JP2693340B2 - Device for controlling the expansion ratio of pre-expanded resin particles - Google Patents
Device for controlling the expansion ratio of pre-expanded resin particlesInfo
- Publication number
- JP2693340B2 JP2693340B2 JP4066121A JP6612192A JP2693340B2 JP 2693340 B2 JP2693340 B2 JP 2693340B2 JP 4066121 A JP4066121 A JP 4066121A JP 6612192 A JP6612192 A JP 6612192A JP 2693340 B2 JP2693340 B2 JP 2693340B2
- Authority
- JP
- Japan
- Prior art keywords
- resin particles
- foaming
- expanded resin
- measuring
- expansion
- 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
Links
- 239000002245 particle Substances 0.000 title claims description 105
- 229920005989 resin Polymers 0.000 title claims description 96
- 239000011347 resin Substances 0.000 title claims description 96
- 238000005187 foaming Methods 0.000 claims description 96
- 238000005070 sampling Methods 0.000 claims description 56
- 238000005303 weighing Methods 0.000 claims description 53
- 239000002994 raw material Substances 0.000 claims description 46
- 238000003860 storage Methods 0.000 claims description 34
- 229920003002 synthetic resin Polymers 0.000 claims description 5
- 239000000057 synthetic resin Substances 0.000 claims description 5
- 238000005259 measurement Methods 0.000 description 28
- 238000000034 method Methods 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000012937 correction Methods 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- -1 for example Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920006248 expandable polystyrene Polymers 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、特にバッチ式の予備発
泡機に適用され、発泡性合成樹脂粒子の予備発泡倍数を
自動的に制御する予備発泡樹脂粒子の発泡倍数制御装置
に関するものである。The present invention relates in particular be applied to a batch type pre-foaming machine, expansion ratio control apparatus of the pre-expanded resin particles to automatically control the pre-expansion ratio of the foamable synthetic resin particles <br/> It is about.
【0002】[0002]
【従来の技術】従来、発泡性ポリスチレン等の発泡性合
成樹脂粒子の予備発泡倍数を制御するには、発泡缶体等
からなる予備発泡機の有効容積を基にし、予め予備発泡
倍数に見合う量の投入原料を計算理論値で求めて設定値
として計測器に入力し、例えば、重量測定用のロードセ
ルを設置した計量タンクで所定重量の原料を自動計量す
る。2. Description of the Related Art Conventionally, in order to control the pre-expansion multiple of expandable synthetic resin particles such as expandable polystyrene, an amount commensurate with the pre-expansion multiple is based on the effective volume of a pre-expanding machine including a foam can body. The input raw material of No. 2 is calculated as a theoretical value and is input as a set value into the measuring instrument. For example, a predetermined weight of raw material is automatically weighed in a weighing tank provided with a load cell for weight measurement.
【0003】続いて、計量された原料は予備発泡機の上
部より投入された後、予備発泡機の底面の有孔板から蒸
気および圧縮エアーが吹き込まれ、この熱媒により発泡
し、膨張する。この発泡は、予備発泡機の上端付近に設
けたレベル計に発泡粒が到達することにより発生される
信号に基づいて蒸気の供給が停止されるまで続けられ
る。Subsequently, the metered raw material is charged from the upper portion of the pre-foaming machine, and then steam and compressed air are blown from the perforated plate on the bottom surface of the pre-foaming machine, and the heat medium foams and expands. This foaming is continued until the supply of steam is stopped on the basis of a signal generated when the foamed particles reach the level meter provided near the upper end of the pre-foaming machine.
【0004】ところで、予備発泡倍数は、吹込蒸気圧力
値、エアーレーション(圧縮エアー投入値)、原料の配
合剤種および、使用する蒸気の質等により変化する。従
って、予備発泡倍数を正確に制御したい場合、作業者
が、発泡を完了して排出された予備発泡樹脂粒子を計量
カップを用いてサンプリングし、予備発泡樹脂粒子の正
味重量と計量カップの容積から実際の予備発泡倍数を算
出し、設定値との誤差に応じて適宜原料投入量を補正す
るという作業を繰り返しているのが実状である。By the way, the pre-expansion multiple varies depending on the blow steam pressure value, aeration (compressed air input value), the type of raw material compounding agent, the quality of steam used, and the like. Therefore, when it is desired to accurately control the pre-expansion multiple, the operator samples the pre-expanded resin particles that have been foamed and is discharged, using a measuring cup, and calculates the net weight of the pre-expanded resin particles and the volume of the measuring cup. The actual situation is to repeat the work of calculating the actual prefoaming multiple and correcting the raw material input amount appropriately according to the error from the set value.
【0005】[0005]
【発明が解決しようとする課題】ところが、上記の如
く、作業者が予備発泡樹脂粒子をサンプリングして予備
発泡倍数を測定し、必要により原料投入量を補正すると
いう方法では、計量カップによる測定および原料投入量
の修正に手間が掛かり、作業が煩雑になる問題を有して
いる。However, as described above, in the method in which the operator samples the pre-expanded resin particles to measure the pre-expansion multiple and corrects the raw material input amount as necessary, the measurement by the measuring cup and There is a problem that it takes time and effort to correct the amount of raw material input and the work becomes complicated.
【0006】[0006]
【課題を解決するための手段】本発明の予備発泡樹脂粒
子の発泡倍数制御装置は、上記の課題を解決するため
に、合成樹脂粒子からなる原料を予備発泡機内で予備発
泡させて予備発泡樹脂粒子を得るに際し、上記の予備発
泡樹脂粒子の予備発泡倍数を制御する予備発泡樹脂粒子
の発泡倍数制御装置において、入力された設定予備発泡
倍数に基づいて原料を供給して予備発泡させる予備発泡
機と、該予備発泡機から排出された予備発泡樹脂粒子を
収納する収納ホッパと、上記収納ホッパの上方に配設さ
れており、その下端面の開口を開閉可能とするダンパー
を有している所定容量の計量容器と、上記収納ホッパの
下部と上記計量容器の上部側面とを連通しているサンプ
リング管と、上記収納ホッパへ排出された予備発泡樹脂
粒子を上記サンプリング管を介して上記計量容器に搬送
して充填するための圧縮空気を該サンプリング管に送る
サンプリング用送風管と、上記計量容器の重量を計量す
るための計量手段と、上記計量容器に予備発泡樹脂粒子
を充填するサンプリング動作を制御するとともに、上記
計量手段により計量された予備発泡樹脂粒子の重量と上
記計量容器の容積とから予備発泡樹脂粒子の発泡倍数を
換算する倍数測定装置制御盤とを備えていることを特徴
とするものである。SUMMARY OF THE INVENTION In order to solve the above problems, a device for controlling the expansion ratio of pre-expanded resin particles according to the present invention is a pre-expanded resin prepared by pre-expanding a raw material made of synthetic resin particles in a pre-expanding machine. In obtaining the particles, in the expansion ratio controller for the pre-expansion resin particles for controlling the pre-expansion multiple of the pre-expansion resin particles, the pre-expansion for pre-expanding by supplying the raw material based on the input pre-expansion multiple
And the pre-expanded resin particles discharged from the pre-expanding machine.
The storage hopper to be stored and the above-mentioned storage hopper.
And a damper that can open and close the opening on the lower end surface
Of a predetermined capacity of the storage container and the storage hopper
A sump that connects the lower part and the upper side of the weighing container.
Ring tube and pre-expanded resin discharged to the above storage hopper
Transfer particles to the weighing container via the sampling tube
And send compressed air to the sampling tube for filling
Weigh the sampling air duct and the weighing container above.
Pre-expanded resin particles in the measuring container and the measuring means for
The sampling operation for filling the
The weight of the pre-expanded resin particles measured by the measuring means and the upper
From the volume of the measuring container and the expansion ratio of the pre-expanded resin particles,
A multiple measurement device control panel for conversion is provided .
【0007】[0007]
【作用】上記の構成によれば、作業者が設定予備発泡倍
数を入力すれば、設定予備発泡倍数に見合う量の原料が
予備発泡機に供給され予備発泡が開始される。そして、
予備発泡して予備発泡機から収納ホッパに排出された予
備発泡樹脂粒子は、上記サンプリング管を介して上記収
納ホッパの上方に設置された所定容積の計量容器に搬送
される。このときの予備発泡樹脂粒子の搬送は、サンプ
リング送風管により上記サンプリング管に送られる圧縮
空気によりなされる。上記サンプリング管は、上記収納
ホッパの下部と上記計量容器の上部側面とを連通させる
ようになっているので、予備発泡樹脂粒子は収納ホッパ
から搬送されてすぐに上記計量容器に所定圧力で充填さ
れる。そして、この計量容器の重量を測定することによ
り上記予備発泡樹脂粒子の予備発泡倍数を検出できる。
これにより、上記予備発泡樹脂粒子の実際の予備発泡倍
数が検出され、これを設定予備発泡倍数と比較し、その
比較された差異を減少させる方向に原料供給量を制御で
きることから、得られた予備発泡樹脂粒子を、その実際
の予備発泡倍数が設定予備発泡倍数の所定範囲内で変動
するように製造することができる。According to the above construction , when the operator inputs the preset pre-expansion multiple, the amount of the raw material commensurate with the preset pre-expansion multiple is supplied to the pre-exposure machine to start the pre-expansion. And
The pre-expanded resin particles that were pre-expanded and discharged from the pre-exposure machine to the storage hopper were collected through the sampling tube.
Transfer to a weighing container with a specified volume installed above the storage hopper
Is done. At this time, the pre-expanded resin particles are transported by the sample
Compression sent to the sampling tube by the ring air tube
Made by air. The sampling tube is stored in the above
Communicate the lower part of the hopper and the upper side surface of the weighing container.
As a result, the pre-expanded resin particles are stored in the hopper.
Immediately after being transported from the
It is. Then, the prefoaming multiple of the prefoamed resin particles can be detected by measuring the weight of the measuring container.
As a result, the actual pre-expansion multiple of the pre-expanded resin particles is detected, this is compared with the set pre-expansion multiple, and the raw material supply amount can be controlled in the direction of reducing the difference thus obtained. The expanded resin particles can be manufactured so that the actual pre-expansion multiple varies within a predetermined range of the set pre-expansion multiple.
【0008】したがって、上記の構成では、予備発泡機
から排出された予備発泡樹脂粒子を、例えば圧縮空気等
により搬送して、収納ホッパから上記計量容器に直接充
填することができるので、実際の予備発泡倍数の測定が
容易となり、作業者は設定予備発泡倍数を設定するだけ
でよい。Therefore, in the above construction, the pre-foamed resin particles discharged from the pre-foaming machine can be conveyed by, for example, compressed air or the like to be directly filled in the measuring container from the storage hopper. Since it is possible to measure the actual prefoaming multiple
It becomes easier and the operator only has to set the preset pre-expansion multiple.
【0009】また、従来は、予備発泡樹脂粒子を手で計
量カップに掬い取って充填し、予備発泡樹脂粒子の上面
を計量カップの上端を同一平面となるようにならしてい
たため、予備発泡樹脂粒子の充填率が変動し易く、計量
誤差が大きくなるため換算される予備発泡樹脂粒子の発
泡倍数も不安定なものとなっていた。Further, conventionally, the pre-expanded resin particles have been scooped and filled into the measuring cup by hand so that the upper surface of the pre-expanded resin particles is flush with the upper end of the measuring cup. Since the packing rate of the particles is likely to change and the measurement error becomes large, the foaming multiple of the pre-foamed resin particles converted is also unstable.
【0010】しかしながら、上記構成では、前記の収納
ホッパより計量容器に所定圧力で予備発泡樹脂粒子が直
接充填されるため、従来より均一かつ迅速に充填される
ことから、作業の効率化を図ることができるとともに、
その充填量を安定化することができ、予備発泡倍数を検
出する際における計量誤差を低減できる。However, in the above structure, the storage
Pre-expanded resin particles are directly applied from the hopper to the weighing container at a specified pressure.
Since it is filled in close contact, it is filled more uniformly and quickly than in the past , which makes it possible to improve work efficiency and
The filling amount can be stabilized, and the measurement error in detecting the prefoaming multiple can be reduced.
【0011】[0011]
【実施例】本発明の一実施例について図1ないし図6に
基づいて説明すれば、以下の通りである。予備発泡樹脂
粒子の発泡倍数制御装置では、例えば図1に示すよう
に、バッチ式の予備発泡機1が使用され、その予備発泡
機1に発泡剤が含浸、または混入された発泡性樹脂粒子
である原料が所定量投入され、その全量が加熱されて予
備発泡され排出された後、予備発泡樹脂粒子が排出され
た予備発泡機1内に新たに所定量の原料が投入されて次
のサイクルが開始されるようになっている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to FIGS. In a device for controlling the expansion ratio of pre-expanded resin particles, for example, as shown in FIG. 1, a batch-type pre-exposure machine 1 is used. A predetermined amount of a certain raw material is charged, and after the whole amount is heated, pre-expanded and discharged, a new predetermined amount of the raw material is charged into the pre-expanding machine 1 from which the pre-expanded resin particles have been discharged, and the next cycle is started. It is supposed to be started.
【0012】上記の原料としては、例えばポリスチレ
ン、ポリエチレン、ポリプロピレン、等の合成樹脂粒子
が用いられ、一方、発泡剤として、ペンタン、ブタン等
の揮発性炭化水素が使用される。As the above raw material, for example, synthetic resin particles such as polystyrene, polyethylene, polypropylene, etc. are used, while as the foaming agent, volatile hydrocarbons such as pentane, butane are used.
【0013】予備発泡機1には、原料供給ローダ2か
ら、ロードセル式の原料重量計3aを有するホッパスケ
ール3を介して原料が所定量供給されるようになってい
る。また、ホッパスケール3には、上記の原料の供給を
制御するための電磁開閉弁3bが設けられている。A predetermined amount of raw material is supplied to the pre-foaming machine 1 from a raw material supply loader 2 through a hopper scale 3 having a load cell type raw material weighing scale 3a. Further, the hopper scale 3 is provided with an electromagnetic opening / closing valve 3b for controlling the supply of the above raw material.
【0014】予備発泡機1の底部には、図示しない吹込
蒸気管および圧縮エアー吹込管が接続され、予備発泡機
1内に蒸気および圧縮エアーが吹き込まれると共に、予
備発泡機1内の撹拌羽根1aがモータ1bにより回転し
て予備発泡が行われるようになっている。また、予備発
泡の終了は、膨張した予備発泡樹脂粒子の上面が予備発
泡機1の上部の所定位置に取り付けた音叉式等のレベル
計1cに到達することにより検出される。A blow steam pipe and a compressed air blow pipe (not shown) are connected to the bottom of the pre-foaming machine 1 so that steam and compressed air are blown into the pre-foaming machine 1 and the stirring blades 1a in the pre-foaming machine 1 are also connected. Is rotated by the motor 1b to perform pre-foaming. The end of the pre-foaming is detected when the upper surface of the expanded pre-foamed resin particles reaches a level meter 1c of a tuning fork type or the like attached at a predetermined position above the pre-foaming machine 1.
【0015】なお、上記レベル計1cの信号は、後述す
る予備発泡機制御盤10に出力され、上記の吹込蒸気管
および圧縮エアー吹込管の制御弁、モータ1bが予備発
泡機制御盤10により制御される。The signal from the level meter 1c is output to a pre-foaming machine control board 10 described later, and the pre-foaming machine control board 10 controls the blow steam pipe and compressed air blowing pipe control valves and the motor 1b. To be done.
【0016】予備発泡機1の下部側面に穿設された排出
ハッチ4が穿設されていて、その排出ハッチ4を開閉す
る排出弁4aが設置されている。この排出弁4aは予備
発泡機制御盤10により制御されるエアシリンダ4bに
より往復移動されて排出ハッチ4の開閉する。A discharge hatch 4 is provided on the lower side surface of the pre-foaming machine 1, and a discharge valve 4a for opening and closing the discharge hatch 4 is provided. The discharge valve 4a is reciprocated by an air cylinder 4b controlled by the pre-foaming machine control panel 10 to open and close the discharge hatch 4.
【0017】また、予備発泡機1の側方、かつ、排出ハ
ッチ4の下方に収納ホッパ5が配設され、その収納ホッ
パ5の上面に開口が設けられていて、予備発泡機1内で
予備発泡が完了した予備発泡樹脂粒子が、排出ハッチ4
から排出され収納ホッパ5に送出される。A storage hopper 5 is disposed on the side of the pre-foaming machine 1 and below the discharge hatch 4, and an opening is provided in the upper surface of the storage hopper 5 so that the pre-foaming machine 1 has a preliminary opening. The pre-expanded resin particles that have been foamed are discharged into the discharge hatch 4.
And discharged to the storage hopper 5.
【0018】また、蒸気により加湿されて粘着して団子
状態となった予備発泡樹脂粒子を解粒し、かつ、所定粒
径以下の予備発泡樹脂粒子を篩過するため、収納ホッパ
5内の上部には、排出ハッチ4側から他方へ下がるよう
に傾斜した所定メッシュの解粒・篩過用網5bが設置さ
れ、図示しないが、解粒・篩過用網5bはモータ等の駆
動手段により水平方向に往復振動するようになってい
る。Further, since the pre-expanded resin particles which have been humidified by the steam and adhered to form a dumpling are disintegrated and the pre-expanded resin particles having a predetermined particle size or less are sieved, the upper part in the storage hopper 5 is Is provided with a sieving / sieving net 5b having a predetermined mesh inclined so as to descend from the discharge hatch 4 side to the other. Although not shown, the sieving / sieving net 5b is horizontally moved by a driving means such as a motor. It reciprocally vibrates in the direction.
【0019】そして、上記の収納ホッパ5の上方には、
予備発泡樹脂粒子の発泡倍数を測定するため、所定容
量、例えば30.64Lでアクリル製などの略円筒状の計量容
器6が、その軸をほぼ垂直に配設されている。なお、計
量容器6の素材としては所定の強度を備えるものであれ
ば特に限定されないが、内部の充填状況が識別できるよ
うに透明状の物が望ましい。Above the storage hopper 5,
In order to measure the expansion ratio of the pre-expanded resin particles, a substantially cylindrical weighing container 6 made of acrylic or the like with a predetermined capacity, for example, 30.64 L is arranged with its axis substantially vertical. The material of the measuring container 6 is not particularly limited as long as it has a predetermined strength, but a transparent material is desirable so that the filling state inside can be identified.
【0020】その計量容器6は上下端に開口を有し、そ
の上端面の開口に、空気は通すが予備発泡樹脂粒子は通
さないメッシュを有する網状壁6aが設けられる一方、
計量容器6の下端面の開口に、その開口を開閉する計量
容器用ダンパー6bが取り付けられている。また、計量
容器6と収納ホッパ5との間には、予備発泡樹脂粒子を
計量容器6から収納ホッパ5に無駄なく戻すように飛散
防止用ホッパ9が配設されている。The measuring container 6 has openings at the upper and lower ends, and a mesh wall 6a having a mesh through which air can pass but pre-expanded resin particles cannot pass is provided at the opening on the upper end surface thereof.
A measuring container damper 6b for opening and closing the opening is attached to the opening of the lower end surface of the measuring container 6. Further, a scattering prevention hopper 9 is arranged between the weighing container 6 and the storage hopper 5 so as to return the pre-expanded resin particles from the weighing container 6 to the storage hopper 5 without waste.
【0021】したがって、計量容器用ダンパー6bを閉
じることにより、計量容器6内は所定容量となり、後述
するように圧縮空気を用いて予備発泡樹脂粒子を収納ホ
ッパ5から計量容器6内に充填しても、網状壁6aから
空気を逃がすことができて、予備発泡樹脂粒子の充填に
支障を生じることはない。Therefore, by closing the measuring container damper 6b, the measuring container 6 has a predetermined capacity, and the pre-foamed resin particles are filled from the storage hopper 5 into the measuring container 6 by using compressed air as described later. However, the air can escape from the mesh wall 6a, and the filling of the pre-foamed resin particles is not hindered.
【0022】さらに、計量容器6と収納ホッパ5の下部
とを連通させるためのサンプリング管7が、計量容器6
の上部側面に連結され、そのサンプリング管7には、計
量容器6方向に圧縮空気を送るサンプリング用送風管8
が接続されていて、前述したように収納ホッパ5から予
備発泡樹脂粒子を計量容器6に搬送できるようになって
いる。Further, a sampling pipe 7 for connecting the weighing container 6 and the lower part of the storage hopper 5 to each other is provided with a sampling pipe 7.
Is connected to the upper side surface of the sampling pipe 7, and a sampling blower pipe 8 for sending compressed air to the measuring container 6 is connected to the sampling pipe 7.
Is connected so that the pre-expanded resin particles can be conveyed from the storage hopper 5 to the weighing container 6 as described above.
【0023】また、サンプリング用送風管8は、それを
開閉する開閉弁8aを備えており、さらに、図示しない
が、その圧縮空気の空気圧を調整する調節弁を介して、
コンプレッサーにより圧縮されて圧縮エアーを蓄えたタ
ンクに接続されている。The sampling blower pipe 8 is provided with an opening / closing valve 8a for opening and closing it, and further, though not shown, through a control valve for adjusting the air pressure of the compressed air,
It is connected to a tank that stores compressed air compressed by a compressor.
【0024】一方、計量容器6の周面中央部には、計量
容器6の重量を測定するため、例えば歪みゲージ式ロー
ドセル(最大計量値10kg)からなる計量手段6cが、等
間隔に3〜4個設置され、よって、各計量手段6c…に
よって計量容器6が吊るされて計量可能な状態となって
いる。On the other hand, in the center of the peripheral surface of the weighing container 6, for measuring the weight of the weighing container 6, for example, a strain gauge type load cell (maximum weighing value of 10 kg) is provided with a weighing means 6c at 3-4 intervals. Individually installed, therefore, the weighing container 6 is hung by each of the weighing means 6c ...
【0025】また、計量容器6の上下動に伴って、計量
容器6に接続されたサンプリング管7が従動するように
サンプリング管7の折曲部に蛇腹部7aが設けられてい
ることから、サンプリング管7によって各計量手段6c
…による測定を阻害することがない。Further, the bellows portion 7a is provided at the bent portion of the sampling pipe 7 so that the sampling pipe 7 connected to the weighing container 6 is driven by the vertical movement of the weighing container 6, so that sampling is performed. Each measuring means 6c by the pipe 7
It does not interfere with the measurement by.
【0026】前記のホッパスケール3の電磁開閉弁3b
等を制御する前述した予備発泡機制御盤10が設けら
れ、その予備発泡機制御盤10は、前記の原料重量計3
aからの信号に基づいて、所定重量の原料を予備発泡機
1に供給するように電磁開閉弁3bを制御するようにな
っている。Electromagnetic on-off valve 3b of the hopper scale 3 described above.
The above-mentioned pre-foaming machine control board 10 for controlling the above is provided.
Based on the signal from a, the electromagnetic opening / closing valve 3b is controlled so as to supply a predetermined weight of raw material to the pre-foaming machine 1.
【0027】別に、サンプリング用送風管8の送風管制
御弁8aを制御する倍数測定装置制御盤11が設けら
れ、その倍数測定装置制御盤11は、サンプリング動作
手順が始動すると、送風管制御弁8aを制御して収納ホ
ッパ5内の予備発泡樹脂粒子をサンプリング管7を通し
て計量容器6内に搬送できるようになっている。Separately, a multiple measuring device control panel 11 for controlling the blow pipe control valve 8a of the sampling blow pipe 8 is provided, and the multiple measuring device control panel 11 starts when the sampling operation procedure starts. The pre-expanded resin particles in the storage hopper 5 can be conveyed to the measuring container 6 through the sampling tube 7 by controlling the above.
【0028】また、倍数測定装置制御盤11は、サンプ
リング動作のタイミングを図るタイマーT1 ・T2 をそ
れぞれ備えており、前述したように、予備発泡機1内で
予備発泡が完了した予備発泡樹脂粒子が、排出ハッチ4
から排出され収納ホッパ5に送出されると、タイマーT
1 (設定時間0〜999秒)を作動させ、そのタイマー
T1 の作動時には送風管制御弁8aを閉じて、サンプリ
ング用送風管8からサンプリング管8への送風を停止す
ることにより、計量容器6内に予備発泡樹脂粒子は充填
されない。Further, the multiple measuring device control panel 11 is provided with timers T 1 and T 2 for timing the sampling operation, respectively, and as described above, the pre-foaming resin in which the pre-foaming is completed in the pre-foaming machine 1 is completed. Particles are exhaust hatch 4
When discharged from the storage hopper 5, the timer T
1 (setting time 0 to 999 seconds) is activated, and when the timer T 1 is activated, the blower pipe control valve 8a is closed to stop the blown air from the sampling blower pipe 8 to the sampling pipe 8 and thereby the measuring container 6 No pre-expanded resin particles are filled therein.
【0029】その上、倍数測定装置制御盤11は、タイ
マーT1 の終了後、計量容器用ダンパー6bを閉状態と
し、タイマーT2 (設定時間0〜99秒)を始動させる
ことにより、計量容器6に予備発泡樹脂粒子を所定圧力
で充填し、そのタイマーT2の終了により送風管制御弁
8aを制御して、タイマーT2 による所定時間だけ予備
発泡樹脂粒子を計量容器6に充填するサンプリング時間
を設定できるようになっている。In addition, the multiple measuring device control panel 11 closes the weighing container damper 6b after the timer T 1 is finished and starts the timer T 2 (setting time 0 to 99 seconds) to start the weighing container. 6 is filled with the pre-expanded resin particles at a predetermined pressure, and when the timer T 2 is finished, the blower pipe control valve 8a is controlled, and the sampling time for filling the pre-expanded resin particles into the measuring container 6 for a predetermined time by the timer T 2. Can be set.
【0030】さらに、倍数測定装置制御盤11は、所定
容量の計量容器6内に、所定圧で充填された予備発泡樹
脂粒子の重量を、各計量手段6c…からの信号に基づい
て計測し、その重量と上記の計量容器6の容量とから実
際の予備発泡樹脂粒子の発泡倍数を換算する。なお、計
量容器6の空重量は予め測定されており、その空重量は
倍数測定装置制御盤11に予め入力されている。Further, the multiple measuring device control panel 11 measures the weight of the pre-expanded resin particles filled in the measuring container 6 having a predetermined capacity at a predetermined pressure based on a signal from each measuring means 6c. The actual expansion ratio of the pre-expanded resin particles is converted from the weight and the capacity of the measuring container 6 described above. The empty weight of the weighing container 6 is measured in advance, and the empty weight is previously input to the multiple measurement device control panel 11.
【0031】倍数測定装置制御盤11は、上記の換算結
果と、予備発泡機制御盤10からの設定予備発泡倍数と
を比較して、それら両者の差異を算出し、予め入力され
た設定誤差と上記の差異と判定して、予備発泡機制御盤
10に信号を出力するようになっている。The multiple measurement device control panel 11 compares the above conversion result with the preset pre-expansion multiples from the pre-expansion machine control panel 10 to calculate the difference between them, and obtains the setting error inputted in advance. A signal is output to the control panel 10 of the pre-foaming machine by judging the difference.
【0032】つまり、倍数測定装置制御盤11は、設定
誤差の範囲内に上記の差異が含まれる場合は、次回の原
料の投入量を、前回の投入量と同一量となるように予備
発泡機制御盤10に制御信号を出力し、逆に、設定誤差
の範囲内に上記の差異が含まれない場合は、上記の差異
から所定の算定式により前回の投入量を変更して、その
変更値を次回の原料の投入量とするように予備発泡機制
御盤10に制御信号を出力する。That is, when the above-mentioned difference is included in the range of the setting error, the multiple measuring device control panel 11 adjusts the amount of the next raw material to be the same as the amount of the previous injection so that the pre-exposure machine has the same amount. When a control signal is output to the control panel 10 and conversely the above difference is not included in the range of the setting error, the previous input amount is changed from the above difference by a predetermined calculation formula, and the changed value is changed. A control signal is output to the pre-foaming machine control panel 10 so that is the next input amount of the raw material.
【0033】その上、倍数測定装置制御盤11は、計量
容器6における計量が終了後に、その計量容器6内の予
備発泡樹脂粒子を収納ホッパ5に戻すように、計量容器
用ダンパー6bを制御するようになっている。Furthermore, the multiple measuring device control panel 11 controls the damper 6b for the weighing container so that the pre-expanded resin particles in the weighing container 6 are returned to the storage hopper 5 after the weighing in the weighing container 6 is completed. It is like this.
【0034】また、倍数測定装置制御盤11には、図2
および図3にも示すように、予備発泡機1の有効容積お
よび設定予備発泡倍数をそれぞれ入力し、表示する回転
クリック式の2個のスイッチ11aがそれぞれ設けられ
ると共に、今回および次回の原料投入量(kg)をそれぞ
れ表示する2個の表示部11bがそれぞれ取り付けら
れ、かつ、サンプリングにより求められた実際の予備発
泡倍数を表示する倍数表示部11cと、その予備発泡倍
数が上記の設定予備発泡倍数から所定の誤差範囲を越え
る時に原料の投入変更量(kg)を表示する変更量表示部
11dとが設けられている。Further, the multiple measuring device control panel 11 has a structure shown in FIG.
As shown in FIG. 3 and FIG. 3, two rotary click type switches 11a for respectively inputting and displaying the effective volume of the pre-foaming machine 1 and the set pre-foaming multiple are provided, and the current and next raw material input amounts Two display parts 11b for displaying (kg) respectively are attached, and a multiple display part 11c for displaying the actual pre-foaming multiple obtained by sampling, and the pre-foaming multiple are the above-mentioned pre-foaming multiples. Is provided with a change amount display portion 11d for displaying the change amount (kg) of the raw material input when a predetermined error range is exceeded.
【0035】さらに、倍数測定装置制御盤11には、各
タイマーT1 およびタイマーT2 を設定して表示する可
変型のスイッチ11eがそれぞれ設けられ、さらに、現
在の予備発泡機1の温度や経過時間などを表示する表示
部11fと、予備発泡結果を例えば図4に示すようにシ
ート11hに印字して出力するためのプリンタ11gと
が設けられている。なお、プリンタ11gでの印字項目
は発泡日時、発泡品種略記号、各回の原料投入量、各回
の測定発泡倍数、発泡重量積算値等である。Further, the multiple measuring device control panel 11 is provided with variable switches 11e for setting and displaying the timers T 1 and T 2 , respectively, and further, the current temperature of the pre-foaming machine 1 and the progress thereof. A display unit 11f for displaying the time and the like, and a printer 11g for printing and outputting the pre-foaming result on a sheet 11h as shown in FIG. 4 are provided. The printing items on the printer 11g include foaming date and time, foaming type abbreviation code, raw material input amount at each time, measured foaming multiple at each time, foaming weight integrated value, and the like.
【0036】一方、予備発泡機制御盤10には、図1に
示すように、原料の計測投入量を表示する計測結果表示
部10a、予備発泡の開始を指示するスタートキー10
b、図示しないが、各種設定値の入力等に用いるテンキ
ー、予備発泡の終了を指示するストップキー等が設けら
れている。On the other hand, on the prefoaming machine control panel 10, as shown in FIG. 1, a measurement result display section 10a for displaying the measured input amount of the raw material, and a start key 10 for instructing the start of prefoaming.
Although not shown, a numeric keypad used for inputting various set values, a stop key for instructing the end of pre-foaming, and the like are provided.
【0037】次に、上記実施例の予備発泡機を用いて、
予備発泡樹脂粒子の発泡倍数を自動補正して制御する方
法について、図5および図6のフローチャートを参照し
ながら説明すると、まず、作業者が、倍数測定装置制御
盤11に、計量容器6の容積、例えば30L、予備発泡機
1の有効容量、例えば 350L、サンプリング用送風管8
の始動後のサンプリング開始時間、例えば60秒、サンプ
リング時間、例えば30秒、設定予備発泡倍数(20〜 100
倍)、例えば50倍、および設定誤差等を設定して入力す
る(ステップ1、以下ステップをSと略す)。Next, using the pre-foaming machine of the above embodiment,
A method for automatically correcting and controlling the foaming multiple of the pre-foamed resin particles will be described with reference to the flowcharts of FIGS. 5 and 6. First, the operator sets the volume of the weighing container 6 on the multiple measuring device control panel 11. , 30 L, effective capacity of the pre-foaming machine 1, eg 350 L, sampling air duct 8
Sampling start time after the start of, for example 60 seconds, sampling time, for example 30 seconds, set pre-expansion multiple (20 ~ 100
X), for example, 50 times, and a setting error and the like are set and input (step 1, hereinafter step is abbreviated as S).
【0038】これに基づいて、倍数測定装置制御盤11
により、上記設定予備発泡倍数および予備発泡機1の有
効容積に対応した原料の投入量が算出され(S2)、そ
の投入量を、例えば、350/50.0=7.0kg として表示する
(S3)。このとき、各装置のクセ等による経験値が有
る場合は、作業者が上記の投入量を調整して入力する
(S4)。Based on this, the multiple measurement device control panel 11
Thus, the input amount of the raw material corresponding to the set pre-expansion multiple and the effective volume of the pre-expansion machine 1 is calculated (S2), and the input amount is displayed as, for example, 350 / 50.0 = 7.0 kg (S3). At this time, if there is an experience value due to the habit of each device, the operator adjusts and inputs the input amount (S4).
【0039】続いて、予備発泡機1を予備発泡機制御盤
10により始動し(S5)、原料を計量し(S6)、予
備発泡機1内に投入(S7)した後、蒸気等により加熱
する(S8)。この加熱により、原料の予備発泡が開始
されて原料の嵩が増加しレベル計1cにより予備発泡の
終了が予備発泡機制御盤10により検出されると(S
9)、排出ハッチ4を開いて、予備発泡樹脂粒子を収納
ホッパ5に排出する(S10)。このとき、倍数測定装
置制御盤11にサンプリング動作のためのトリガ信号を
出力する。Subsequently, the pre-foaming machine 1 is started by the pre-foaming machine control panel 10 (S5), the raw materials are weighed (S6), charged into the pre-foaming machine 1 (S7), and then heated by steam or the like. (S8). By this heating, the pre-foaming of the raw material is started and the bulk of the raw material is increased, and when the level meter 1c detects the end of the pre-foaming by the pre-foaming machine control panel 10 (S
9), the discharge hatch 4 is opened, and the pre-expanded resin particles are discharged into the storage hopper 5 (S10). At this time, a trigger signal for the sampling operation is output to the multiple measurement device control panel 11.
【0040】次に、倍数測定装置制御盤11は、タイマ
ーT1 を始動し、設定時間、例えば60秒間、送風管制御
弁8aを閉じて、サンプリング用送風管8からサンプリ
ング管8への送風を停止することにより、計量容器6内
に予備発泡樹脂粒子を充填せず、充填待ち時間を設定す
る。Next, the multiplex measuring device control panel 11 starts the timer T 1 and closes the blower pipe control valve 8a for a set time, for example, 60 seconds to blow air from the sampling blower pipe 8 to the sampling pipe 8. By stopping, the pre-expanded resin particles are not filled in the measuring container 6 and the filling waiting time is set.
【0041】その後、タイマーT1 が終了すると、計量
容器用ダンパー6bを閉状態とし、計量容器6内に予備
発泡樹脂粒子を所定圧力、例えば3kg/cm2の圧縮空気圧
で搬送充填してサンプリングを開始(S11)すると共
に、タイマーT2 を始動する。そのタイマーT2 が設定
時間TS 例えば30秒に達して終了すると(S12)、サ
ンプリング用送風管8および送風管制御弁8aを制御し
て、予備発泡樹脂粒子の搬送を停止することで、予備発
泡樹脂粒子を所定時間のみ搬送し充填する。After that, when the timer T 1 ends, the damper 6b for the measuring container is closed, and the pre-expanded resin particles are fed into the measuring container 6 at a predetermined pressure, for example, compressed air pressure of 3 kg / cm 2 , and sampling is performed. At the same time as starting (S11), the timer T 2 is started. When the timer T 2 reaches a set time T S, for example, 30 seconds and ends (S12), the sampling blower tube 8 and the blower tube control valve 8a are controlled to stop the conveyance of the pre-expanded resin particles, and thereby the preliminary operation is completed. The expanded resin particles are conveyed and filled only for a predetermined time.
【0042】その次に、計量容器6の重量を、各計量手
段6c…により測定し、計量手段6c内の予備発泡樹脂
粒子の重量、例えば 622gを計測する(S13)。その
後、その重量と計量容器6の容積とから発泡倍数、例え
ば 48.2 倍を換算し(S14)、その発泡倍数を表示す
る。Then, the weight of the weighing container 6 is measured by each of the weighing means 6c, and the weight of the pre-expanded resin particles in the weighing means 6c, for example, 622 g is measured (S13). Then, the foaming multiple, for example, 48.2 times is converted from the weight and the volume of the measuring container 6 (S14), and the foaming multiple is displayed.
【0043】このとき、換算した発泡倍数、および他の
発泡条件、例えば原料投入量などをプリンタ11gによ
り、例えば図4に示すように印字して出力する。そし
て、上記の換算発泡倍数から、所定の予め設定されてい
る算定式により、例えば 7.0kg×(48.2/50.0) ≒6.7kg
のように補正した原料投入量を算出する。At this time, the converted foaming multiple and other foaming conditions, such as the amount of raw material input, are printed and output by the printer 11g as shown in FIG. 4, for example. Then, from the above conversion foaming multiple, by a predetermined preset calculation formula, for example, 7.0 kg × (48.2 / 50.0) ≒ 6.7 kg
The raw material input amount corrected as described above is calculated.
【0044】この算出値を次回の原料投入量として、倍
数測定装置制御盤11の表示部11bに表示し、かつ、
プリンタ11gにて原料投入量、測定発泡倍数などを印
字し、その補正された原料投入量を示す制御信号を予備
発泡機制御盤10に出力する(S15)。This calculated value is displayed as the next raw material input amount on the display section 11b of the multiple measurement device control panel 11, and
The raw material input amount, the measured foaming multiple, and the like are printed by the printer 11g, and a control signal indicating the corrected raw material input amount is output to the prefoaming machine control panel 10 (S15).
【0045】一方、S10にて1バッチの予備発泡が完
了することから、複数バッチの連続予備発泡(初期値ゼ
ロ、設定発泡回数X)が設定されている場合(S1
6)、バッチカウンターにて今までの予備発泡回数に1
を加え(S17)、その発泡回数の総数と設定回数Xと
を比較し(S18)、発泡回数の総数がXより小さい
と、S6に移り、バッチカウンターの発泡総数が設定回
数Xに達するまで、上記の予備発泡サイクルを繰り返
す。On the other hand, since one batch of pre-foaming is completed in S10, a plurality of batches of continuous pre-foaming (initial value zero, set foaming number X) is set (S1).
6), 1 at the number of pre-foaming so far at the batch counter
(S17), the total number of foaming times and the set number of times X are compared (S18), and when the total number of foaming times is smaller than X, the process proceeds to S6, until the total number of foaming of the batch counter reaches the set number of times X, Repeat the above prefoaming cycle.
【0046】その後、上記のバッチカウンターの発泡総
数がXとなると、別サイロへの発泡が有るか否かを判別
して(S19)、別サイロへの発泡が有れば、さらに、
発泡倍数の変更が有るか否かを判別し(S20)、変更
があればS1に移り、変更が無ければS6に移る。ま
た、S19での判別で別サイロへの発泡が無ければ発泡
を終了し(S21)、予備発泡機1を停止し(S2
2)、予備発泡操作が完了する。After that, when the total number of foaming in the batch counter becomes X, it is judged whether or not there is foaming in another silo (S19), and if there is foaming in another silo, further,
It is determined whether or not the foaming multiple has been changed (S20). If there is a change, the process proceeds to S1, and if there is no change, the process proceeds to S6. If it is judged in S19 that there is no foaming in another silo, the foaming is ended (S21) and the pre-foaming machine 1 is stopped (S2).
2), the pre-foaming operation is completed.
【0047】このように上記実施例の予備発泡樹脂粒子
の発泡倍数制御装置では、得られた予備発泡樹脂粒子の
サンプリング等による実際の予備発泡倍数の測定が倍数
測定装置制御盤11により自動的に迅速に行われるの
で、作業者は、吹き込み蒸気圧力、原料の配合剤種など
の予備発泡条件の変動要因を考慮せずとも、設定予備発
泡倍数および許容誤差を設定するのみで、所望する発泡
倍数の予備発泡樹脂粒子を得ることができる。Thus, the pre-expanded resin particles of the above example
In the foaming multiple control device , the actual measurement of the prefoaming multiple by sampling the obtained prefoamed resin particles or the like is automatically and quickly performed by the multiple measuring device control board 11, so that the operator is required to blow the steam pressure, It is possible to obtain the pre-expanded resin particles having a desired expansion ratio, only by setting the set pre-expansion multiple and the allowable error, without considering the factors for varying the pre-expansion conditions such as the compounding agent type of the raw material.
【0048】このことから、上記の予備発泡樹脂粒子の
発泡倍数制御装置は、作業者の操作が大幅に簡素化され
て自動化でき、無人化も可能となる。From the above, the pre-expanded resin particles
The foaming multiplex control device greatly simplifies the operator's operation, can be automated, and can be unmanned.
【0049】ところで、従来は、予備発泡樹脂粒子を手
で計量カップに掬い取って充填し、予備発泡樹脂粒子の
上面を計量カップの上端を同一平面となるようにならし
ていたため、予備発泡樹脂粒子の充填率が変動し易く、
計量誤差が大きくなるため換算される予備発泡樹脂粒子
の発泡倍数も不安定なものとなっていた。By the way, conventionally, since the pre-expanded resin particles are scooped and filled in the measuring cup by hand so that the upper surface of the pre-expanded resin particles is flush with the upper end of the measuring cup, the pre-expanded resin particles are The packing rate of particles easily fluctuates,
Since the measurement error becomes large, the foaming multiple of the pre-foamed resin particles converted is also unstable.
【0050】しかしながら、上記の予備発泡樹脂粒子の
発泡倍数制御装置は、前記の収納ホッパ5と計量容器6
とをサンプリング管7によって連通させているので、サ
ンプリング用送風管8により所定圧力で予備発泡樹脂粒
子が充填されるため、従来より迅速で、均一に、かつ密
に充填されることから、作業の効率化を図ることができ
るとともに、その充填量を安定化することができ、予備
発泡倍数を検出する際における計量誤差を低減できる。However, of the above-mentioned pre-expanded resin particles,
The foaming multiple control device includes the storage hopper 5 and the weighing container 6 described above.
, And the pre-expanded resin particles are filled with the sampling blower pipe 8 at a predetermined pressure, so that they can be filled more quickly, uniformly, and densely than in the conventional case . Can be more efficient
In addition, the filling amount can be stabilized, and the measurement error in detecting the prefoaming multiple can be reduced.
【0051】ところで、予備発泡樹脂粒子の発泡倍数
は、1バッチの予備発泡機1内における上層、中層、下
層で5%程度変動することがあるが、同一の例えば中層
においてはバッチ間の発泡倍数は殆ど変動しない。By the way, the expansion ratio of the pre-expanded resin particles may vary by about 5% between the upper layer, the middle layer and the lower layer in one batch of the pre-expanding machine 1, but the same expansion ratio between batches, for example, in the middle layer. Changes little.
【0052】したがって、上記の予備発泡樹脂粒子の発
泡倍数制御装置では、予備発泡樹脂粒子の予備発泡機1
からの排出時から、サンプリング開始時間、およびサン
プリング時間を一定に制御しているため、1バッチの予
備発泡機1内におけるサンプリング部位を安定化でき
て、計量誤差を低減できる。Therefore, the generation of the above-mentioned pre-expanded resin particles
In the foam multiple control device , the pre-expanding machine 1 for pre-expanding resin particles is used.
Since the sampling start time and the sampling time are controlled to be constant from the time of discharge from, the sampling site in one batch of the prefoaming machine 1 can be stabilized, and the measurement error can be reduced.
【0053】そこで、上記の予備発泡樹脂粒子の発泡倍
数制御装置における計量方法の測定精度を調べた。ま
ず、予め発泡された発泡倍数62倍の予備発泡樹脂粒子
(乾燥品)を、上述した倍数測定方法にてサンプリング
計量を、10回同様に繰り返して、各計量値および換算倍
数から精度を算出した。Therefore, the expansion ratio of the above pre-expanded resin particles
The measurement accuracy of the weighing method in the number control device was investigated. First, pre-expanded pre-expanded resin particles having an expansion ratio of 62 times (dry product) were repeatedly sampled and measured in the same manner 10 times by the above-described multiple measurement method, and the accuracy was calculated from each measured value and the conversion multiple. .
【0054】このとき、装置の条件として、計量容器6
の容量を30.64 L、重量の計量手段6cとして歪みゲー
ジ式ロードセル(最大計量値20kg)を4個用い、サンプ
リング用送風管8の圧縮空気圧を3kg/cm2とした。At this time, as the condition of the apparatus, the measuring container 6
The capacity was 30.64 L, four strain gauge type load cells (maximum weight value 20 kg) were used as the weight measuring means 6c, and the compressed air pressure of the sampling air duct 8 was 3 kg / cm 2 .
【0055】この計量結果を表1に示した。この結果か
ら明らかなように、平均値mに対する±2.5S(確率99%
内に含まれる発泡倍数)は59.6〜62.4倍となり、±2.5S
/m=±2.3 %の精度を示したことから、バラツキの少
ない良好な精度を示した。The results of this measurement are shown in Table 1. As is clear from this result, ± 2.5S (probability 99%) with respect to the average value m
The foaming ratio included within is 59.6 to 62.4 times, ± 2.5S
Since the accuracy was /m=±2.3%, the accuracy was good with little variation.
【0056】[0056]
【表1】 [Table 1]
【0057】次に、さらにサンプリング精度の向上を図
るために、重量の計量手段6cとしての歪みゲージ式ロ
ードセル(最大計量値20kg)を代えて、最大計量値10kg
の歪みゲージ式ロードセルを、同様に4個用い、予備発
泡樹脂粒子の62倍品に代えて59倍品を用いて、他は上記
と同一の条件で10回サンプリング計量を行った。この
結果を表2に示した。Next, in order to further improve the sampling accuracy, the strain gauge type load cell (maximum weighing value 20 kg) as the weighing means 6c is replaced with a maximum weighing value 10 kg.
Similarly, four strain gauge type load cells were used, and instead of the 62-fold pre-expanded resin particles, the 59-fold product was used, and the sampling measurement was performed 10 times under the same conditions as above. The results are shown in Table 2.
【0058】この結果から明らかなように、乾燥品の計
量値の幅は、 520〜530gと10g あるが、倍数に換算する
と57.8〜59.9倍であり、 1.1倍の幅となる。平均値mに
対する±2.5S(確率99%内に含まれる発泡倍数)は52.7
〜59.2倍となり、±2.5S/m=±1.6 %の精度を示した
ことから、バラツキのより少ない良好な精度を示した。As is clear from this result, the range of the measured value of the dried product is 520 to 530 g and 10 g, but when converted to a multiple, it is 57.8 to 59.9 times, which is 1.1 times the range. ± 2.5S for the average value m (expansion ratio included in probability 99%) is 52.7
It was up to 59.2 times, and the accuracy was ± 2.5 S / m = ± 1.6%, which showed good accuracy with less variation.
【0059】これは、サンプリング用予備発泡樹脂粒
子、および計量容器6等の総重量が10kgを越えない程度
であり、また、重量の計量手段6cとしての歪みゲージ
式ロードセルを最大計量値10kgのものを使用し、歪みゲ
ージ式ロードセルの計量精度が最大値に近くなるに伴い
向上することから、歪みゲージ式ロードセルの計量誤差
の低減に起因するものと考えられた。This is because the total weight of the pre-expanded resin particles for sampling, the weighing container 6 and the like does not exceed 10 kg, and the strain gauge type load cell as the weighing means 6c has a maximum weighing value of 10 kg. It is considered that this is due to the reduction in the measurement error of the strain gauge type load cell, since the strain gauge type load cell improves the measurement accuracy as it approaches the maximum value.
【0060】[0060]
【表2】 [Table 2]
【0061】次に、予備発泡される予備発泡樹脂粒子
は、加熱用蒸気により水分を含有しており、上記の59倍
品(乾燥品)に、水分約16%含ませて試料とし、上記と
同様に、上記の試料を7回繰り返してサンプリング計量
を行った。この結果を表3に示した。また、同一の試料
を作業者の手によるカップ計量にて8回繰り返してサン
プリング計量しそれぞれの発泡倍数を換算した。それら
の結果を表4に示した。Next, the pre-expanded resin particles to be pre-expanded contain water by the steam for heating, and about 59% of the above-mentioned 59 times product (dry product) was added to make a sample. Similarly, the above sample was repeated 7 times for sampling and weighing. The results are shown in Table 3. Further, the same sample was repeatedly sampled and weighed eight times by the cup weighing by the operator, and the foaming multiples of each were converted. Table 4 shows the results.
【0062】表3の結果から明らかなように、水分含有
品の計量値の幅は、 568〜580gと12g あるが、倍数に換
算すると52.7〜53.9倍であり、 1.2倍の幅となる。ま
た、平均値mに対する±2.5S(99%) は52.2〜54.7倍とな
り、±2.5S/m=±2.3 %の精度を示したことから、水
分含有品の計量精度は、乾燥品に対して若干の精度低下
が見られたが、実用上においてはバラツキの少ない良好
な精度を示した。As is clear from the results shown in Table 3, the range of measured values of the water-containing product is 568 to 580 g and 12 g, which is 52.7 to 53.9 times, which is 1.2 times the range when converted to a multiple. In addition, ± 2.5S (99%) for the average value m was 52.2 to 54.7 times, showing an accuracy of ± 2.5S / m = ± 2.3%. Although a slight decrease in precision was observed, it showed good precision with little variation in practical use.
【0063】一方、作業者の手によるカップ計量におけ
る発泡倍数の幅は、表4に示すように、52.1〜55.4倍で
あり 3.3倍の幅となる。また、平均値mに対する±2.5S
(確率99%の範囲内での発泡倍数)は51.0〜56.2倍とな
り、±2.5S/m=±4.9 %の精度を示したことから、本
実施例での計量方法の方が、所定圧力で充填するため
に、均一に密に充填できて充填誤差を低減でき、計量精
度に優れていることが明らかとなった。On the other hand, as shown in Table 4, the width of the foaming multiple in the cup weighing by the operator is 52.1 to 55.4 times, which is 3.3 times the width. Also, ± 2.5S for the average value m
The (foaming multiple within the range of 99% probability) was 51.0 to 56.2 times, and the accuracy of ± 2.5 S / m = ± 4.9% was shown. Therefore, the weighing method in this example is more accurate at a predetermined pressure. It became clear that the filling can be performed uniformly and densely, the filling error can be reduced, and the weighing accuracy is excellent.
【0064】[0064]
【表3】 [Table 3]
【0065】[0065]
【表4】 [Table 4]
【0066】次に、上記の水分を含有させた59倍品を用
いて、サンプリング用送風管8の圧縮空気の空気圧を3
kg/cm2から、2kg/cm2に代えてサンプリング計量したと
ころ、計量値が562gで、換算した発泡倍数は54.5であっ
た。さらに、サンプリング用送風管8の圧縮空気の空気
圧を3kg/cm2から、1kg/cm2に代えてサンプリング計量
したところ、計量値が544gで、換算した発泡倍数は56.3
であった。Next, using the 59-fold product containing the above water, the air pressure of the compressed air in the sampling air duct 8 is set to 3
When sampling / weighing was performed instead of 2 kg / cm 2 from kg / cm 2 , the measured value was 562 g and the converted foaming multiple was 54.5. Furthermore, when the sampling air pressure of the compressed air in the sampling air duct 8 was changed from 3 kg / cm 2 to 1 kg / cm 2 , the measured value was 544 g, and the converted foaming multiple was 56.3.
Met.
【0067】また、各空気圧を上記のように代えて、計
量容器6における充填をそれぞれ観察したところ、サン
プリング用送風管8の圧縮空気の空気圧が3kg/cm2で
は、約20秒で充填され、2kg/cm2では、約25秒、1kg/c
m2では約35秒であり、目視による計量容器6の充填状態
の観察では3kg/cm2および2kg/cm2での充填性が良好で
あり、1kg/cm2での充填は不良であった。なお、4kg/c
m2以上では予備発泡樹脂粒子が変形することがあった。When the air pressure was changed as described above and the filling in the measuring container 6 was observed, when the compressed air in the sampling air duct 8 had an air pressure of 3 kg / cm 2 , it was filled in about 20 seconds. At 2kg / cm 2 , about 25 seconds, 1kg / c
m 2 was about 35 seconds, and the visual observation of the filling state of the measuring container 6 showed that the filling property was good at 3 kg / cm 2 and 2 kg / cm 2 , and the filling at 1 kg / cm 2 was poor. . 4kg / c
At m 2 or more, the pre-expanded resin particles were sometimes deformed.
【0068】これらの結果から、サンプリング用送風管
8の空気圧は、1.5 〜3.5 kg/cm2の範囲で用いることが
でき、さらに、2〜3kg/cm2の範囲が最適と考えられ
た。[0068] From these results, the air pressure of the sampling blower tube 8 may be used in the range of 1.5 ~3.5 kg / cm 2, further the range of 2-3 kg / cm 2 was considered optimal.
【0069】次に、予備発泡の際における水分含量を補
正して、乾燥品での予備発泡倍数を算出する制御方法に
ついて説明する。まず、発泡直後の種々の発泡倍数の予
備発泡樹脂粒子を上述したように一定量サンプリング
し、重量を測定して発泡倍数を換算した結果と、同予備
発泡樹脂粒子を乾燥後、再度サンプリングし、同様に発
泡倍数を換算した結果とを比較したところ、発泡直後の
予備発泡樹脂粒子の含水率は、平均で約3%であった。
ただし、上記の含水率は、乾燥品と未乾燥品とで計量容
器への充填性が異なるため充填率が異なり、みかけの含
水率である。Next, a control method for correcting the water content in the pre-expansion and calculating the pre-expansion multiple in the dried product will be described. First, a predetermined amount of pre-expanded resin particles having various expansion ratios immediately after foaming were sampled in a fixed amount as described above, and the result of converting the expansion ratio by measuring the weight, drying the pre-expanded resin particles, and sampling again, Similarly, when compared with the result obtained by converting the expansion ratio, the water content of the pre-expanded resin particles immediately after expansion was about 3% on average.
However, the above-mentioned water content is an apparent water content because the filling rate is different between the dry product and the undried product because the filling property into the measuring container is different.
【0070】そこで、同容量の乾燥品と未乾燥品との水
分含量を正確に測定して比較したところ、未乾燥品の含
水率は約7%であった。つまり、4%は充填性の差によ
り相殺されたことになる。Therefore, when the moisture contents of the same amount of the dried product and the undried product were accurately measured and compared, the moisture content of the undried product was about 7%. That is, 4% is offset by the difference in filling property.
【0071】したがって、みかけの含水率を補正すれ
ば、発泡直後の未乾燥品である予備発泡樹脂粒子におい
ても、ほぼ乾燥品と同等の発泡倍数を備えることができ
て、以後の発泡プロセスに有用である。よって、含水率
の補正は、例えば計量容器6、あるいは予備発泡機1の
倍数測定装置制御盤11での容量設定値を3%上乗せす
ることで可能となる。Therefore, if the apparent water content is corrected, even the pre-expanded resin particles which are undried products immediately after foaming can be provided with a foaming multiple almost equal to that of the dried product, which is useful for the subsequent foaming process. Is. Therefore, the water content can be corrected, for example, by adding 3% to the capacity set value in the measuring container 6 or the multiple measurement device control panel 11 of the pre-foaming machine 1.
【0072】ただし、このような補正は、用いる予備発
泡機1や原料が所定範囲のものであれば、有効である
が、用いる予備発泡機1や原料が所定範囲外となると、
補正の値も代える必要があるので、上記の補正の値に特
に限定されるものではない。However, such correction is effective if the pre-foaming machine 1 and the raw material used have a predetermined range, but if the pre-foaming machine 1 and the raw material used are out of the predetermined range,
Since the correction value also needs to be changed, it is not particularly limited to the above correction value.
【0073】なお、上記実施例の予備発泡樹脂粒子の発
泡倍数制御装置では、計量容器6による計量が完了し、
発泡倍数を換算し補正値を算出した後に、次回の原料を
投入した例を挙げたが、各バッチにおける換算された発
泡倍数と設定発泡倍数の差異が所定範囲内であれば、原
料の投入後、直ちに次回の原料を前回の原料投入量で投
入するように原料投入を制御してもよい。これにより、
バッチ式の予備発泡機1における連続製造における原料
投入の完了の待ち時間を低減できるので、連続製造にお
ける予備発泡を迅速化できる。In addition, the generation of the pre-expanded resin particles of the above example
In the bubble multiple control device , the measurement by the measuring container 6 is completed,
An example was given in which the raw material was added next time after converting the foaming multiple and calculating the correction value.However, if the difference between the converted foaming multiple and the set foaming multiple in each batch is within the predetermined range, after the raw material is added. Alternatively, the raw material charging may be controlled so that the next raw material is immediately charged at the previous raw material charging amount. This allows
Since it is possible to reduce the waiting time for completing the raw material charging in the continuous production in the batch type prefoaming machine 1, the prefoaming in the continuous production can be accelerated.
【0074】[0074]
【発明の効果】本発明の予備発泡樹脂粒子の発泡倍数制
御装置は、以上にように、入力された設定予備発泡倍数
に基づいて原料を供給して予備発泡させる予備発泡機
と、該予備発泡機から排出された予備発泡樹脂粒子を収
納する収納ホッパと、上記収納ホッパの上方に配設され
ており、その下端面の開口を開閉可能とするダンパーを
有している所定容量の計量容器と、上記収納ホッパの下
部と上記計量容器の上部側面とを連通しているサンプリ
ング管と、上記収納ホッパへ排出された予備発泡樹脂粒
子を上記サンプリング管を介して上記計量容器に搬送し
て充填するための圧縮空気を該サンプリング管に送るサ
ンプリング用送風管と、上記計量容器の重量を計量する
ための計量手段と、上記計量容器に予備発泡樹脂粒子を
充填するサンプリング動作を制御するとともに、上記計
量手段により計量された予備発泡樹脂粒子の重量と上記
計量容器の容積とから予備発泡樹脂粒子の発泡倍数を換
算する倍数測定装置制御盤とを備えている構成である。 As described above, the apparatus for controlling the expansion ratio of the pre-expanded resin particles of the present invention is a pre-expansion machine for supplying the raw material and pre-expanding it based on the input pre-expansion multiple.
And collect the pre-expanded resin particles discharged from the pre-expanding machine.
The storage hopper to be stored and the above-mentioned storage hopper.
And a damper that can open and close the opening on the bottom surface
Below the weighing container of the specified capacity and the storage hopper
Part that communicates between the upper part and the side surface of the measuring container.
Ring and pre-expanded resin particles discharged to the above storage hopper
Transport the child to the weighing container via the sampling tube
To send compressed air to the sampling tube for filling
Weigh the air duct for sampling and the weighing container above.
And the pre-expanded resin particles in the measuring container.
Controls the sampling operation for filling and
The weight of the pre-expanded resin particles measured by the measuring means and
Change the expansion ratio of the pre-expanded resin particles from the volume of the measuring container.
It is a configuration provided with a multiple measurement device control panel for calculation.
【0075】それゆえ、上記構成では、予備発泡機から
排出された予備発泡樹脂粒子を、例えば圧縮空気等によ
り搬送して、収納ホッパから上記計量容器に直接充填す
ることができるので、実際の予備発泡倍数の測定が容易
となり、作業者は設定予備発泡倍数を設定するだけでよ
く、作業者の操作が大幅に簡素化できるという効果を奏
する。Therefore, in the above configuration, the pre-foamed resin particles discharged from the pre-foaming machine can be conveyed by, for example, compressed air or the like, and directly filled from the storage hopper into the measuring container. Easy measurement of prefoaming multiple
Therefore , the operator only needs to set the preset pre-expansion multiple, and the operation of the operator can be greatly simplified.
【0076】また、上記構成では、前記の収納ホッパよ
り計量容器に所定圧力で予備発泡樹脂粒子が充填される
ため、従来の計量方法と比べてより均一かつ迅速に充填
できることから、作業の効率化を図ることができるとと
もに、その充填量を安定化することができる。よって、
予備発泡倍数を検出する際における計量誤差を低減でき
ることから、得られた予備発泡樹脂粒子の発泡倍数の安
定化を図ることもできるという効果を奏する。Further, in the above structure, the storage hopper is
Since the pre-expanded resin particles are filled into the weighing container at a predetermined pressure, the filling can be performed more uniformly and quickly compared to the conventional weighing method, and the work efficiency can be improved.
In fact, the filling amount can be stabilized. Therefore,
Since it is possible to reduce the measurement error when detecting the pre-expansion multiple, it is possible to stabilize the expansion factor of the obtained pre-expanded resin particles.
【図1】本発明の予備発泡樹脂粒子の発泡倍数制御装置
の構成図である。FIG. 1 is a configuration diagram of an expansion ratio control device for pre-expanded resin particles of the present invention.
【図2】上記発泡倍数制御装置における倍数測定装置制
御盤の構成図である。FIG. 2 is a configuration diagram of a multiplex measuring device control panel in the foaming multiplex control device.
【図3】上記倍数測定装置制御盤の正面図である。FIG. 3 is a front view of the control panel of the multiple measurement device.
【図4】上記倍数測定装置制御盤から予備発泡結果が印
字されて出力される印字シートの要部正面図である。FIG. 4 is a front view of a main part of a print sheet on which a result of pre-foaming is printed and output from the control panel of the multiple measurement device.
【図5】上記の予備発泡樹脂粒子の発泡倍数の制御方法
を示すフローチャートの前半部である。FIG. 5 is a first half of a flowchart showing a method for controlling the expansion ratio of the pre-expanded resin particles.
【図6】上記の予備発泡樹脂粒子の発泡倍数の制御方法
を示すフローチャートの後半部である。FIG. 6 is the second half of the flowchart showing the method for controlling the expansion ratio of the pre-expanded resin particles.
1 予備発泡機 6 計量容器 1 Pre-foaming machine 6 Measuring container
Claims (1)
で予備発泡させて予備発泡樹脂粒子を得るに際し、上記
の予備発泡樹脂粒子の予備発泡倍数を制御する予備発泡
樹脂粒子の発泡倍数制御装置において、 入力された設定予備発泡倍数に基づいて原料を供給して
予備発泡させる予備発泡機と、 該予備発泡機から排出された予備発泡樹脂粒子を収納す
る収納ホッパと、 上記収納ホッパの上方に配設されており、その下端面の
開口を開閉可能とするダンパーを有している所定容量の
計量容器と、 上記収納ホッパの下部と上記計量容器の上部側面とを連
通しているサンプリング管と、 上記収納ホッパへ排出された予備発泡樹脂粒子を上記サ
ンプリング管を介して上記計量容器に搬送して充填する
ための圧縮空気を該サンプリング管に送るサンプリング
用送風管と、 上記計量容器の重量を計量するための計量手段と、 上記計量容器に予備発泡樹脂粒子を充填するサンプリン
グ動作を制御するとともに、上記計量手段により計量さ
れた予備発泡樹脂粒子の重量と上記計量容器の容積とか
ら予備発泡樹脂粒子の発泡倍数を換算する倍数測定装置
制御盤とを備えている ことを特徴とする予備発泡樹脂粒
子の発泡倍数制御装置。1. A pre-expansion resin particle expansion ratio control device for controlling the pre-expansion ratio of the pre-expanded resin particles when pre-expanding a raw material composed of synthetic resin particles in a pre-expansion machine. In, the raw material is supplied based on the set pre-expansion multiple
A pre-foaming machine for pre-foaming and a pre-foamed resin particle discharged from the pre-foaming machine are stored.
And a storage hopper that is disposed above the storage hopper,
It has a damper that can open and close the opening
Connect the weighing container to the bottom of the storage hopper and the upper side of the weighing container.
The sampling tube that passes through and the pre-expanded resin particles discharged to the storage hopper are added to the above-mentioned support.
Transport it to the above measuring container through a sampling pipe and fill it.
For sending compressed air to the sampling tube
Blower pipe, measuring means for measuring the weight of the measuring container, and a sampler for filling the measuring container with pre-expanded resin particles.
Control the operation of the
The weight of the pre-expanded resin particles and the volume of the measuring container
Measuring device for converting the expansion ratio of pre-expanded resin particles
An expansion ratio control device for pre-expanded resin particles, comprising a control board .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4066121A JP2693340B2 (en) | 1992-03-24 | 1992-03-24 | Device for controlling the expansion ratio of pre-expanded resin particles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4066121A JP2693340B2 (en) | 1992-03-24 | 1992-03-24 | Device for controlling the expansion ratio of pre-expanded resin particles |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05269737A JPH05269737A (en) | 1993-10-19 |
JP2693340B2 true JP2693340B2 (en) | 1997-12-24 |
Family
ID=13306733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4066121A Expired - Fee Related JP2693340B2 (en) | 1992-03-24 | 1992-03-24 | Device for controlling the expansion ratio of pre-expanded resin particles |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2693340B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102199828B1 (en) * | 2020-09-10 | 2021-01-07 | 박득용 | EPS furnace apparatus |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH059331A (en) * | 1991-06-28 | 1993-01-19 | Taikai Kogyo Kk | Automatic apparatus for measuring ratio |
-
1992
- 1992-03-24 JP JP4066121A patent/JP2693340B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05269737A (en) | 1993-10-19 |
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