JPH0684037B2 - Extruder control method - Google Patents

Extruder control method

Info

Publication number
JPH0684037B2
JPH0684037B2 JP61175738A JP17573886A JPH0684037B2 JP H0684037 B2 JPH0684037 B2 JP H0684037B2 JP 61175738 A JP61175738 A JP 61175738A JP 17573886 A JP17573886 A JP 17573886A JP H0684037 B2 JPH0684037 B2 JP H0684037B2
Authority
JP
Japan
Prior art keywords
pressure
temperature
barrel
extruder
groove
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP61175738A
Other languages
Japanese (ja)
Other versions
JPS6331730A (en
Inventor
禎二 清水
勝啓 井口
憲司 野沢
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine 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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP61175738A priority Critical patent/JPH0684037B2/en
Publication of JPS6331730A publication Critical patent/JPS6331730A/en
Publication of JPH0684037B2 publication Critical patent/JPH0684037B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • B29C48/92Measuring, 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
    • 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
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/64Screws with two or more threads
    • B29C48/66Barrier threads, i.e. comprising primary and secondary threads whereby the secondary thread provides clearance to the barrel for material movement
    • 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
    • B29C2948/92019Pressure
    • 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
    • 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
    • B29C2948/92495Treatment of equipment, e.g. purging, cleaning, lubricating or filter exchange
    • 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
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • 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
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing
    • 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
    • B29C2948/9299Treatment of equipment, e.g. purging, cleaning, lubricating or filter exchange
    • 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
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、溶融プラスチック材料を成形する押出成形
機、射出成形機および吹込成形機(以下これらを総称し
て押出機等という)の制御方法に係り、特に良品質の成
形を行うため、材料の押出し溶融を行うスクリュに主フ
ライトとバリアフライト(副フライト)とを設けて、バ
レル内面との間にソリッド溝とメルト溝とを形成したバ
リア形のスクリュを使用する押出機等の制御方法に関す
る。
Description: TECHNICAL FIELD The present invention relates to a method for controlling an extrusion molding machine, an injection molding machine and a blow molding machine (hereinafter collectively referred to as an extruder etc.) for molding a molten plastic material. In particular, in order to perform high-quality molding, a barrier for forming a solid groove and a melt groove between the inner surface of the barrel and a main flight and a barrier flight (sub-flight) are provided in the screw for extruding and melting the material. The present invention relates to a control method for an extruder or the like using a screw of a rectangular shape.

〔従来の技術〕[Conventional technology]

押出機等の制御の目標は、適切に設計された押出スクリ
ュを用いて、バレル温度を適当に設定し、所定の押出量
の溶融材料を均一にかつ安定して次工程へ供給すること
である。このために、初期においてはスクリュヘッド部
の溶融材料の圧力ならびに温度の定値制御が行われた。
しかし、これのみの制御では限界があり、時には溶融の
不安定さを助長する逆効果があることが判明した。すな
わち、これはソリッドベッドのブレークアップという現
象によるもので、一般に固形状の未溶融物の解体という
意味であるが、スクリュの溝内で固形材料が供給部、圧
縮部、計量部を経て次第に溶融材料に変って行く溶融工
程の途中で発生する溶融の不安定状態を示すものであ
る。このような現象を回避するため、スクリュの最長の
部分を占める溶融促進部に、固形成分と溶融成分を分離
する棚としてバリアフライトを新しく設けたのがバリア
形のスクリュである。この新しいバリア形のスクリュの
改善効果は見るべきものがあったが、さらにこの効果を
拡大したものは次のような診断制御システムである。
The goal of control of extruders, etc., is to set the barrel temperature appropriately by using an appropriately designed extrusion screw, and to uniformly and stably supply the molten material of a predetermined extrusion amount to the next step. . Therefore, in the initial stage, constant value control of the pressure and temperature of the molten material in the screw head portion was performed.
However, it has been found that this control alone has a limit and sometimes has an adverse effect of promoting instability of melting. In other words, this is due to the phenomenon of breakup of the solid bed, which generally means the dismantling of solid unmelted material, but in the groove of the screw, the solid material gradually melts through the supply section, compression section, and measurement section. This shows an unstable state of melting that occurs during the melting process in which the material changes. In order to avoid such a phenomenon, a barrier flight is newly provided with a barrier flight as a shelf for separating a solid component and a molten component in the melting promoting portion which occupies the longest portion of the screw. The improvement effect of this new barrier type screw was remarkable, but what further expanded this effect is the following diagnostic control system.

すなわち、本出願人は、先に前記ソリッドベッドのブレ
ークアップを含めて、その他の不安定に対し、溶融促進
部に設けた圧力センサと、スクリュの駆動端に設けた位
置センサからの信号によって圧力波形を検出し、所定の
基準データと比較および対照させて、その相関性の統計
量を算出して、その正常または異常の判別を行い、異常
の際にさらに追試を行うという溶融工程の自動診断制御
システムを提案し、特願昭60−81369号(特公平2−580
92号)として特許出願を行った。
That is, the applicant of the present invention has previously responded to other instabilities including the break-up of the solid bed by using a signal from the pressure sensor provided in the melting promoting portion and the position sensor provided at the driving end of the screw. Automatic diagnosis of melting process that detects waveforms, compares and compares them with predetermined reference data, calculates the statistics of their correlation, determines normality or abnormality, and performs additional test in case of abnormality Proposed a control system, Japanese Patent Application No. 60-81369 (Japanese Patent Publication No. 2-580)
No. 92) filed a patent application.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、前記自動診断制御システムにおいては、
異常の判断に対して、肝要なバレル温度の設定について
の制御が明確になっていない。従来、メルト溝内圧力の
値は、一義的に決められず、スクリュの構造、材料の特
性およびスクリュの回転速度等によって異なるものであ
り、制御の目安としては考えられないものであった。し
かし、その後前記自動診断制御システムの診断結果では
前述の諸元が一度選択されると、正常溶融工程において
は前記メルト溝内圧力はほとんど一定であるという特徴
が明確になってきた。また、前記診断結果によれば、第
8図に示すスクリュ溝内の溶融状態を示すモデル図が考
えられる。第8図(a),(b)および(c)におい
て、参照符号10はバレル、12はスクリュ、60は主フライ
ト、62はバリアフライト、56はソリッド溝、58はメルト
溝をそれぞれ示す。第8図(a)は溶融不足状態で、メ
ルト成分がメルト溝58に充満していず、バレル設定温度
を上げる必要を感じるが、押出量を増加するためにメル
ト溝内圧力をむやみに上げるように操作すると、第8図
(c)のような溶融過剰状態を生じ、ソリッドベッドの
ブレイクアップを発生して逆効果を示す。定性的には、
メルト成分とソリッド成分がバリアフライト62によって
明確に分離されているという条件が満たされる範囲内に
おいて、メルト溝内圧力は高い程良い結果を得ることが
できる。これが第8図(b)の適性溶融状態である。こ
の判断に苦しむ微少な範囲は、前記自動診断制御システ
ムの圧力波形が正常と判断される状態であることも明確
になった。
However, in the automatic diagnostic control system,
The control for setting the barrel temperature, which is essential for determining abnormalities, is not clear. Conventionally, the value of the pressure in the melt groove is not uniquely determined, and varies depending on the screw structure, material characteristics, screw rotation speed, and the like, and cannot be considered as a guide for control. However, after that, according to the diagnosis result of the automatic diagnosis control system, once the above-mentioned specifications are selected, it has become clear that the pressure in the melt groove is almost constant in the normal melting process. Further, according to the diagnosis result, a model diagram showing a molten state in the screw groove shown in FIG. 8 can be considered. 8 (a), (b) and (c), reference numeral 10 is a barrel, 12 is a screw, 60 is a main flight, 62 is a barrier flight, 56 is a solid groove, and 58 is a melt groove. In FIG. 8 (a), the melt component is not sufficiently filled, and the melt component does not fill the melt groove 58, and it is necessary to raise the barrel set temperature. When it is operated to, the excessive melting state as shown in FIG. 8 (c) is generated, and break-up of the solid bed occurs, which has the opposite effect. Qualitatively,
As long as the condition that the melt component and the solid component are clearly separated by the barrier flight 62 is satisfied, the higher the melt groove pressure, the better the result. This is the proper melting state of FIG. 8 (b). It has also been clarified that the minute range in which this determination suffers is a state where the pressure waveform of the automatic diagnostic control system is determined to be normal.

そこで、本発明の目的は、バリア形のスクリュをもつ押
出機の溶融工程に係るバレル設定温度を、前記自動診断
制御システムによって前記溶融工程の正常であることを
確認し、しかる後にメルト溝内圧力の目標値を明確に
し、この目標値を基準圧力として最適化することができ
る押出機等の制御方法を提供することにある。
Therefore, an object of the present invention is to confirm the barrel set temperature related to the melting process of an extruder having a barrier type screw by the automatic diagnostic control system to confirm that the melting process is normal, and then to determine the melt groove pressure. The object of the present invention is to provide a control method for an extruder or the like that can clarify the target value of and optimize the target value as the reference pressure.

〔問題点を解決するための手段〕[Means for solving problems]

従って、本発明に係る押出機等の制御方法は、分割して
温度制御されるバレル中に供給されるプラスチック固形
材料を、主フライトおよびバリアフライトを備えたスク
リュの回転により押出し溶融し、この押出し溶融工程を
経た溶融材料を押出成形、射出成形もしくは吹込成形す
る押出機等の制御方法において、前記スクリュの溶融促
進部におけるメルト溝内圧力およびソリッド溝内圧力よ
りなる圧力波形を前記バリアフライトおよび前記主フラ
イトそれぞれの位置との関係において計測しかつサンプ
リングを行い、このサンプリングデータにより前記溶融
工程を正常と判定した際に前記メルト溝内圧力の目標値
との偏差を求め、この偏差が圧力許容値を越えた場合に
前記溶融促進部に近接するバレル温度制御帯のバレル設
定温度の制御を行い、前記メルト溝内圧力を一定範囲内
に維持することを特徴とする。
Therefore, the control method of the extruder or the like according to the present invention is such that the plastic solid material that is divided and supplied into the temperature-controlled barrel is extruded and melted by the rotation of the screw provided with the main flight and the barrier flight, and this extrusion is performed. In a method of controlling an extruder or the like for extrusion molding, injection molding or blow molding of a molten material that has undergone a melting step, a pressure waveform composed of a pressure inside the melt groove and a pressure inside the solid groove in the melt promoting portion of the screw is the barrier flight and the above. The measurement is performed in relation to the position of each main flight and sampling is performed, and when the melting process is determined to be normal based on this sampling data, the deviation from the target value of the pressure in the melt groove is obtained, and this deviation is the allowable pressure value. When the temperature exceeds the melting point, the barrel set temperature in the barrel temperature control zone close to the melting accelerator is controlled. , And maintains the melt groove pressure within a certain range.

また、前記押出機等の制御方法において、圧力センサか
らの前記メルト溝内圧力および前記ソリッド溝内圧力を
示す圧力信号は信号処理器を介して選別入力すると共に
A/D変換器を介してサンプリングデータをCPUに入力し、
位置センサからの前記バリアフライトと前記主フライト
の位置を示す位置信号は直接前記CPUに入力し、前記圧
力波形の比較により前記溶融工程が正常と判断した際に
前記メルト溝内圧力の偏差が圧力許容値を越えないよう
にバレル設定温度を更新する演算を行い、更新温度信号
を出力インタフェースを介して前記溶融促進部に近接す
るバレル温度制御帯の温度調節計に出力するよう構成す
る。
Further, in the control method of the extruder or the like, a pressure signal indicating the pressure in the melt groove and the pressure in the solid groove from a pressure sensor is selectively input through a signal processor.
Input sampling data to CPU via A / D converter,
A position signal indicating the position of the barrier flight and the main flight from the position sensor is directly input to the CPU, and when the melting process is judged to be normal by the comparison of the pressure waveforms, the deviation of the melt groove pressure is the pressure. A calculation is performed to update the barrel set temperature so as not to exceed the allowable value, and the updated temperature signal is output to the temperature controller in the barrel temperature control zone adjacent to the melting promoting section via the output interface.

なお、前記押出機等の制御方法において、さらに前記ス
クリュヘッド部の溶融材料の温度を測定してこの温度と
設定温度との偏差を求め、この偏差が温度許容値を越え
た場合に前記ヘッド部に近接するバレル温度制御帯のバ
レル設定温度の制御を行い、前記ヘッド部の溶融材料の
温度を一定範囲内に維持するようにすれば好適である。
In the method of controlling the extruder or the like, the temperature of the molten material in the screw head portion is further measured to obtain a deviation between this temperature and a set temperature, and when the deviation exceeds a temperature allowable value, the head portion is It is preferable to control the barrel set temperature of the barrel temperature control zone close to the above to maintain the temperature of the molten material in the head portion within a certain range.

〔作用〕[Action]

本発明に係る押出機等の制御方法によれば、正常に運転
されている押出機等において、その溶融工程に何等かの
異常が生ずると、各センサからのサンプリングデータに
基づく圧力波形に異常が生じ、前記自動診断制御システ
ムにより、異常が検出されて警報の出力やスローダウン
の応急処置が行われる。その回復過程において、圧力波
形が正常に戻れば、メルト溝内圧力ならびにスクリュヘ
ッド部の溶融材料の温度はいずれも目標値との偏差が求
められ、この偏差が圧力ならびに温度許容値の範囲に維
持されるように、スクリュの溶融促進部ならびにヘッド
部にそれぞれ近接するバレル温度制御帯のバレル設定温
度が最適値に制御される。このようにして、従来判断に
苦しんだメルト溝内圧力の設定を短時間の運転で見極
め、これを目安として制御を行い、押出機の総合性能を
最大限に向上させることができる。
According to the control method for an extruder or the like according to the present invention, in an extruder or the like that is normally operating, if any abnormality occurs in the melting process, an abnormality occurs in the pressure waveform based on the sampling data from each sensor. When this happens, the automatic diagnosis control system detects an abnormality and outputs an alarm or takes a first-aid measure for slowdown. If the pressure waveform returns to normal during the recovery process, deviations from the target values are required for both the melt groove pressure and the temperature of the molten material in the screw head, and these deviations are maintained within the pressure and temperature allowable range. As described above, the barrel set temperatures of the barrel temperature control zones near the melting promoting portion and the head portion of the screw are controlled to the optimum values. In this way, the setting of the pressure in the melt groove, which has been difficult to judge in the past, can be determined in a short time of operation, and control can be performed using this as a guide to maximize the overall performance of the extruder.

〔実施例〕〔Example〕

次に、本発明に係る押出機等の制御方法の実施例につ
き、添付図面を参照しながら以下詳細に説明する。
Next, an embodiment of a method for controlling an extruder or the like according to the present invention will be described in detail below with reference to the accompanying drawings.

第1図は、本発明に係る押出機等の制御方法を実施する
押出機の一実施例を示す概略構成図である。第1図にお
いて、参照符号10はバレルを示し、このバレル10の内部
にスクリュ12が挿通配置される。このスクリュ12のヘッ
ド部には、押出成形型としてのTダイ14が設けられる。
また、このスクリュ12の基部は、減速機16を介して駆動
モータ18に接続される。また、前記バレル10の外周に
は、加熱用のヒータ20が装着され、またその近辺に温度
センサが適宜設けられ、これらは温度調節計21,22,23,2
5および27によりそれぞれ分割して制御される。このヒ
ータ20に対して外部冷却用のファン24が適宜設けられ、
スクリュ12の基部側にプラスチックの固形材料を供給す
るホッパ11が設けられる。スクリュ12には、主フライト
60とバリアフライト62とが設けられ、この二種類のフラ
イトを備える所がスクリュ12の溶融促進部で、この部分
に対応するバレル10に、第8図に示すメルト溝58および
ソリッド溝56の溝内圧力を検出するための圧力センサ26
が設けられる。さらに、スクリュ12のヘッド部に対応す
るバレル10に溶融材料の温度を検出する温度センサ28が
設けられる。また、スクリュ12の基部の端部12aには主
フライト60およびバリアフライト62の位置を検出する位
置センサ30が設けられる。圧力センサ26および温度セン
サ28で検出された信号は、それぞれ信号処理器32および
34を介してマルチプレクサ36により選択的にA/D変換器3
8に供給され、サンプリングデータとなりCPU40に入力す
る。一方、位置センサ30からの信号は、信号処理器42を
介して直接CPU40に入力する。これら諸入力データは、
内部メモリ44に記憶される。やがて、これら圧力波形な
らびに温度は予め記憶保持した基準圧力データならびに
目標温度と比較される。CPU40には、CRTディスプレイ46
やプリンタ48等の出力機器、キーボード53からなる入力
設定器およびフロッピディスク50等の外部メモリが適宜
接続される。また、CPU40に対しては、出力インタフェ
ース52を介して異常警報を行うブザー54やさらにマルチ
プレクサ51を介して選択的に温度調節計21,22,23,25お
よび27が接続される。
FIG. 1 is a schematic configuration diagram showing an embodiment of an extruder for carrying out a method for controlling an extruder and the like according to the present invention. In FIG. 1, reference numeral 10 indicates a barrel, and a screw 12 is inserted and arranged inside the barrel 10. A T die 14 as an extrusion mold is provided at the head portion of the screw 12.
The base of the screw 12 is connected to the drive motor 18 via the speed reducer 16. Further, a heater 20 for heating is attached to the outer periphery of the barrel 10, and a temperature sensor is appropriately provided in the vicinity thereof, and these are temperature controllers 21, 22, 23, 2
It is controlled separately by 5 and 27. An external cooling fan 24 is appropriately provided for the heater 20,
A hopper 11 for supplying a plastic solid material is provided on the base side of the screw 12. Main flight to screw 12
60 and a barrier flight 62 are provided, and the place where these two types of flights are provided is the melting promoting portion of the screw 12, and the melt groove 58 and the solid groove 56 shown in FIG. Pressure sensor 26 for detecting internal pressure
Is provided. Further, the barrel 10 corresponding to the head portion of the screw 12 is provided with a temperature sensor 28 for detecting the temperature of the molten material. A position sensor 30 that detects the positions of the main flight 60 and the barrier flight 62 is provided at the end 12a of the base of the screw 12. The signals detected by the pressure sensor 26 and the temperature sensor 28 are supplied to the signal processor 32 and the signal processor 32, respectively.
A / D converter 3 selectively by multiplexer 36 via 34
It is supplied to 8 and becomes sampling data and is input to CPU 40. On the other hand, the signal from the position sensor 30 is directly input to the CPU 40 via the signal processor 42. These input data are
It is stored in the internal memory 44. Eventually, these pressure waveforms and temperatures are compared with the reference pressure data and the target temperature stored and stored in advance. CPU40 has a CRT display 46
An output device such as a printer or a printer 48, an input setting device including a keyboard 53, and an external memory such as a floppy disk 50 are appropriately connected. Further, to the CPU 40, temperature controllers 21, 22, 23, 25 and 27 are selectively connected via a buzzer 54 that issues an abnormal alarm via an output interface 52 and further via a multiplexer 51.

次に、圧力センサ26とスクリュ12との詳細な関係配置を
示すと、第4図(a)および(b)に示す通りである。
第4図(a)および(b)において、スクリュ12が回転
すると、圧力センサ26はメルト溝58の溝内圧力をバリア
フライト62から主フライト60にわたり検出し、さらに回
転すると、主フライト60からバリアフライト62にわたる
ソリッド溝56の溝内圧力を検出する。また、位置センサ
30は、第5図(a)に示すように、スクリュ端部12aに
取付けた信号発生用カラー64に対向して設け、その回転
偏位に応じて、第5図(b)に示すようなフライトの位
置信号を発生する。従って、位置センサ30としては、例
えば近接スイッチを好適に使用することができる。
Next, the detailed relational arrangement between the pressure sensor 26 and the screw 12 is as shown in FIGS. 4 (a) and 4 (b).
In FIGS. 4A and 4B, when the screw 12 rotates, the pressure sensor 26 detects the pressure inside the melt groove 58 from the barrier flight 62 to the main flight 60, and when the screw 12 further rotates, the pressure sensor 26 moves from the main flight 60 to the barrier. The pressure inside the solid groove 56 over the flight 62 is detected. Also the position sensor
As shown in FIG. 5 (a), the reference numeral 30 is provided so as to face the signal generating collar 64 attached to the screw end 12a, and as shown in FIG. 5 (b) depending on the rotational deviation thereof. Generates flight position signals. Therefore, as the position sensor 30, for example, a proximity switch can be preferably used.

次に、前述のように構成さた押出機の制御方法につき、
その動作に基づいて説明する。
Next, regarding the control method of the extruder configured as described above,
A description will be given based on the operation.

まず、バレル温度を所定設定温度まで上昇させ、スクリ
ュ12の回転速度を所定の回転数に保持して、プラスチッ
ク固形材料を供給する。溶融工程に異常がなければ、圧
力センサ26によりメルト溝内圧とソリッド溝内圧をバリ
アフライト位置と主フライト位置との関連において計測
し、サンプリングを行う。また、温度センサ28により、
スクリュ12のヘッド部の溶融材料の温度も計測される。
これらサンプリングデータは、時系列的に行われ、圧力
波形としてCPU40を介し内部メモリ44に記憶される。次
に、統計演算が行われて許容限界が設定され、圧力波形
のグラフィック表示が第6図に示すように行われ、この
測定圧力波形と正常波形の比較演算が第7図に示すよう
に実行される。次に、正常または異常の判別を行う。異
常の場合は、先ず時系列的に安定しているかどうかを判
別する。次いで、順次各種異常波形と比較し、最も類似
性の高い波形を選択する。このようにして異常の原因を
確認する。類似性の高い波形がなければ記憶する。これ
は一種の試験結果の追試で、原因の複雑な現象に対する
診断方法としては有効である。このようにして、異常が
解消し正常に復帰したならば、前記メルト溝内圧力の目
標値との偏差を求め、この偏差が圧力許容値以内にある
ように近接するバレル温度制御帯の温度調節計22および
23のバレル設定温度の修正を行う。このバレル設定温度
の修正を行うため、このバレル設定温度を更新する演算
を行い、更新温度信号を出力インタフェース52とマルチ
プレクサ51を介し、温度調節計22および23へ選択的に出
力する。このような溶融工程におけるバレル温度の変化
は、必ずスクリュ12のヘッド部の溶融材料に影響を与え
ることが考慮されるので、従来と同様にヘッド部の温度
センサ28による温度検出を行い、このヘッド部に近接す
るバレル温度制御帯の温度調節計27のバレル設定温度の
更新を実施する。
First, the barrel temperature is raised to a predetermined set temperature, the rotation speed of the screw 12 is maintained at a predetermined rotation speed, and the solid plastic material is supplied. If there is no abnormality in the melting process, the pressure in the melt groove and the pressure in the solid groove are measured by the pressure sensor 26 in relation to the barrier flight position and the main flight position, and sampling is performed. Also, by the temperature sensor 28,
The temperature of the molten material in the head part of the screw 12 is also measured.
These sampling data are performed in time series and are stored in the internal memory 44 via the CPU 40 as a pressure waveform. Next, the statistical calculation is performed, the allowable limit is set, the graphic display of the pressure waveform is performed as shown in FIG. 6, and the comparison calculation of the measured pressure waveform and the normal waveform is executed as shown in FIG. To be done. Next, normality or abnormality is determined. In the case of abnormality, first, it is determined whether or not the time series is stable. Then, the various abnormal waveforms are sequentially compared and the waveform with the highest similarity is selected. In this way, the cause of the abnormality is confirmed. If there is no waveform with high similarity, it is stored. This is a supplementary test of a kind of test result, and is effective as a diagnostic method for a complicated cause phenomenon. In this way, when the abnormality is eliminated and the state returns to normal, the deviation of the melt groove pressure from the target value is obtained, and the temperature adjustment of the adjacent barrel temperature control zone is performed so that this deviation is within the pressure allowable value. 22 and
Correct the barrel set temperature of 23. In order to correct the barrel set temperature, a calculation for updating the barrel set temperature is performed, and the updated temperature signal is selectively output to the temperature controllers 22 and 23 via the output interface 52 and the multiplexer 51. It is considered that such a change in the barrel temperature in the melting step necessarily affects the molten material of the head portion of the screw 12, so the temperature is detected by the temperature sensor 28 of the head portion as in the conventional case, and this head is used. The barrel set temperature of the temperature controller 27 in the barrel temperature control zone near the section is updated.

第2図と第3図は、第1図に示す押出機のプログラム例
を示すフローチャートである。第2図において、ステッ
プaは初期設定である。ステップbはサンプリングのタ
イミングをとるもので、第6図に示すバリアフライトの
位置を示す位置信号がアンドゲートに存在するとき、サ
ンプリングを開始する。そしてステップcで圧力波形の
サンプリングを行う。ステップdは再びバリアフライト
の位置を示す位置信号が現れたときサンプリングを終了
し、ステップeで得られたデータの処理を行う。ステッ
プfおよびgは必要に応じて行うスクリュヘッド部の温
度サンプリングとそのデータ処理である。ステップhは
圧力波形のサンプリングデータについて統計演算および
比較演算を実施し、異常波形を判断し、異常のときは時
系列データサンプリングが安定しているかどうか判断を
行い、順次各種異常波形と比較し、最も類似性の高い波
形を選択し、異常原因を解明して修復処理を行うもので
ある。ステップiは溶融工程が正常であることを確認し
てステップj以降のメルト溝内圧力の定値制御に移るこ
とを示す。第3図のフローチャートは、第2図に示すプ
ログラムが終了した後、ステップn以降のスクリュヘッ
ド部の溶融材料温度の定値制御を実行することを示すも
のである。
2 and 3 are flowcharts showing a program example of the extruder shown in FIG. In FIG. 2, step a is an initial setting. Step b is for sampling timing, and when the position signal indicating the position of the barrier flight shown in FIG. 6 exists in the AND gate, sampling is started. Then, in step c, the pressure waveform is sampled. In step d, sampling is terminated when the position signal indicating the position of the barrier flight appears again, and the data obtained in step e is processed. Steps f and g are temperature sampling of the screw head portion and data processing thereof, which are performed as needed. In step h, statistical calculation and comparison calculation are performed on the sampling data of the pressure waveform to determine an abnormal waveform, and when abnormal, it is determined whether the time-series data sampling is stable and sequentially compared with various abnormal waveforms. The most similar waveform is selected, the cause of abnormality is clarified, and repair processing is performed. Step i shows that after confirming that the melting process is normal, the process moves to constant value control of the melt groove pressure after step j. The flowchart of FIG. 3 shows that after the program shown in FIG. 2 is finished, the constant value control of the molten material temperature of the screw head portion after step n is executed.

〔発明の効果〕〔The invention's effect〕

前述した実施例から明らかなように、本発明に係る押出
機等の制御方法によれば、従来判断に苦しんだ溶融工程
の状態が自動診断制御システムによって明確になり、メ
ルト溝内圧力の設定を短時間の運転で容易に見極めら
れ、これを基準にしたバレル設定温度の最適制御が可能
となり、さらにスクリュヘッド部の溶融材料の温度制御
を加味することにより押出機の総合性能を最大限に向上
させることができる。
As is apparent from the above-described examples, according to the control method for the extruder and the like according to the present invention, the state of the melting process, which has been difficult to judge by the conventional method, is clarified by the automatic diagnosis control system, and the setting of the melt groove pressure is performed. It can be easily identified in a short time of operation, and it becomes possible to optimally control the barrel set temperature based on this, and further improve the overall performance of the extruder by adding temperature control of the molten material in the screw head. Can be made.

なお、その他本発明の精神を逸脱しない範囲内において
種々の設計変更をなし得ることは勿論である。
Needless to say, various design changes can be made without departing from the spirit of the present invention.

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

第1図は本発明に係る押出機等の制御方法を実施する押
出機の一実施例を示す概略構成図、第2図および第3図
は第1図に示す押出機の制御プログラム例をそれぞれ示
すフローチャート、第4図(a),(b)は第1図に示
す圧力センサの取付状態を示す要部拡大断面図および縦
断面図、第5図(a),(b)は第1図に示す位置セン
サの取付状態を示す要部拡大側面図および圧力センサの
圧力特性線図、第6図は本発明に係る制御方法によりサ
ンプリングされた圧力波形の表示例を示す特性曲線図、
第7図は圧力波形の基準データと測定データの比較表示
例を示す説明図、第8図(a),(b),(c)はスク
リュ溝内の溶融状態をそれぞれ示すモデル図である。 10……バレル、11……ホッパ 12……スクリュ、14……Tダイ 16……減速機、18……駆動モータ 20……ヒータ、21,22,23,25,27……温度調節計 24……冷却用ファン、26……圧力センサ 28……温度センサ、30……位置センサ 32,34,42……信号処理器 36,51……マルチプレクサ、38……A/D変換器 40……CPU、44……内部メモリ 46……CRTディスプレイ、48……プリンタ 50……フロッピディスク 52……出力インタフェース、53……キーボード 54……ブザー、60……主フライト 62……バリアフライト
FIG. 1 is a schematic configuration diagram showing an embodiment of an extruder for carrying out the control method of the extruder and the like according to the present invention, and FIGS. 2 and 3 are respectively control program examples of the extruder shown in FIG. FIG. 4 (a) and FIG. 4 (b) are enlarged cross-sectional views and longitudinal cross-sectional views of the main part showing the mounting state of the pressure sensor shown in FIG. 1, and FIGS. 5 (a) and 5 (b) are FIG. FIG. 6 is an enlarged side view of a main part showing a mounting state of the position sensor shown in FIG. 4 and a pressure characteristic diagram of the pressure sensor. FIG. 6 is a characteristic curve diagram showing a display example of a pressure waveform sampled by the control method according to the present invention.
FIG. 7 is an explanatory diagram showing a comparative display example of the reference data of the pressure waveform and the measured data, and FIGS. 8 (a), (b) and (c) are model diagrams showing the molten state in the screw groove, respectively. 10 …… Barrel, 11 …… Hopper 12 …… Screw, 14 …… T-die 16 …… Reducer, 18 …… Drive motor 20 …… Heater, 21,22,23,25,27 …… Temperature controller 24 ...... Cooling fan, 26 …… Pressure sensor 28 …… Temperature sensor, 30 …… Position sensor 32,34,42 …… Signal processor 36,51 …… Multiplexer, 38 …… A / D converter 40 …… CPU, 44 ... Internal memory 46 ... CRT display, 48 ... Printer 50 ... Floppy disk 52 ... Output interface, 53 ... Keyboard 54 ... Buzzer, 60 ... Main flight 62 ... Barrier flight

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭53−145874(JP,A) 特開 昭58−92545(JP,A) 特公 平2−58092(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-53-145874 (JP, A) JP-A-58-92545 (JP, A) JP-B 2-58092 (JP, B2)

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】分割して温度制御されるバレル中に供給さ
れるプラスチック固形材料を、主フライトおよびバリア
フライトを備えたスクリュの回転により押出し溶融し、
この押出し溶融工程を経た溶融材料を押出成形、射出成
形もしくは吹込成形する押出機等の制御方法において、
前記スクリュの溶融促進部におけるメルト溝内圧力およ
びソリッド溝内圧力よりなる圧力波形を前記バリアフラ
イトおよび前記主フライトそれぞれの位置との関係にお
いて計測しかつサンプリングを行い、このサンプリング
データにより前記溶融工程を正常と判定した際に前記メ
ルト溝内圧力の目標値との偏差を求め、この偏差が圧力
許容値を越えた場合に前記溶融促進部に近接するバレル
温度制御帯のバレル設定温度の制御を行い、前記メルト
溝内圧力を一定範囲内に維持することを特徴とする押出
機等の制御方法。
1. A plastic solid material fed into a barrel whose temperature is controlled in a divided manner is extruded and melted by rotation of a screw provided with a main flight and a barrier flight,
In a method for controlling an extruder or the like for extrusion molding, injection molding or blow molding the molten material that has gone through this extrusion melting step,
The pressure waveform consisting of the pressure inside the melt groove and the pressure inside the solid groove in the melting promoting portion of the screw is measured and sampled in relation to the positions of the barrier flight and the main flight respectively, and the melting step is performed by this sampling data. When it is determined to be normal, the deviation from the target value of the melt groove pressure is obtained, and when this deviation exceeds the allowable pressure value, the barrel set temperature of the barrel temperature control zone close to the melting promoting section is controlled. A method for controlling an extruder or the like, characterized in that the pressure in the melt groove is maintained within a certain range.
【請求項2】特許請求の範囲第1項記載の押出機等の制
御方法において、圧力センサからの前記メルト溝内圧力
および前記ソリッド溝内圧力を示す圧力信号は信号処理
器を介して選別入力すると共にA/D変換器を介してサン
プリングデータをCPUに入力し、位置センサからの前記
バリアフライトと前記主フライトの位置を示す位置信号
は直接前記CPUに入力し、前記圧力波形の比較により前
記溶融工程が正常と判断した際に前記メルト溝内圧力の
偏差が圧力許容値を越えないようにバレル設定温度を更
新する演算を行い、更新温度信号を出力インタフェース
を介して前記溶融促進部に近接するバレル温度制御帯の
温度調節計に出力することからなる押出機等の制御方
法。
2. A method for controlling an extruder or the like according to claim 1, wherein pressure signals indicating the pressure in the melt groove and the pressure in the solid groove from a pressure sensor are selectively input through a signal processor. And the sampling data is input to the CPU via the A / D converter, the position signal indicating the position of the barrier flight and the main flight from the position sensor is directly input to the CPU, and the comparison is made by the pressure waveform. When it is judged that the melting process is normal, the operation to update the barrel set temperature is performed so that the deviation of the pressure in the melt groove does not exceed the allowable pressure value, and the updated temperature signal is output to the proximity of the melting promoting unit via the output interface. A method of controlling an extruder or the like, which comprises outputting to a temperature controller in a barrel temperature control zone.
【請求項3】分割して温度制御されるバレル中に供給さ
れるプラスチック固形材料を、主フライトおよびバリア
フライトを備えたスクリュの回転により押出し溶融し、
この押出し溶融工程を経た溶融材料を押出成形、射出成
形もしくは吹込成形する押出機等の制御方法において、
前記スクリュの溶融促進部におけるメルト溝内圧力およ
びソリッド溝内圧力よりなる圧力波形を前記バリアフラ
イトおよび前記主フライトそれぞれの位置との関係にお
いて計測しかつサンプリングを行い、このサンプリング
データにより前記溶融工程を正常と判定した際に前記メ
ルト溝内圧力の目標値との偏差を求め、この偏差が圧力
許容値を越えた場合に前記溶融促進部に近接するバレル
温度制御帯のバレル設定温度の制御を行い、前記メルト
溝内圧力を一定範囲内に維持し、さらに前記スクリュの
ヘッド部の溶融材料の温度を測定してこの温度と設定温
度との偏差を求め、この偏差が温度許容値を越えた場合
に前記ヘッド部に近傍するバレル温度制御帯のバレル設
定温度の制御を行い、前記ヘッド部の溶融材料の温度を
一定範囲内に維持することを特徴とする押出機等の制御
方法。
3. A plastic solid material fed into a barrel whose temperature is controlled in a divided manner is extruded and melted by rotation of a screw provided with a main flight and a barrier flight,
In a method for controlling an extruder or the like for extrusion molding, injection molding or blow molding the molten material that has gone through this extrusion melting step,
The pressure waveform consisting of the pressure inside the melt groove and the pressure inside the solid groove in the melting promoting portion of the screw is measured and sampled in relation to the positions of the barrier flight and the main flight respectively, and the melting step is performed by this sampling data. When it is determined to be normal, the deviation from the target value of the melt groove pressure is obtained, and when this deviation exceeds the allowable pressure value, the barrel set temperature of the barrel temperature control zone close to the melting promoting section is controlled. When the pressure in the melt groove is maintained within a certain range, the temperature of the molten material in the head portion of the screw is further measured to obtain the deviation between this temperature and the set temperature, and when this deviation exceeds the temperature allowable value. The temperature of the molten material in the head part is maintained within a certain range by controlling the barrel set temperature in the barrel temperature control zone near the head part. The method of extruder or the like, characterized in Rukoto.
【請求項4】特許請求の範囲第3項記載の押出機等の制
御方法において、圧力センサからの前記メルト溝内圧力
および前記ソリッド溝内圧力を示す圧力信号と温度セン
サからの前記スクリュのヘッド部の溶融材料の温度を示
す温度信号とは、それぞれ信号処理器を介して選別入力
すると共にA/D変換器を介してサンプリングデータをCPU
に入力し、位置センサからの前記バリアフライトと前記
主フライトの位置を示す位置信号は直接前記CPUに入力
し、前記圧力波形の比較により前記溶融工程が正常と判
断した際に前記メルト溝内圧力の偏差が圧力許容値を越
えないようにバレル設定温度を更新する演算を行い、更
新温度信号を出力インタフェースを介して前記溶融促進
部に近接するバレル温度制御帯の温度調節計に出力し、
さらに前記ヘッド部の溶融材料の温度の偏差が温度許容
値を越えないようにバレル設定温度を更新する演算を行
い、別の更新温度信号を前記出力インタフェースを介し
て前記ヘッド部に近接するバレル温度制御帯の別の温度
調節計に出力することからなる押出機等の制御方法。
4. A method of controlling an extruder or the like according to claim 3, wherein a pressure signal from the pressure sensor indicating the pressure in the melt groove and the pressure in the solid groove and a head of the screw from a temperature sensor. The temperature signal indicating the temperature of the molten material in the part is selected and input via the signal processor and the sampling data is sent to the CPU via the A / D converter.
The position signal indicating the positions of the barrier flight and the main flight from the position sensor is directly input to the CPU, and the pressure in the melt groove when the melting process is judged to be normal by comparing the pressure waveforms. The calculation of updating the barrel set temperature so that the deviation does not exceed the allowable pressure value, and outputs the updated temperature signal to the temperature controller in the barrel temperature control zone close to the melting promoting section via the output interface,
Further, a calculation for updating the barrel set temperature is performed so that the deviation of the temperature of the molten material in the head portion does not exceed the allowable temperature value, and another update temperature signal is sent to the barrel temperature close to the head portion via the output interface. A method for controlling an extruder or the like, which comprises outputting to another temperature controller in the control zone.
JP61175738A 1986-07-28 1986-07-28 Extruder control method Expired - Fee Related JPH0684037B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61175738A JPH0684037B2 (en) 1986-07-28 1986-07-28 Extruder control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61175738A JPH0684037B2 (en) 1986-07-28 1986-07-28 Extruder control method

Publications (2)

Publication Number Publication Date
JPS6331730A JPS6331730A (en) 1988-02-10
JPH0684037B2 true JPH0684037B2 (en) 1994-10-26

Family

ID=16001383

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61175738A Expired - Fee Related JPH0684037B2 (en) 1986-07-28 1986-07-28 Extruder control method

Country Status (1)

Country Link
JP (1) JPH0684037B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001073933A (en) * 1999-09-01 2001-03-21 Bridgestone Corp Positive-displacement extruding machine and extruding method for viscous material
KR102635501B1 (en) * 2019-02-21 2024-02-13 엘에스엠트론 주식회사 Injection Molding Apparatus
CN112248395A (en) * 2020-09-25 2021-01-22 安徽德尔电气集团有限公司 Extruder temperature control system for cable production

Also Published As

Publication number Publication date
JPS6331730A (en) 1988-02-10

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