JPH08230020A - Extruder output controlling method of continuous extruder and controlling device thereof - Google Patents

Extruder output controlling method of continuous extruder and controlling device thereof

Info

Publication number
JPH08230020A
JPH08230020A JP7037238A JP3723895A JPH08230020A JP H08230020 A JPH08230020 A JP H08230020A JP 7037238 A JP7037238 A JP 7037238A JP 3723895 A JP3723895 A JP 3723895A JP H08230020 A JPH08230020 A JP H08230020A
Authority
JP
Japan
Prior art keywords
extruder
polymer material
amount
inlet
continuous
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.)
Withdrawn
Application number
JP7037238A
Other languages
Japanese (ja)
Inventor
Katsuhiko Nakai
勝彦 中井
Nobutsugu Tada
信嗣 多田
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP7037238A priority Critical patent/JPH08230020A/en
Publication of JPH08230020A publication Critical patent/JPH08230020A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/39Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/385Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92085Velocity
    • B29C2948/92095Angular velocity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92209Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • B29C2948/9238Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/9239Screw or gear
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • B29C2948/92409Die; Nozzle zone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92542Energy, power, electric current or voltage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92828Raw material handling or dosing, e.g. active hopper or feeding device
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92885Screw or gear
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92952Drive section, e.g. gearbox, motor or drive fluids

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE: To stably extrude polymeric material from an extruder to be connected with a kneader. CONSTITUTION: In the running of an extruder 3, which continuously extrudes polymeric material fed through a chute tube 2 thereto through the rotation of a screw 4, the sojouring state of the polymeric material at the inlet of the extruder 3 is monitored with a monitor camera 8. The image of the monitor camera 8 is inputted in a computer 11 so as to be picture-processed in order to be converted into the stay amount, which indicates the staying state. By inputting the above-mentioned stay amount and the measured values sent from the rotational frequency measuring apparatus 13, the temperature sensor of material 12, and the wattmeter of a motor 14 in a controlling device 15 and the outputting the number-of-rotation setting device 16 of the screw and the driving motor 17 of a material feeder, the number of rotation of the screw and the feeding of polymeric material at the inlet of the extruder are controlled.

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、合成樹脂等の高分子材
料を連続式の混練機と押出機を用いて押出す工程におけ
る、連続式押出機の押出量の制御方法及びその制御装置
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling an extrusion amount of a continuous extruder and a control apparatus therefor in a process of extruding a polymer material such as a synthetic resin using a continuous kneader and an extruder. It is a thing.

【0002】[0002]

【従来の技術】連続式の混練機と押出機を用いた高分子
材料の押出し工程においては、混練機出口と押出機入口
を連結するシュート管を設置して混練機で溶融混練され
た高分子材料を押出機に供給する。押出機では押出機内
のスクリューを電動機によって回転させながら、スクリ
ューに沿って押出している。
2. Description of the Related Art In a process of extruding a polymer material using a continuous kneading machine and an extruder, a chute tube connecting the kneading machine outlet and the extruder inlet is installed to melt and knead the polymer. Feed material to extruder. In the extruder, the screw inside the extruder is rotated by an electric motor and is extruded along the screw.

【0003】特開平6−54573号では、混練機の高
分子材料の温度と混練機電動機の負荷状態から、混練機
の高分子材料の供給量と押出量を制御する方法を開示し
ているが、混練機1台の制御方法を開示したものであ
り、混練機と押出機が連結された連続押出工程の運転制
御方法について開示したものはない。
Japanese Unexamined Patent Publication (Kokai) No. 6-54573 discloses a method of controlling the supply amount and the extrusion amount of the polymer material of the kneader based on the temperature of the polymer material of the kneader and the load state of the motor of the kneader. However, it discloses a control method for one kneader, and does not disclose an operation control method for a continuous extrusion process in which the kneader and the extruder are connected.

【0004】[0004]

【発明が解決しようとする課題】混練機と押出機を連結
し、連続して運転を行うには、押出機の高分子材料入口
の高分子材料滞留量の制御が課題である。例えば、前記
高分子材料滞留量は、高分子材料のグレード切替や、押
出機ダイスの一次側に設置されるスクリーンの詰り状況
など、通常運転時における条件変更によって変化する。
滞留量が多すぎると高分子材料が入口で冷え、冷えた高
分子材料が押出され押出機内の高分子材料圧力が上昇
し、逆に少な過ぎるとサージングが発生し、いずれの場
合も、押出し製品の品質に悪影響する。すなわち、滞留
量には多からず少なからずの適正範囲が存在する。この
適正範囲内で連続的に押出すには、押出機入口の高分子
材料の滞留状態を見ながら、押出機のスクリュー回転数
を変更したり、押出機への高分子材料供給量を変更した
りする必要があるが、この監視操作は常時行わなければ
ならず、その作業量は極めて大きいものがある。
In order to connect the kneading machine and the extruder and continuously operate them, the control of the retention amount of the polymer material at the polymer material inlet of the extruder is a problem. For example, the retention amount of the polymer material changes depending on the condition change during the normal operation such as the grade change of the polymer material and the clogging of the screen installed on the primary side of the extruder die.
If the retention amount is too large, the polymer material will cool at the inlet, the cooled polymer material will be extruded and the pressure of the polymer material in the extruder will rise, and conversely, if it is too small, surging will occur. Adversely affect the quality of. That is, there is a proper range in which the amount of stay is not a little large and is not small. To continuously extrude within this proper range, change the screw speed of the extruder or change the amount of polymer material supplied to the extruder while observing the retention state of the polymer material at the extruder inlet. However, this monitoring operation must be performed at all times, and the amount of work required is extremely large.

【0005】しかしながら、混練機と連結した押出機の
運転において、押出機入口の高分子材料の滞留状態を定
量化し、混練機と押出機との連続自動運転方法に関して
記載した先行技術を本願出願人は、見出せなかった。
However, in the operation of the extruder connected to the kneading machine, the applicant of the present invention described the prior art which quantifies the retention state of the polymer material at the extruder inlet and describes the continuous automatic operation method of the kneading machine and the extruder. Could not be found.

【0006】そこで、本発明の目的は、上述の点に鑑み
て、高分子材料の押出しをさらに好適に自動制御できる
連続式押出機の押出量制御方法およびその制御装置を提
供することにある。
Therefore, in view of the above points, an object of the present invention is to provide a method for controlling an extrusion amount of a continuous extruder and a control apparatus therefor capable of more preferably automatically controlling extrusion of a polymer material.

【0007】[0007]

【課題を解決するための手段】このような目的を達成す
るために、請求項1の発明は、混練機の高分子材料出口
と押出機の高分子材料入口とをシュート管で連結し、高
分子材料を連続的に混練、押出す工程において、混練機
の高分子材料出口と押出機の高分子材料入口との間の高
分子材料の滞留量を計測し、当該計測の結果に応じて、
押出機スクリューの回転数およびまたは、前記混練機か
ら前記押出機への高分子材料の供給量を制御することを
特徴とする。
In order to achieve such an object, the invention of claim 1 connects a polymer material outlet of a kneading machine and a polymer material inlet of an extruder with a chute pipe, In the step of continuously kneading and extruding the molecular material, the residence amount of the polymer material between the polymer material outlet of the kneader and the polymer material inlet of the extruder is measured, and according to the result of the measurement,
The number of revolutions of the extruder screw and / or the supply amount of the polymer material from the kneading machine to the extruder is controlled.

【0008】請求項2の発明は、請求項1の発明に加え
て、前記押出機の高分子材料入口に前記高分子材料を撮
影するためのモニターカメラを設置し、該モニターカメ
ラから得られた映像を画像処理装置に入力し、該画像処
理装置の画像処理により前記高分子材料の滞留量を計測
することを特徴とする。
According to a second aspect of the present invention, in addition to the first aspect of the invention, a monitor camera for photographing the polymer material is installed at the polymer material inlet of the extruder, and the monitor camera is obtained from the monitor camera. It is characterized in that an image is input to an image processing apparatus and the amount of retention of the polymer material is measured by image processing of the image processing apparatus.

【0009】請求項3の発明は、混練機と連続式押出機
との間をシュート管で連結し、前記混練機から前記連続
式押出機へ供給される高分子材料の押出量を制御する連
続式押出器の制御装置において、混練機の高分子材料出
口と押出機の高分子材料入口との間の高分子材料の滞留
量を前記押出量を制御するための運転制御量の1つとし
て計測する計測手段と、当該計測された滞留量および他
の運転制御量に基づき前記押出量を制御する制御手段と
を具えたことを特徴とする。
According to a third aspect of the present invention, a kneading machine and a continuous extruder are connected by a chute pipe, and a continuous amount of the polymer material supplied from the kneading machine to the continuous extruder is controlled. In a control device of a extruder, a retention amount of a polymer material between a polymer material outlet of a kneader and a polymer material inlet of the extruder is measured as one of operation control amounts for controlling the extrusion amount. And a control means for controlling the extrusion amount based on the measured staying amount and other operation control amount.

【0010】請求項4の発明は、請求項3の発明に加え
て、前記押出機の高分子材料入口に設置され、前記高分
子材料を撮影するための撮影手段と、該撮影手段から得
られた映像を画像処理して前記高分子材料の滞留量を取
得する画像処理手段とを前記計測手段が有することを特
徴とする。
According to a fourth aspect of the present invention, in addition to the third aspect of the present invention, a photographing means for photographing the polymeric material is installed at the polymeric material inlet of the extruder, and is obtained from the photographing means. The measuring means has an image processing means for performing image processing on the captured image to obtain the retention amount of the polymer material.

【0011】[0011]

【作用】本願発明者は押出機の入口で発生する高分子材
料の滞留量が品質に影響することを発見し、その知見に
基づき請求項1、3の発明では、高分子材料の連続式押
出機前の滞留量を計測し、その計測結果に応じて、押出
機のスクリュー回転数およびまたは、高分子材料の供給
量を制御することにより上記滞留量の影響を除去する。
The present inventor has found that the amount of residence of the polymeric material generated at the inlet of the extruder affects the quality, and based on this finding, the invention of claims 1 and 3 provides continuous extrusion of the polymeric material. The retention amount before the machine is measured, and the screw rotation speed of the extruder and / or the supply amount of the polymer material is controlled according to the measurement result to remove the influence of the retention amount.

【0012】請求項2、4の発明では、高分子材料を撮
影し、その撮影結果から滞留量を取得する。
According to the second and fourth aspects of the invention, the polymer material is photographed, and the staying amount is acquired from the photographed result.

【0013】[0013]

【実施例】以下、図面を参照して本発明の実施例を詳細
に説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0014】本発明を適用した制御システムの一例を図
1に示す。図1において、1は連続式混練機(混練機と
略す)、2は混練機1の出口と押出機3の入口とを連結
するシュート管である。なお、本実施例で言うシュート
管とは、混練機1の出口と押出機3の入り口を連結する
縦方向の鋼製の管である。3は押出機、4は回転により
高分子材料を押し出すためのスクリュー、5はスクリュ
ー4を回転させる電動機である。6は高分子材料を供給
する高分子材料供給機、7は押出機の高分子材料入口を
照らす照明である。8は押出機3の入口の高分子材料滞
留状態を写し出すモニターカメラで、9のモニターでそ
の映像が見られる。10は画像処理ボードで、9のモニ
ターの端子から画像データ(イメージ)が入力される。
11はコンピュータで、入力された画像データの処理装
置として機能し、撮像された画像データを滞留量を表す
運転制御量に変換し、その運転制御量を出力する。運転
制御量とは、押出機3を含む生産設備の機器を制御する
ために用いる各種パラメータの値を総称する用語であ
り、本実施例では、運転制御量の1つとして高分子材料
の滞留量を用意する。滞留量は画像処理結果から得られ
る定量的数値であって、押出機入口の高分子材料滞留
量、押出機入口の高分子材料ピーク高さ、高分子材料の
面積占有率(高分子材料の面積/押出機入口面積百分
率)で表される。
FIG. 1 shows an example of a control system to which the present invention is applied. In FIG. 1, 1 is a continuous kneader (abbreviated as a kneader), and 2 is a chute tube that connects the outlet of the kneader 1 and the inlet of the extruder 3. The chute tube referred to in the present embodiment is a vertical steel tube that connects the outlet of the kneading machine 1 and the inlet of the extruder 3. Reference numeral 3 is an extruder, 4 is a screw for pushing out a polymer material by rotation, and 5 is an electric motor for rotating the screw 4. Reference numeral 6 is a polymer material supply machine for supplying the polymer material, and 7 is an illumination for illuminating the polymer material inlet of the extruder. Reference numeral 8 is a monitor camera for showing the state of retention of the polymer material at the entrance of the extruder 3, and the image can be seen on the monitor of 9. An image processing board 10 receives image data from the monitor terminal 9.
Reference numeral 11 denotes a computer, which functions as a processing device for the input image data, converts the captured image data into an operation control amount representing a stay amount, and outputs the operation control amount. The operation control amount is a general term for the values of various parameters used to control the equipment of the production facility including the extruder 3. In this embodiment, the amount of retention of the polymer material is one of the operation control amounts. To prepare. The retention amount is a quantitative value obtained from the image processing results, and the retention amount of the polymer material at the extruder inlet, the peak height of the polymer material at the extruder inlet, the area occupancy rate of the polymer material (area of the polymer material / Percentage of extruder inlet area).

【0015】12は押出機内の高分子材料温度(他の運
転制御量の1つ)を測定する為の温度検出器、13はス
クリューの回転数測定器、14は電動機5の電力計であ
る。これら機器の計測データは画像処理により得られた
高分子材料の滞留量と共に制御装置15に入力される。
制御装置15では、これらの入力データから図2のフロ
ーチャートに従って制御内容を決定する。押出機3のス
クリュー4の回転数設定器16は制御装置15から指示
された回転数を電動機4の回転数として設定する。さら
に供給器駆動、モータ17へもその回転数の指示が送ら
れる。
Reference numeral 12 is a temperature detector for measuring the temperature of the polymer material in the extruder (one of other operation control amounts), 13 is a screw rotation speed measuring device, and 14 is a power meter of the electric motor 5. The measurement data of these devices are input to the control device 15 together with the retention amount of the polymer material obtained by the image processing.
The control device 15 determines the control content from these input data according to the flowchart of FIG. The rotation speed setting device 16 of the screw 4 of the extruder 3 sets the rotation speed instructed by the control device 15 as the rotation speed of the electric motor 4. Further, an instruction of the number of rotations is sent also to the drive of the feeder and the motor 17.

【0016】このようなシステム構成において、押出機
3の高分子材料入口に設置したモニターカメラ8で得ら
れる高分子材料の滞留状態の映像が、コンピュータ11
に入力され画像処理され、滞留量を表す各種の運転制御
量の形態で定量化される。この高分子材料滞留量と、押
出機3のスクリュー4の回転数(高分子材料の押出量に
対応)、押出機内3の高分子材料温度、電動機5の負荷
状態とを制御装置15に入力する。制御装置15では設
定した制御ルールに従って、押出機3のスクリュー回転
数設定器16および高分子材料供給器駆動モーター17
にそれぞれ回転数を出力する。
In such a system configuration, an image of the retention state of the polymer material obtained by the monitor camera 8 installed at the polymer material inlet of the extruder 3 is displayed on the computer 11.
Is image-processed and quantified in the form of various operation control amounts that represent the stay amount. This residence amount of the polymer material, the rotation speed of the screw 4 of the extruder 3 (corresponding to the extrusion amount of the polymer material), the temperature of the polymer material in the extruder 3, and the load state of the electric motor 5 are input to the control device 15. . In the control device 15, according to the set control rule, the screw rotation speed setting device 16 of the extruder 3 and the polymer material feeder drive motor 17
The rotation speed is output to each.

【0017】本実施例では図2に示す制御シーケンスに
従って、スクリュー4の回転数および高分子材料の供給
量(供給器駆動モーター17の回転数)を制御する。す
なわち、高分子材料温度が高い時は、スクリュー4の回
転数をダウンさせるとともに、高分子材料供給量を減じ
る(図2のステップS1〜S7)。さらに高分子材料の
滞留量が適正範囲に入るよう押出機スクリューの回転数
を制御する(図2のステップS6〜S13,S14)。
更には、押出機3の電動機5の負荷状態が高い時はスク
リュー4の回転数をダウンさせるとともに、高分子材料
供給量を減じる(図2のステップS3〜S5)という制
御が自動的に行われる。
In this embodiment, the rotation speed of the screw 4 and the supply amount of the polymer material (rotation speed of the feeder drive motor 17) are controlled according to the control sequence shown in FIG. That is, when the polymer material temperature is high, the rotation speed of the screw 4 is reduced and the supply amount of the polymer material is reduced (steps S1 to S7 in FIG. 2). Further, the rotation speed of the extruder screw is controlled so that the retention amount of the polymer material falls within an appropriate range (steps S6 to S13 and S14 in FIG. 2).
Furthermore, when the load condition of the electric motor 5 of the extruder 3 is high, the rotation speed of the screw 4 is reduced and the supply amount of the polymer material is reduced (steps S3 to S5 in FIG. 2), which is automatically controlled. .

【0018】次に、本発明に係わる滞留量の計測方法に
ついて説明する。押出機入口の高分子材料撮影をする
と、高分子材料部分が背景より明るく、画像の輝度にそ
の特徴が現われる。そこで、コンピュータ11では入力
した1画面分の画像データの中で輝度が一定の範囲にあ
る画像データで閉区画を構成する領域を輪郭線検出手法
等の周知の画像処理技術を用いて抽出する。抽出された
領域が高分子材料の画像部分となるので、領域の高さに
一定係数を乗じることにより上述の高分子材料のピーク
高さを取得する。また上記領域の画素数を数えることに
より面積を取得し、この面積から高分子材料の面積占有
率を計算する。
Next, the method of measuring the staying amount according to the present invention will be described. When the polymer material is photographed at the entrance of the extruder, the polymer material portion is brighter than the background, and the characteristic appears in the brightness of the image. Therefore, the computer 11 extracts a region forming a closed section by the image data whose brightness is in a constant range from the input image data for one screen by using a well-known image processing technique such as a contour line detection method. Since the extracted region becomes an image portion of the polymer material, the peak height of the polymer material is obtained by multiplying the height of the region by a constant coefficient. Further, the area is acquired by counting the number of pixels in the above area, and the area occupancy of the polymer material is calculated from this area.

【0019】[0019]

【発明の効果】請求項1、3の発明では、高分子材料の
連続式押出機前の滞留量を計測し、その計測結果に応じ
て、押出機スクリューの回転数およびまたは、高分子材
料の滞留量を制御することにより上記滞留量の影響を除
去する。これにより高品質の高分子材料を提供できる。
According to the first and third aspects of the present invention, the retention amount of the polymer material before the continuous extruder is measured, and the rotation speed of the extruder screw and / or the polymer material is measured according to the measurement result. By controlling the retention amount, the influence of the retention amount is removed. Thereby, a high quality polymer material can be provided.

【0020】請求項2、4の発明では、高分子材料を撮
影し、その撮影結果から滞留量を取得する。これにより
従来、行われなかった滞留量の計測が可能となる。
According to the second and fourth aspects of the invention, the polymer material is photographed, and the staying amount is obtained from the photographed result. As a result, it becomes possible to measure the retention amount, which has not been performed conventionally.

【0021】さらに、これらの発明により、オペレータ
が行っていた押出機運転の監視操作および運転操作が好
適に自動化でき、従来、これらの作業に多くの工数を必
要とするという問題があったが、これが解消でき、押出
機の監視操作および運転操作の作業工数を大幅に削減す
る事ができる。又、高分子材料温度や電動機の負荷状態
を基準値内、許容値内に調整して運転できるので、通常
運転時の条件変更等においても常に押出機の運転を安定
に維持できる。
Further, according to these inventions, the monitoring operation and the operation operation of the extruder operation performed by the operator can be favorably automated, and conventionally there has been a problem that a lot of man-hours are required for these operations. This can be solved, and the man-hours for monitoring and operating the extruder can be significantly reduced. Further, since the polymer material temperature and the load condition of the electric motor can be adjusted to operate within the reference value and the allowable value, the extruder operation can always be stably maintained even when the conditions are changed during normal operation.

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

【図1】本発明実施例のシステム構成を示すブロック図
である。
FIG. 1 is a block diagram showing a system configuration of an embodiment of the present invention.

【図2】本発明の制御ルール例を示すフローチャートで
ある。
FIG. 2 is a flowchart showing an example of control rules of the present invention.

【符号の説明】[Explanation of symbols]

1 (連続式)混練機 2 シュート管 3 (連続式)押出機 4 スクリュー 5 電動機 6 高分子材料供給機 7 照明 8 モニターカメラ 9 モニター 10 画像処理ボード 11 コンピュータ 12 温度検出器 13 回転数測定器 14 電力計 15 制御装置 16 回転数設定器 17 供給器駆動モータ 1 (Continuous type) Kneader 2 Chute tube 3 (Continuous type) Extruder 4 Screw 5 Electric motor 6 Polymer material feeder 7 Illumination 8 Monitor camera 9 Monitor 10 Image processing board 11 Computer 12 Temperature detector 13 Rotation speed meter 14 Power meter 15 Control device 16 Rotation speed setting device 17 Feeder drive motor

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 混練機の高分子材料出口と押出機の高分
子材料入口とをシュート管で連結し、高分子材料を連続
的に混練、押出す工程において、 混練機の高分子材料出口と押出機の高分子材料入口との
間の高分子材料の滞留量を計測し、 当該計測の結果に応じて、押出機スクリューの回転数お
よびまたは、前記混練機から前記押出機への高分子材料
の供給量を制御することを特徴とする連続式押出機の押
出量制御方法。
1. In the step of continuously kneading and extruding a polymer material, the polymer material outlet of the kneader and the polymer material inlet of the extruder are connected by a chute tube, and the polymer material outlet of the kneader is used. The retention amount of the polymer material between the extruder and the polymer material inlet is measured, and the rotation speed of the extruder screw and / or the polymer material from the kneader to the extruder is measured according to the measurement result. A method for controlling the extrusion rate of a continuous extruder, which comprises controlling the supply rate of
【請求項2】 前記押出機の高分子材料入口に前記高分
子材料を撮影するためのモニターカメラを設置し、該モ
ニターカメラから得られた映像を画像処理装置に入力
し、該画像処理装置の画像処理により前記高分子材料の
滞留量を計測することを特徴とする請求項1に記載の連
続式押出機の押出量制御方法。
2. A monitor camera for photographing the polymer material is installed at an inlet of the polymer material of the extruder, and an image obtained from the monitor camera is input to an image processing apparatus, and the image processing apparatus is operated. The method for controlling the extrusion amount of a continuous extruder according to claim 1, wherein the retention amount of the polymer material is measured by image processing.
【請求項3】 混練機と連続式押出機との間をシュート
管で連結し、前記混練機から前記連続式押出機へ供給さ
れる高分子材料の押出量を制御する連続式押出器の制御
装置において、 混練機の高分子材料出口と押出機の高分子材料入口との
間の高分子材料の滞留量を前記押出量を制御するための
運転制御量の1つとして計測する計測手段と、 当該計測された滞留量および他の運転制御量に基づき前
記押出量を制御する制御手段とを具えたことを特徴とす
る連続式押出機の制御装置。
3. A continuous extruder control for connecting a kneading machine and a continuous extruder with a chute tube to control an extrusion rate of a polymer material supplied from the kneading machine to the continuous extruder. In the apparatus, measuring means for measuring the amount of retention of the polymer material between the polymer material outlet of the kneader and the polymer material inlet of the extruder as one of the operation control amounts for controlling the extrusion amount, A controller for a continuous extruder, comprising: a control unit that controls the extrusion amount based on the measured staying amount and another operation control amount.
【請求項4】 前記押出機の高分子材料入口に設置さ
れ、前記高分子材料を撮影するための撮影手段と、該撮
影手段から得られた映像を画像処理して前記高分子材料
の滞留量を取得する画像処理手段とを前記計測手段が有
することを特徴とする請求項3に記載の連続式押出機の
制御装置。
4. A photographing means installed at the inlet of the polymeric material of the extruder, for photographing the polymeric material, and an image obtained from the photographing means is image-processed to retain the polymeric material. The control device for a continuous extruder according to claim 3, wherein the measuring means has an image processing means for acquiring the.
JP7037238A 1995-02-24 1995-02-24 Extruder output controlling method of continuous extruder and controlling device thereof Withdrawn JPH08230020A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7037238A JPH08230020A (en) 1995-02-24 1995-02-24 Extruder output controlling method of continuous extruder and controlling device thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7037238A JPH08230020A (en) 1995-02-24 1995-02-24 Extruder output controlling method of continuous extruder and controlling device thereof

Publications (1)

Publication Number Publication Date
JPH08230020A true JPH08230020A (en) 1996-09-10

Family

ID=12492041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7037238A Withdrawn JPH08230020A (en) 1995-02-24 1995-02-24 Extruder output controlling method of continuous extruder and controlling device thereof

Country Status (1)

Country Link
JP (1) JPH08230020A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014008760A (en) * 2012-07-03 2014-01-20 Japan Steel Works Ltd:The Method of resin raw material discharge and recycle upon raw material oversupply to extruder and discharge and recycle apparatus
WO2016024435A1 (en) * 2014-08-11 2016-02-18 株式会社神戸製鋼所 Kneader internal inspection device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014008760A (en) * 2012-07-03 2014-01-20 Japan Steel Works Ltd:The Method of resin raw material discharge and recycle upon raw material oversupply to extruder and discharge and recycle apparatus
WO2016024435A1 (en) * 2014-08-11 2016-02-18 株式会社神戸製鋼所 Kneader internal inspection device
JP2016037028A (en) * 2014-08-11 2016-03-22 株式会社神戸製鋼所 Internal part inspection device for kneader
CN106659996A (en) * 2014-08-11 2017-05-10 株式会社神户制钢所 Kneader internal inspection device
US10322527B2 (en) 2014-08-11 2019-06-18 Kobe Steel, Ltd. Kneader internal inspection device

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