JPS6331730A - Control of extruder or the like - Google Patents

Control of extruder or the like

Info

Publication number
JPS6331730A
JPS6331730A JP61175738A JP17573886A JPS6331730A JP S6331730 A JPS6331730 A JP S6331730A JP 61175738 A JP61175738 A JP 61175738A JP 17573886 A JP17573886 A JP 17573886A JP S6331730 A JPS6331730 A JP S6331730A
Authority
JP
Japan
Prior art keywords
pressure
temperature
barrel
groove
melt
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.)
Granted
Application number
JP61175738A
Other languages
Japanese (ja)
Other versions
JPH0684037B2 (en
Inventor
Teiji Shimizu
清水 禎二
Katsuhiro Iguchi
勝啓 井口
Kenji Nozawa
野沢 憲司
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

Abstract

PURPOSE:To permit the optimal control of a barrel setting temperature, by providing an automatic diagnosis control system with respect to a pressure in a melt promoting unit. CONSTITUTION:An extruder extrudes and melts the solid material of plastic, supplied into a barrel 10, whose temperature is controlled dividedly, by a screw 12 equipped with a main flight 60 and a barrier flight 62, there after, molds by extrusion through a T die 24, for example. Pressure waveforms, formed by a pressure in a melt groove 58 and a pressure in a solid groove 56 in the melt promoting unit of the screw 12, are measured by a pressure sensor 26 in a relation with respect to respective positions of the barrier flight 62 and the main flight 60 and, further, samplings are effected. When a melting process is judged as normal from the data of the sampling, a difference between the pressure in the melt groove 58 and an objective value is obtained. When the difference has exceeded a pressure allowable value, the barrel setting temperature of the temperature regulating meters 22, 23 of a barrel temperature control belt near the melt promoting unit is controlled whereby the pressure in the melt groove 62 is maintained within a given range.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、熔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。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a method for controlling an extrusion molding machine, an injection molding machine, and a blow molding machine (hereinafter collectively referred to as extruders, etc.) that mold molten plastic material. In order to achieve especially high-quality molding, the screw that extrudes and melts the material is equipped with a main flight and a barrier flight (sub-flight).
The present invention relates to a method of controlling an extruder, etc. that uses a barrier-type screw that has a solid groove and a melt groove formed between it and the inner surface of a barrel.

〔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。
The goal of controlling an extruder, etc. is to use an appropriately designed extrusion screw, set the barrel temperature appropriately, and uniformly and stably supply a predetermined extrusion amount of molten material to the next process. . For this reason, in the early stages, constant value control of the pressure and temperature of the molten material in the screw head was performed.

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、−般に固形状の未熔融物の解体という
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、固形成分と熔融成分を分離す
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。
However, it has been found that this control alone has its limits and sometimes has the opposite effect of promoting melting instability. In other words, this is due to the phenomenon of solid bed breakup, which generally means the breaking up of solid unmelted material, as the solid material passes through the feeding section, compression section, and metering section in the groove of the screw. This shows an unstable state of melting that occurs during the melting process where the material gradually changes to molten material. In order to avoid such a phenomenon, a barrier-type screw has a new barrier flight installed in the melting promotion section, which occupies the longest part of the screw, as a shelf to separate the solid component and the molten component. The improvement effect of this new barrier-type screw was noteworthy, but what expanded this effect even further was 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熔融工程の自動診断制御
システムを提案し、特願昭60−81369号として特
許出願を行った。
That is, the present applicant previously solved the problem of other instability, including break-up of the solid bed, by using signals from a pressure sensor provided in the melting promotion section and a position sensor provided at the drive end of the screw. Automatic diagnosis of the melting process that detects the waveform, compares and contrasts it with predetermined standard data, calculates the correlation statistics, determines whether it is normal or abnormal, and performs additional tests in the event of an abnormality. He proposed a control system and filed a patent application as Japanese Patent Application No. 81369/1983.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

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、正常熔融工程において
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)、 (bl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。
However, in the automatic diagnostic control system,
There is no clear control over the barrel temperature setting, which is important for determining abnormalities. Conventionally, the value of the melt groove internal pressure could not be determined uniquely, and varied depending on the structure of the screw, the characteristics of the material, the rotational speed of the screw, etc., and could not be considered as a guideline for control. However, the diagnosis result of the automatic diagnosis control system has since become clear that once the above-mentioned parameters are selected, the pressure within the melt groove is almost constant during the normal melting process. Further, according to the above diagnosis results, a model diagram showing the molten state in the screw groove shown in FIG. 8 can be considered. In FIGS. 8(a), (bl 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,
58 indicates melt grooves, respectively.

第8図[a)は熔融不足状態で、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
融過剰状態を生し、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)の通性溶融状態である。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。
Fig. 8 [a] shows a state of insufficient melting, where the melt components are not filling the melt groove 58, and it is felt that it is necessary to raise the barrel temperature setting, but it is difficult to increase the pressure inside the melt groove unnecessarily in order to increase the extrusion amount. If this operation is performed, an excessive melting state as shown in FIG. 8(C) will occur, and breakup of the solid bed will occur, resulting in 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 pressure in the melt groove, the better the result. This is the facultative molten state shown in FIG. 8(b). It has also become clear that this small range in which it is difficult to judge is a state in which the pressure waveform of the automatic diagnostic control system is judged 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
出機の熔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熔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。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to confirm that the barrel temperature in the melting process of an extruder having a barrier type screw is normal by using the automatic diagnostic control system, and then to control the temperature in the melt groove. It is an object of the present invention to provide a control method for an extruder, etc., which can clarify a target value of pressure and optimize this target value as a 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、この押出し熔融工程を
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 method for controlling an extruder, etc. according to the present invention involves extruding and melting a plastic solid material supplied into a barrel whose temperature is controlled in parts by rotating a screw equipped 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 a molten material that has undergone a melting process, a pressure waveform consisting of a melt groove internal pressure and a solid groove internal pressure in the melting promotion section of the screw is controlled by the barrier flight and the solid groove pressure. Measurement and sampling are performed in relation to the position of each main flight, 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 determined, and this deviation is the pressure tolerance value. If the temperature exceeds the melting point, the barrel temperature control zone in the vicinity of the melt promoting section is controlled to maintain the pressure within the melt groove 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熔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 method for controlling the extruder, etc., pressure signals indicating the melt groove internal pressure and the solid groove internal pressure from the pressure sensor are selectively inputted via a signal processor and sampled via an A/D converter. The data is input to the CPU, position signals indicating the positions of the barrier flight and the main flight from the position sensor are directly input to the CPU, and when it is determined that the melting process is normal by comparing the pressure waveforms, the melt Calculations are performed to update the barrel temperature so that the deviation in the groove pressure does not exceed the pressure tolerance, and the updated temperature signal is output via the output interface to the temperature controller in the barrel temperature control zone near the melting promotion section. Configure it to do so.

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 addition, in the method for controlling the extruder, etc., the temperature of the molten material in the screw head section is further measured to determine the deviation between this temperature and the set temperature, and if this deviation exceeds the temperature tolerance, the head section is Preferably, the temperature of the molten material in the head section is maintained within a certain range by controlling the barrel temperature in a barrel temperature control zone adjacent to the barrel temperature control zone.

〔作用〕[Effect]

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g91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
を最大服に向上させることができる。
According to the method for controlling an extruder or the like according to the present invention, if any abnormality occurs in the melting process of the extruder or the like that is normally operating, the pressure waveform based on the sampling data from each sensor will be abnormal. The automatic diagnosis control system detects the abnormality and takes emergency measures such as g91 output and slowdown. During the recovery process, if the pressure waveform returns to normal, the pressure inside the melt groove and the temperature of the molten material at the screw head are both determined to be deviations from the target values, and this deviation is maintained within the permissible pressure and temperature ranges. In this way, the barrel temperature control zones in the barrel temperature control zones that are close to the melting promotion section and the head section of the screw are controlled to optimal values. In this way, it is possible to ascertain the setting of the pressure in the melt groove, which has been difficult to judge in the past, in a short period of operation, and to perform control using this as a guide or guide, thereby improving the overall performance of the extruder to its maximum.

〔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, embodiments of the method for controlling an extruder, etc. 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1oの
内部にスクリュ12が挿通配置される。このスクリュ1
2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1
6を介して駆動モータ18に接続される。
FIG. 1 is a schematic diagram showing an embodiment of an extruder for implementing the method for controlling an extruder, etc. according to the present invention. In FIG. 1, reference numeral 10 indicates a barrel, and a screw 12 is inserted and disposed inside this barrel 1o. This screw 1
The head portion of No. 2 is provided with a T-die 14 as an extrusion mold. Further, the base of this screw 12 is connected to the reducer 1
6 to a drive motor 18.

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゜22.23.25および2
7によりそれぞれ分割して制御される。このヒータ2o
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
IJ58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1
2のヘッド部に対応するバレル1o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3o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38
に供給され、サンプリングデータとなりCPU40に入
力する。−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、C
PU40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。
Further, a heater 20 for heating is provided on the outer periphery of the barrel 10.
is installed, and temperature sensors are appropriately installed near it, and these are connected to temperature controllers 21, 22, 23, 25 and 2.
7 and are controlled separately. This heater 2o
A fan 24 for external cooling is appropriately provided for the screw 12, and a hopper 11 for supplying solid plastic material is provided on the base side of the screw 12. The screw 12 is provided with a main flight 60 and a barrier flight 62, and the place where these two types of flights are provided is the melting promotion part of the screw 12,
A pressure sensor 26 for detecting the pressure in the melt IJ 58 and the solid groove 56 shown in FIG. 8 is provided in the barrel 10 corresponding to this portion. Furthermore, screw 1
A temperature sensor 28 for detecting the temperature of the molten material is provided in the barrel 1o corresponding to the head portion of No. 2. Furthermore, a position sensor 3o is provided at the base end 12a of the screw 12 to detect the positions of the main flight 60 and the barrier flight 62. The signals detected by the pressure sensor 26 and the temperature sensor 28 are selectively sent to an A/D converter 38 by a multiplexer 36 via signal processors 32 and 34, respectively.
The data is supplied to the CPU 40 as sampling data. - On the other hand, the signal from the position sensor 30 is input directly to the CPU 40 via the signal processor 42. These various input data are stored in the internal memory 44. Eventually, these pressure waveforms and temperatures are compared with reference pressure data and target temperature stored in advance. The CPU 40 is appropriately connected to output devices such as a CRT display 46 and a printer 48, an input setting device including a keyboard 53, and an external memory such as a floppy disk 50. Also, C
For the PU 40, there is a buzzer 54 that issues an abnormality alarm via an output interface 52, and a multiplexer 51.
Temperature controllers 21, 22, 23, 25 and 27 are selectively connected via.

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(alおよび(blに示す通りであ
る。第4図(a)および(′b)において、スフリユ1
2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i56の溝内圧力を検出
する。
Next, the detailed relationship between the pressure sensor 26 and the screw 12 is shown in FIG. 4 (al and (bl). In FIG.
2 rotates, the pressure sensor 26 detects the pressure in the groove of the melt groove 58 from the barrier flight 62 to the main flight 60, and as it rotates further, the pressure sensor 26 detects the pressure in the groove of the solid i56 from the main flight 60 to the barrier flight 62.

また、位置センサ30は、第5図(al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。
In addition, the position sensor 30, as shown in FIG. 5 (al),
It is provided opposite to a signal generating collar 64 attached to the screw end 12a, and generates a flight position signal as shown in FIG. 5(b) in accordance with its rotational deviation. Therefore, as the position sensor 30, for example, a proximity switch can be suitably used.

次に、前述のように構成され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, a method for controlling the extruder configured as described above will be explained based on its 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。
First, the barrel temperature is raised to a predetermined set temperature, the rotational speed of the screw 12 is maintained at a predetermined rotational speed, and the plastic solid material is supplied.

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CPU
40を介し内部メモリ44に記憶される。
If there is no abnormality in the melting process, the pressure sensor 26 measures the internal pressure of the melt groove and the internal pressure of the solid groove in relation to the barrier flight position and the main flight position, and performs sampling. Furthermore, the temperature of the molten material at the head portion of the screw 12 is also measured by the temperature sensor 28 . These sampling data are processed in time series and are processed as pressure waveforms by the CPU.
40 and stored in internal memory 44.

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。
Next, statistical calculations are performed to set acceptable limits, a graphical display of the pressure waveform is performed as shown in Figure 6, and a comparison calculation between the measured pressure waveform and the normal waveform is performed as shown in Figure 7. be done. Next, it is determined whether it is normal or abnormal.

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。
In the case of an abnormality, first it is determined whether it is stable over time. Next, it sequentially compares with various abnormal waveforms and selects the waveform with the highest similarity. In this way, the cause of the abnormality can be confirmed. If there is no highly similar waveform, it is memorized.

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5
2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。このような熔融工程における
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、
このへ・7ド邪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。
This is a kind of follow-up test for test results, and is effective as a diagnostic method for phenomena with complex causes. In this way, once the abnormality has been resolved and the state has returned to normal, the deviation of the pressure in the melt groove from the target value is determined, and the temperature of the adjacent barrel temperature control zone is adjusted so that this deviation is within the pressure tolerance. Total 22
And 23, the barrel temperature setting is corrected. In order to correct this barrel set temperature, a calculation is performed to update this barrel set temperature, and an updated temperature signal is output to interface 5.
2 and multiplexer 51, it is selectively output to temperature controllers 22 and 23. It is considered that such a change in barrel temperature during the melting process will definitely affect the melted material in the head portion of the screw 12, so the temperature is detected by the temperature sensor 28 in the head portion as in the past.
The barrel temperature setting of the temperature controller 27 in the barrel temperature control zone near the 7th and 7th points 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に、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 example programs for the extruder shown in FIG. 1. In FIG. 2, step a is initial setting. Step b is to determine the timing of sampling, and starts sampling when a position signal indicating the position of the barrier flight shown in FIG. 6 is present in the AND gate. Then, in step C, the pressure waveform is sampled. In step d, sampling is terminated when a 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 and data processing performed as necessary. Step h performs statistical calculations and comparison calculations on the sampling data of the pressure waveform, determines abnormal waveforms, determines whether the time series data sampling is stable in the case of abnormality, and sequentially compares with various abnormal waveforms. The most similar waveform is selected, the cause of the abnormality is determined, and repair processing is performed. Step i indicates that after confirming that the melting process is normal, the process moves to constant value control of the pressure in the melt groove from step j onward. The flowchart in FIG. 3 shows that after the program shown in FIG. 2 is completed, constant value control of the temperature of the molten material in the screw head portion after step n is executed.

〔発明の効果〕〔Effect of the invention〕

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 clear from the above embodiments, according to the method for controlling an extruder, etc. according to the present invention, the state of the melting process, which was difficult to judge in the past, can be clarified by the automatic diagnostic control system, and the setting of the pressure inside the melt groove can be made clear. This can be easily determined in a short period of operation, and the barrel temperature setting can be optimally controlled based on this. Furthermore, by adding temperature control to the molten material in the screw head, the overall performance of the extruder can be maximized. can be done.

なお、その信奉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。
It goes without saying that various design changes can be made without departing from the spirit of the invention.

【図面の簡単な説明】[Brief explanation 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櫃略構成図、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)、 (blは第1図に
示す圧力センサの取付状態を示す要部拡大横断面図およ
び縦断面図、第5図(al、 (bl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
ンサの出力特性線図、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(al、 (b)、 (
C1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グイ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、、、 CP U      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 特許出願人   東芝機械株式会社 FIG、 ’3(a’> FIG、 5(b) B桁 FIG、6 FIG、7 PQ5.04SensorIIl)LノC0ell−c
I!n1IJICOIrlll(ILlutlFIG、
FIG. 1 is a schematic configuration diagram of an extruder that implements the method for controlling an extruder, etc. according to the present invention, and FIGS. 2 and 3 show an example of a control program for the extruder shown in FIG. 1. The flowchart shown in FIG. 4(a), (bl is an enlarged cross-sectional view and vertical cross-sectional view of the main part showing the installation state of the pressure sensor shown in FIG. 1, and FIG. 5(al), (BL is the same as in FIG. FIG. 6 is an enlarged side view of the main parts showing the installation state of the position sensor and an output characteristic line 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. are explanatory diagrams showing comparative display examples of pressure waveform reference data and measured data;
C1 is a model diagram showing the molten state inside the screw groove. 10, Barrel 11. ,,Hopper 12),
, screw 14. ,, Tgui16, ,
, 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 Patent Applicant Toshiba Machine Co., Ltd. FIG, '3(a'> FIG, 5(b) B digit FIG, 6 FIG, 7 PQ5.04SensorIIl) L No C0ell-c
I! n1IJICOIrllll(ILlutlFIG,
8

Claims (4)

【特許請求の範囲】[Claims] (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 solid plastic material supplied into a barrel whose temperature is controlled in parts is extruded and melted by the rotation of a screw equipped with a main flight and a barrier flight, and the molten material that has gone through this extrusion melting process is extruded and injection molded. In a method for controlling an extruder or the like for molding or blow molding, a pressure waveform consisting of a melt groove internal pressure and a solid groove internal pressure in the melting promotion part of the screw is measured in relation to the respective positions of the barrier flight and the main flight. Then, sampling is performed, and when the melting process is determined to be normal based on the sampling data, the deviation of the pressure in the melt groove from the target value is determined, and if this deviation exceeds the pressure tolerance, the melting process is determined to be normal. A method for controlling an extruder, etc., comprising controlling a barrel temperature in a barrel temperature control zone to maintain the pressure within the melt groove within a certain range.
(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) In the method for controlling an extruder or the like according to claim 1, pressure signals indicating the pressure in the melt groove and the pressure in the solid groove from the pressure sensor are selectively inputted via a signal processor, and Sampling data is input to the CPU via an A/D converter, position signals indicating the positions of the barrier flight and the main flight from the position sensor are directly input to the CPU, and the melting process is determined by comparing the pressure waveforms. When it is determined that the melt groove is normal, a calculation is performed to update the barrel set temperature so that the deviation of the pressure in the melt groove does not exceed the pressure tolerance value, and an updated temperature signal is output to the barrel adjacent to the melting promotion section through an output interface. A method of controlling an extruder, etc., which consists of outputting to a temperature controller in a temperature control zone.
(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
囲内に維持することを特徴とする押出機等の制御方法。
(3) The solid plastic material supplied into a barrel whose temperature is controlled in parts is extruded and melted by the rotation of a screw equipped with a main flight and a barrier flight, and the molten material that has gone through this extrusion melting process is extruded and injection molded. In a method for controlling an extruder or the like for molding or blow molding, a pressure waveform consisting of a melt groove internal pressure and a solid groove internal pressure in the melting promotion part of the screw is measured in relation to the respective positions of the barrier flight and the main flight. Then, sampling is performed, and when the melting process is determined to be normal based on the sampling data, the deviation of the pressure in the melt groove from the target value is determined, and if this deviation exceeds the pressure tolerance, the melting process is determined to be normal. The barrel temperature in the barrel temperature control zone is controlled to maintain the pressure within the melt groove within a certain range, and the temperature of the molten material at the head of the screw is measured to determine the deviation between this temperature and the set temperature. is determined, and if this deviation exceeds a temperature tolerance value, the barrel temperature control zone in the barrel temperature control zone adjacent to the head section is controlled to maintain the temperature of the molten material in the head section within a certain range. Characteristic control method for extruder, etc.
(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) In the method for controlling an extruder or the like according to claim 3, a pressure signal indicating the pressure in the melt groove and the pressure in the solid groove from a pressure sensor and a pressure signal indicating the pressure in the head portion of the screw from a temperature sensor are provided. Temperature signals indicating the temperature of the molten material are input selectively through a signal processor and sampled data are sent to the CPU via an A/D converter.
A position signal indicating the positions of the barrier flight and the main flight from the position sensor is directly input to the CPU, and when it is determined that the melting process is normal by comparing the pressure waveforms, the pressure in the melt groove is Calculations are performed to update the barrel set temperature so that the deviation does not exceed the allowable pressure value.
Outputting an updated temperature signal to a temperature controller in a barrel temperature control zone adjacent to the melting promotion section via an output interface, and further setting the barrel so that the temperature deviation of the melted material in the head section does not exceed a temperature tolerance value. A method for controlling an extruder, etc., comprising performing a calculation to update the temperature, and outputting another updated temperature signal to another temperature controller in a barrel temperature control zone close to the head section via the output interface.
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 true JPS6331730A (en) 1988-02-10
JPH0684037B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6641766B1 (en) * 1999-09-01 2003-11-04 Bridgestone Corporation Positive displacement extrusion of viscous material
KR20200102244A (en) * 2019-02-21 2020-08-31 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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6641766B1 (en) * 1999-09-01 2003-11-04 Bridgestone Corporation Positive displacement extrusion of viscous material
KR20200102244A (en) * 2019-02-21 2020-08-31 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
JPH0684037B2 (en) 1994-10-26

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