JPH0745117B2 - Continuous ejection type self-weight pressurizing device - Google Patents

Continuous ejection type self-weight pressurizing device

Info

Publication number
JPH0745117B2
JPH0745117B2 JP2309540A JP30954090A JPH0745117B2 JP H0745117 B2 JPH0745117 B2 JP H0745117B2 JP 2309540 A JP2309540 A JP 2309540A JP 30954090 A JP30954090 A JP 30954090A JP H0745117 B2 JPH0745117 B2 JP H0745117B2
Authority
JP
Japan
Prior art keywords
product
surface plate
foaming
temperature
time
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2309540A
Other languages
Japanese (ja)
Other versions
JPH04182095A (en
Inventor
徳三 小林
肇 能勢
晃穂 松本
邦義 神田
登紘 土屋
照夫 赤須
Original Assignee
オーエム機器株式会社
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 オーエム機器株式会社 filed Critical オーエム機器株式会社
Priority to JP2309540A priority Critical patent/JPH0745117B2/en
Publication of JPH04182095A publication Critical patent/JPH04182095A/en
Publication of JPH0745117B2 publication Critical patent/JPH0745117B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Lining Or Joining Of Plastics Or The Like (AREA)
  • Press Drives And Press Lines (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は,製品同士の接着,製品に樹脂を注入して発
泡させるときあるいはコンクリートを注入するとき等に
使用して好適な連続取出式自重加圧装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is suitable for continuous take-out self-weight used for adhering products to each other, for pouring resin into products for foaming, or for pouring concrete. The present invention relates to a pressure device.

〔従来の技術〕[Conventional technology]

製品に一定時間,一定の加圧力を付与するのは製品同士
あるいは製品と他の部材を接着したり,製品の内部に発
泡樹脂を充填してこれを発泡させたりするときに必要な
操作であるが,従来はこの操作を製品を加圧装置の間に
ライン状に流す連続式と,製品を多段プレスの間に挟ん
で加圧するバッチ式の二通りの方法で行っていた。
Applying a certain amount of pressure to a product for a certain period of time is a necessary operation when adhering products to each other or between a product and another member, or filling the inside of a product with foamed resin to foam it. However, in the past, this operation was performed by two methods: a continuous method in which the product is flowed in a line between pressurizing devices and a batch method in which the product is sandwiched between multi-stage presses and pressurized.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

連続式の場合は所定の加圧時間を確保するために加圧装
置が非常に長くなる欠点があり,また,バッチ式ではバ
ッチごとに段取り替えをしなければならないから,能率
が上がらないという欠点があった。例えば,発泡樹脂充
填パネルの製造を例にとると,連続式ではコイル状に巻
いたパネル素材(薄金属板)をライン状に繰り出してロ
ール成形,発泡液注入,発泡,切断等の操作を一貫して
行わせるが,成形ロールによる連続成形であるため,例
えば,表面に成形される凸条,凹溝等の幅,深さ等断面
が一様でないものは不可能で,同一断面製品の専用ライ
ンとならざるを得ない欠点があった。また,ライン設備
が非常に長くなり,このラインのほぼ全長に亘って保
温,加圧保持装置が必要であるから,所要スペース,設
備額共に大きなものとなる。
In the case of the continuous type, there is a drawback that the pressurizing device becomes very long in order to secure a predetermined pressurizing time, and in the batch type, the setup must be changed for each batch, so that the efficiency cannot be improved. was there. For example, taking the manufacture of foamed resin filled panels as an example, in the continuous type, the coiled panel material (thin metal plate) is fed out in a line to perform roll molding, foaming liquid injection, foaming, cutting and other operations consistently. However, since it is continuous molding using molding rolls, it is not possible to use ridges, grooves, etc. formed on the surface that have uneven widths, depths, etc. There was a drawback that it had to be a line. In addition, the line equipment becomes very long, and it is necessary to maintain heat and pressurize and hold it over almost the entire length of the line, resulting in large space requirements and equipment costs.

一方バッチ式では成形して仮組したパネル製品を多段プ
レスの各段に挿入し,一定の温度,圧力を保って発泡液
を注入し,この状態を一定時間保持して発泡させるが,
成形工程とは切り離されるため,どの様な断面形状のも
のでも可能である反面,段取り替えをバッチごとに行わ
なければならないから,能率が悪いという欠点があっ
た。また,定盤(多段プレス)には発泡カスが付着する
から,段取り変えの際にはこれを清掃して除去しなけれ
ばならないのであるが,各定盤間の上下間隔は約80〜12
0mmと狭くて清掃道具等を挿入し難く,このため,その
清掃には非常に長い時間を要する。さらに,発泡操作の
間は遊び時間になるという問題もあった。
On the other hand, in the batch method, the panel products that are molded and temporarily assembled are inserted into each stage of the multi-stage press, the foaming liquid is injected while maintaining a constant temperature and pressure, and this state is maintained for a certain period of time for foaming.
Since it is separated from the molding process, any cross-sectional shape can be used, but on the other hand, setup change must be performed for each batch, which is a disadvantage of inefficiency. Also, since foam debris adheres to the surface plate (multi-stage press), it must be cleaned and removed when changing the setup, but the vertical spacing between each surface plate is approximately 80 to 12
Since it is as narrow as 0 mm, it is difficult to insert a cleaning tool, etc. Therefore, it takes a very long time to clean it. Furthermore, there was a problem that there was play time during the foaming operation.

ところで,最近の雨戸や扉等の建築用部品は多品種,多
様化しており,また,連続式では成形できない非常に複
雑な断面形状をしているものが多いから,ほとんどがバ
ッチ式による発泡処理方法を採用している。バッチ式の
最大の欠点は前記したとおりの能率の悪さであるが,一
例を挙げると,10枚重ねの場合に発泡完了までには以下
の時間を要す。
By the way, recent building parts such as shutters and doors are diversified and diversified, and most of them have extremely complicated cross-sectional shapes that cannot be formed by the continuous method, so most of them are foamed by the batch method. The method is adopted. The biggest drawback of the batch method is the inefficiency as described above, but as an example, in the case of stacking 10 sheets, the following time is required until the foaming is completed.

定番の各段への製品挿入 ……1分 製品の予熱 ……1.5分 発泡液の注入 ……0.8分 (一枚に5秒,10枚で5×10=50) キュア(発泡)時間 ……5分 製品取り出し ……1分 定盤の清掃 ……10分 合計 ……約20分 すなわち,一枚当たり発泡させるのに約20÷10=2分の
所要時間を要す。
Inserting the product into each standard stage: 1 minute Preheating the product: 1.5 minutes Injecting the foaming liquid: 0.8 minutes (5 seconds for one sheet, 5 x 10 = 50 for 10 sheets) Cure (foaming) time ... 5 minutes Product removal ...... 1 minute Surface plate cleaning ...... 10 minutes Total ...... About 20 minutes In other words, it takes about 20/10 = 2 minutes to foam each sheet.

そこで,この発明は,バッチ式と連続式の双方の長所を
採用した連続取出式自重加圧装置を具現したものであ
る。
Therefore, the present invention embodies a continuous take-out type self-weight pressurizing device that employs the advantages of both batch type and continuous type.

〔課題を解決するための手段〕[Means for Solving the Problems]

以上の課題を解決するため,この発明は以下の手段を講
じた。
In order to solve the above problems, the present invention has taken the following means.

製品に一定時間,一定の加圧力を付与した後これら製
品を連続して取り出す連続取出式加圧装置であって,製
品を定盤に載せた製品載置定盤を,この製品載置定盤を
一定の数積み上げた段の下に順次挿入して積み上げた前
記製品載置定盤群の自重で加圧するとともに,最上段の
前記製品載置定盤を逐次搬出してなる連続取出式自重加
圧装置。
A continuous take-out type pressurizing device for continuously taking out these products after applying a constant pressing force to the products for a certain period of time. Are sequentially inserted under a certain number of stacked stages to apply pressure by the weight of the product mounting surface plate group that has been stacked, and the uppermost product mounting surface plate is sequentially unloaded and continuously ejected by self-weighting. Pressure device.

前記において,製品載置定盤の積み上げを恒温室の
中で行い,製品に一定の温度を付与してなる連続取出式
自重加圧装置。
In the above, the continuous take-out type self-weight pressurizing device in which the product mounting surface plates are stacked in a thermostatic chamber and a constant temperature is applied to the products.

をそれぞれ提供したものである。Are provided respectively.

〔作用〕[Action]

以上の手段をとることにより,製品に必要な加圧力と加
圧時間は所定の重量を有する製品載置定盤の積み上げの
段数で確保できるから,特別な加圧装置は必要としない
し,また,加圧後の製品の取り出しは連続してできる。
さらに,この製品載置定盤の積み上げを恒温室等の中で
行えば,加圧時間中,一定の温度を付与することもでき
る。
By taking the above means, the pressurizing force and the pressurizing time required for the product can be secured by the number of stacking stages of the product placing platen having a predetermined weight, so that no special pressurizing device is required. The product after pressing can be taken out continuously.
Further, by stacking the product mounting plates in a temperature-controlled room or the like, it is possible to apply a constant temperature during the pressurizing time.

〔実施例〕〔Example〕

以下,この発明の実施例を発泡樹脂充填パネルの製造を
例にとって図面を参照して説明する。
An embodiment of the present invention will be described below with reference to the drawings by taking an example of manufacturing a foamed resin filled panel.

第1図は発泡樹脂充填パネルの製造工程を示す斜視図,
第2図〜第4図は製造装置の正面図,平面図,側面図で
あるが,この製造装置は搬入装置1,発泡装置2,搬送装置
3,搬出装置4および清掃戻し装置5等からなる。
FIG. 1 is a perspective view showing a manufacturing process of a foamed resin filled panel,
2 to 4 are a front view, a plan view and a side view of the manufacturing apparatus. The manufacturing apparatus includes a carry-in device 1, a foaming device 2 and a carrying device.
3. Consists of a carry-out device 4 and a cleaning-back device 5.

搬入装置1は所定の仮組形状に成形し,内部に発泡液を
注入できる空間を形成した製品(ここではパネル製品6a
と呼ぶ)を発泡等を行う恒温室7へ搬入する装置であっ
て,恒温室7へ向かう搬入コンベア8を敷設しておき,
この搬入コンベア8によって一定の投入位置でパネル製
品6aを載せた製品載置定盤(以下,単に定盤という)9
を恒温室7へ搬入する。
The carry-in device 1 is a product that is formed into a predetermined temporary assembly shape and has a space inside which a foaming liquid can be injected (here, the panel product 6a
(Referred to as “equipment”) is carried in to the temperature-controlled room 7 for foaming, and a carry-in conveyor 8 to the temperature-controlled room 7 is laid in advance.
A product placing platen (hereinafter simply referred to as a platen) 9 on which the panel product 6a is placed at a constant loading position by the carry-in conveyor 8.
To the temperature-controlled room 7.

発泡装置2は恒温室7内に搬入されてきたパネル製品6a
に発泡液を注入して発泡させる装置である。その構成
は,まず,40〜60℃に保持された恒温室7(入口側の一
定域は予熱室7aとなっている)を設けておき,パネル製
品6aを載せて搬入されてきた定盤9をこの恒温室7内の
所定位置で停止させる。この位置で定盤9を下からリフ
ト10で持ち上げ,この持ち上げたものをフック11で係止
してこの下側に空間を作り,この空間に搬入されてきた
定盤9を挿入する。この操作を繰り返してパネル製品6a
を載せたままの定盤9を所定段に積み上げて行く。な
お,このとき,挿入した定盤9をすでに積み上げた定盤
9の段に揃えるために,定盤9の周囲から整姿機12を設
けることがある。次に,下から一定の段のパネル製品6a
に注入機13によって発泡液を注入し,これが一定位置ま
で上送されて積み上げられる間に発泡させるのである。
注入された発泡液を発泡させるためには一定の加圧条件
下,一定温度で一定時間その状態を保持させる必要があ
るが,これを恒温室7内の温度と定盤9の重量および搬
入タクトに基づく積み上げ段数および上方への移送時間
によって確保する。第5図は注入機13の説明図である
が,それぞれタンク14,15内に貯溜したP液とR液の発
泡用二液を各々ポンプ16,17で注入ヘッド18に送り,こ
の注入ヘッド18をパネル製品6aの注入孔に挿入して二液
を混合しながら注入するものである。なお,ここで使用
する定盤9はその表面が直接パネル製品6aと接触するも
のであるから,相当の平面度および平滑度を必要とす
る。そのため,硬質クロームメッキ等の表面処理をして
おくのが望ましい。また,このような処理をすることに
よってその表面に付着する発泡液の除去も容易になる。
第6図は以上の恒温室7を一定温度に保つための説明図
であるが,温水ボイラー50で加熱した温水をポンプ51で
熱交換器52との間に循環させ,さらに,この熱交換器52
で熱吸収した温風をファン53で恒温室7との間に循環さ
せる。そして,温水ボイラー50から熱交換器52に至る循
環経路にバイパス通路54を設けておき,この分岐点に設
けた切換弁55を切り換えて温度調節を行うのである。な
お,この切換弁55の操作は恒温室7内の温度,湿度を定
盤9に直接触れる温度センサー56や湿度センサー57で検
出し,中央制御装置58から発する電気的信号によって自
動的に行う(第10図参照)。ところで,このとき,恒温
室7の室温をできるだけ均一に保つため,温風を定盤9
の下部周囲から吹き出し,上方から排風するようにす
る。さらに,図示は省略するが,恒温室7の上部にファ
ン等を設けてこれでかき混ぜれば,室温はさらに均一化
する。第7図は以上のリフト10とフック11の関係を示す
要部断面図であるが,フック11は搬入コンベア8の両側
に二ケずつ設けられて定盤9を搬入位置よりやや高い位
置で下から支えているものである。このため,搬入コン
ベア8の外側にこれと平行にフック11を固嵌したフック
軸59を軸支し,このフック軸59をエアーシリンダ60で回
動させてフック11と定盤9の係脱を行う。すなわち,パ
ネル製品6aを載せた新たな定盤9が搬入されると,リフ
ト10を油圧シリンダ61等で上昇させてこの定盤9を持ち
上げる。定盤9がフック11で支えられた定盤9の下側に
到達すると,エアーシリンダ60を作動させてフック11を
定盤9から離脱させる。この状態のまま,積み上げられ
たすべての定盤9をリフト10でフック11の上まで持ち上
げる。次に,フック11を元に戻してリフト10を下降させ
れば,搬入されてきた定盤9が積み上げの一番下になっ
て全体がフック11で支えられることになる。このとき,
リフト10で持ち上げる定盤9ができるだけフック11で支
えられている定盤9に接近できるように(言い換えれ
ば,フック11の厚みをできるだけ大きくできるように)
フック11の挿入部11aは先細の楔形にしておくととも
に,挿入部11aが挿入される定盤9の上面端部には大き
な面取りの傾斜部9aを形成しておく。こうすると,定盤
9を持ち上げるときにこの傾斜部9aが挿入部11aを押し
上げ,その離脱を容易にする効果もある。さらに,フッ
ク軸59は定盤9の外方,かつ,下方に位置させ,エアー
シリンダ60に作動不良があっても,定盤9の重量はフッ
ク11を係合方向に回動させるようにして安全を保つ。な
お,フック11の必要以上の回動はストッパー62で規制さ
れる。第8図は定盤9と定盤9の間隔を保つためのスペ
ーサ63の側面図,第9図は正面図であるが,このスペー
サ63を定盤9の傾斜部9a等にブラケット64で支えられる
支持軸65の回りに回動可能に構成する。すなわち,パネ
ル製品6aを載せたり取り外したりするときにこのスペー
サ63が邪魔になるときもあるが,このようなときにはス
ペーサ63を回動させて定盤9外に出しておけば邪魔にも
ならず,散逸もしない。なお,このスペーサ63は定盤9
の端に四個程度設けられればよく,また,回動させたと
き,その最高部は定盤9の上面よりも低くなることが条
件である。第10図は注入機13のより具体的な内容を示す
説明図であるが,この場合,注入ヘッド18を独立気泡用
のもの18aと連続気泡用のもの18bの二つに分け,独立気
泡用の注入ヘッド18aにはP1液とR1液を供給するタンク1
4a,15aとポンプ16a,17aのラインを,連続気泡用の注入
ヘッド18bにはP2液とR2液を供給するタンク14b,15bとポ
ンプ16b,17bのラインをそれぞれ別々に形成しておく。
注入ヘッド18a,18bの構造は注入ヘッド18a,18b内に外部
へ噴出する経路とタンク14,15へ循環する経路を形成し
たスプール66a,66bを収容し,このスプール66a,66bを油
圧シリンダ67a,67bの作動によって切り換えるものであ
る。注入量は注入ヘッド18からの噴出量と注入時間で決
まるが,このため,ポンプ16a,16b,17a,17bを可変容量
ポンプとしてその吐出量調整を吐出量調整ダイアル68a,
68b,69a,69b(70a,70b,71a,71bはこれらを動かすモー
タ)で行うとともに,油圧シリンダ67a,67bの伸縮をソ
レノイドバルブ72a,72bで行う。なお,これらの各操作
は前記した中央制御装置58から出力される電気的信号に
よって自動的に行われる。すなわち,パネル製品6aの形
状や用途等に基づく発泡液の注入条件を予めパネル製品
6aごとにバーコード73として記憶させ(このバーコード
73は恒温室7に搬入される定盤9等に貼っておく),こ
のバーコード73に記憶された情報をバーコードリーダ74
で読みとって中央制御装置58に電気的信号として入力
し,この入力信号に基づいて吐出量調整ダイアル68a,68
b,69a,69bの調整とソレノイドバルブ72a,72bの開通時間
の設定が行われるのである。なお,中央制御装置58には
この他に前記した注入条件を手動で入力できるテンキー
式の手動入力装置75や装置の指導開始日時を入力できる
指導開始入力装置76等が接続されている。さらに,ポン
プ16a,16b,17a,17bの吐出側に設けられた流量計77a,77
b,78a,78bで読み取った値も入力されるようになってい
る。一方,中央制御装置58から発っせられる信号は前記
した吐出量調整ダイアル68a,68b,69a,69bやソレノイド
バルブ72a,72bの他にポンプの駆動モータ79a,79b,80a,8
0b,熱交換器81a,81b82a,82bを介してポンプ16a,16b,17
a,17bと並列に接続される高低切換回路を開閉する開閉
弁83a,83b,84a,84b,注入ヘッド18a,18bの選択を表示す
る表示装置85,注入情報をプリントするプリンター86の
他,図示は省略する搬送コンベア8,後記する搬出コンベ
ア20等の各駆動モータ,フック11のエアーシリンダ60や
リフト10の油圧シリンダ61,後記する搬送装置3の搬送
機19等あらゆる駆動装置へ送られ,この中央制御装置58
で集中的に制御する。第11図はパネル製品6aに付着する
発泡カスをそぎ落とすためのスクレーパ87の斜視図,第
12図は要部断面図であるが,パネル製品6aの注入孔88付
近には発泡液の漏れによる発泡カスが付着しているか
ら,定盤9が積み上げられて行く間にパネル製品6aの表
面に当接してこれをそぎ落とすスクレーパ87を設けたも
のである。なお,パネル製品6aおよびこれを載置する定
盤9の表面は多少出入りがあるから,この出入りがあっ
てもパネル製品6aおよびこれを載置する定盤9の表面は
多少出入りがあるから,この出入りがあってもパネル製
品6aが積み上げられて行く間に引っ掛かからないように
スクレーパ87を斜めに取り付けるるとともに,スクレー
パ87が常にパネル製品6aの表面に当接するようにスプリ
ング89で弾性的に付勢しておく。また,スクレーパ87の
下方にはそぎ落とした発泡カスを受け止める樋90を付設
しておき,この樋90で発泡カスを収集箱91に導く。とこ
ろで,定盤9上の載せられたパネル製品6aは搬入コンベ
ア8によって連続して移送されるが,発泡位置でフック
11やリフト10で多段に積み上げられるときには,これら
の作動は短時間で完了するから,大部分は停止した間欠
送りとなる。したがって,注入作業はこの停止時間に行
えばよいから,注入ヘッド18の注入孔88への挿入を始め
とする各種の注入作業の容易性は確保できる。
The foaming device 2 is a panel product 6a that has been brought into the temperature-controlled room 7.
This is a device for injecting a foaming liquid into the foam and foaming it. The structure is such that a constant temperature room 7 (40 ° C. to 60 ° C.) (a certain area on the inlet side is a preheating room 7 a) is provided, and a platen 9 that has been loaded with the panel product 6 a is loaded. Is stopped at a predetermined position in the temperature-controlled room 7. At this position, the surface plate 9 is lifted from below by a lift 10, the lifted part is locked by a hook 11, a space is formed below this, and the surface plate 9 carried into this space is inserted. Repeat this operation for panel product 6a
The surface plates 9 with the above are placed in a predetermined stack. At this time, a dressing machine 12 may be provided around the surface plates 9 in order to align the inserted surface plates 9 with the steps of the already stacked surface plates 9. Next, from the bottom, a certain level of panel product 6a
The injecting machine 13 injects the foaming liquid into the container, and the foaming liquid is transferred to a certain position and foamed while being piled up.
In order to foam the injected foaming liquid, it is necessary to maintain the condition at a constant temperature and for a constant time under a constant pressurizing condition. It is secured by the number of stacking stages based on the above and transfer time to the upper side. FIG. 5 is an explanatory view of the injection machine 13. The two foaming liquids of the P liquid and the R liquid stored in the tanks 14 and 15 are sent to the injection head 18 by the pumps 16 and 17, respectively. Is inserted into the injection hole of the panel product 6a and injected while mixing the two liquids. Note that the surface plate 9 used here has a surface that directly contacts the panel product 6a, and therefore requires considerable flatness and smoothness. Therefore, it is desirable to perform surface treatment such as hard chrome plating. Further, such treatment also facilitates removal of the foaming liquid adhering to the surface.
FIG. 6 is an explanatory view for keeping the temperature-controlled room 7 at a constant temperature. The hot water heated by the hot water boiler 50 is circulated between the heat exchanger 52 by the pump 51 and the heat exchanger 52. 52
The warm air, which has been absorbed by, is circulated between the constant temperature chamber 7 and the fan 53. Then, a bypass passage 54 is provided in the circulation path from the hot water boiler 50 to the heat exchanger 52, and the switching valve 55 provided at this branch point is switched to adjust the temperature. The switching valve 55 is operated by detecting the temperature and humidity in the temperature-controlled room 7 by a temperature sensor 56 and a humidity sensor 57 that directly contact the surface plate 9 and automatically by an electric signal emitted from a central controller 58 ( (See Figure 10). By the way, at this time, in order to keep the room temperature of the temperature-controlled room 7 as uniform as possible, warm air is blown on the platen 9.
Make sure that the air is blown out from around the bottom of the and the air is exhausted from above. Further, although not shown, if a fan or the like is provided above the temperature-controlled room 7 and agitated with this, the room temperature is further homogenized. FIG. 7 is a cross-sectional view showing the relationship between the lift 10 and the hook 11 as described above. Two hooks 11 are provided on each side of the carry-in conveyor 8 so that the surface plate 9 is located slightly higher than the carry-in position. It is supported from. For this reason, a hook shaft 59 having a hook 11 fixedly mounted on the outside of the carry-in conveyor 8 is pivotally supported in parallel with this, and the hook shaft 59 is rotated by an air cylinder 60 to disengage the hook 11 from the surface plate 9. To do. That is, when a new surface plate 9 on which the panel product 6a is placed is carried in, the lift 10 is raised by the hydraulic cylinder 61 or the like to lift the surface plate 9. When the surface plate 9 reaches the lower side of the surface plate 9 supported by the hooks 11, the air cylinder 60 is operated to disengage the hooks 11 from the surface plate 9. In this state, all the stacked surface plates 9 are lifted up by the lifts 10 onto the hooks 11. Next, when the hook 11 is returned to the original position and the lift 10 is lowered, the surface plate 9 that has been carried in is at the bottom of the stack, and the entire hook is supported by the hook 11. At this time,
Make the surface plate 9 lifted by the lift 10 as close as possible to the surface plate 9 supported by the hooks 11 (in other words, make the thickness of the hooks 11 as large as possible).
The insertion portion 11a of the hook 11 is formed in a tapered wedge shape, and a large chamfered inclined portion 9a is formed at the upper end of the surface plate 9 into which the insertion portion 11a is inserted. In this way, when the surface plate 9 is lifted up, the inclined portion 9a pushes up the insertion portion 11a, which facilitates its removal. Further, the hook shaft 59 is positioned outside and below the surface plate 9 so that even if the air cylinder 60 has a malfunction, the weight of the surface plate 9 causes the hook 11 to rotate in the engaging direction. Keep safe. The stopper 62 prevents the hook 11 from rotating more than necessary. FIG. 8 is a side view of the spacer 63 for keeping the space between the surface plate 9 and the surface plate 9, and FIG. 9 is a front view. The spacer 63 is supported on the inclined portion 9a of the surface plate 9 by the bracket 64. It is configured to be rotatable around a supported support shaft 65. That is, when the panel product 6a is placed or removed, the spacer 63 sometimes becomes an obstacle, but in such a case, it is not an obstacle if the spacer 63 is rotated and taken out of the surface plate 9. , Neither dissipated. The spacer 63 is a surface plate 9
It suffices that about four be provided at the end of the table, and when rotated, the highest part thereof should be lower than the upper surface of the surface plate 9. FIG. 10 is an explanatory view showing the more specific contents of the injection machine 13. In this case, the injection head 18 is divided into two parts, one for independent bubbles 18a and one for continuous bubbles 18b Tank 1 for supplying P1 liquid and R1 liquid to injection head 18a of
Lines 4a, 15a and pumps 16a, 17a are formed separately in the injection head 18b for continuous bubbles, and tanks 14b, 15b for supplying P2 liquid and R2 liquid and pumps 16b, 17b are separately formed.
The structure of the injection heads 18a, 18b is such that the injection heads 18a, 18b accommodate spools 66a, 66b which form a path for ejecting to the outside and a path for circulation to the tanks 14, 15, and these spools 66a, 66b are connected to a hydraulic cylinder 67a, It is switched by the operation of 67b. The injection amount is determined by the injection amount from the injection head 18 and the injection time. For this reason, the pumps 16a, 16b, 17a, and 17b are used as variable displacement pumps, and the discharge amount is adjusted by the discharge amount adjusting dial 68a,
68b, 69a, 69b (70a, 70b, 71a, 71b are motors for moving these), and hydraulic cylinders 67a, 67b are expanded and contracted by solenoid valves 72a, 72b. Each of these operations is automatically performed by an electric signal output from the central controller 58. That is, the injection conditions of the foaming liquid based on the shape and use of the panel product 6a are set in advance in the panel product
Each 6a is stored as a barcode 73 (this barcode
73 is attached to the surface plate 9 or the like which is carried into the temperature-controlled room 7), and the information stored in the barcode 73 is read by the barcode reader 74.
Is read and input as an electric signal to the central control unit 58, and based on this input signal, the discharge amount adjusting dials 68a, 68
The adjustment of b, 69a, 69b and the setting of the opening time of the solenoid valves 72a, 72b are performed. In addition to this, the ten-key type manual input device 75 capable of manually inputting the above-mentioned injection conditions, the instruction start input device 76 capable of inputting the instruction start date and time of the device, and the like are connected to the central controller 58. Furthermore, the flowmeters 77a, 77a provided on the discharge side of the pumps 16a, 16b, 17a, 17b
The values read by b, 78a and 78b are also input. On the other hand, the signal issued from the central control unit 58 is the pump drive motors 79a, 79b, 80a, 8 in addition to the above-mentioned discharge rate adjusting dials 68a, 68b, 69a, 69b and solenoid valves 72a, 72b.
0b, pumps 16a, 16b, 17 via heat exchangers 81a, 81b 82a, 82b
Open / close valves 83a, 83b, 84a, 84b for opening / closing a high / low switching circuit connected in parallel with a, 17b, a display device 85 for displaying selection of the injection heads 18a, 18b, a printer 86 for printing injection information, and other drawings Are omitted, and each drive motor of the conveyer 8, the carry-out conveyer 20 and the like described later, the air cylinder 60 of the hook 11 and the hydraulic cylinder 61 of the lift 10, the conveyer 19 of the conveyer 3 described later, and the like are sent to all kinds of drive devices. Central controller 58
Centrally control with. FIG. 11 is a perspective view of a scraper 87 for scraping off foam residue attached to the panel product 6a.
Figure 12 is a cross-sectional view of the main part, but since foam residue due to the leakage of foam liquid adheres to the vicinity of the injection hole 88 of the panel product 6a, the surface of the panel product 6a while the surface plate 9 is being stacked. A scraper 87 is provided which abuts against and scrapes off the scraper. Since the surface of the panel product 6a and the surface plate 9 on which the panel product 6 is mounted are slightly in and out, the surface of the panel product 6a and the surface plate 9 on which the panel product 6a is mounted are slightly in and out, The scraper 87 is attached diagonally so that the scraper 87 does not get caught while the panel products 6a are being stacked even if there is such an entrance / exit. At the same time, the scraper 87 is elastically supported by the spring 89 so that the scraper 87 always contacts the surface of the panel product 6a. Keep urging. Further, a gutter 90 for receiving the scraped foam residue is attached below the scraper 87, and the foam residue is guided to the collection box 91 by this gutter 90. By the way, the panel products 6a placed on the surface plate 9 are continuously transferred by the carry-in conveyor 8, but are hooked at the foaming position.
When stacked in multiple stages with 11 or lift 10, these operations are completed in a short time, and most of them are stopped intermittent feed. Therefore, since the injection work may be performed during this stop time, the ease of various injection works including the insertion of the injection head 18 into the injection hole 88 can be ensured.

搬送装置3は発泡処理が完了して積み上げの最上段に上
がってきた発泡パネル製品6bを別の位置まで搬送する装
置であり,昇降機能と搬送機能を有する搬送機19によ
る。すなわち,搬送機19によって最上段の発泡パネル製
品6bを定盤9ごと吊り上げて側方位置まで搬送し,この
位置で恒温室7から出る搬出コンベア20の上に降ろすの
である。第13図はこの搬送機19の具体例を示す正面図で
あるが,搬入コンベア8と搬出コンベア20のそれぞれ上
方に渡されたレール92の上を走行する台車93から定盤9
とほぼ等しい広がりの矩形体のフレーム94を油圧シリン
ダ95で昇降可能に吊り下げ,このフレーム94の四隅に設
けられた各々大小二つのフック96,97で定盤9の端を引
っ掛けて走行するのである。
The transfer device 3 is a device that transfers the foamed panel products 6b that have been raised to the top of the stack after the foaming process is completed to another position, and is based on the transfer device 19 that has a lifting function and a transfer function. That is, the uppermost foam panel product 6b is lifted together with the platen 9 by the carrier machine 19 and conveyed to the side position, and at this position, the foamed panel product 6b is unloaded onto the carry-out conveyor 20 coming out of the temperature-controlled room 7. FIG. 13 is a front view showing a concrete example of the carrier 19. The carriage 93 to the surface plate 9 traveling on rails 92 provided above the carry-in conveyor 8 and the carry-out conveyor 20, respectively.
A rectangular frame 94 having a width substantially equal to that of the frame 94 is suspended by a hydraulic cylinder 95 so that the frame 94 can be moved up and down, and two large and small hooks 96 and 97 provided at the four corners of the frame 94 hook the ends of the surface plate 9 for traveling. is there.

すなわち,発泡パネル製品6bの厚みの関係で定盤9間は
あまり広くはできないので,最初は厚みも薄く,かつ,
掛かり深さも浅い小フック96で吊り上げ,十分吊り上が
ったところで,厚みも厚く,かつ掛かり深さも深い大フ
ック97でつかみ直すのである。なお,大小のフック96,9
7とも,定盤9に対する係脱動作は油圧シリンダ98,99の
作動で行い,この油圧シリンダ98,99の作動は前記した
中央制御装置58から発する指令に基づいて自動的に行わ
れる。また,大小のフック96,97で定盤9を吊り上げた
とき,定盤9とフレーム94との間には当て材100を介在
させ,定盤9は上下方向には動かない構造にして安全性
を確保する。
That is, since the space between the surface plates 9 cannot be made too wide due to the thickness of the foam panel product 6b, the thickness is thin at first, and
The small hook 96, which has a small hooking depth, is used to hang it up, and when it is sufficiently hung up, the large hook 97, which is thick and has a deep hooking depth, is used to grasp it again. In addition, large and small hooks 96, 9
7, the engagement / disengagement operation with respect to the surface plate 9 is performed by the operation of the hydraulic cylinders 98, 99, and the operation of the hydraulic cylinders 98, 99 is automatically performed based on the command issued from the central controller 58 described above. Further, when the surface plate 9 is lifted by the large and small hooks 96 and 97, the padding material 100 is interposed between the surface plate 9 and the frame 94, and the surface plate 9 is structured so as not to move in the vertical direction for safety. Secure.

搬出装置4は搬出コンベア20によって恒温室7から発送
されてきた発泡パネル製品6bを定盤9の上から取り去る
装置であり,この操作ができるためのスペースを有し,
適当な突出装置や搬出シュートを備えているものである
(突き出しは人力によるのでもよい)。なお,搬出され
た発泡パネル製品6bは本組等の次の工程に廻される。
The carry-out device 4 is a device for removing the foam panel product 6b sent from the temperature-controlled room 7 by the carry-out conveyor 20 from the surface plate 9, and has a space for performing this operation.
It is equipped with an appropriate projecting device and a discharging chute (the projecting may be done manually). In addition, the discharged foam panel product 6b is sent to the next process such as the main assembly.

清掃戻し装置5は空になった定盤9の表裏面を清掃し,
パネル製品6aを載置する位置まで回送する装置である。
すなわち,定盤9には漏れ出た発泡液が付着しているか
ら,これを清掃して除去しなければならないのである
が,このため,搬出コンベア20上に強制回転させられる
清掃ローラ21を設けておき,この間をくぐらせて定盤9
を清掃する。清掃された定盤9は始端と終端が搬出コン
ベア20と搬入コンベア8に交錯する回送コンベア22に載
せられて元の投入位置まで送られる。なお,この回送コ
ンベア22は搬出,搬入コンベア20,8と交錯しているか
ら,定盤9の引き継ぎ個所に昇降機23を設け,この昇降
機23の昇降で引き継ぎさせるようにしている。この他,
各コンベア8,20,22の経路には定盤9を案内するための
ガイドローラ24等を設けておく。そして,最初の投入位
置に戻された定盤9には再びパネル製品6aが載せられ,
搬入コンベア8で恒温室7へ搬入される。
The cleaning back device 5 cleans the front and back surfaces of the empty surface plate 9,
This is a device for feeding the panel product 6a to the position where it is placed.
That is, since the leaking foaming liquid adheres to the surface plate 9 and must be removed by cleaning it, for this reason, a cleaning roller 21 forcibly rotated is provided on the carry-out conveyor 20. Let's go through this space and platen 9
To clean. The cleaned surface plate 9 is placed on the forwarding conveyor 22 where the start end and the end end intersect with the carry-out conveyor 20 and the carry-in conveyor 8 and sent to the original loading position. Since the transfer conveyor 22 intersects with the carry-out and carry-in conveyors 20 and 8, an elevator 23 is provided at a place where the surface plate 9 is taken over, and the elevator 23 moves up and down to take over. Besides this,
Guide rollers 24, etc. for guiding the surface plate 9 are provided on the paths of the conveyors 8, 20, 22. Then, the panel product 6a is placed on the surface plate 9 returned to the initial loading position again,
It is carried into the temperature-controlled room 7 by the carry-in conveyor 8.

以上の各装置を中央制御装置58によって定盤9の流れに
沿ったプログラムで作動させれば,パネル製品6aに発泡
液を注入してこれを発泡パネル製品6bとするための搬
入,発泡,搬送,搬出,清掃戻しの各操作が連続して自
動的に行われるのである。そして,その処理時間は定盤
9の搬送タクト時間で決り,また,これによって恒温室
7での定盤9の積み上げ段数も決まる。
If each of the above devices is operated by the central controller 58 according to the program following the flow of the surface plate 9, the foaming liquid is injected into the panel product 6a to carry it into the foaming panel product 6b, foaming, and conveying. The operations of unloading and cleaning back are continuously and automatically performed. The processing time is determined by the transport tact time of the surface plate 9, and the stacking number of the surface plate 9 in the temperature-controlled room 7 is also determined by this.

すなわち,発泡処理には40〜60℃の雰囲気温度を保ち,
キュア時間5分,キュア圧力0.2kg/cm2の条件が必要で
あるが,これを1,300mm×2,500mm×25mmの鉄製の定盤9
(重量は640kgになり,これを一段載せたことによって
受ける面圧は0.02kg/cm2となる)を用いてタクト時間を
30秒に設定すれば(したがって,0.5分おきに一枚ずつ仕
上がることになる),必要なキュア圧力0.2kg/cm2を得
るためには0.2÷0.02=10となり,少なくとも,この上
に10段重ねれば定盤9の自重のみで特別の加圧装置は要
らないことになる。一方,必要なキュア時間5分を得る
ためには5÷0.5=10となるから,前の10段の下にもう1
0段重ねればよいことになる。また,予熱時間1.5分をと
るとすれば,1.5÷0.5=3となり,さらに3段とればよ
いことになる。したがって,最低10+10+3=23段積み
重ねれば十分ということになる。
That is, for the foaming process, keep the ambient temperature of 40-60 ° C,
A curing time of 5 minutes and a curing pressure of 0.2 kg / cm 2 are required. These are 1,300 mm × 2,500 mm × 25 mm iron surface plate 9
(Weight becomes 640 kg, and the surface pressure received by placing this one step becomes 0.02 kg / cm 2 )
If it is set to 30 seconds (thus, one sheet will be finished every 0.5 minutes), 0.2 ÷ 0.02 = 10 to obtain the required curing pressure of 0.2 kg / cm 2 , and at least 10 steps above this. If they are piled up, only the weight of the surface plate 9 is required and no special pressure device is needed. On the other hand, in order to obtain the required cure time of 5 minutes, 5 ÷ 0.5 = 10.
It is enough to stack 0 layers. If the preheating time is 1.5 minutes, 1.5 ÷ 0.5 = 3, which means that 3 more stages are required. Therefore, it is sufficient to stack at least 10 + 10 + 3 = 23 layers.

なお,以上の装置の運転開始時,短時間で定盤9を所定
温度(40〜60℃)に上げるため,搬入コンベア8の上下
に加熱装置(図示省略)を取り付けるようにすれば,作
業開始までのウォーミングアップ時間を短縮でき,より
効率的な作業が可能となる。また,前記の説明で恒温室
7は発泡装置2の部分だけとしたが,装置全体を恒温室
7とすることも考えられる。
It should be noted that, in order to raise the surface plate 9 to a predetermined temperature (40 to 60 ° C.) in a short time at the start of the operation of the above apparatus, if a heating device (not shown) is attached above and below the carry-in conveyor 8, the work will start. It is possible to shorten the warming-up time up to and work more efficiently. Further, in the above description, the temperature-controlled room 7 is limited to the foaming device 2, but it is also conceivable to use the entire device as the temperature-controlled room 7.

その他,以上の説明は発泡処理についてのものである
が,同様なことは接着その他の処理についても適用でき
ることはもちろんである。
In addition, although the above description relates to the foaming process, the same thing can be applied to the other processes such as bonding.

ところで,以上のような装置で発泡樹脂充填パネルを製
造すれば,次のような有益な効果が期待できる。すなわ
ち,製品の形状に限定されない従来のバッチ式の良さと
連続式の効率の良さとを兼ね備えることができたのであ
る。具体的には, i)発泡処理を始めとする各処理は各コンベア8,21,22
の作動による連続式であるから,遊び時間等がなく効率
が良い。すなわち,前記したように30秒タクトに設定す
ればバッチ式のものに比べて少なくとも4倍の能率を有
する。
By the way, if the foamed resin filled panel is manufactured by the above apparatus, the following beneficial effects can be expected. That is, it was possible to combine the goodness of the conventional batch type, which is not limited to the shape of the product, and the good efficiency of the continuous type. Specifically, i) each processing including foaming processing is performed on each conveyor 8, 21, 22
Since it is a continuous type by the operation of, there is no play time and it is efficient. That is, as described above, if the tact time is set to 30 seconds, the efficiency is at least four times that of the batch type.

ii)発泡処理は定盤9を積み上げて行うものであり,ま
た,各コンベア8,21,22はエンドレスに周回するもので
あるから,装置全体が占めるスペースは小さくて足り,
連続式のように長い距離の保温,加圧装置を必要としな
い。
ii) Since the foaming process is performed by stacking the platens 9 and the conveyors 8, 21, 22 circulate endlessly, the space occupied by the entire apparatus is small,
Does not require a long-distance heat insulation and pressurizing device unlike the continuous type.

iii)バッチ式で従来非常に多くの時間を要していた空
になった定盤9の清掃がこのように流れ作業式の自動で
できるようになったので,結果として大幅な時間短縮が
可能になった。
iii) With the batch method, it became possible to clean the empty surface plate 9 which required a lot of time in the past by such a flow work type automatic, and as a result, it is possible to greatly reduce the time. Became.

iv)定盤9の十分な積み上げ段数を確保しておけば,タ
クト時間も変更でき,その結果,処理能力を適宜調整す
ることができる。
iv) If a sufficient number of stacking stages of the surface plate 9 is secured, the tact time can be changed, and as a result, the processing capacity can be adjusted appropriately.

v)各処理操作は定盤9ごと行うものであり,また,こ
の上に載せるパネル製品6aの形状を変えたとしてもそれ
に影響を受けないのであるから,流れている製品の間に
形状の異なる製品を挟むようなことも可能であり,異品
種混合生産ができる。
v) Each processing operation is performed on the surface plate 9, and even if the shape of the panel product 6a placed on this is not affected, the shape of the flowing product differs. It is also possible to sandwich products, enabling mixed production of different products.

vi)定盤9の発泡位置での積み上げは間欠送りとなり,
この停止している間に発泡液の注入を行うものであるか
ら,この作業に支障を来さない。
vi) Stacking of the surface plate 9 at the foaming position is intermittent feed,
Since the foaming liquid is injected during this stop, this work is not hindered.

〔発明の効果〕〔The invention's effect〕

以上,この発明は前記したものであるから,すなわち,
単に製品6aを載せた定盤9を一定段に積み上げるだけで
必要な加圧力および時間を確保できたものであるから,
従来のバッチ式のような特別なプレス装置等を必要とせ
ず,かつ,段取り替えも必要としないので,能率の良い
装置を低コストで製作できる。また,製品形状は自由で
あるから,連続式のように製品形状に制約を受けるとい
ったこともない。さらに,定盤9の積み上げは上方に行
うものであるから,設置スペースはきわめて小さくて足
りる。この他,定盤9の積み上げを恒温室7等で行え
ば,一定の加圧力,時間の他に一定の温度も付与してそ
の適用性をより拡大する。
As described above, the present invention is as described above, that is,
Since the necessary pressing force and time can be secured simply by stacking the platen 9 on which the product 6a is placed in a certain level,
Since no special press equipment such as the conventional batch type is required and no setup change is required, a highly efficient device can be manufactured at low cost. Moreover, since the product shape is free, there is no restriction on the product shape unlike the continuous type. Further, since the platens 9 are piled up, the installation space is extremely small. In addition, if the surface plates 9 are stacked in the temperature-controlled room 7 or the like, a certain pressure is applied and a certain temperature is applied in addition to the time, so that the applicability thereof is further expanded.

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

第1図はこの発明の実施例を示す発泡樹脂充填パネルの
製造工程を示す斜視図,第2図〜第4図はこのパネル製
造装置の要部を示す正面図,平面図,側面図,第5図は
注入機の説明図,第6図は恒温室の説明図,第7図はフ
ックとリフトの関係を示す一部断面図,第8図はスペー
サの状態を示す側面図,第9図は正面図,第10図は注入
機の概要を示す説明図,第11図はスクレーパの斜視図,
第12図はその要部の断面図,第13図は搬送機の側面図で
ある。 (符号) 6a……製品 7……恒温室 9……製品載置定盤
FIG. 1 is a perspective view showing a manufacturing process of a foamed resin-filled panel showing an embodiment of the present invention, and FIGS. 2 to 4 are front views, plan views, side views, and FIG. Fig. 5 is an explanatory view of an injection machine, Fig. 6 is an explanatory view of a temperature-controlled room, Fig. 7 is a partial sectional view showing the relationship between hooks and lifts, Fig. 8 is a side view showing the state of spacers, and Fig. 9 Is a front view, FIG. 10 is an explanatory view showing the outline of the injection machine, FIG. 11 is a perspective view of the scraper,
FIG. 12 is a sectional view of the main part, and FIG. 13 is a side view of the carrier. (Code) 6a …… Product 7 …… Constant temperature room 9 …… Product mounting platen

───────────────────────────────────────────────────── フロントページの続き (72)発明者 神田 邦義 岡山県岡山市今2丁目7番1号 オーエム 機器株式会社岡山本社内 (72)発明者 土屋 登紘 茨城県東茨城郡桂村北方2178番地 オーエ ム機器株式会社茨城工場内 (72)発明者 赤須 照夫 茨城県東茨城郡桂村北方2178番地 オーエ ム機器株式会社茨城工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kuniyoshi Kanda Kuniyoshi Kanda 2-7-1 Ima 2-chome, Okayama City, Okayama Prefecture OEM Equipment Co., Ltd. Okayama Main Office (72) Inventor Toko Tsuchiya 2178, Kitamura, Higashi-Ibaraki-gun, Ibaraki Ohe Mu Equipment Co., Ltd. Ibaraki Plant (72) Inventor Teruo Akasu 2178, Kitamura Kitamura, Higashi Ibaraki District, Ibaraki Prefecture O Equipment Co., Ltd. Ibaraki Factory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】製品(6a)に一定時間,一定の加圧力を付
与した後これら製品(6a)を連続して取り出す連続取出
式加圧装置であって,前記製品(6a)を定盤に載せた製
品載置定盤(9)を,この製品載置定盤(9)を一定の
数積み上げた段の下に順次挿入して積み上げた前記製品
載置定盤(9)群の自重で加圧するとともに,最上段の
前記製品載置定盤(9)を逐次搬出してなる連続取出式
自重加圧装置。
1. A continuous take-out pressurizing device for continuously taking out a product (6a) after applying a constant pressure to the product (6a) for a predetermined time, wherein the product (6a) is placed on a surface plate. The product placing surface plates (9) placed on the product placing surface plates (9) are sequentially inserted under a step in which a certain number of the product placing surface plates (9) are stacked, and the product placing surface plates (9) are stacked by their own weight. A continuous take-out type self-weight pressurizing device which pressurizes and successively carries out the uppermost product placing surface plate (9).
【請求項2】製品載置定盤(9)の積み上げを恒温室
(7)の中で行い,製品(6a)に一定の温度を付与して
なる請求項記載の連続取出式自重加圧装置。
2. A continuous take-out type self-weight pressurizing device according to claim 1, wherein the product placing platens (9) are stacked in a constant temperature chamber (7) and a constant temperature is applied to the product (6a). .
JP2309540A 1990-11-14 1990-11-14 Continuous ejection type self-weight pressurizing device Expired - Fee Related JPH0745117B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2309540A JPH0745117B2 (en) 1990-11-14 1990-11-14 Continuous ejection type self-weight pressurizing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2309540A JPH0745117B2 (en) 1990-11-14 1990-11-14 Continuous ejection type self-weight pressurizing device

Publications (2)

Publication Number Publication Date
JPH04182095A JPH04182095A (en) 1992-06-29
JPH0745117B2 true JPH0745117B2 (en) 1995-05-17

Family

ID=17994246

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2309540A Expired - Fee Related JPH0745117B2 (en) 1990-11-14 1990-11-14 Continuous ejection type self-weight pressurizing device

Country Status (1)

Country Link
JP (1) JPH0745117B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6040692B2 (en) * 2012-10-03 2016-12-07 住友ベークライト株式会社 Manufacturing method of laminate

Also Published As

Publication number Publication date
JPH04182095A (en) 1992-06-29

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