JPH06220240A - Pre-expander - Google Patents

Pre-expander

Info

Publication number
JPH06220240A
JPH06220240A JP2625793A JP2625793A JPH06220240A JP H06220240 A JPH06220240 A JP H06220240A JP 2625793 A JP2625793 A JP 2625793A JP 2625793 A JP2625793 A JP 2625793A JP H06220240 A JPH06220240 A JP H06220240A
Authority
JP
Japan
Prior art keywords
raw material
foaming
expanded
feed
main body
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
Application number
JP2625793A
Other languages
Japanese (ja)
Inventor
Takeshi Yamanaka
猛 山中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Machinery and Metal Co Ltd
Original Assignee
Toyo Machinery and Metal Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Machinery and Metal Co Ltd filed Critical Toyo Machinery and Metal Co Ltd
Priority to JP2625793A priority Critical patent/JPH06220240A/en
Publication of JPH06220240A publication Critical patent/JPH06220240A/en
Pending legal-status Critical Current

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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)

Abstract

PURPOSE:To obtain a pre-expander for a foamable resin adapted so that the expansion ratio may be corrected at once by changing the metering value of feed pellets according to the deviation when the signal sent from a metering device is compared with the set value, and the sent signal is outside the tolerance range of the set value. CONSTITUTION:A feed metering hopper 8B is provided above a pre-expander body 2 for pre-expanding foamable resin pellets; a feed metering device 8F is provided on the feed metering hopper 8B; a bottom closing device 8C is provided on the bottom of the feed metering hopper 8B; a pre-expanded particle metering device 5 is provided adjacent to the pre-expander body 2 and meters the pre-expanded particles sent from the pre-expander body 2; the signal of the pre-expanded particles sent from the pre-expanded particle meter 5 is compared with the set expansion ratio in a controller 6; and when the sent value of the pre-expanded particles is outside the tolerance range of the set value, the feed rate of the feed is increased or decreased according to the deviation from the tolerance range by means of the feed metering device 8F.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、発泡倍率を常時検出
し、これをフィードバックすることにより予備発泡倍率
を常時一定に保つ事ができる発泡樹脂の予備発泡装置に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a prefoaming device for a foamed resin which can always keep the prefoaming ratio constant by constantly detecting the foaming ratio and feeding it back.

【0002】[0002]

【従来の技術】予備発泡装置は、発泡成形機に供給する
樹脂粒子を予め所定の倍率に発泡させておく装置で、予
備発泡させられた樹脂粒子はサイロに貯蔵され、熟成さ
せられた後、発泡成形機に供給される。発泡成形機での
発泡状態を一定に保ち、均質な発泡樹脂製品を継続的に
生産するためには、一定の予備発泡粒子が発泡成形機に
供給され続ける事が重要である。
2. Description of the Related Art A prefoaming device is a device for preliminarily foaming resin particles to be supplied to a foam molding machine at a predetermined ratio. The prefoamed resin particles are stored in a silo and aged. Supplied to a foam molding machine. In order to keep the foamed state in the foam molding machine constant and continuously produce a homogeneous foamed resin product, it is important that a certain amount of pre-expanded particles be continuously supplied to the foam molding machine.

【0003】従来の予備発泡機では、予備発泡倍率を設
定する方法として、発泡時間を固定タイマーで設定す
る方法や、光電センサを予備発泡機本体に固定的に設
置しておき、固定センサにて発泡粒子が検出されると発
泡完了とするという方法がある。前者の方法の場合、タ
イマーによる時間設定が固定であり、後者の場合は光電
センサの高さが固定されているため、予備発泡倍率にば
らつきが発生した場合、所定の倍率にまで修正するのに
非常に時間がかかるという問題があった。
In the conventional pre-foaming machine, as a method of setting the pre-foaming ratio, a method of setting a foaming time with a fixed timer or a photoelectric sensor fixedly installed in the main body of the pre-foaming machine is used. There is a method of completing the foaming when the foamed particles are detected. In the case of the former method, the time setting by the timer is fixed, and in the case of the latter, the height of the photoelectric sensor is fixed, so if there is a variation in the prefoaming ratio, it is possible to correct it to a predetermined ratio. There was a problem that it took a very long time.

【0004】[0004]

【発明が解決しようとする課題】本発明はかかる従来例
の欠点を解決するためになされたもので、その目的とす
る処は、計量装置からの計量信号と設定値とを比較し、
計量信号が設定値の許容範囲から外れている場合には乖
離幅に合わせて原料投入量を変更して、発泡倍率を直ち
に修正出来るようにした発泡樹脂の予備発泡装置を提供
するにある。
SUMMARY OF THE INVENTION The present invention has been made in order to solve the drawbacks of the conventional example, and the purpose thereof is to compare a weighing signal from a weighing device with a set value,
An object of the present invention is to provide a pre-expansion device for a foamed resin in which the amount of raw material input is changed according to the deviation width when the measurement signal is out of the allowable range of the set value so that the expansion ratio can be immediately corrected.

【0005】[0005]

【課題を解決するための手段】前記解決課題達成のため
に請求項1に記載の発泡樹脂の予備発泡装置(A)は、 発泡樹脂ペレットを予備発泡させる予備発泡機本体
(2)と、 予備発泡機本体(2)の原料受給部(8E)上に設けられた
投入原料計量ホッパ(8B)と、 投入原料計量ホッパ(8B)に付設された投入原料計量装
置(8F)と、 投入原料計量ホッパ(8B)の底部に設けられ、投入原料
計量ホッパ(8B)の底部を開閉する底部開閉装置(8C)と、 予備発泡機本体(2)から送出された予備発泡粒子の計
量を行う予備発泡粒計量装置(5)と、 予備発泡粒計量装置(5)からの予備発泡粒計量信号と
設定発泡倍率とを比較して前記予備発泡計量値が設定値
の許容値を越えている場合には、許容値からの乖離幅に
対応させて前記投入原料計量装置(8F)により原料の計量
を増減する制御装置(6)とで構成されたことを特徴とす
る。
[Means for Solving the Problems] In order to achieve the above-mentioned problems, a prefoaming device (A) for foaming resin according to claim 1 is a prefoaming machine main body for prefoaming foamed resin pellets.
(2), the input raw material measuring hopper (8B) provided on the raw material receiving section (8E) of the pre-foaming machine main body (2), and the input raw material measuring device (8F) attached to the input raw material measuring hopper (8B). ) And a bottom opening / closing device (8C) provided at the bottom of the input raw material weighing hopper (8B) for opening and closing the bottom of the input raw material weighing hopper (8B), and pre-expanded particles sent from the pre-expanding machine body (2). The pre-expanded-particle measuring device (5) for measuring the pre-expanded-particle measuring signal (5) and the pre-expanded-particle measuring signal from the pre-expanded-particle measuring device (5) are compared with the set expansion ratio, and the pre-expanded measured value indicates the allowable value of the set value. If it exceeds the limit, it is characterized by being configured with a control device (6) for increasing or decreasing the amount of raw material measured by the input raw material measuring device (8F) according to the deviation from the allowable value.

【0006】これにより予備発泡機本体(2)の予備発泡
粒子を毎回計量して発泡倍率を計算し、発泡倍率が設定
倍率の許容範囲外であれば、その乖離幅に対応させて前
記投入原料計量装置(8F)により原料の計量を増減させて
倍率補正を行う事ができ、発泡倍率の管理を非常に厳密
且つ正確に行う事ができ、最終発泡成形品の品質向上を
はかる事ができるという利点がある。
As a result, the pre-expanded particles of the main body of the pre-expanding machine (2) are weighed each time to calculate the expansion ratio, and if the expansion ratio is outside the allowable range of the set expansion ratio, the input raw material is made to correspond to the deviation width. The metering device (8F) can be used to increase or decrease the amount of raw material to correct the ratio, which makes it possible to control the expansion ratio very strictly and accurately, and to improve the quality of the final foamed molded product. There are advantages.

【0007】[0007]

【実施例】以下、本発明を図示実施例に従って詳述す
る。予備発泡機本体(2)は、底部が球面状に形成された
円筒状の加熱筒(7)と、加熱筒(7)の天井部に設置された
投入原料供給部(8)並びに加熱筒(7)内に設置された回転
翼(9)を駆動する駆動装置(10)とで構成されている。加
熱筒(7)の底部には蒸気配管(11)と前記駆動装置(10)と
が設置されており、蒸気を底部から加熱筒(7)内部に送
り込み且つ回転翼(9)を回転させる事が出来るようにな
っている。
The present invention will be described in detail below with reference to the illustrated embodiments. The main body of the pre-foaming machine (2) has a cylindrical heating cylinder (7) having a spherical bottom, a charging raw material supply section (8) and a heating cylinder (8) installed on the ceiling of the heating cylinder (7). It is composed of a drive unit (10) for driving a rotary blade (9) installed inside the unit (7). A steam pipe (11) and the drive device (10) are installed at the bottom of the heating cylinder (7), and steam is sent from the bottom into the heating cylinder (7) and the rotary blades (9) are rotated. You can do it.

【0008】(12)は蒸気配管(11)に設置された開閉弁
で、制御装置(6)により制御されるようになっており、
(20)は加熱筒(7)に設置された圧力計である。
(12) is an on-off valve installed in the steam pipe (11), which is controlled by the control device (6),
(20) is a pressure gauge installed in the heating cylinder (7).

【0009】加熱筒(7)の底部には細孔(14)を多数穿設
した底板(13)が設置されており、高温蒸気が細孔(14)を
通って内部に流入するようになっている。駆動装置(10)
は加熱筒(7)の中心に設置された回転軸(15)に接続され
ており、回転翼(9)を回転するようになっている。回転
翼(9)は回転軸(15)に複数本設置されており、加熱筒(7)
内に掛け渡された固定翼(16)の間を回転するようになっ
ている。
A bottom plate (13) having a large number of pores (14) is installed at the bottom of the heating cylinder (7) so that high temperature steam can flow into the interior through the pores (14). ing. Drive (10)
Is connected to a rotary shaft (15) installed at the center of the heating cylinder (7) and rotates the rotary blade (9). A plurality of rotors (9) are installed on the rotating shaft (15), and the heating cylinder (7)
It is designed to rotate between the fixed wings (16) that are suspended inside.

【0010】(21)は加熱筒(7)の底部側面に設置された
開閉装置、(22)は開閉装置(21)に接続された乾燥用ドラ
イベッドである。勿論、これに限られる事はないが、開
閉装置(21)は本実施例では開閉シリンダを使用してい
る。
Reference numeral (21) is an opening / closing device installed on the bottom side surface of the heating cylinder (7), and reference numeral (22) is a dry bed for drying connected to the opening / closing device (21). Of course, the present invention is not limited to this, but the opening / closing device (21) uses an opening / closing cylinder in this embodiment.

【0011】ドライベッド(22)は底部に細孔(14)が多数
穿設された床板(23)が設置されており、底部から供給さ
れるドライエアーがベッド(22)内に吹き込まれるように
なっている。
The dry bed (22) is provided with a floor plate (23) having a large number of pores (14) at its bottom, so that dry air supplied from the bottom is blown into the bed (22). Has become.

【0012】(5)は予備発泡粒計量装置で、予備発泡粒
子収納駕篭部(5A)と、前記駕篭部(5A)の直下に設置され
た予備発泡粒計量本体部(5B)とで構成されており、駕篭
部(5A)はドライベッド(22)の底部に、予備発泡粒計量本
体部(5B)の収納部(5C)はドライベッド(22)の天井部にそ
れぞれ接続されている。
(5) is a pre-expanded-particle measuring device, which is composed of a pre-expanded-particle storing basket (5A) and a pre-expanded-particle measuring main body (5B) installed directly below the basket (5A). The cross section (5A) is connected to the bottom of the dry bed (22), and the storage section (5C) of the pre-expanded-particle measuring main body section (5B) is connected to the ceiling of the dry bed (22).

【0013】(6)は制御装置で、予備発泡粒計量本体部
(5B)に接続されて予備発泡粒計量本体部(5B)の計量信
号、圧力計(20)の圧力信号や、予備発泡機本体(2)の側
面に装着され、内部の発泡樹脂の発泡完了を検知する検
知装置(4)からの発泡完了検知信号などを取り込めるよ
うになっている。更に、制御装置(6)は、開閉弁(12)や
後述する投入原料計量装置(8F)に接続されている。(T)
は制御装置(6)内に設置されたタイマである。
(6) is a control device, which is a pre-expanded-particle measuring main body
Connected to (5B) and installed on the side of the pre-foaming machine main body (2) and the measurement signal of the main body (5B) of pre-expanded granules, and the side of the main body of the pre-foaming machine (2) completes the foaming of the foaming resin inside. A bubbling completion detection signal or the like from the detection device (4) for detecting is detected. Further, the control device (6) is connected to the on-off valve (12) and the input material measuring device (8F) described later. (T)
Is a timer installed in the control device (6).

【0014】(8)は加熱筒(7)の天井部に設置された投入
原料供給部で、投入原料供給部(8)は上部に配置された
原料計量部(8G)と、その直下に配置された原料受給部(8
E)とで構成されている。原料計量部(8G)は、投入原料計
量ホッパ(8B)と、投入原料計量ホッパ(8B)を支持し且つ
投入原料計量ホッパ(8B)に供給された原料の計量を行う
投入原料計量装置(8F)と、投入原料計量ホッパ(8B)の底
部に設置され、投入原料計量ホッパ(8B)の底部を開閉す
る底部開閉装置(8C)とで構成されている。投入原料計量
装置(8F)としては例えばロードセルのようなものが使用
される。原料受給部(8E)は予備発泡機本体(2)の天井部
に設置されており、投入原料受け(8A)と、投入原料受け
(8A)の底部に設けられた本体用底部開閉装置(8D)とで構
成されており、原料計量部(8G)にて計量された原料樹脂
ペレット(1)を加熱筒(7)に供給するようになっている。
Reference numeral (8) is a charging raw material supply section installed on the ceiling of the heating cylinder (7), and the charging raw material supply section (8) is arranged directly below the raw material measuring section (8G). Raw material receiving unit (8
E) and. The raw material measuring section (8G) supports the input raw material measuring hopper (8B) and the input raw material measuring hopper (8B), and measures the input raw material supplied to the input raw material measuring hopper (8B) (8F). ) And a bottom opening / closing device (8C) installed at the bottom of the input raw material weighing hopper (8B) for opening and closing the bottom of the input raw material weighing hopper (8B). As the input raw material measuring device (8F), for example, a load cell or the like is used. The raw material receiving part (8E) is installed on the ceiling of the main body of the pre-foaming machine (2), and it receives the input raw material (8A) and the input raw material.
It is composed of a bottom opening / closing device (8D) for the main body provided at the bottom of (8A), and supplies the raw material resin pellets (1) measured by the raw material measuring section (8G) to the heating cylinder (7). It is like this.

【0015】しかして、原料ペレット(1)を投入原料計
量ホッパ(8B)に供給し、投入原料計量装置(8F)にて原料
ペレット(1)の重量の計量を行う。原料ペレット(1)の計
量値は制御装置(6)によって予め設定されている。前ロ
ットの予備発泡が終了し、予備発泡機本体(2)から予備
発泡粒子が排出されると、底部開閉装置(8C)(8D)を開い
て計量が完了した原料樹脂ペレット(1)を予備発泡機本
体(2)に供給する。投入原料受け(8A)は計量された原料
ペレット(1)の単なるガイドで、底部開閉装置(8C)(8D)
は同期して開閉するようになっている。供給された樹脂
ペレット(1)は予備発泡機本体(2)によって予備発泡が行
われるが、この間に次ロットの原料ペレット(1)が計量
されている。予備発泡が終了し、乾燥用ドライベッド(2
2)に予備発泡粒(1)が排出されてしまうと、原料計量部
(8G)と本体用底部開閉装置(8D)を作動させて次ロットの
原料ペレット(1)を予備発泡機本体(2)に供給し、予備発
泡作業を再開する。
Then, the raw material pellets (1) are supplied to the input raw material measuring hopper (8B), and the weight of the raw material pellets (1) is measured by the input raw material measuring device (8F). The measured value of the raw material pellets (1) is preset by the control device (6). When the pre-foaming of the previous lot is completed and the pre-foamed particles are discharged from the main body of the pre-foaming machine (2), the bottom opening / closing devices (8C) (8D) are opened to reserve the raw material resin pellets (1) that have been weighed. Supply to the foamer body (2). The input raw material receiver (8A) is simply a guide for the measured raw material pellets (1), and the bottom opening / closing device (8C) (8D)
Are designed to open and close in synchronization. The supplied resin pellets (1) are pre-foamed by the pre-foaming machine body (2), and the raw material pellets (1) of the next lot are measured during this time. After pre-foaming is completed, dry bed (2
If the pre-expanded granules (1) are discharged into 2), the raw material measuring section
(8G) and the main body bottom opening / closing device (8D) are operated to supply the raw material pellets (1) of the next lot to the prefoaming machine main body (2), and the prefoaming operation is restarted.

【0016】原料樹脂ペレット(1)の計量・投入値は樹
脂の種類、発泡製品の種類その他の条件によって適宜選
定される。
The measured and input values of the raw material resin pellets (1) are appropriately selected depending on the type of resin, the type of foamed product and other conditions.

【0017】予備発泡機本体(2)には、底部から高温蒸
気が供給されており、加熱筒(7)内に設置された回転翼
(9)を回転駆動することにより、投入された原料樹脂ペ
レット(1)を加熱しつつ撹拌する。撹拌作業は固定翼(1
6)と回転翼(9)によって効果的に行われる。この作業に
よって原料樹脂ペレット(1)は次第に発泡してその容積
を増して行く。予備発泡粒子の発泡が進行してその容積
を増して行く。
The pre-foaming machine main body (2) is supplied with high-temperature steam from the bottom and is installed in the heating cylinder (7).
By driving the (9) to rotate, the charged raw material resin pellets (1) are stirred while being heated. Fixed work (1
Effectively done by 6) and rotor (9). By this operation, the raw material resin pellets (1) gradually foam and increase in volume. The foaming of the pre-expanded particles proceeds to increase the volume thereof.

【0018】蒸気の供給時間は、制御装置(6)内に内蔵
されているタイマ(T)にて制御され、前記タイマ(T)がタ
イムアップすると予備発泡がほぼ完了している事にな
る。従って、タイマ(T)のタイムアップで発泡作業の終
了とし、加熱筒(7)の底部側面に設置された開閉装置(2
1)を開き、予備発泡完了粒子をドライベッド(22)内に投
入し、次の予備発泡作業に備える。
The supply time of steam is controlled by a timer (T) built in the control device (6), and when the timer (T) is up, pre-foaming is almost completed. Therefore, when the timer (T) is up, the foaming work is finished, and the opening / closing device (2) installed on the bottom side surface of the heating cylinder (7) is
1) is opened and the pre-expanded particles are put into the dry bed (22) to prepare for the next pre-expansion work.

【0019】発泡作業が終了すると加熱筒(7)の底部側
面に設置された開閉装置(21)を開き、予備発泡完了粒子
をドライベッド(22)内に投入する。ドライベッド(22)に
投入されるとドライベッド(22)に供給されているドライ
エアーにて迅速に乾燥され、予備発泡粒子収納駕篭部(5
A)にその一部が空送される。駕篭部(5A)一杯に充填され
ると底部開閉扉(5D)を開いて前記駕篭部(5A)の直下に設
置された予備発泡粒計量本体部(5B)に予備発泡粒子を投
入する。ここで予備発泡粒子の重量を測定し、この予備
発泡計量値を制御装置(6)に送り、前記駕篭部(5A)で計
量した容積をここで計量した重量で割り、発泡倍率を計
算する。
When the foaming operation is completed, the opening / closing device (21) installed on the bottom side surface of the heating cylinder (7) is opened, and the pre-expanded particles are put into the dry bed (22). When it is put in the dry bed (22), it is quickly dried by the dry air supplied to the dry bed (22), and the pre-expanded particle storage basket (5
Part of it is sent by air to A). When the iron basket (5A) is fully filled, the bottom opening / closing door (5D) is opened, and the pre-expanded particles are put into the pre-expanded-particle measuring main body (5B) installed just below the nozzle basket (5A). Here, the weight of the pre-expanded particles is measured, and this pre-expansion measurement value is sent to the control device (6), and the volume measured by the cross basket portion (5A) is divided by the weight measured here to calculate the expansion ratio.

【0020】予備発泡計量が完了するとドライベッド(2
2)へ空送によって戻され、ドライベッド(22)に残留して
いる予備発泡粒子と共に次工程であるサイロに空送され
る。サイロでは、空送された予備発泡粒が数ロット分貯
蔵熟成されている。一方、予備発泡機計量によって算出
された発泡倍率が設定倍率の許容範囲内であれば、その
まま次の予備発泡作業に入る。しかしながら、許容範囲
外であれば、乖離幅に対応させて投入原料計量装置(8F)
の計量を制御装置(6)にて変更し、次ロットからの倍率
補正を行う。
When the pre-foaming measurement is completed, the dry bed (2
It is returned by air to 2), and is pre-expanded in the dry bed (22) together with the pre-expanded particles, and then air-delivered to the next step, a silo. In the silo, several lots of pre-expanded granules that have been sent by air are stored and aged. On the other hand, if the expansion ratio calculated by the preliminary expansion machine measurement is within the allowable range of the set expansion ratio, the next pre-expansion work is started as it is. However, if it is outside the allowable range, the input raw material metering device (8F) is used according to the deviation width.
Change the weighing in the control device (6) and correct the magnification from the next lot.

【0021】即ち、予備発泡粒計量装置(5)からの予備
発泡計量信号と予め制御装置(6)に入力されている計量
倍率とを比較し、発泡倍率が不足していると判断される
場合には、次ロットの発泡作業において、制御装置(6)
の指令により原料ペレット(1)の計量を前記乖離幅に合
わせて減少させる。これにより、原料ペレット(1)の単
位重量に対する蒸気量(正確には蒸気の持つ熱量)が増
加して原料ペレット(1)の予備発泡が促進され、これに
合わせて発泡倍率が大きくなる。
That is, when it is determined that the foaming ratio is insufficient by comparing the pre-expansion measuring signal from the pre-expansion particle measuring device (5) with the measurement ratio inputted in advance to the control device (6). In the foaming work of the next lot, the control device (6)
In accordance with the command, the amount of raw material pellets (1) is reduced according to the deviation width. As a result, the amount of steam per unit weight of the raw material pellets (1) (to be exact, the amount of heat of the steam) increases, pre-foaming of the raw material pellets (1) is promoted, and the expansion ratio increases accordingly.

【0022】逆に、発泡倍率過多の場合には、次ロット
において制御装置(6)の指令により原料ペレット(1)の計
量を前記乖離幅に併せて増加させ、次ロットの発泡倍率
を下げる。なお、原料ペレット(1)の増減だけで発泡倍
率の調整が困難である場合には、蒸気通流時間のタイマ
制御(蒸気通流時間を長くすることにより原料ペレット
(1)に対する熱量が増加し、予備発泡倍率を増大させる
事になる。)、蒸気通流量制御(開閉弁(12)の弁開度を
大きくし、蒸気の通流量を大きくする事により原料ペレ
ット(1)に対する熱量が増加し、予備発泡倍率を増大さ
せる事になる。)などを併用する事が出来る。さらに予
備発泡の安定性を確保するために検知装置(4)を併用す
る事もできる。その場合、検知装置(4)は加熱筒(7)の側
面に設けられており、この検知装置(4)からの検知信号
によって発泡作業の完了を検知する事になる。
On the other hand, when the expansion ratio is excessive, the control unit (6) in the next lot increases the amount of the raw material pellets (1) in accordance with the deviation width, and the expansion ratio in the next lot is decreased. If it is difficult to adjust the expansion ratio simply by increasing or decreasing the raw material pellets (1), control the steam flow time with a timer (by increasing the steam flow time, the raw material pellets
The amount of heat for (1) increases and the prefoaming ratio increases. ), Steam flow rate control (By increasing the valve opening of the on-off valve (12) and increasing the flow rate of steam, the amount of heat to the raw material pellets (1) increases, and the pre-foaming ratio increases. ) Etc. can be used together. Further, a detection device (4) can be used together to ensure the stability of pre-foaming. In that case, the detection device (4) is provided on the side surface of the heating cylinder (7), and the completion of the foaming work is detected by the detection signal from the detection device (4).

【0023】前述の蒸気通流時間の調整は、作業者が外
部入力装置を使用して乖離幅に合わせて経験的に原料計
量値を変更してもよいが、例えば、タイムテーブルを作
成しておき、前記乖離幅に対応する最適原料重量を予め
制御装置(6)に入力しておき、自動的に原料計量値が修
正されるようにしていてもよい。
The above-mentioned adjustment of the steam flow time may be carried out by an operator using an external input device to empirically change the raw material measured value in accordance with the deviation width. Alternatively, the optimum raw material weight corresponding to the deviation width may be input to the control device (6) in advance, and the raw material measurement value may be automatically corrected.

【0024】[0024]

【発明の効果】本発明は、予備発泡計量装置からの予備
発泡計量信号と設定発泡倍率とを比較して前記予備発泡
計量値が設定値の許容値を越えている場合には、許容値
からの乖離幅に対応させて原料計量値を制御するように
なっているので、その乖離幅に対応させて原料計量値を
調節する事が出来、これにより原料ペレット単位当たり
の蒸気量を調節して倍率補正を行う事ができるものであ
り、発泡倍率の管理を非常に厳密且つ正確に行う事がで
き、最終発泡成形品の品質向上をはかる事ができるとい
う利点がある。
The present invention compares the pre-foaming metering signal from the pre-foaming metering device with the set foaming ratio, and when the pre-foaming measured value exceeds the allowable value of the set value, the pre-foaming measured value is changed from the allowable value. Since the raw material measurement value is controlled in accordance with the deviation width of the raw material, the raw material measurement value can be adjusted in accordance with the deviation width, thereby adjusting the vapor amount per raw material pellet unit. Since the magnification can be corrected, the foaming ratio can be controlled very strictly and accurately, and the quality of the final foamed molded product can be improved.

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

【図1】本発明にかかる予備発泡装置の全体のフロー図
FIG. 1 is an overall flow chart of a pre-foaming device according to the present invention.

【図2】本発明の予備発泡装置の制御フローチャートFIG. 2 is a control flowchart of the pre-foaming device of the present invention.

【符号の説明】[Explanation of symbols]

(1)…発泡樹脂ペレット (2)…予備発泡機本体 (4)…検知装置 (5)…予備発泡粒計量装
置 (6)…制御装置 (8C)…底部開閉装置 (8E)…投入原料計量ホッパ (8F)…投入原料計量装置 (11)…蒸気配管 (12)…開閉弁
(1)… Expanded resin pellets (2)… Preliminary foaming machine main body (4)… Detection device (5)… Preliminary foamed particle metering device (6)… Control device (8C)… Bottom opening / closing device (8E)… Feed material metering Hopper (8F) ... Input material metering device (11) ... Steam pipe (12) ... Open / close valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 発泡樹脂ペレットを予備発泡させ
る予備発泡機本体と、予備発泡機本体の投入原料受給部
上に設けられた投入原料計量ホッパと、投入原料計量ホ
ッパに付設された投入原料計量装置と、投入原料計量ホ
ッパの底部に設けられ、投入原料計量ホッパの底部を開
閉する底部開閉装置と、予備発泡機本体から送出された
予備発泡粒子の計量を行う予備発泡粒計量装置と、予備
発泡粒計量装置からの予備発泡計量信号と設定発泡倍率
とを比較して前記計量値が設定値の許容値を越えている
場合には、許容値からの乖離幅に対応させて前記投入原
料計量装置により投入原料の計量を増減する制御装置と
で構成されたことを特徴とする予備発泡装置。
1. A prefoaming machine main body for prefoaming expanded resin pellets, a charging raw material measuring hopper provided on a charging raw material receiving section of the preliminary foaming machine main body, and a charging raw material measuring device attached to the charging raw material measuring hopper. And a bottom opening / closing device provided at the bottom of the input material measuring hopper for opening and closing the bottom of the input material measuring hopper, a pre-expanded particle measuring device for measuring the pre-expanded particles sent from the pre-expanding machine main body, and pre-expanding When the pre-foaming measurement signal from the particle measuring device is compared with the set expansion ratio and the measured value exceeds the allowable value of the set value, the input raw material measuring device is made to correspond to the deviation from the allowable value. And a control device for increasing or decreasing the amount of raw material to be charged by the pre-foaming device.
JP2625793A 1993-01-20 1993-01-20 Pre-expander Pending JPH06220240A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2625793A JPH06220240A (en) 1993-01-20 1993-01-20 Pre-expander

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2625793A JPH06220240A (en) 1993-01-20 1993-01-20 Pre-expander

Publications (1)

Publication Number Publication Date
JPH06220240A true JPH06220240A (en) 1994-08-09

Family

ID=12188212

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2625793A Pending JPH06220240A (en) 1993-01-20 1993-01-20 Pre-expander

Country Status (1)

Country Link
JP (1) JPH06220240A (en)

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