JPH0680816A - Apparatus for automatic determination of expansion ratio - Google Patents
Apparatus for automatic determination of expansion ratioInfo
- Publication number
- JPH0680816A JPH0680816A JP4257504A JP25750492A JPH0680816A JP H0680816 A JPH0680816 A JP H0680816A JP 4257504 A JP4257504 A JP 4257504A JP 25750492 A JP25750492 A JP 25750492A JP H0680816 A JPH0680816 A JP H0680816A
- Authority
- JP
- Japan
- Prior art keywords
- measuring
- expansion ratio
- expanded particles
- drying
- particles
- 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.)
- Pending
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、発泡性熱可塑性樹脂粒
子を回分式予備発泡機で発泡させた予備発泡粒子の発泡
倍率を自動的に測定する自動倍率測定装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an automatic magnification measuring device for automatically measuring the expansion ratio of pre-expanded particles obtained by expanding expandable thermoplastic resin particles by a batch type pre-expanding machine.
【0002】[0002]
【従来の技術】従来より、発泡性熱可塑性樹脂粒子を原
料として発泡樹脂製品を製造する場合には、予め原料粒
子を所定の発泡倍率まで予備発泡させ、この予備発泡粒
子を成形機でさらに発泡させて製品を成形しているが、
予備発泡には連続式と回分式(いわゆるバッチ式)との
2方法がある。回分式方法は、連続式方法に比し、予備
発泡粒子の発泡むらが少なくて均質な製品が得られ、ま
た多種類の予備発泡粒子の要求に迅速に対応できる等の
理由により、最近では回分式方法が一般に採用されてい
る。2. Description of the Related Art Conventionally, in the case of producing a foamed resin product using expandable thermoplastic resin particles as a raw material, the raw material particles are pre-expanded to a predetermined expansion ratio, and the pre-expanded particles are further expanded by a molding machine. I am molding the product by
There are two methods for pre-foaming: continuous method and batch method (so-called batch method). Compared to the continuous method, the batch method has less foaming unevenness of the pre-expanded particles, a homogeneous product can be obtained, and it is possible to quickly respond to the requirements of various kinds of pre-expanded particles. The formula method is generally adopted.
【0003】前記回分式予備発泡方法では、まず、一定
量の原料粒子を予備発泡機に供給して水蒸気等の加熱媒
体により所定の発泡倍率まで予備発泡させた後、この予
備発泡粒子を回分式に取り出す。次に、取り出した予備
発泡粒子を熟成サイロを経由して成形機に供給するとと
もに、その一部を一定量のバケツ等の容器にサンプリン
グ採取して重量を測定し、この重量を換算表により発泡
倍率に換算する。次に、この換算値を予め設定した所定
倍率と比較し、両倍率間の偏差に応じて予備発泡機への
加熱媒体又は原料粒子の供給量を調節することにより所
定の発泡倍率の維持を図っていた。但し、上記操作でサ
ンプリング採取以降の操作はすべて人手によっている。In the batch type pre-expanding method, first, a predetermined amount of raw material particles are supplied to a pre-expanding machine to be pre-expanded to a predetermined expansion ratio by a heating medium such as steam, and then the pre-expanded particles are batch type. Take it out. Next, the extracted pre-expanded particles are supplied to the molding machine via the aging silo, and a part of them is sampled in a container such as a bucket and weighed, and the weight is expanded according to a conversion table. Convert to magnification. Next, this conversion value is compared with a preset predetermined expansion ratio, and the predetermined expansion ratio is maintained by adjusting the supply amount of the heating medium or the raw material particles to the pre-expansion machine according to the deviation between both expansion ratios. Was there. However, in the above operation, all operations after sampling and sampling are done manually.
【0004】ところで、最近は、発泡樹脂製品の用途が
魚箱、野菜箱等の容器から家電製品の緩衝材まで多岐に
わたっており、用途に応じた原料粒子の銘柄、粒径及び
発泡倍率が多種多様になっており、また、製品の品質安
定や生産性向上のため発泡倍率には正確性が強く要求さ
れている。しかし、同一発泡倍率でも原料粒子の銘柄、
粒径によって原料供給量が変わり、また同一粒径でも、
原料粒子製造から発泡までの日数によって原料粒子中の
発泡剤の含有量が経時変化して発泡速度に差が生じ、更
にまた予備発泡完了後も発泡槽内の残熱により一部が発
泡して発泡倍率が変わってしまうことがある。従って、
正確な発泡倍率を得るためには、発泡倍率の正確な測定
が不可欠である。By the way, recently, the applications of foamed resin products have been varied from containers such as fish boxes and vegetable boxes to cushioning materials for home electric appliances, and various brands of raw material particles, particle sizes and expansion ratios are available according to the applications. In addition, the expansion ratio is strongly required to be accurate in order to stabilize product quality and improve productivity. However, even with the same expansion ratio, the brand of raw material particles,
The amount of raw material supplied changes depending on the particle size, and even with the same particle size,
Depending on the number of days from the production of the raw material particles to the foaming, the content of the foaming agent in the raw material particles changes with time, resulting in a difference in the foaming rate. The expansion ratio may change. Therefore,
Accurate measurement of the expansion ratio is essential to obtain an accurate expansion ratio.
【0005】しかるに、従来は、サンプリング採取以降
の操作を人手によっているため、求めた発泡倍率に個人
差が生じ、また測定容器の容量、形状によって発泡倍率
が変わるという問題があった。さらに、測定に人手を取
られるという問題もあった。本発明者は、上述のような
問題点を取り除くために発泡倍率の自動測定装置を開発
し、先に提案した(特願平3−185598号)。However, conventionally, since the operations after sampling and sampling are manually performed, there is a problem that the obtained expansion ratio varies among individuals and that the expansion ratio changes depending on the volume and shape of the measuring container. Further, there is a problem that the measurement is labor intensive. The present inventor has developed an automatic measuring device for the expansion ratio in order to eliminate the above-mentioned problems, and has previously proposed it (Japanese Patent Application No. 3-185598).
【0006】上記自動測定装置は、図2に示した如き構
成からなっている。図2において、1は予備発泡機、2
は自動測定装置である。The above automatic measuring device has a structure as shown in FIG. In FIG. 2, 1 is a pre-foaming machine, 2
Is an automatic measuring device.
【0007】この予備発泡機1は回分式(いわゆるバッ
チ式)で、基台3に発泡槽4を設け、発泡槽4の排出側
に送粒ホッパ5を取り付けてなるものである。発泡槽4
は、上部に締切弁6を備えた供給口7と、下部にエアシ
リンダ駆動式蓋8を備えた排出口9と、内部に攪拌機
(図示省略)とをそれぞれ設けている。送粒ホッパ5
は、内部に張設された整粒用篩10の下方にサンプリン
グ用吸込管11が突設されるとともに、下部の排出口1
2に送粒用ブロア13が接続され、上部に回収フィーダ
14を備えている。This pre-foaming machine 1 is of a batch type (so-called batch type), in which a base 3 is provided with a foaming tank 4 and a discharging hopper 5 is attached to the discharge side of the foaming tank 4. Foaming tank 4
Is provided with a supply port 7 having a shut-off valve 6 in the upper part, a discharge port 9 having an air cylinder drive type lid 8 in the lower part, and an agitator (not shown) inside. Grain feeding hopper 5
Is provided with a sampling suction pipe 11 projecting below the sieving sieve 10 stretched inside, and a discharge port 1 at the bottom.
2, a granulation blower 13 is connected, and a recovery feeder 14 is provided on the upper part.
【0008】また、自動測定装置2は、ケース15内に
測定容器16と充填フィーダ17とをとそれぞれ計重器
18及びエアシリンダ19により吊り下げ、制御装置2
0を付設してなるものである。測定容器16は、筒状の
金網製容器で、内部に回転式モータダンパ21がその上
方に一定容積の測定空間22を形成するように装着さ
れ、上部に供給口23及び掃除空気口24と、下部に受
けホッパ25とを備えている。受けホッパ25の排出口
26は、可撓管27を介して回収フィーダ14に接続さ
れている。充填フィーダ17は、供給口23の上方にエ
アシリンダ19により昇降自在に、且つ供給口23の底
部に接離自在に吊り下げられており、可撓管28を介し
て吸込管11に接続されている。計重器18はロードセ
ル等からなり、測定容器16内が空のとき0点になるよ
うに調整しておく。制御装置20は、発泡倍率測定から
発泡槽4への原料粒子の供給量調節に至る一連の操作を
自動化するものである。Further, the automatic measuring device 2 suspends the measuring container 16 and the filling feeder 17 in the case 15 by means of a weighing device 18 and an air cylinder 19, respectively, and the control device 2
0 is attached. The measuring container 16 is a cylindrical wire netting container, inside of which a rotary motor damper 21 is mounted so as to form a measuring space 22 having a constant volume above it, and a supply port 23 and a cleaning air port 24 at the upper part and a lower part. And a receiving hopper 25. The discharge port 26 of the receiving hopper 25 is connected to the recovery feeder 14 via a flexible tube 27. The filling feeder 17 is hung above and below the supply port 23 by an air cylinder 19 so as to be movable up and down and freely attached to and detached from the bottom of the supply port 23, and is connected to the suction pipe 11 via a flexible pipe 28. There is. The weighing device 18 is composed of a load cell or the like, and is adjusted so as to be 0 point when the inside of the measuring container 16 is empty. The control device 20 automates a series of operations from the measurement of the expansion ratio to the adjustment of the supply amount of the raw material particles to the foaming tank 4.
【0009】この自動倍率測定装置2は、予備発泡機1
の操業時に次のように作用する。まず、締切弁6を開
き、原料粒子供給装置(図示省略)により所定量の原料
粒子29を供給口7から発泡槽4内に供給した後、締切
弁6を閉じる。続いて、発泡槽4内に水蒸気等の加熱媒
体を吹き込み、原料粒子29を所定の発泡倍率まで予備
発泡させた後、蓋8を開いて予備発泡した粒子30排出
口9から送粒ホッパ5内に排出し、篩10で整粒された
予備発泡粒子30をブロア13で排出口12から熟成サ
イロを経由して成形機に供給する。This automatic magnification measuring device 2 comprises a pre-foaming machine 1
It operates as follows when operating. First, the shutoff valve 6 is opened, a predetermined amount of the raw material particles 29 is supplied from the supply port 7 into the foaming tank 4 by the raw material particle supply device (not shown), and then the shutoff valve 6 is closed. Subsequently, a heating medium such as steam is blown into the foaming tank 4 to pre-foam the raw material particles 29 to a predetermined expansion ratio, and then the lid 8 is opened to pre-foam the particles 30 from the discharge port 9 to the inside of the particle feeding hopper 5. Then, the pre-expanded particles 30 that have been discharged to the molding machine and sized by the sieve 10 are supplied to the molding machine from the discharge port 12 by the blower 13 via the aging silo.
【0010】その際、制御装置20からの信号により、
エアシリンダ19が充填フィーダ17を下降させて測定
容器16の供給口23の底部に接触させ、充填フィーダ
17が可撓管28及び吸込管11を介して予備発泡粒子
30の一部をサンプリング採取し、測定容器16のの測
定空間22内に充填する。充填が完了すると、エアシリ
ンダ19は充填フィーダ17を上昇させて、供給口23
から離隔させる。At this time, the signal from the controller 20 causes
The air cylinder 19 lowers the filling feeder 17 to bring it into contact with the bottom of the supply port 23 of the measurement container 16, and the filling feeder 17 samples a part of the pre-expanded particles 30 through the flexible tube 28 and the suction tube 11. , The measurement space 22 of the measurement container 16 is filled. When the filling is completed, the air cylinder 19 raises the filling feeder 17, and the supply port 23
Away from.
【0011】次に、計重器18が測定空間22内の予備
発泡粒子30の重量を測定し、その測定値を電気信号と
して制御装置20に発信する。制御装置20は計重器1
8からの電気信号を記憶した後、モータダンパ21を開
いて測定空間22内の予備発泡粒子30を受けホッパ2
5内に排出し、排出口26から可撓管27を介して回収
フィーダ14により送粒ホッパ5内に回収する。続い
て、掃除空気口24から圧縮空気を吹き込んで測定容器
16内を掃除し、モータダンパ21を閉じて次回の測定
に備える。Next, the weighing device 18 measures the weight of the pre-expanded particles 30 in the measurement space 22 and sends the measured value to the control device 20 as an electric signal. The control device 20 is a scale 1
After storing the electrical signal from the hopper 2, the motor damper 21 is opened to receive the pre-expanded particles 30 in the measurement space 22.
5, and is collected in the granulating hopper 5 from the discharge port 26 via the flexible tube 27 by the collection feeder 14. Subsequently, compressed air is blown from the cleaning air port 24 to clean the inside of the measurement container 16, and the motor damper 21 is closed to prepare for the next measurement.
【0012】上記操作を所定回数繰り返すと、制御装置
20は複数個の測定重量を平均して予備発泡粒子30の
比重を算出し、比重を発泡倍率に換算する。続いて、該
換算値を予め入力しておいた所定の設定倍率と比較し、
両倍率間の偏差に応じた制御信号を前記原料粒子供給装
置に発信する。原料粒子供給装置は、制御信号を受けて
次の予備発泡に使用する原料粒子29の供給量を調整し
た後、発泡槽4に供給する。以後、上記一連の操作を繰
り返すのである。When the above operation is repeated a predetermined number of times, the control device 20 averages a plurality of measured weights to calculate the specific gravity of the pre-expanded particles 30, and converts the specific gravity into the expansion ratio. Then, the converted value is compared with a preset magnification that has been input in advance,
A control signal corresponding to the deviation between the two magnifications is transmitted to the raw material particle supply device. The raw material particle supply device receives the control signal and adjusts the supply amount of the raw material particles 29 used for the next pre-foaming, and then supplies the raw material particles 29 to the foaming tank 4. After that, the above series of operations is repeated.
【0013】[0013]
【発明が解決しようとする課題】ところで、原料粒子2
9は発泡槽4内で水蒸気等の加熱媒体により加熱されて
発泡するので、その結果生じた予備発泡粒子30は湿気
を含んでおり、またその湿りの程度が原料粒子29の種
類、発泡倍率、加熱時間等によりバッチ毎に異なってい
る。そのため、上記の自動倍率測定装置2によれば、測
定倍率に誤差が生じたり、予備発泡粒子30が可撓管2
8中を円滑に送粒されないという問題があった。本発明
は、上記の自動倍率測定装置2を改良して、上述のよう
な問題点を取り除くことを目的とする。By the way, the raw material particles 2
9 is heated by a heating medium such as steam in the foaming tank 4 and foams, so that the resulting pre-foamed particles 30 contain moisture, and the degree of wetness thereof depends on the kind of the raw material particles 29, the expansion ratio, It varies from batch to batch depending on the heating time. Therefore, according to the automatic magnification measuring device 2 described above, an error may occur in the measurement magnification, or the pre-expanded particles 30 may be included in the flexible tube 2.
There was a problem that particles were not smoothly sent in the 8th. An object of the present invention is to improve the above automatic magnification measuring device 2 to eliminate the above-mentioned problems.
【0014】[0014]
【課題を解決するための手段】上記目的を達成するため
に、本発明の自動倍率測定装置は内部に一定容積の測定
空間を形成可能な測定容器と、回分式予備発泡機より排
出される予備発泡粒子の一部を前記測定空間内に供給す
る充填フィーダと、前記測定空間内に供給された予備発
泡粒子の重量を測定し、その測定値を電気信号として発
信する計重器と、該計重器からの電気信号を予備発泡粒
子の発泡倍率に換算し、該換算値と予め設定した所定倍
率との偏差に応じた制御信号を発信して、前記予備発泡
機内への原料供給量を調整する制御装置とを具備すると
ともに、前記予備発泡機の排出側と前記充填フィーダと
の間に上流側より順次エアインゼクタと乾燥容器とを接
続し、該乾燥容器に乾燥空気供給装置を接続した構成と
している。In order to achieve the above object, the automatic magnification measuring device of the present invention comprises a measuring container in which a measuring space having a constant volume can be formed, and a preliminary discharge from a batch type prefoaming machine. A filling feeder for supplying a part of the expanded particles into the measurement space, a weighting device for measuring the weight of the pre-expanded particles supplied in the measurement space, and transmitting the measured value as an electric signal, and the meter. The electric signal from the weighting device is converted into the expansion ratio of the pre-expanded particles, and a control signal corresponding to the deviation between the conversion value and a preset predetermined ratio is transmitted to adjust the amount of raw material supplied into the pre-expansion machine. And a control device for controlling the temperature of the pre-foaming machine, the air injector and the drying container are sequentially connected from the upstream side between the discharge side of the pre-foaming machine and the filling feeder, and the drying air supply device is connected to the drying container. There is.
【0015】[0015]
【作用】上記構成の自動倍率測定装置においては、予備
発泡機が排出した予備発泡粒子の一部をエアインゼクタ
がサンプリング採取して、いったん乾燥容器内に供給す
る。この予備発泡粒子は乾燥容器内で乾燥空気供給装置
から吹き込まれる乾燥空気により乾燥された後、充填フ
ィーダにより測定容器の測定空間内に供給される。この
ようにして乾燥された予備発泡粒子は乾燥容器から円滑
に測定容器に送粒されるとともに、湿気により測定倍率
に発生する誤差を解消する。In the automatic magnification measuring device having the above structure, the air injector samples and collects a part of the pre-expanded particles discharged by the pre-expanding machine and once supplies the pre-expanded particles into the drying container. The pre-expanded particles are dried in the dry container by the dry air blown from the dry air supply device, and then are supplied into the measurement space of the measurement container by the filling feeder. The pre-expanded particles dried in this way are smoothly transferred from the drying container to the measuring container, and at the same time, the error caused in the measurement magnification due to moisture is eliminated.
【0016】[0016]
【実施例】以下、本発明の一実施例を図1に基づいて説
明する。図1は、予備発泡機31に本発明の自動倍率測
定装置32を適用した場合の全体構成を示している。こ
の予備発泡機31は回分式で、基台33に発泡槽34を
設け、発泡槽34の排出側に送粒ホッパ35を取り付け
てなるものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. FIG. 1 shows the overall configuration when the automatic magnification measuring device 32 of the present invention is applied to the pre-foaming machine 31. The pre-foaming machine 31 is of a batch type and has a base 33 provided with a foaming tank 34, and a granulating hopper 35 is attached to the discharge side of the foaming tank 34.
【0017】発泡槽34は、上部の供給口36より供給
された原料粒子を水蒸気等の加熱媒体により加熱して所
定の発泡倍率まで予備発泡させた後、この予備発泡粒子
を下部の排出口37から回分式に送粒ホッパ35に排出
するもので、内部に攪拌機(図示省略)を有し、供給口
36に締切弁38と排出口37にエアシリンダ駆動式蓋
39とを備えている。In the foaming tank 34, the raw material particles supplied from the upper supply port 36 are heated by a heating medium such as steam to pre-expand to a predetermined expansion ratio, and then the pre-expanded particles are discharged to the lower discharge port 37. It is to be discharged batchwise to the particle feeding hopper 35, has an agitator (not shown) inside, and has a shutoff valve 38 at the supply port 36 and an air cylinder drive type lid 39 at the discharge port 37.
【0018】送粒ホッパ35は、発泡槽34から排出さ
れた予備発泡粒子を受けて、下部の排出口40から熟成
サイロを経由して成形機に供給するもので、内部にブロ
ック化した予備発泡粒子を取り除くための篩41が張設
されるとともに、篩41の下方にサンプリング用吸込管
42が突設され、排出口40に送粒ブロア43が接続さ
れ、さらに上部に回収フィーダ44を備えている。The granulating hopper 35 receives the pre-expanded particles discharged from the foaming tank 34 and supplies the pre-expanded particles from the lower discharge port 40 to the molding machine through the aging silo. A sieve 41 for removing particles is stretched, a sampling suction pipe 42 is projected below the sieve 41, a granulation blower 43 is connected to the discharge port 40, and a recovery feeder 44 is provided on the upper portion. There is.
【0019】また、自動倍率測定装置32は、ケース4
5内に測定容器46と充填フィーダ47とをそれぞれ計
重機48及びエアシリンダ49により吊り下げ、また前
記送粒ホッパ35の吸込管42と充填フィーダ47との
間に上流側より順次締切コック50、ボールコック5
1、エアインゼクタ52及び乾燥容器53を接続すると
ともに、乾燥容器53に乾燥空気供給装置54を接続
し、さらに制御装置55を付設してなるものである。Further, the automatic magnification measuring device 32 has a case 4
5, a measuring container 46 and a filling feeder 47 are suspended by a weighing machine 48 and an air cylinder 49, respectively, and between the suction pipe 42 of the granulating hopper 35 and the filling feeder 47, a shut-off cock 50 from the upstream side in order. Ball cock 5
1, the air injector 52 and the drying container 53 are connected, the drying air supply device 54 is connected to the drying container 53, and the control device 55 is additionally provided.
【0020】測定容器46は、パンチングプレートや金
網製の筒状容器で、内部に回転式モータダンパ56がそ
の上方に一定容積(1〜20L程度)の測定空間57を
形成するように開閉自在に装着され、上部に予備発泡粒
子の供給口58及び掃除空気口59と、下部に受けホッ
パ60とを備えている。受けホッパ60は、下端の排出
口61が可撓管62を介して前記送粒ホッパ35の回収
フィーダ44に接続されている。なお、モータダンパ5
6は、スライド式等であってもよい。The measuring container 46 is a cylindrical container made of a punching plate or a wire mesh, and a rotary motor damper 56 is installed therein so that it can be opened and closed so as to form a measuring space 57 having a constant volume (about 1 to 20 L) above it. In addition, a pre-expanded particle supply port 58 and a cleaning air port 59 are provided in the upper part, and a receiving hopper 60 is provided in the lower part. The receiving hopper 60 has a discharge port 61 at the lower end connected to the recovery feeder 44 of the grain feeding hopper 35 via a flexible tube 62. The motor damper 5
6 may be a slide type or the like.
【0021】充填フィーダ47は、測定容器46の供給
口58の上方にエアシリンダ49により昇降するよう
に、且つ測定誤差を無くするために供給口58の底部に
接離自在に配置されており、可撓管63を介して乾燥容
器53の底部に接続されている。計重機48はロードセ
ル等からなり、測定容器46内が空のとき0点になるよ
うに予め調整しておく。締切コック50、ボールコック
51は、エアインゼクタ52より上流側の管内を乾燥す
るためのもので、締切コック50はボールコック51の
上流側から分岐した下管に接続されている。エアインゼ
クタ52は、前記送粒ホッパ35に排出された予備発泡
粒子の一部を吸込管42を介してサンプリング採取し、
乾燥容器53に供給するためのもので、その吐出側が乾
燥容器53の上部に接続されている。The filling feeder 47 is arranged above the supply port 58 of the measuring container 46 so as to be moved up and down by an air cylinder 49, and is arranged at the bottom of the supply port 58 so as to be contactable and separable in order to eliminate a measurement error. It is connected to the bottom of the drying container 53 via a flexible tube 63. The weighing machine 48 is composed of a load cell or the like, and is adjusted in advance so as to reach 0 point when the inside of the measuring container 46 is empty. The shutoff cock 50 and the ball cock 51 are for drying the inside of the pipe upstream of the air injector 52, and the shutoff cock 50 is connected to a lower pipe branched from the upstream side of the ball cock 51. The air injector 52 samples a part of the pre-expanded particles discharged to the particle feeding hopper 35 through the suction pipe 42,
It is for supplying to the drying container 53, and its discharge side is connected to the upper part of the drying container 53.
【0022】乾燥容器53は、パンチングプレートや金
網製の筒状容器で、底部に回転式モータダンパ64が開
閉自在に装着され、前記送粒ホッパ35の上部に取り付
けられている。なお、モータダンパ64は、スライド式
等であってもよい。乾燥空気供給装置54は、乾燥容器
53に温度が常温〜70℃の乾燥空気を供給するための
もので、基台65上に送風ブロア66と熱交換器67と
を接続して取り付け、熱交換器67の吐出側が乾燥容器
53の底部に接続されている。なお、場合によっては、
熱交換器67を省略してもよい。The drying container 53 is a cylindrical container made of a punching plate or a wire mesh. A rotary motor damper 64 is attached to the bottom of the drying container 53 so as to be openable and closable, and is attached to the upper part of the grain feeding hopper 35. The motor damper 64 may be of a slide type or the like. The dry air supply device 54 is for supplying dry air having a temperature of room temperature to 70 ° C. to the drying container 53, and is installed by connecting the blower blower 66 and the heat exchanger 67 on the base 65 to perform heat exchange. The discharge side of the container 67 is connected to the bottom of the drying container 53. In some cases,
The heat exchanger 67 may be omitted.
【0023】制御装置55は、予備発泡粒子のサンプリ
ング採取及び乾燥から、発泡倍率測定及び発泡槽34へ
の原料粒子の供給量調整に至る一連の操作を自動化する
ためのものである。The control device 55 is for automating a series of operations from the sampling and drying of the pre-expanded particles to the measurement of the expansion ratio and the adjustment of the supply amount of the raw material particles to the expansion tank 34.
【0024】次に、上記構成における作用について説明
する。まず、ボールコック51を閉じて締切コック50
を開き、締切コック50及びエアインゼクタ52から圧
縮空気を吹き込んで吸込管42から乾燥容器53に至る
管内を乾燥し、予備発泡粒子が該管内を円滑に送粒され
るようにしておく。乾燥が終わると締切コック50を閉
じ、ボールコック51を開く。Next, the operation of the above structure will be described. First, the ball cock 51 is closed and the deadline cock 50 is closed.
Then, compressed air is blown from the shutoff cock 50 and the air injector 52 to dry the inside of the pipe from the suction pipe 42 to the drying container 53 so that the pre-foamed particles are smoothly fed into the pipe. When the drying is completed, the dead cock 50 is closed and the ball cock 51 is opened.
【0025】次に予備発泡機31において、締切弁38
を開き、原料粒子供給装置(図示省略)により所定量の
原料粒子68を供給口36から発泡槽34内に供給した
後、締切弁38を閉じる。原料粒子68にはポリスチレ
ン系樹脂、ポリエチレン、ポリプロピレン等のポリオレ
フィン系樹脂粒子やポリウレタン系樹脂粒子等を使用す
る。続いて、発泡槽34内に水蒸気等の加熱媒体を吹き
込み、原料粒子68を所定の発泡倍率まで予備発泡させ
た後、蓋39を開いて予備発泡した粒子69を排出口3
7から送粒ホッパ35内に排出し、篩41で整流された
予備発泡粒子69を送粒ブロア43で排出口40から熟
成サイロを経由して成形機に供給する。Next, in the pre-foaming machine 31, the shut-off valve 38
And a predetermined amount of raw material particles 68 are supplied from the supply port 36 into the foaming tank 34 by a raw material particle supply device (not shown), and then the shutoff valve 38 is closed. As the raw material particles 68, polystyrene resin, polyolefin resin particles such as polyethylene and polypropylene, polyurethane resin particles and the like are used. Then, a heating medium such as steam is blown into the foaming tank 34 to pre-foam the raw material particles 68 to a predetermined foaming ratio, and then the lid 39 is opened to pre-foam the particles 69.
The pre-expanded particles 69 discharged from No. 7 into the granulating hopper 35 and rectified by the sieve 41 are supplied to the molding machine from the discharge port 40 by the granulating blower 43 via the aging silo.
【0026】その際、自動倍率測定装置32において
は、制御装置55からの信号により、エアインゼクタ5
2が吸込管42を介して予備発泡粒子69の一部をサン
プリング採取し、乾燥容器53内に供給する。サンプリ
ング量は、発泡倍率測定に必要な量よりも若干多い目と
する。なお、エアインゼクタ52でサンプリング採取す
る理由は、ブロア等でサンプリング採取すると、予備発
泡粒子69が収縮して測定倍率と実倍率との間に差を生
じるからである。続いて、乾燥空気供給装置54が乾燥
空気を乾燥容器53内に吹き込んで予備発泡粒子69を
乾燥させる。乾燥時間は10〜30秒程度とするのが好
ましい。At this time, in the automatic magnification measuring device 32, the signal from the control device 55 causes the air injector 5 to operate.
2 samples a part of the pre-expanded particles 69 through the suction pipe 42 and supplies the pre-expanded particles 69 into the drying container 53. The sampling amount is slightly larger than the amount required for measuring the expansion ratio. The reason for sampling with the air injector 52 is that if the sampling is performed with a blower or the like, the pre-expanded particles 69 contract and a difference occurs between the measurement magnification and the actual magnification. Then, the dry air supply device 54 blows dry air into the drying container 53 to dry the pre-expanded particles 69. The drying time is preferably about 10 to 30 seconds.
【0027】乾燥が完了すると、エアシリンダ49が充
填フィーダ47を下降させて測定容器46の供給口58
の底部に接触させ充填フィーダ47が可撓管63を介し
て乾燥容器53内の予備発泡粒子69を所要量だけ吸引
し、一定の空気圧力(0.5〜3.5kg/cm2 )をもっ
て測定容器46の測定空間57に過不足なく充填する。
充填が完了すると、エアシリンダ49は充填フィーダ4
7を上昇させて、供給口58から離隔させる。なお、乾
燥容器53内に残った余分の予備発泡粒子69は、モー
タダンパ64を開いて送粒ホッパ35内に回収する。When the drying is completed, the air cylinder 49 lowers the filling feeder 47 and the supply port 58 of the measuring container 46.
The pre-expanded particles 69 in the drying container 53 are sucked by the required amount through the flexible tube 63 by contacting with the bottom of the container, and measured with a constant air pressure (0.5 to 3.5 kg / cm 2 ). The measurement space 57 of the container 46 is filled with just enough.
When the filling is completed, the air cylinder 49 moves to the filling feeder 4
7 is lifted and separated from the supply port 58. The extra pre-expanded particles 69 remaining in the drying container 53 are collected in the particle feeding hopper 35 by opening the motor damper 64.
【0028】エアシリンダ49が上昇すると、計重器4
8が測定空間57内の予備発泡粒子69の重量を測定
し、その測定値を電気信号として制御装置55に発信す
る。制御装置55は、計重器48からの電気信号を記憶
した後、モータダンパ56を開いて測定空間57内の予
備発泡粒子69を受けホッパ60内に排出し、排出口6
1から可撓管62を介して回収フィーダ44により送粒
ホッパ35内に回収する。続いて掃除空気口59から測
定容器46内に圧縮空気を吹き込んで測定容器46内を
掃除した後、モータダンパ56を閉じて次回の測定に備
えるWhen the air cylinder 49 rises, the weighing device 4
8 measures the weight of the pre-expanded particles 69 in the measurement space 57 and sends the measured value to the control device 55 as an electric signal. After storing the electric signal from the weighing device 48, the control device 55 opens the motor damper 56, receives the pre-expanded particles 69 in the measurement space 57, and discharges them into the hopper 60.
The powder is collected from the No. 1 through the flexible tube 62 by the collection feeder 44 into the granulating hopper 35. Subsequently, compressed air is blown into the measurement container 46 from the cleaning air port 59 to clean the inside of the measurement container 46, and then the motor damper 56 is closed to prepare for the next measurement.
【0029】上記と同じ操作を所定回数(例えば3回程
度)繰り返すと制御装置55は、計重器48からの複数
個の測定重量を平均して予備発泡粒子69の比重を算出
し、比重を発泡倍率に換算する。続いて、該換算値を予
め入力しておいた所定の設定倍率と比較し、両倍率間の
偏差が±1以上の場合には偏差に応じた制御信号を前記
原料粒子供給装置の計重器に発信する。該計重器は、制
御信号を受けて次の予備発泡に使用する原料粒子68の
供給量を調整した後、発泡槽34に供給するとともに、
この供給量を電気信号として制御装置55に入力する。When the same operation as described above is repeated a predetermined number of times (for example, about three times), the control device 55 averages a plurality of measured weights from the weighting device 48 to calculate the specific gravity of the pre-expanded particles 69, and determines the specific gravity. Convert to foaming ratio. Subsequently, the converted value is compared with a predetermined set magnification inputted in advance, and when the deviation between both magnifications is ± 1 or more, a control signal corresponding to the deviation is sent to the weighing device of the raw material particle supplying device. Call. The weighing device, after receiving the control signal and adjusting the supply amount of the raw material particles 68 used for the next pre-expansion, supplies the same to the foaming tank 34, and
This supply amount is input to the control device 55 as an electric signal.
【0030】以後、上記一連の操作を繰り返すのである
が、制御装置55が特定の原料粒子68及び発泡倍率に
対する最新の補正済み供給量を記憶しているので、次回
同一の原料粒子68及び発泡倍率で予備発泡を行なう場
合には、自動的に同一条件で予備発泡を行なうことがで
きる。また、モータダンパ56、64で切り替えること
により、1台の自動倍率測定装置32で複数台の予備発
泡機31に対応することも可能である。After that, the above series of operations are repeated, but since the control device 55 stores the latest corrected supply amount for the specific raw material particles 68 and the expansion ratio, the same raw material particles 68 and the expansion ratio will be used next time. When the pre-foaming is performed in step 1, the pre-foaming can be automatically performed under the same conditions. Further, by switching between the motor dampers 56 and 64, it is possible for one automatic magnification measuring device 32 to correspond to a plurality of pre-foaming machines 31.
【0031】上記のように本実施例の自動倍率測定装置
32においては、乾燥容器53内で予備発泡粒子69を
乾燥するとともに、吸込管42から乾燥容器53に至る
管内も乾燥するので、湿気により測定倍率に発生する誤
差が解消し、また予備発泡粒子69の管内送粒が円滑に
なる。As described above, in the automatic magnification measuring device 32 of this embodiment, the pre-expanded particles 69 are dried in the drying container 53, and the inside of the suction pipe 42 to the drying container 53 is also dried. The error generated in the measurement magnification is eliminated, and the pre-expanded particles 69 can be smoothly fed into the pipe.
【0032】[0032]
【発明の効果】本発明は、以上説明したように、予備発
泡機から排出された予備発泡粒子の一部をエアインゼク
タによりサンプリング採取し乾燥容器内にいったん供給
し、該予備発泡粒子を乾燥空気供給装置からの乾燥空気
により乾燥する構成としたので、湿気により測定倍率に
発生する誤差が解消し、極めて正確な発泡倍率をもって
予備発泡を行なうことができるのみならず、予備発泡粒
子の管内送粒が円滑になるという利点を有する。なお、
実施例で説明したように、予備発泡機から乾燥容器に至
る管内を乾燥すると、予備発泡粒子の管内送粒がより一
層円滑になる。As described above, according to the present invention, a part of the pre-expanded particles discharged from the pre-expanding machine is sampled by the air injector and once supplied into the drying container, and the pre-expanded particles are supplied with the dry air. Since it is configured to dry with the dry air from the device, the error that occurs in the measurement magnification due to humidity is eliminated, not only can pre-foaming be performed with an extremely accurate expansion ratio, but also pre-expanded particles can be fed into the pipe. It has the advantage of being smooth. In addition,
As described in the examples, when the inside of the pipe from the pre-foaming machine to the drying container is dried, the pre-foamed particles can be more smoothly fed into the pipe.
【図1】本発明の自動倍率測定装置を回分式予備発泡機
に適用した一実施例の全体構成図である。FIG. 1 is an overall configuration diagram of an embodiment in which an automatic magnification measuring device of the present invention is applied to a batch type prefoaming machine.
【図2】従来(先願)の自動倍率測定装置を回分式予備
発泡機に適用した一例の全体構成図である。FIG. 2 is an overall configuration diagram of an example in which a conventional (prior application) automatic magnification measuring device is applied to a batch type prefoaming machine.
31 予備発泡機 32 自動倍率測
定装置 46 測定容器 47 充填フィー
ダ 48 計重器 52 エアインゼ
クタ 53 乾燥容器 54 乾燥空気供
給装置 55 制御装置 57 測定空間 68 原料粒子 69 予備発泡粒
子31 Pre-foaming machine 32 Automatic magnification measuring device 46 Measuring container 47 Filling feeder 48 Weigher 52 Air injector 53 Drying container 54 Dry air supply device 55 Control device 57 Measuring space 68 Raw material particle 69 Pre-foaming particle
Claims (1)
測定容器と、回分式予備発泡機より排出される予備発泡
粒子の一部を前記測定空間内に供給する充填フィーダ
と、前記測定空間内に供給された予備発泡粒子の重量を
測定し、その測定値を電気信号として発信する計重器
と、該計重器からの電気信号を予備発泡粒子の発泡倍率
に換算し、該換算値と予め設定した所定倍率との偏差に
応じた制御信号を発信して、前記予備発泡機内への原料
供給量を調整する制御装置とを具備するとともに、前記
予備発泡機の排出側と前記充填フィーダとの間に上流側
より順次エアインゼクタと乾燥容器とを接続し、該乾燥
容器に乾燥空気供給装置を接続したことを特徴とする自
動倍率測定装置。1. A measuring container capable of forming a measuring space having a constant volume therein, a filling feeder for supplying a part of the pre-expanded particles discharged from a batch type pre-expanding machine into the measuring space, and the measuring space. The weight of the pre-expanded particles supplied to the inside is measured, and a weighing device that transmits the measured value as an electric signal, and the electric signal from the weighing device is converted into the expansion ratio of the pre-expanded particles, and the converted value And a control device for transmitting a control signal according to a deviation from a preset predetermined scaling factor to adjust the amount of raw material supplied into the pre-foaming machine, and the discharge side of the pre-foaming machine and the filling feeder. An automatic magnification measuring device, characterized in that an air injector and a drying container are connected in sequence from the upstream side to a drying air supply device connected to the drying container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4257504A JPH0680816A (en) | 1992-08-31 | 1992-08-31 | Apparatus for automatic determination of expansion ratio |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4257504A JPH0680816A (en) | 1992-08-31 | 1992-08-31 | Apparatus for automatic determination of expansion ratio |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0680816A true JPH0680816A (en) | 1994-03-22 |
Family
ID=17307218
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4257504A Pending JPH0680816A (en) | 1992-08-31 | 1992-08-31 | Apparatus for automatic determination of expansion ratio |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0680816A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000037988A1 (en) * | 1998-12-18 | 2000-06-29 | Karl Storz Gmbh & Co. Kg | Endoscope lens, and an endoscope equipped with such a lens |
WO2005087475A1 (en) * | 2004-03-15 | 2005-09-22 | Kaneka Corporation | Bulk density measuring equipment and measuring method of prefoamed particle, and method for producing prefoamed particle |
JP2007218588A (en) * | 2006-02-14 | 2007-08-30 | Kaneka Corp | Method of measuring bulk density of prefoamed particles |
WO2015056461A1 (en) | 2013-10-18 | 2015-04-23 | 株式会社カネカ | Bulk-density measuring device for pre-expanded particles and method for manufacturing pre-expanded particles |
CN111169017A (en) * | 2020-01-17 | 2020-05-19 | 南京师范大学 | Continuous-to-separate feeding and discharging system for photocuring 3D printing |
-
1992
- 1992-08-31 JP JP4257504A patent/JPH0680816A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000037988A1 (en) * | 1998-12-18 | 2000-06-29 | Karl Storz Gmbh & Co. Kg | Endoscope lens, and an endoscope equipped with such a lens |
DE19858785A1 (en) * | 1998-12-18 | 2000-07-06 | Storz Karl Gmbh & Co Kg | Endoscope lens and endoscope with such a lens |
DE19858785C2 (en) * | 1998-12-18 | 2002-09-05 | Storz Karl Gmbh & Co Kg | Endoscope lens and endoscope with such a lens |
WO2005087475A1 (en) * | 2004-03-15 | 2005-09-22 | Kaneka Corporation | Bulk density measuring equipment and measuring method of prefoamed particle, and method for producing prefoamed particle |
JP2007218588A (en) * | 2006-02-14 | 2007-08-30 | Kaneka Corp | Method of measuring bulk density of prefoamed particles |
JP4680086B2 (en) * | 2006-02-14 | 2011-05-11 | 株式会社カネカ | Method for measuring bulk density of pre-expanded particles |
WO2015056461A1 (en) | 2013-10-18 | 2015-04-23 | 株式会社カネカ | Bulk-density measuring device for pre-expanded particles and method for manufacturing pre-expanded particles |
US10131076B2 (en) | 2013-10-18 | 2018-11-20 | Kaneka Corporation | Bulk-density measuring device for pre-expanded particles and method for manufacturing pre-expanded particles |
CN111169017A (en) * | 2020-01-17 | 2020-05-19 | 南京师范大学 | Continuous-to-separate feeding and discharging system for photocuring 3D printing |
CN111169017B (en) * | 2020-01-17 | 2021-11-26 | 南京师范大学 | Continuous-to-separate feeding and discharging system for photocuring 3D printing |
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