth to the running direction of surfacing materials and their vertical movements and the change of their angles for controlling the altitudinal position between the upper and lower surfacing materials can be made possible.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】硬質表面材(合板、金属板、
樹脂板他)、硬質ウレタンフォーム(イソシアヌレート
変性を含む)よりなるサンドイッチパネル(用途:建
材、保冷、冷蔵用パネル他)の連続生産方法に関する。
TECHNICAL FIELD The hard surface material (plywood, metal plate,
The present invention relates to a continuous production method of sandwich panels (use: building materials, cold storage, refrigeration panels, etc.) made of rigid urethane foam (including isocyanurate-modified).

【0002】[0002]

【従来技術】硬質ウレタン発泡体のサンドイッチパネル
を連続製造する代表的方式は、下面材を水平に設置され
た搬送コンベアで発泡・硬化装置へ送り込み、上面材は
テンショナーロールを下面材上のある高さに配置して、
発泡・硬化の入口において下面材とある角度を有する楔
型空間を作る態様で供給される水平式である。発泡体原
料は、下面材に注入される。パネル製品の幅、厚み、発
泡材料特性等によって注入の方法は幾つか採用されてい
る。注入した原料が面材上に均一に広がり、かつ均一な
厚みである必要がある。かつ、原料を注入された下面材
が発泡・硬化装置に入る前に、原料液の発泡・硬化の進
行は許容範囲に制限しなければならない。
2. Description of the Related Art A typical method for continuously producing sandwich panels made of rigid urethane foam is to feed a lower surface material to a foaming / curing device by a horizontally installed conveyor, and to use a tensioner roll as a top material on a lower surface material. Place it on
It is a horizontal type which is supplied in such a manner that a wedge-shaped space having an angle with the lower surface material is formed at an inlet of foaming and hardening. The foam raw material is injected into the lower surface material. Several injection methods are employed depending on the width and thickness of the panel product and the characteristics of the foam material. It is necessary that the injected raw material is uniformly spread on the face material and has a uniform thickness. Further, before the lower surface material into which the raw material is injected enters the foaming / curing device, the progress of the foaming / curing of the raw material liquid must be limited to an allowable range.

【0003】前記原材料注入特性を実現する種々の注入
法が実用されている。すなわち、パネル幅が狭く、薄物
(約30mm以下)では、ミキシングヘッドが1台の1
点注入法、中厚み(約50mm)程度で、原料の反応性
が一般的な場合には、2台で注入する方式が採用されて
いる。より厚い(100mm程度)、一般反応性材料で
は、面材の搬送速度、硬化速度等を考慮してミキシング
ヘッドを面材の幅方向に移動させるトラバース方式があ
る。また、幅広(600〜1500mm)のパネル製造
用に、下面材上の幅方向に注入ノズル孔を多数配列した
シャワーノズル方式が採用されている。
[0003] Various injection methods for realizing the raw material injection characteristics have been put to practical use. That is, for a thin panel (about 30 mm or less) with a narrow panel width, one
In the case of a point injection method, a medium thickness (approximately 50 mm), and the reactivity of the raw material is general, a method of injecting with two units is adopted. For a thicker (about 100 mm), general reactive material, there is a traverse method in which the mixing head is moved in the width direction of the face material in consideration of the speed of transport of the face material, the curing speed, and the like. Further, for manufacturing a wide panel (600 to 1500 mm), a shower nozzle system in which a number of injection nozzle holes are arranged in a width direction on a lower surface material is adopted.

【0004】いずれの注入方式も両面が軟質面材(クラ
フト紙、アスファルトフェルト、アルミ箔、ガラスペー
パーなど)または、上面軟質面材、下面硬質面材の組み
合わせにおいて利用されている方式である。下面材が硬
質面材(石膏ボード、木毛セメント板、合板)、上面材
が軟質面材の代表例は、軟質面材をロールに沿わせて挿
入する反転式を用いている。反転する上面材に原料を注
入するために、原料散布のミキシングヘッドの配備空間
を広くとることが可能で、トラバース方式を採用してい
る。
[0004] Any of the injection methods is a method in which both surfaces are used as a soft surface material (kraft paper, asphalt felt, aluminum foil, glass paper, etc.) or a combination of an upper surface soft surface material and a lower surface hard surface material. A typical example in which the lower surface material is a hard surface material (plaster board, wood wool cement board, or plywood) and the upper surface material is a soft surface material uses an inversion type in which the soft surface material is inserted along a roll. In order to inject the raw material into the upper surface material to be inverted, the space for installing the mixing head for dispersing the raw material can be widened, and a traverse method is adopted.

【0005】[0005]

【発明が解決しようとする課題】前記、従来の技術に記
述したような硬質ウレタンサンドイッチパネルを連続製
造する原料注入方法は実使用されている。しかしなが
ら、パネル面材の選択、反応性の異なる原料注入、パネ
ル幅への対応、および、設備の稼働率の点で多くの課題
を有している。
The raw material injection method for continuously manufacturing a rigid urethane sandwich panel as described in the prior art is actually used. However, there are many problems in selection of panel surface materials, injection of raw materials having different reactivities, adaptation to panel widths, and equipment operation rates.

【0006】連続稼働の点から硬質ウレタンサンドイッ
チパネル連続製造装置として望ましい設備は、同一設備
で面材の硬・軟材質に拘らず製造可能であることである
が、反転式製造装置が上下軟質面材、および、上軟質面
材、下硬質面材に対応できるのみで、水平式装置は両面
軟質面材のパネル製造のみに使用されている。すなわ
ち、稼働率低下の最大の原因は原料注入の方式によりも
たらされている。
[0006] From the viewpoint of continuous operation, a desirable equipment as a continuous production apparatus of a hard urethane sandwich panel is that it can be produced by the same equipment regardless of the hard or soft material of the face material. Only horizontal and vertical panels are used for the production of panels with double-sided soft facings, only capable of handling upper and lower soft facings. That is, the greatest cause of the decrease in the operation rate is brought by the method of material injection.

【0007】高性能原料注入方式とは、パネルの幅、厚
み、および、原料液の反応速度等によらず対応できるこ
とである。このような技術的観点より前記従来技術を見
ると、改良すべき課題を有している。 (1)1点注入(1ミキシングヘッド)法にては、面材
上に可及的速やかに、かつ、均一に原料液を拡げる散布
充填性に限界がある。したがって、適用可能なパネル
は、幅が狭く、薄物(30mm以下)に限定される。 (2)2点注入(2ミキシングヘッド)法では、パネル
幅は大きくなり(600〜900mm)、中厚50mm
程度まで製造可能になるが、散布充填性に同様に課題を
残している。 (3)トラバース方式(1ミキシングヘッド)では、厚
み制御が容易で、平面の平滑性に優れた方法として採用
されているが、水平式において両面硬質面材を使用する
には配備空間の確保の点で課題を有している。すなわ
ち、各種原料の散布充填を充たすトラバース駆動機構を
配備するには大きな配備空間が必要である。 (4)シャワーノズル方式は、1〜2台のミキシングヘ
ッドで攪拌混合した原料液を面材上に渡されたノズル部
の多数のノズル孔より散布するために、散布充填性は優
れている。しかしながら、発泡フォームによるノズルの
詰まりがほかの方法に比較して容易に生じ、それを洗浄
・更新する頻度による稼働率低下という課題を有してい
る。
[0007] The high-performance raw material injection method is capable of coping with the width and thickness of the panel and the reaction speed of the raw material liquid. Looking at the above-mentioned prior art from such a technical viewpoint, there is a problem to be improved. (1) In the one-point injection (one mixing head) method, there is a limit in the spray filling property for spreading the raw material liquid on the face material as quickly and uniformly as possible. Therefore, applicable panels are narrow and limited to thin objects (30 mm or less). (2) In the two-point injection (two mixing head) method, the panel width becomes large (600 to 900 mm) and the medium thickness is 50 mm.
Although it can be manufactured to a certain degree, the problem remains in the spray filling property as well. (3) In the traverse method (one mixing head), the thickness control is easy, and the method is adopted as a method excellent in flatness. There is a problem in the point. In other words, a large deployment space is required to dispose the traverse drive mechanism that satisfies the spray filling of various raw materials. (4) In the shower nozzle method, the raw material liquid stirred and mixed by one or two mixing heads is sprayed from a large number of nozzle holes of the nozzle portion provided on the face material, and thus the spray filling property is excellent. However, there is a problem that the clogging of the nozzle by the foamed foam easily occurs as compared with other methods, and the operation rate is reduced due to the frequency of cleaning and renewing the nozzle.

【0008】原料液の散布充填性の他に、反応速度の早
い原料液を使用する場合、原料液を加圧用コンベアの入
口近くで散布する必要がある。しかしながら、コンベア
に近いほど楔形空間の先端に近く狭いため、ミキシング
ヘッドの設置がなお困難になる。更に、反応速度の速い
特殊処方の原料の混合には大型の特殊ミキシングヘッド
を必要とし、それに伴い配備空間が大きくなり、設置が
益々困難となる。また、硬質上面材を使用してサンドイ
ッチパネルを生産する場合、ミキシングヘッドを設置す
る空間、すなわち、楔形空間の開き角度を大きく取って
上面材の挿入を行うと、上下面材先端が一致し難い。更
に、上面材が硬質で曲がりにくい性質であると、加圧用
コンベア入り口から離れた広い空間になる位置で注入す
ることになる。ダブルコンベア等を使用したサンドイッ
チパネルの連続成形の場合、発泡が始まる前に、ダブル
コンベア内の加圧・硬化域にパネルを導入しなければ、
未充填、又は厚み不良の原因となる。特に、面材が厚く
曲がりにくい場合、パネルサイズ(幅、厚み)が大きい
場合、また反応速度が早い配合系の場合顕著となる。
When a raw material liquid having a high reaction rate is used in addition to the spray filling property of the raw material liquid, it is necessary to spray the raw material liquid near the inlet of the pressurizing conveyor. However, the closer to the conveyor, the closer to the tip of the wedge-shaped space, the narrower the installation of the mixing head becomes. Furthermore, the mixing of the raw materials of the special formula having a high reaction rate requires a large-sized special mixing head, and accordingly, the arrangement space becomes large and the installation becomes more and more difficult. In addition, when a sandwich panel is produced using a hard upper surface material, when the upper surface material is inserted by increasing the opening angle of the mixing head installation space, that is, the wedge-shaped space, the upper and lower surface material tips are difficult to match. . Further, when the upper surface material is hard and hard to bend, the material is injected at a position in a wide space away from the entrance of the pressurizing conveyor. In the case of continuous molding of sandwich panels using a double conveyor, etc., before foaming starts, if the panel is not introduced into the pressure / hardening area in the double conveyor,
It causes unfilling or poor thickness. In particular, when the surface material is thick and hard to bend, when the panel size (width and thickness) is large, and when the reaction rate is high in the compounding system, it becomes remarkable.

【0009】[0009]

【課題を解決するための手段】本発明において、前記課
題を解決する手段として、加圧用ダブルコンベアへ継続
して移送される下面材料上に硬質ウレタン原料液を散布
し、該硬質ウレタン原料を下面材料と上面材料により挟
んだ帯状、または、板状パネルを前記ダブルコンベアで
加圧し、発泡・硬化させてなるサンドイッチパネルを連
続生産する装置において、ダブルコンベアの入り口付近
に在って、上下面材とダブルコンベアの入口で作る楔形
空間の両横側に硬質ウレタン原料を注入する対向した1
対のミキシングヘッドを近接して複数対具備し、該複数
対の内、向き合う1対のミキシングヘッドより原料を注
入し、原料注入状況により随時、待機する他の1対のミ
キシングヘッドに切り替えること、かつ、原料を注入す
るミキシングヘッドは、個別に、または、対をなす1対
が、原料注入の高さ、および、原料注入方向角度を、そ
れぞれ上下、および、左右に変化させうる運動自由度を
有する機構により駆動される、サンドイッチパネルを連
続製造することを特徴とする連続生産用硬質ウレタン注
入方式を提案するものである。
In the present invention, as a means for solving the above-mentioned problems, a hard urethane raw material liquid is sprayed on a lower surface material continuously transferred to a double conveyor for pressurization, and the hard urethane raw material is spread on the lower surface material. In a device for continuously producing a sandwich panel formed by pressing a band-shaped or plate-shaped panel sandwiched between a material and an upper surface material by the double conveyor and foaming and curing the same, the upper and lower surface materials are located near an entrance of the double conveyor. And the opposite side where hard urethane raw material is injected on both sides of the wedge-shaped space created at the entrance of the double conveyor
A plurality of pairs of mixing heads are provided close to each other, and the raw material is injected from a pair of the mixing heads facing each other, and the mixing head is switched to another pair of mixing heads that are on standby at any time depending on the raw material injection state. In addition, the mixing heads for injecting the raw materials individually or in pairs form a moving degree of freedom that can change the height of the raw material injection and the angle of the raw material injection direction up and down and left and right, respectively. The present invention proposes a continuous production hard urethane injection method characterized by continuously manufacturing sandwich panels driven by a mechanism having the same.

【0010】軟質面材を硬質ウレタン原料の両面に使用
するサンドイッチパネルの連続生産にては、面材間隔は
広く取ることが可能で支障は生じない。また、上面軟質
面材、下面硬質面材よりなるサンドイッチパネルの生産
方法も個別の装置で確立している。しかしながら、生産
の効率性から生産装置をみると、同一の設備にて、硬軟
質いずれの面材を使用したサンドイッチパネルも生産可
能な装置が望ましい。本発明は、ミキシングヘッドのノ
ズル部を下面材支持ロールの外側から挿入するために、
上下面材間隔は狭くても支障が無い。したがって、柔軟
性に欠ける上面材を、下面材に平行、または、両面材の
なす角度小さくして、コンベアに送り込む。挿入角度が
下面材と平行に移り変わる位置での面材の曲げ変形を無
くす、または、小さくすることが可能である。すなわ
ち、両面軟質面材から、下硬質面材、上面は柔軟性に欠
ける面材まで、同一の装置で生産できる。
In the continuous production of sandwich panels using a soft urethane material on both sides of a hard urethane raw material, the distance between the urethane materials can be widened without any problem. In addition, a method for producing a sandwich panel composed of an upper soft surface material and a lower hard surface material has been established using individual devices. However, from the viewpoint of production efficiency, from the viewpoint of production equipment, an apparatus capable of producing a sandwich panel using both hard and soft face materials in the same facility is desirable. The present invention, in order to insert the nozzle portion of the mixing head from the outside of the lower surface material support roll,
There is no problem even if the distance between the upper and lower surfaces is small. Therefore, the upper surface material lacking in flexibility is sent to the conveyor in parallel with the lower surface material or at a smaller angle formed by both surface materials. It is possible to eliminate or reduce the bending deformation of the face material at a position where the insertion angle changes parallel to the lower face material. That is, it can be produced with the same equipment from a soft double-sided surface material to a lower hard surface material and a surface material lacking in flexibility on the upper surface.

【0011】[0011]

【発明の実施の形態】前記、課題を解決する手段の具体
的形態について、以下に詳述する。 1. 原料注入機構 1.1 ミキシングヘッド設置方法 下面材搬送コンベア幅の外側に位置し、対向するミキシ
ングヘッドを対にして、複数対並べ配置する。硬質ウレ
タン原料混合液の注入は、コンベア上の下面材へ、コン
ベアの外横側から対向する対のノズルにより散布する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Specific embodiments of the means for solving the problems will be described below in detail. 1. 1. Raw Material Injection Mechanism 1.1 Mixing Head Installation Method A plurality of mixing heads, which are located outside the width of the lower surface material conveyor and are opposed to each other, are arranged side by side. The hard urethane raw material mixture is injected into the lower surface material on the conveyor by a pair of nozzles facing each other from the outer side of the conveyor.

【0012】1.2 連続原料注入法 連続生産時のノズル部の詰り現象が発生する前に、適宜
に待機中のほかのミキシングヘッド対に原料注入作業を
切り替える。また、2対のミキシングヘッド対を定期的
に切り替える作業手順も可能である。この方法、すなわ
ち、定期的に注入ヘッドを切り替える方法は反応の早い
配合系において特に有効である。
1.2 Continuous Raw Material Injection Method Before the clogging phenomenon of the nozzle portion at the time of continuous production, the raw material injection operation is appropriately switched to another mixing head pair in a standby state. In addition, a work procedure for periodically switching between the two mixing head pairs is also possible. This method, that is, a method of periodically switching the injection head, is particularly effective in a compounding system having a fast reaction.

【0013】1.3 連続注入監視機構 ミキシングヘッドのノズル部からの原料吐出及び、その
充填状況を監視して、状況を監視者に伝達するカメラ装
置、またはカメラ装置に類する注入状況モニター装置を
具備してもよい。この時監視者は専任でなくてもよく、
注入状況を画像解析的に処理して、自動的にミキシング
ヘッドの位置、および、設置条件の調製を行っても良
い。ノズル部からの原料吐出及び充填状況監視に最適な
位置は、両面材間、かつ、ノズル部に近接したところで
ある。両面材間が狭い場合、例えば、柔軟性に欠ける面
材のような場合には両面材間の平行平面付近で、両面材
間の外より監視を行う。または、小型カメラを用いてフ
ォームの立ち上り状態を撮影する。
1.3 Continuous Injection Monitoring Mechanism Equipped with a camera device for monitoring the discharge of raw materials from the nozzle portion of the mixing head and the filling status thereof and transmitting the status to a monitor, or an injection status monitoring device similar to a camera device. May be. At this time, the watcher does not have to be full-time,
The position of the mixing head and the setting conditions may be automatically adjusted by processing the injection state by image analysis. The optimum position for discharging the raw material from the nozzle portion and monitoring the state of filling is between the double-sided materials and close to the nozzle portion. In the case where the space between the both surfaces is narrow, for example, in the case of a surface material lacking flexibility, monitoring is performed from the outside between the both surfaces near the parallel plane between the two surfaces. Alternatively, the rising state of the form is photographed using a small camera.

【0014】2. 注入位置、および、その調製方法 原料注入は、移動する連続帯状、または、板状下面材の
中央部に向かって、搬送コンベアの両側よりミキシング
ヘッドにより注入する。注入量、注入位置などはパネル
のサイズ、移送速度(生産性他)、配合系の性質等によ
り変える必要がある。これら加工条件を充足させる為
に、発泡機の能力だけでなく、発泡機の数、ミキシング
ヘッドの注入位置(上下、左右)により対応・処理す
る。注入されたウレタン原料の散布形状は、広範囲、か
つ、ミキシングヘッド対それぞれの原料散布間に空間が
出来ないように行う。原料注入の方向、量は、任意に調
節され、パネルの厚み、ライン速度、原料液の反応性、
吐出時の飛距離などによって決定される。例えば、従来
の散布法では、樹脂化の速い材料には対応出来なかった
ものが、本方法では処理可能である。特に、面材が厚く
曲がりにくい場合、パネルサイズ(幅、厚み)が大きい
場合、また、反応速度が速い配合系の場合顕著となる。
このような場合でも、横から注入すれば、ノズルの径程
度の隙間があればコンベア入口に近接した最適位置に注
入可能となる。
2. Injection position and its preparation method Raw material is injected by a mixing head from both sides of the conveyer toward the center of the moving continuous strip-shaped or plate-shaped lower surface material. The injection amount, injection position, and the like need to be changed depending on the size of the panel, the transfer speed (productivity, etc.), the properties of the compounding system, and the like. In order to satisfy these processing conditions, not only the capacity of the foaming machine but also the number of the foaming machines and the mixing head injection position (up and down, left and right) are handled and processed. The distribution of the injected urethane raw material is performed in a wide range so that there is no space between the mixing head and each raw material. The direction and amount of raw material injection are arbitrarily adjusted, and the thickness of the panel, line speed, reactivity of raw material liquid,
It is determined by the flight distance at the time of ejection. For example, the conventional spraying method cannot cope with a material that is made of resin quickly, but can be processed by the present method. In particular, when the face material is thick and hard to bend, when the panel size (width and thickness) is large, and when the reaction rate is high, the composition becomes remarkable.
Even in such a case, if the injection is performed from the side, the injection can be performed at the optimum position close to the entrance of the conveyor if there is a gap of about the diameter of the nozzle.

【0015】実施例1 連続製造設備の構成は、面材搬送装置1、加圧用ダブル
コンベア2、ミキシングへッド(ウレタン発泡機)A、
B、C、D、監視カメラ4等からなるが、本発明は、こ
の内、ミキシングへッドの設置位置、および、操作方法
に関するもので、設備の配置を図面を参照しながら説明
する。図1.は配置の鳥瞰図である。下面硬質面材5、
上面柔軟性に欠ける面材6よりなるサンドイッチパネル
を連続製造する工程略図である。両面材は、搬送装置1
により加圧用コンベア2へ移送される。ミキシングヘッ
ドは、両面材間5、6、かつ、両面材の外側にA、B対
及びC、D対として設置される。又原料液を両面材間に
注入させるミキシングヘッドのノズル部は、ミキシング
ヘッドAのノズル部7(以下A7の要領で略す),B
7’対、C8,D8’対の2対よりなり、通常、ノズル
部は両面材間に差し込まれる。図1では、C8,D8’
対より原料液9を注入している。注入された原料液9は
両面材間にサンドイッチされ、加圧用コンベア内にて発
泡・硬化反応が進行する。
Embodiment 1 The construction of the continuous manufacturing equipment is as follows: a face material transporting apparatus 1, a double conveyor for pressurizing 2, a mixing head (urethane foaming machine) A,
B, C, D, the surveillance camera 4 and the like. The present invention relates to the installation position of the mixing head and the operation method, and the arrangement of the equipment will be described with reference to the drawings. FIG. Is a bird's-eye view of the arrangement. Lower surface material 5,
It is process schematic which manufactures the sandwich panel which consists of the surface material 6 lacking in upper surface flexibility continuously. Double-sided material is transport device 1
To the pressurizing conveyor 2. Mixing heads are installed as A, B pairs and C, D pairs outside the double-sided material, between 5, 6 between the double-sided materials. The nozzles of the mixing head for injecting the raw material liquid between the two surfaces are the nozzles 7 of the mixing head A (hereinafter abbreviated as A7), B
There are two pairs of 7 'pairs and C8 and D8' pairs, and the nozzle portion is usually inserted between the two side materials. In FIG. 1, C8, D8 '
The raw material liquid 9 is injected from the pair. The injected raw material liquid 9 is sandwiched between both surfaces, and a foaming / curing reaction proceeds in the pressurizing conveyor.

【0016】図2.はミキシングヘッドの設置状態であ
る。ミキシングヘッド11は、面材進行方向に対し前後
に角度を変更できる(面材端辺に直角な線となす角度を
水平角とよぶ)。また、平行な上下面材間の高さ位置調
整のための上下動、および、角度(下面材と平行面で、
この面に垂直でヘッドの中心軸を通る面がなす角度を仰
角とよぶ)を持たす角度変更が可能である。ノズル部1
2にコレステロール状に樹脂が付着し、液の吐出パター
ンが変わり始めた場合にミキシングヘッドの洗浄を行う
が、このためにミキシングヘッドの設置台13は、支持
枠14上を後退する移動も可能である。
FIG. Is the installation state of the mixing head. The angle of the mixing head 11 can be changed back and forth with respect to the surface material advancing direction (an angle formed by a line perpendicular to the edge of the surface material is called a horizontal angle). In addition, the vertical movement for adjusting the height position between the parallel upper and lower surface materials, and the angle (in the parallel surface with the lower surface material,
The angle formed by a plane perpendicular to this plane and passing through the center axis of the head is called an elevation angle). Nozzle part 1
When the cholesterol-like resin adheres to 2 and the discharge pattern of the liquid starts to change, the mixing head is washed. For this reason, the mixing head installation table 13 can be moved backward on the support frame 14. is there.

【0017】加圧用ベルトコンベア2の駆動軸より約1
000mmの位置から、面材搬送方向の上手、下手に注
入ノズルセンター間200mmの間隔で、それぞれ1対
のミキシングヘッドを設置した。ヘッドの取り付け水平
角は30度、仰角15度、平行面材間の中央位置にセッ
トした。
Approximately 1 from the drive shaft of the pressing belt conveyor 2
From the position of 000 mm, a pair of mixing heads were installed at an interval of 200 mm between the injection nozzle centers at the upper side and the lower side in the surface material transport direction. The horizontal angle at which the head was attached was set at 30 degrees, the elevation angle was 15 degrees, and the head was set at the center position between the parallel plane members.

【0018】汎用硬質ウレタン原料液9を注入し100
mm厚みのサンドイッチパネルを連続生産した。原料液
の硬化の進行状況を図3.に示すが、理想的に進行し
た。この時、注入後の硬化の進行状況は、硬質ウレタン
原料液によって異なる。
The general-purpose hard urethane raw material liquid 9 is poured and 100
mm-thick sandwich panels were continuously produced. Fig. 3 shows the progress of curing of the raw material liquid. As shown in the figure, it proceeded ideally. At this time, the progress of the curing after the injection differs depending on the hard urethane raw material liquid.

【0019】図4.には、注入切り替え時の散布原料パ
ターン16を示す。ミキシングヘッドが正常な原料充填
を行っている場合、面材進行方向の上手中央へ向かって
吐出される原料液は先端部が手前部より先に面材上に着
地して、先に発泡・膨張を開始する。その膨張力により
手前部の原料液を面材端部に押し出し、均一な厚みのサ
ンドイッチ発泡体となる。この観点よりミキシングヘッ
ドの注入角度の設定を行った。面材の進行方向上手に設
置されたA、B対よりC、Dに切り替える場合、また、
その逆の場合、次のような手順で行った。 1)搬送コンベア1の両側に配備された対向する1対の
ノズル部より搬送装置の原料レイダウン部で下面材5の
中央位置に向かって原料混合液9を注入する。 2)A、および、Bミキシングヘッド対の注入状態に
て、散布原料液の充填性に不正常な現象が現われ、C、
および、Dミキシングヘッド対に切り替える場合; ・A,B対から、A,B対よりコンベア流れの上流方向
に位置するC,D対への切り替えにおいては、A,B対
の停止以前にC8,D8’対ノズルより原料液を吐出
し、C8,D8’対ノズルより吐出した原料液が作る散
布パターン17が、A7,B7’対の散布パターン18
位置に着くと同時にA,B対の注入を停止する。直ち
に、A、および、Bミキシングヘッドは後退して、ミキ
シングヘッド洗浄を行い、次の交換の待機状態になる。 ・逆にC,D対よりA,B対へ切り替えを行う場合、C
8,D8’対が吐出を終了し、その吐出液の最終散布パ
ターン19がA7,B7’対の吐出パターン20内に入
ると同時にA,B対の吐出を開始する。注入を停止した
C、および、Dミキシングヘッドは退避してミキシング
ヘッド洗浄作業に入る。
FIG. Shows a spraying material pattern 16 at the time of switching the injection. When the mixing head is filling the raw material normally, the raw material liquid discharged toward the center of the surface material in the advancing direction of the surface material lands on the surface material before the front part, and foams and expands first. To start. Due to the expansion force, the raw material liquid at the near side is extruded toward the end of the face material, and a sandwich foam having a uniform thickness is obtained. From this viewpoint, the injection angle of the mixing head was set. When switching to C and D from A and B pairs installed well in the traveling direction of the face material,
In the opposite case, the procedure was as follows. 1) The raw material mixture 9 is injected from a pair of opposed nozzles provided on both sides of the conveyor 1 toward the center of the lower surface material 5 at the raw material lay-down portion of the conveyor. 2) In the injection state of the A and B mixing head pairs, an abnormal phenomenon appears in the filling property of the spraying material liquid, and C,
And when switching to the D mixing head pair; In switching from the A, B pair to the C, D pair located in the upstream direction of the conveyor flow from the A, B pair, C8, C8, The spray pattern 17 formed by discharging the raw material liquid from the D8 'pair nozzle and the raw material liquid discharged from the C8, D8' pair nozzle is a spray pattern 18 of A7, B7 'pair.
Upon reaching the position, the injection of the A and B pairs is stopped. Immediately, the A and B mixing heads retreat, perform mixing head cleaning, and wait for the next replacement.・ Conversely, when switching from C and D pairs to A and B pairs, C
The discharge of the A and B pairs starts at the same time as the final spray pattern 19 of the discharge liquid enters the discharge pattern 20 of the A7 and B7 'pairs. The C and D mixing heads whose injection has been stopped are evacuated to start the mixing head cleaning operation.

【0020】結果的に、製造された硬質ウレタン発泡材
料をサンドイッチしたパネルは未充填、厚不良のない良
好な製品であった。
As a result, the panel sandwiched with the produced rigid urethane foam material was a good product with no filling and no defective thickness.

【0021】実施例2 反応性の速い原料液において、定期的にミキシングヘッ
ドを切り替える注入方法で製造を行った。この方法で連
続生産が可能であれば生産性に与える効果は非常に大き
い。例えば、汎用原料で、4〜8時間連続製造可能であ
っても、前記特殊処方の原料になると15〜30分に短
縮される。すなわち、ミキシングヘッドの洗浄のため
に、製造装置を一時停止しなければならず、生産性にあ
たえる影響は大きい。A,B対とC,D対の2対のミキ
シングへッドを10分毎に定期的切替えによって特殊原
料を注入した。結果は、上記反応性の速い原料組成であ
っても連続生産可能であった。
Example 2 A raw material liquid having a high reactivity was produced by an injection method in which a mixing head was periodically switched. If continuous production is possible by this method, the effect on productivity is very large. For example, even if it is a general-purpose raw material and can be continuously manufactured for 4 to 8 hours, the raw material of the special formulation is reduced to 15 to 30 minutes. In other words, the manufacturing apparatus must be temporarily stopped for cleaning the mixing head, which greatly affects the productivity. A special raw material was injected by periodically switching the two pairs of mixing heads A and B and C and D every 10 minutes. As a result, continuous production was possible even with the raw material composition having a high reactivity.

【0022】[0022]

【発明の効果】硬質ウレタン発泡体サンドイッチパネル
の連続製造に用いる原料液注入ミキシングヘッドを、搬
送される上下面材外の横側に2対配備し、ミキシングヘ
ッドの原料吐出状況の監視により、または、定期的に待
機中の別の1対と適時交換することによって、原料液を
常時性状吐出状態に保ちながら連続生産出来た。また、
ミキシングへッドの配備空間が上下面材外にあるために
面材上に配備空間の確保が不必要となり、両面材は平
行、または、小さい角度で加圧用コンベアに搬送可能と
なり、上面材に大きな曲げ変形を加えなくても発泡・硬
化処理部へ供給出来た。したがって、下面材の硬軟面材
性質と共に、上面材も硬質面材から柔軟性を欠く面材ま
で使用したサンドイッチパネルの連続生産が可能になっ
た。このことは、設備の生産性向上に寄与することが大
きかった。
According to the present invention, two pairs of raw material liquid injection mixing heads used for continuous production of a rigid urethane foam sandwich panel are provided on the lateral side outside the upper and lower surface materials to be conveyed, by monitoring the raw material discharge state of the mixing head, or In addition, by performing timely replacement with another pair that is on standby at regular intervals, continuous production could be performed while the raw material liquid was always kept in the property discharge state. Also,
Since the mixing head deployment space is outside the upper and lower surface materials, it is not necessary to secure a deployment space on the surface material, and both surfaces can be conveyed to the pressing conveyor in parallel or at a small angle. It could be supplied to the foaming / curing section without significant bending deformation. Accordingly, it has become possible to continuously produce a sandwich panel using a hard surface material and a surface material lacking flexibility as well as a hard soft surface material property of a lower surface material. This greatly contributed to improving the productivity of the equipment.

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

【図1】実施例を示す製造設備の配置鳥瞰図である。FIG. 1 is a bird's-eye view of an arrangement of manufacturing equipment showing an embodiment.

【図2】ミキシングヘッドの取り付け実施例を示す図で
ある。
FIG. 2 is a view showing an embodiment of mounting a mixing head.

【図3】実施例における注入原料液の発泡・硬化の経時
変化である。
FIG. 3 is a graph showing changes over time in foaming and curing of an injection raw material liquid in Examples.

【図4】ミキシングヘッド対の切り替え手順を示す実施
例である。
FIG. 4 is an embodiment showing a procedure for switching a mixing head pair.

【符号の説明】 1.面材搬送装置 2.加圧用ダブルコンベア A、B、C、D.ミキシングヘッド 4.監視カメラ 5.硬質下面材 6.柔軟性に欠ける上面材 7,7’、8,8’. ミキシングヘッドのノズル部 9.注入された原料液 11.ミキシングヘッド 12.ノズル部 13.ミキシングヘッドの設置台 14.支持枠 16.17.18.19.散布原料パターン[Explanation of Codes] 1. Surface material transfer device Double conveyor for pressurization A, B, C, D. Mixing head 4. Surveillance camera 5. Hard lower surface material 6. Top material 7,7 ', 8,8' lacking flexibility. 8. Nozzle section of mixing head Raw material liquid injected 11. Mixing head 12. Nozzle part 13. Mixing head installation base 14. Support frame 16.17.18.19. Spraying raw material pattern

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29L 9:00 Continued on the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical display B29L 9:00

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 加圧用ダブルコンベアへ継続して移送さ
れる下面材料上に硬質ウレタン原料液を散布し、該硬質
ウレタン原料を下面材料と上面材料により挟んだ帯状、
または、板状パネルを、前記ダブルコンベアで加圧し、
発泡・硬化させてなるサンドイッチパネルを連続生産す
る装置において、ダブルコンベアの入り口付近に在っ
て、上下面材の作る楔型空間の両横側に硬質ウレタン原
料を注入する対向した1対のミキシングヘッドを近接し
て複数対具備し、該複数対の内、向き合う1対のミキシ
ングヘッドより原料を注入し、原料注入状況により随
時、待機する他の1対のミキシングヘッドに切り替える
ことと、原料を注入するミキシングヘッドは、個別に、
または、対をなす1対が、原料注入高さ、および原料注
入方向角度を、それぞれ上下、および、左右に変化させ
うる運動自由度を有する機構により駆動されるサンドイ
ッチパネルを連続製造することを特徴とする連続生産用
硬質ウレタン注入方法。
1. A hard urethane raw material liquid is sprayed on a lower surface material continuously transferred to a pressurizing double conveyor, and the hard urethane raw material is strip-shaped between the lower surface material and the upper surface material.
Or, press the plate-shaped panel with the double conveyor,
In a device for continuously producing foamed and cured sandwich panels, a pair of opposing mixing units located near the entrance of a double conveyor, injecting hard urethane raw material into both sides of a wedge-shaped space created by upper and lower panels. A plurality of heads are provided in close proximity to each other, of which a raw material is injected from a pair of mixing heads facing each other, and, depending on the raw material injection status, is switched to another pair of mixing heads that are on standby as needed. The mixing heads to be injected are individually
Alternatively, a pair of pairs continuously manufactures a sandwich panel driven by a mechanism having a degree of freedom of movement capable of changing a raw material injection height and a raw material injection direction angle up and down and left and right, respectively. Hard urethane injection method for continuous production.
JP19825896A 1996-07-09 1996-07-09 Hard urethane injection method for continuous production Expired - Fee Related JP3659531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19825896A JP3659531B2 (en) 1996-07-09 1996-07-09 Hard urethane injection method for continuous production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19825896A JP3659531B2 (en) 1996-07-09 1996-07-09 Hard urethane injection method for continuous production

Publications (2)

Publication Number Publication Date
JPH1024431A true JPH1024431A (en) 1998-01-27
JP3659531B2 JP3659531B2 (en) 2005-06-15

Family

ID=16388144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19825896A Expired - Fee Related JP3659531B2 (en) 1996-07-09 1996-07-09 Hard urethane injection method for continuous production

Country Status (1)

Country Link
JP (1) JP3659531B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004060629A1 (en) * 2003-01-07 2004-07-22 Mitsubishi Rayon Co., Ltd. Belt type continuous plate manufacturing device and method of manufacturing sheet polymer
JP2021525669A (en) * 2018-05-28 2021-09-27 エクテック エンジニアード クォーツ テクノロジー ゲゼルシャフト ミット ベシュレンクテル ハフツング Methods and equipment for forming artificial stone plates

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101570090B1 (en) * 2015-07-29 2015-11-18 주식회사 소노마코리아 Extruding type multilayer concrete panel manufacturing apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004060629A1 (en) * 2003-01-07 2004-07-22 Mitsubishi Rayon Co., Ltd. Belt type continuous plate manufacturing device and method of manufacturing sheet polymer
JP2021525669A (en) * 2018-05-28 2021-09-27 エクテック エンジニアード クォーツ テクノロジー ゲゼルシャフト ミット ベシュレンクテル ハフツング Methods and equipment for forming artificial stone plates

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