JP2001260193A - Method for controlling injection molding machine - Google Patents

Method for controlling injection molding machine

Info

Publication number
JP2001260193A
JP2001260193A JP2000072330A JP2000072330A JP2001260193A JP 2001260193 A JP2001260193 A JP 2001260193A JP 2000072330 A JP2000072330 A JP 2000072330A JP 2000072330 A JP2000072330 A JP 2000072330A JP 2001260193 A JP2001260193 A JP 2001260193A
Authority
JP
Japan
Prior art keywords
heater
temperature
torque
heating cylinder
molding machine
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
JP2000072330A
Other languages
Japanese (ja)
Other versions
JP3794610B2 (en
Inventor
Akira Ito
晃 伊藤
Yoshihiko Makino
嘉彦 牧野
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP2000072330A priority Critical patent/JP3794610B2/en
Publication of JP2001260193A publication Critical patent/JP2001260193A/en
Application granted granted Critical
Publication of JP3794610B2 publication Critical patent/JP3794610B2/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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/76Measuring, controlling or regulating
    • B29C45/78Measuring, controlling or regulating of temperature
    • 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76003Measured parameter
    • B29C2945/76026Energy, power
    • 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76003Measured parameter
    • B29C2945/76033Electric 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76003Measured parameter
    • B29C2945/7611Velocity
    • B29C2945/7612Velocity rotational 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76177Location of measurement
    • B29C2945/7618Injection unit
    • B29C2945/76214Injection unit drive means
    • 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76344Phase or stage of measurement
    • B29C2945/76367Metering
    • 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76494Controlled parameter
    • B29C2945/76531Temperature
    • 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
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76655Location of control
    • B29C2945/76658Injection unit
    • B29C2945/76668Injection unit barrel

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for controlling an injection molding machine which can stabilize the torque of a metering motor irrespective of the lot of a resin by controlling the ratio between the melting of the resin by shearing heat and the melting by the heat of a heater. SOLUTION: The torque model of the metering motor is obtained in advance when conforming articles are obtained. A controller 13, in actual molding, controls a current passage control part 14 to make the torque of the motor approach the torque model, and the control part, when the actual torque of the motor is larger than the torque model, controls a heating cylinder 10 to increase its temperature. When the actual torque of the motor is smaller than the torque model, the cylinder is controlled to decrease its temperature.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は射出成形機の制御方
法に関し、特に加熱シリンダの温度制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling an injection molding machine, and more particularly to a method for controlling a temperature of a heating cylinder.

【0002】[0002]

【従来の技術】射出成形機においては、加熱シリンダ内
で樹脂を溶融させ、この溶融樹脂を金型のキャビティ内
に射出して成形を行う。加熱シリンダの温度、溶融樹脂
の射出圧力や保圧等の制御の良し悪しは成型品の品質に
大きな影響を与える。このうち、特に加熱シリンダの温
度について言えば、内部の樹脂の溶融状態に影響を与え
る。
2. Description of the Related Art In an injection molding machine, a resin is melted in a heating cylinder, and the molten resin is injected into a cavity of a mold for molding. The control of the temperature of the heating cylinder, the injection pressure of the molten resin, the holding pressure, etc., has a great effect on the quality of the molded product. Of these, the temperature of the heating cylinder, in particular, affects the molten state of the resin inside.

【0003】射出成形機において樹脂を溶融する手段と
して次の2種類がある。
There are the following two types of means for melting a resin in an injection molding machine.

【0004】A.加熱シリンダの周囲に配設されたヒー
タに加えられる熱量による溶融。
A. Melting due to the amount of heat applied to the heater arranged around the heating cylinder.

【0005】B.加熱シリンダ内に配置されたスクリュ
によって樹脂がせん断されることにより発生する、いわ
ゆるせん断発熱による溶融。
B. Melting due to so-called shear heat generated when resin is sheared by a screw arranged in a heating cylinder.

【0006】通常の射出成形機では、上記の2つが合わ
さった状態で樹脂の溶融が行われており、それぞれの比
率が変わると樹脂の溶融状態も異なってくる。言い換え
れば、加熱シリンダ内の樹脂の溶融の割合は、Aによる
溶融と、Bによる溶融の割合が時間によってばらつくこ
とが避けられない。これによって、樹脂の溶融状態がば
らつき、計量モータのトルク・計量時間等がばらついて
しまう。これらのばらつきは、成型品の品質がばらつく
原因となる。
In an ordinary injection molding machine, the resin is melted in a state where the above two are combined, and the molten state of the resin changes when the ratio of each changes. In other words, the rate of melting of the resin in the heating cylinder is inevitable that the rate of melting by A and the rate of melting by B vary with time. As a result, the molten state of the resin varies, and the torque and the measuring time of the measuring motor vary. These variations cause the quality of the molded product to vary.

【0007】一方、成形に用いる樹脂は、同じ種類であ
ってもロット毎に平均分子量や分子量の分布が微妙に異
なるために、同じ温度条件で可塑化しても樹脂の溶融状
態に違いが現れる。その結果、計量モータの計量回転時
のトルクがロットにより異なってしまっていた。これも
成型品の品質がばらつく原因となる。
On the other hand, the average molecular weight and the distribution of molecular weights are slightly different from lot to lot even if the resin used for molding is the same kind, so that even if the resin is plasticized under the same temperature condition, a difference appears in the molten state of the resin. As a result, the torque at the time of the weighing rotation of the weighing motor was different depending on the lot. This also causes the quality of the molded product to vary.

【0008】[0008]

【発明が解決しようとする課題】これまで、加熱シリン
ダの周囲に配設されたヒータの制御は以下のようにして
行われている。加熱シリンダには、その温度を検出する
ために熱電対等による温度センサが設置されている。そ
して、この温度センサからの検出信号に基づいてヒータ
への通電を制御するためのコントローラが備えられてい
る。コントローラは、ソリッドステートリレー(以下、
SSRと呼ぶ)のような通電制御手段を介してヒータへ
の通電を制御する。すなわち、加熱シリンダの温度を安
定に保つために、温度センサを用いて加熱シリンダの温
度を計測し、その結果から、ヒータに流す電流をコント
ロールしているSSRをコントローラで制御し、温度を
制御するようにしている。
Heretofore, control of a heater arranged around a heating cylinder has been performed as follows. The heating cylinder is provided with a temperature sensor such as a thermocouple for detecting the temperature. A controller is provided for controlling energization of the heater based on a detection signal from the temperature sensor. The controller is a solid state relay (hereinafter
The power supply to the heater is controlled through power supply control means such as SSR. That is, in order to keep the temperature of the heating cylinder stable, the temperature of the heating cylinder is measured using a temperature sensor, and based on the result, the SSR controlling the current flowing through the heater is controlled by the controller to control the temperature. Like that.

【0009】しかし、温度条件が同じでロットの異なる
樹脂を用いた場合、前に述べたように、加熱シリンダ内
の樹脂の溶融状態の割合(せん断発熱による溶融とヒー
タ発熱による溶融との割合)が異なる。その結果、計量
回転時の計量モータのトルクが樹脂のロットにより異な
ってしまう。これに対して、従来は熟練技能者が成型品
の品質を確認しながら、加熱シリンダの温度設定を手動
で変えて対処しており、熟練を必要としていた。
However, when resins of different lots are used under the same temperature conditions, as described above, the ratio of the molten state of the resin in the heating cylinder (the ratio of the melting by shearing heat and the melting by heater heating). Are different. As a result, the torque of the weighing motor during the weighing rotation differs depending on the lot of the resin. Conventionally, a skilled technician has manually adjusted the temperature setting of the heating cylinder while checking the quality of the molded product, which required skill.

【0010】そこで、本発明の課題は、樹脂のせん断発
熱による溶融とヒータ発熱による溶融の割合を制御でき
るようにして、樹脂のロットによらずに計量モータのト
ルクを安定させることのできる射出成形機の制御方法を
提供することにある。
Accordingly, an object of the present invention is to provide an injection molding method capable of controlling the ratio of melting caused by heat generated by shearing of resin and melting caused by heating by a heater, thereby stabilizing the torque of a metering motor regardless of the resin lot. To provide a method of controlling the machine.

【0011】[0011]

【課題を解決するための手段】本発明による射出成形機
の制御方法は、加熱シリンダの周囲にヒータが配設され
ると共に、温度センサが設置され、前記温度センサから
の検出信号を受けて前記ヒータへの通電を通電制御手段
を介して制御するコントローラを備えた射出成形機にお
いて、あらかじめ良品が得られる時の計量モータのトル
クモデルを求めておき、前記コントローラは、実成形に
際しては、前記トルクモデルに近付くように前記通電制
御手段を制御し、しかも該通電制御手段は、実際の計量
モータのトルクが前記トルクモデルより大きい場合、前
記加熱シリンダの温度を上げるように制御し、実際の計
量モータのトルクが前記トルクモデルより小さい場合、
前記加熱シリンダの温度を下げるように制御することを
特徴とする。
According to a method of controlling an injection molding machine according to the present invention, a heater is provided around a heating cylinder, a temperature sensor is provided, and a detection signal is received from the temperature sensor. In an injection molding machine equipped with a controller for controlling energization of a heater via an energization control means, a torque model of a weighing motor for obtaining a good product is obtained in advance. The energization control means is controlled so as to approach the model, and the energization control means controls to increase the temperature of the heating cylinder when the actual torque of the weighing motor is larger than the torque model. Is smaller than the torque model,
The temperature of the heating cylinder is controlled to be lowered.

【0012】本制御方法においては、前記コントローラ
が、前記トルクモデルにおけるヒータによる発熱量と樹
脂のせん断発熱量との比率モデルを保存し、前記加熱シ
リンダの温度制御に際しては前記比率モデルに近付くよ
うに制御する。
In the present control method, the controller stores a ratio model of a heating value of the heater in the torque model and a shear heating value of the resin, and approaches the ratio model when controlling the temperature of the heating cylinder. Control.

【0013】本制御方法においてはまた、前記加熱シリ
ンダ内に樹脂が充填されしかもスクリュを回転させない
状態にて、前記ヒータにより発生される熱量と前記加熱
シリンダの温度との対応関係をあらかじめ計測してお
き、前記コントローラは、実成形において前記スクリュ
を回転させた状態にて得られる前記温度センサからの検
出信号を受け、前記通電制御手段により前記ヒータに与
えられた電流及び時間とに基づいて前記ヒータにより発
生される熱量を算出し、更に前記対応関係と算出された
熱量とに基づいて、実成形において検出された加熱シリ
ンダ温度とヒータの発熱による温度上昇分との差又は割
合を前記せん断発熱による温度上昇分として算出し、更
にロギングデータとして出力するようにしても良い。
In the present control method, the relationship between the amount of heat generated by the heater and the temperature of the heating cylinder is measured in advance in a state where the resin is filled in the heating cylinder and the screw is not rotated. The controller receives a detection signal from the temperature sensor obtained in a state where the screw is rotated in actual molding, and controls the heater based on a current and time given to the heater by the power supply control unit. Calculate the amount of heat generated by the above, further based on the corresponding relationship and the calculated amount of heat, the difference or ratio between the heating cylinder temperature detected in the actual molding and the temperature rise due to the heat generated by the heater is calculated by the shear heat. It may be calculated as a temperature rise and output as logging data.

【0014】前記通電制御手段はソリッドステートリレ
ーで実現することができる。
The power supply control means can be realized by a solid state relay.

【0015】前記算出された差又は割合は成型品の品質
情報として記録あるいは表示するようにされても良い。
[0015] The calculated difference or ratio may be recorded or displayed as quality information of the molded product.

【0016】[0016]

【発明の実施の形態】図1を参照して、本発明の実施の
形態について説明する。図1において、加熱シリンダ1
0の周囲にはヒータ11が配設されている。図1ではヒ
ータ11は象徴的に1個のみ示しているが、実際には加
熱シリンダ10の軸方向に間隔をおいて複数箇所に設置
される。ヒータ11には、その温度を加熱シリンダ10
の温度として検出するために熱電対等による温度センサ
12が設置されている。そして、温度センサ12からの
検出信号及び後述する情報に基づいてヒータ11への通
電を制御するためのコントローラ13が備えられてい
る。コントローラ13は、SSRによる通電制御部14
を介してヒータ11への通電を制御する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG. In FIG. 1, a heating cylinder 1
A heater 11 is provided around 0. Although only one heater 11 is shown symbolically in FIG. 1, actually, the heater 11 is installed at a plurality of locations at intervals in the axial direction of the heating cylinder 10. The heater 11 is supplied with the temperature of the heating cylinder 10.
A temperature sensor 12 such as a thermocouple is provided to detect the temperature as a temperature. Further, a controller 13 is provided for controlling energization of the heater 11 based on a detection signal from the temperature sensor 12 and information described later. The controller 13 includes a power supply control unit 14 based on the SSR.
The power supply to the heater 11 is controlled via the.

【0017】本発明による制御方法は以下のようにして
実行される。
The control method according to the present invention is executed as follows.

【0018】(1)条件出し作業において良品が得られ
た時の計量モータのトルクモデルをあらかじめ基準モデ
ルとして求めておく。この基準モデルは、1ショット当
たりのスクリュ位置と計量モータのトルクとの対応関係
を示しており、コントローラ13内のメモリに保存され
る。また、基準のトルクモデルにおけるヒータによる発
熱量と樹脂のせん断発熱量との比率モデルを求めてお
く。この比率モデルは、1ショット当たりのスクリュ位
置に対する前記ヒータによる発熱量と樹脂のせん断発熱
量の比率を示しており、コントローラ13内のメモリに
保存される。なお、スクリュ位置は既設のスクリュ位置
センサで知ることができ、計量モータのトルクは供給さ
れる電流値から算出することができる。
(1) A torque model of the weighing motor when a non-defective product is obtained in the condition setting work is obtained in advance as a reference model. This reference model indicates the correspondence between the screw position per shot and the torque of the metering motor, and is stored in a memory in the controller 13. In addition, a ratio model of the calorific value of the heater and the shear calorific value of the resin in the reference torque model is obtained in advance. This ratio model indicates the ratio between the amount of heat generated by the heater and the amount of heat generated by shearing the resin with respect to the screw position per shot, and is stored in the memory in the controller 13. Note that the screw position can be known by an existing screw position sensor, and the torque of the metering motor can be calculated from the supplied current value.

【0019】図2は求められた基準モデルの一例を示
す。
FIG. 2 shows an example of the obtained reference model.

【0020】(2)コントローラ13は、実成形に際し
ては、上記の基準モデルに近付くように通電制御部14
を制御する。図3は、実成形における1ショット当たり
のスクリュ位置と計量モータのトルクとの対応関係の一
例を示している。前に述べた理由で、実際のスクリュ位
置と計量モータのトルクとの対応関係と、図2に示され
た基準モデルとの間には差が生じる。コントローラ13
は、1ショットの間にスクリュ位置センサから得られる
スクリュ位置と計量モータの電流値をサンプリングして
電流値からトルクを算出し、スクリュ位置と計量モータ
のトルクとの対応関係を基準モデルと比較する。そし
て、実際の対応関係と基準モデルとの間の差を無くすよ
うに通電部14を制御する。
(2) During actual molding, the controller 13 controls the energization control unit 14 so as to approach the reference model.
Control. FIG. 3 shows an example of the correspondence between the screw position per shot and the torque of the metering motor in actual molding. For the reasons mentioned above, there is a difference between the correspondence between the actual screw position and the torque of the metering motor and the reference model shown in FIG. Controller 13
Samples the screw position obtained from the screw position sensor and the current value of the metering motor during one shot, calculates the torque from the current value, and compares the correspondence between the screw position and the torque of the metering motor with the reference model. . Then, the power supply unit 14 is controlled so as to eliminate the difference between the actual correspondence and the reference model.

【0021】例えば、実際の計量モータのトルクが基準
モデルにおけるトルクより高めであった場合には、樹脂
の溶融を促進するためにヒータ11による発熱量を増や
すように制御する。これは、基準トルクより実際のトル
クが高いということは、樹脂の溶融が促進されていない
ということであり、この場合、ヒータ11の発熱量を増
して樹脂の溶融を促進させる。一方、基準トルクより実
際のトルクが低い場合には、樹脂の溶融が促進されすぎ
てサラサラの状態になっている可能性が大であるので、
ヒータ11の発熱量を下げるか、ヒータ11への電力供
給を遮断する。但し、ヒータ11の発熱量をむやみに変
動させることは、せん断発熱による溶融とヒータ発熱に
よる溶融のバランスをくずすことになるので、これらの
割合を考慮して通電制御部14に対する制御を行う。
For example, when the actual torque of the metering motor is higher than that of the reference model, control is performed so as to increase the amount of heat generated by the heater 11 in order to promote melting of the resin. The fact that the actual torque is higher than the reference torque means that the melting of the resin is not promoted. In this case, the amount of heat generated by the heater 11 is increased to promote the melting of the resin. On the other hand, if the actual torque is lower than the reference torque, it is highly possible that the melting of the resin is promoted too much and the resin is in a smooth state.
The amount of heat generated by the heater 11 is reduced, or power supply to the heater 11 is cut off. However, if the calorific value of the heater 11 is fluctuated unnecessarily, the balance between the melting caused by the shearing heat and the melting caused by the heating of the heater is lost.

【0022】すなわち、上記の制御に際しては、通電制
御部14に対する制御ゲインを、前記比率モデルから加
熱シリンダ10内の樹脂のせん断発熱量とヒータ11の
発熱量の割合を求めてその割合に近付くように制御す
る。
That is, in the above-mentioned control, the control gain for the power supply control unit 14 is set so as to approach the ratio by calculating the ratio of the shear heating value of the resin in the heating cylinder 10 to the heating value of the heater 11 from the ratio model. To control.

【0023】せん断発熱による温度上昇分の算出は以下
のようにして行われる。
Calculation of the temperature rise due to shear heat is performed as follows.

【0024】(A)あらかじめ、せん断発熱させない場
合、すなわち加熱シリンダ10内に樹脂を充填ししかも
スクリュを回転させない場合における、ヒータ11によ
り発生される熱量(ヒータに流れる電流値と通電時間と
により算出される)とヒータ11における温度上昇、す
なわち加熱シリンダ10の温度上昇(温度センサ12の
検出値)との対応関係を求めておく。この対応関係もコ
ントローラ13内のメモリに保存される。図4は、上記
の対応関係の一例を示す。
(A) The amount of heat generated by the heater 11 (calculated from the value of the current flowing through the heater and the energizing time) when no shear heat is generated in advance, that is, when the resin is filled in the heating cylinder 10 and the screw is not rotated. ) And the temperature rise in the heater 11, that is, the temperature rise of the heating cylinder 10 (the value detected by the temperature sensor 12) is determined in advance. This correspondence is also stored in the memory in the controller 13. FIG. 4 shows an example of the above correspondence.

【0025】(B)実成形に入ると、コントローラ13
は温度センサ12による検出温度をサンプリングして記
憶すると共に、ヒータ11に流される電流とその時間と
によりヒータ11で発生される熱量を上記サンプリング
周期で算出して記憶する。
(B) When the actual molding starts, the controller 13
Samples the temperature detected by the temperature sensor 12 and stores it, and calculates and stores the amount of heat generated by the heater 11 based on the current flowing through the heater 11 and the time thereof in the sampling cycle.

【0026】(C)コントローラ13は更に、上記
(A)、(B)で得られた情報、すなわち前記対応関係
と算出された熱量とに基づいて、実成形において検出さ
れた加熱シリンダ温度とヒータ11の発熱による温度上
昇分との差又は割合をせん断発熱による温度上昇分とし
て算出して出力する。これはプリンタにより記録した
り、ディスプレイにて表示することができる。
(C) The controller 13 further calculates the heating cylinder temperature and the heater temperature detected in the actual molding on the basis of the information obtained in (A) and (B) above, that is, the correspondence and the calculated heat quantity. The difference or ratio from the temperature rise due to the heat generation of No. 11 is calculated and output as the temperature rise due to the shear heat. This can be recorded by a printer or displayed on a display.

【0027】図5には、実際の加熱シリンダ10の温度
上昇(せん断発熱よる上昇分を含む)とヒータ11の発
熱量との関係の一例を示す。ここで、図5に示されたあ
るヒータ発熱量での加熱シリンダ温度と、図4に示され
た上記あるヒータ発熱量での加熱シリンダ温度との差又
は割合が、せん断発熱によるものであることは明らかで
ある。
FIG. 5 shows an example of the relationship between the actual temperature rise of the heating cylinder 10 (including the rise due to shear heat generation) and the amount of heat generated by the heater 11. Here, the difference or ratio between the heating cylinder temperature at a certain heater heating value shown in FIG. 5 and the heating cylinder temperature at the certain heater heating value shown in FIG. 4 is due to shear heating. Is clear.

【0028】このようにして、上記の対応関係からせん
断発熱分を知ることができ、その推移を知ることもでき
る。これは、樹脂の溶融状態を左右しているせん断発熱
とヒータ11の発熱との割合の変化の推移が分かること
を意味する。せん断発熱分の推移は、コントローラ13
から成型品の品質情報の1つとして出力される。
In this way, the shear heat generation can be known from the above-mentioned correspondence, and its transition can also be known. This means that the change in the ratio between the shear heat and the heat generated by the heater 11 that determines the molten state of the resin can be understood. The change in the amount of shear heat is determined by the controller 13.
Is output as one of the quality information of the molded product.

【0029】(D)上記のようにして、せん断発熱量と
ヒータによる発熱量とを求め、それらを前記比率モデル
に近付くように制御ゲインによってヒータ11への通電
が制御されることにより、樹脂のせん断発熱による溶融
とヒータ11の発熱による溶融の割合が制御される。そ
の結果、樹脂のロットが変わっても樹脂の溶融状態が安
定し、計量モータのトルクが基準モデルに近付いて安定
する。
(D) As described above, the amount of heat generated by the shear and the amount of heat generated by the heater are determined, and the energization to the heater 11 is controlled by the control gain so as to approach the ratio model. The ratio of melting due to shear heat and melting due to heat generated by the heater 11 is controlled. As a result, even if the lot of the resin changes, the molten state of the resin is stabilized, and the torque of the metering motor approaches the reference model and stabilizes.

【0030】本形態によれば、加熱シリンダ10の温度
とヒータ11に流す電流を調整している通電制御部14
の出力とにより、加熱シリンダ10の温度上昇における
せん断発熱の割合がわかる。よって、コントローラ13
の出力により、せん断発熱の推移がわかり、樹脂の溶融
状態の推移を知ることができると共に、成型品の品質情
報として出力することができる。勿論、上記(1)、
(3)、(A)〜(C)におけるヒータ11の温度設定
条件は同じである。
According to the present embodiment, the energization control unit 14 that adjusts the temperature of the heating cylinder 10 and the current flowing through the heater 11
The output of (1) indicates the ratio of the shear heat generated when the temperature of the heating cylinder 10 rises. Therefore, the controller 13
With the output of (1), the transition of the heat generated by shearing can be known, the transition of the molten state of the resin can be known, and the quality information of the molded product can be output. Of course, the above (1),
(3) The temperature setting conditions of the heater 11 in (A) to (C) are the same.

【0031】なお、コントローラ13は、射出成形機本
体を制御するために備えられている制御装置で実現する
こともできるし、この制御装置とは別に専用に備えられ
ても良い。また、本発明は、計量回転モータが電動の油
圧式、電動式のいずれのタイプの射出成形機にも適用で
きることは言うまでも無い。
The controller 13 can be realized by a control device provided for controlling the main body of the injection molding machine, or can be provided separately from the control device. In addition, it goes without saying that the present invention can be applied to any type of injection molding machine in which the metering rotation motor is an electric hydraulic type or an electric type.

【0032】[0032]

【発明の効果】本発明によれば、樹脂のロットが変わっ
ても加熱シリンダにおけるヒータによる樹脂溶融とせん
断発熱による樹脂溶融との割合を安定させることができ
て樹脂の溶融状態を均一にすることができるので、計量
モータのトルクが安定し、もって成型品の品質のばらつ
きを無くすことができる。また、せん断発熱の推移もロ
ギングデータとして知ることができる。
According to the present invention, even if the lot of the resin changes, the ratio of the melting of the resin by the heater in the heating cylinder and the melting of the resin by the shear heat can be stabilized, and the molten state of the resin can be made uniform. As a result, the torque of the weighing motor is stabilized, and the variation in the quality of the molded product can be eliminated. Also, the transition of the shear heat can be known as logging data.

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

【図1】本発明による制御方法を実施するための構成を
示したブロック図である。
FIG. 1 is a block diagram showing a configuration for implementing a control method according to the present invention.

【図2】本発明において求められる計量モータのトルク
とスクリュ位置との関係の基準モデルの一例を示した図
である。
FIG. 2 is a diagram showing an example of a reference model of a relationship between a torque of a metering motor and a screw position obtained in the present invention.

【図3】実成形における計量モータのトルクとスクリュ
位置との対応関係の実際の例を示した図である。
FIG. 3 is a diagram showing an actual example of a correspondence relationship between a torque of a metering motor and a screw position in actual molding.

【図4】スクリュを回転させずヒータのみの発熱で樹脂
の溶融を行った場合のヒータ発熱量と加熱シリンダ温度
との関係を示した図である。
FIG. 4 is a diagram showing a relationship between a heating value of a heater and a heating cylinder temperature in a case where a resin is melted only by a heater without rotating a screw.

【図5】スクリュを回転させてせん断発熱とヒータの発
熱で樹脂の溶融を行った場合のヒータ発熱量と加熱シリ
ンダ温度との関係を示した図である。
FIG. 5 is a diagram showing a relationship between a heating value of a heater and a heating cylinder temperature when a resin is melted by shearing heat generation and heat generation of a heater by rotating a screw.

【符号の説明】[Explanation of symbols]

10 加熱シリンダ 11 ヒータ 12 温度センサ 13 コントローラ 14 通電制御部 Reference Signs List 10 heating cylinder 11 heater 12 temperature sensor 13 controller 14 energization control unit

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 加熱シリンダの周囲にヒータが配設され
ると共に、温度センサが設置され、前記温度センサから
の検出信号を受けて前記ヒータへの通電を通電制御手段
を介して制御するコントローラを備えた射出成形機にお
いて、 あらかじめ良品が得られる時の計量モータのトルクモデ
ルを求めておき、 前記コントローラは、実成形に際しては、前記トルクモ
デルに近付くように前記通電制御手段を制御し、しかも
該通電制御手段は、実際の計量モータのトルクが前記ト
ルクモデルより大きい場合、前記加熱シリンダの温度を
上げるように制御し、実際の計量モータのトルクが前記
トルクモデルより小さい場合、前記加熱シリンダの温度
を下げるように制御することを特徴とする射出成形機の
制御方法。
A heater is provided around a heating cylinder, a temperature sensor is provided, and a controller that receives a detection signal from the temperature sensor and controls energization to the heater through energization control means is provided. In the injection molding machine provided, a torque model of a weighing motor when a good product is obtained is obtained in advance, and the controller controls the energization control means so as to approach the torque model at the time of actual molding. The energization control means controls to increase the temperature of the heating cylinder when the actual torque of the weighing motor is larger than the torque model, and controls the temperature of the heating cylinder when the actual torque of the weighing motor is smaller than the torque model. A method for controlling an injection molding machine, characterized in that control is performed so as to reduce the pressure.
【請求項2】 請求項1記載の射出成形機の制御方法に
おいて、前記コントローラは、前記トルクモデルにおけ
るヒータによる発熱量と樹脂のせん断発熱量との比率モ
デルを保存しており、前記加熱シリンダの温度制御に際
しては前記比率モデルに近付くように制御することを特
徴とする射出成形機の制御方法。
2. The method for controlling an injection molding machine according to claim 1, wherein the controller stores a ratio model between a heating value of the heater in the torque model and a shear heating value of the resin in the torque model. A method for controlling an injection molding machine, wherein temperature control is performed so as to approach the ratio model.
【請求項3】 請求項1記載の射出成形機の制御方法に
おいて、 前記加熱シリンダ内に樹脂が充填されしかもスクリュを
回転させない状態にて、前記ヒータにより発生される熱
量と前記加熱シリンダの温度との対応関係をあらかじめ
計測しておき、 前記コントローラは、実成形において前記スクリュを回
転させた状態にて得られる前記温度センサからの検出信
号を受け、前記通電制御手段により前記ヒータに与えら
れた電流及び時間とに基づいて前記ヒータにより発生さ
れる熱量を算出し、更に前記対応関係と算出された熱量
とに基づいて、実成形において検出された加熱シリンダ
温度とヒータの発熱による温度上昇分との差又は割合を
前記せん断発熱による温度上昇分として算出し、更にロ
ギングデータとして出力することを特徴とする射出成形
機の制御方法。
3. The control method for an injection molding machine according to claim 1, wherein the amount of heat generated by the heater, the temperature of the heating cylinder and the temperature of the heating cylinder are set in a state in which the heating cylinder is filled with resin and the screw is not rotated. The controller receives a detection signal from the temperature sensor obtained in a state where the screw is rotated in actual molding, receives a detection signal from the temperature sensor, and supplies a current supplied to the heater by the energization control unit. And the amount of heat generated by the heater based on the time, and further, based on the correspondence and the calculated amount of heat, the heating cylinder temperature detected in actual molding and the temperature rise due to the heat generated by the heater. The difference or ratio is calculated as a temperature rise due to the shear heating, and further output as logging data. Control method for a molding machine.
【請求項4】 請求項2あるいは3記載の射出成形機の
制御方法において、前記通電制御手段はソリッドステー
トリレーであることを特徴とする射出成形機の制御方
法。
4. The control method for an injection molding machine according to claim 2, wherein said energization control means is a solid state relay.
【請求項5】 請求項3記載の射出成形機の制御方法に
おいて、前記算出された差又は割合を成型品の品質情報
として記録あるいは表示することを特徴とする射出成形
機の制御方法。
5. The control method for an injection molding machine according to claim 3, wherein the calculated difference or ratio is recorded or displayed as quality information of a molded product.
JP2000072330A 2000-03-15 2000-03-15 Control method of injection molding machine Expired - Fee Related JP3794610B2 (en)

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Publication number Priority date Publication date Assignee Title
US7261538B2 (en) 2003-02-24 2007-08-28 Fanuc Ltd Monitoring device for an injection molding machine
JP2008290464A (en) * 2008-09-08 2008-12-04 Sumitomo Heavy Ind Ltd Injection molding machine and its temperature monitoring method
JP2009137083A (en) * 2007-12-04 2009-06-25 Sumitomo Heavy Ind Ltd Temperature display device for injection molding machine
JP2010228303A (en) * 2009-03-27 2010-10-14 Nissei Plastics Ind Co Controller of injection molding machine
EP2447034A1 (en) * 2010-10-27 2012-05-02 Sumitomo Heavy Industries, Ltd. Injection moulding machine comprising an energy consumption detecting part
JP2015020344A (en) * 2013-07-19 2015-02-02 宇部興産機械株式会社 Control method for measuring process of injection molding machine
DE102018122693A1 (en) 2017-09-25 2019-03-28 Engel Austria Gmbh Shaping machine with a plasticizing unit
CN115139481A (en) * 2021-03-31 2022-10-04 住友重机械工业株式会社 Injection molding machine, control device for injection molding machine, and control method for injection molding machine

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7261538B2 (en) 2003-02-24 2007-08-28 Fanuc Ltd Monitoring device for an injection molding machine
JP2009137083A (en) * 2007-12-04 2009-06-25 Sumitomo Heavy Ind Ltd Temperature display device for injection molding machine
JP2008290464A (en) * 2008-09-08 2008-12-04 Sumitomo Heavy Ind Ltd Injection molding machine and its temperature monitoring method
JP4638533B2 (en) * 2008-09-08 2011-02-23 住友重機械工業株式会社 Injection molding machine and temperature monitoring method thereof
JP2010228303A (en) * 2009-03-27 2010-10-14 Nissei Plastics Ind Co Controller of injection molding machine
EP2447034A1 (en) * 2010-10-27 2012-05-02 Sumitomo Heavy Industries, Ltd. Injection moulding machine comprising an energy consumption detecting part
JP2015020344A (en) * 2013-07-19 2015-02-02 宇部興産機械株式会社 Control method for measuring process of injection molding machine
DE102018122693A1 (en) 2017-09-25 2019-03-28 Engel Austria Gmbh Shaping machine with a plasticizing unit
AT520465A1 (en) * 2017-09-25 2019-04-15 Engel Austria Gmbh Shaping machine with a plasticizing unit
AT520465B1 (en) * 2017-09-25 2019-10-15 Engel Austria Gmbh Shaping machine with a plasticizing unit
CN115139481A (en) * 2021-03-31 2022-10-04 住友重机械工业株式会社 Injection molding machine, control device for injection molding machine, and control method for injection molding machine

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