JPH0494915A - Control method for injection molding machine - Google Patents
Control method for injection molding machineInfo
- Publication number
- JPH0494915A JPH0494915A JP21205990A JP21205990A JPH0494915A JP H0494915 A JPH0494915 A JP H0494915A JP 21205990 A JP21205990 A JP 21205990A JP 21205990 A JP21205990 A JP 21205990A JP H0494915 A JPH0494915 A JP H0494915A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- injection molding
- molding machine
- controlling
- heating
- 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
Links
- 238000001746 injection moulding Methods 0.000 title claims description 25
- 238000000034 method Methods 0.000 title claims description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 59
- 239000000463 material Substances 0.000 claims abstract description 53
- 239000011347 resin Substances 0.000 claims abstract description 31
- 229920005989 resin Polymers 0.000 claims abstract description 31
- 230000007246 mechanism Effects 0.000 claims abstract description 26
- 238000000465 moulding Methods 0.000 claims abstract description 11
- 230000008859 change Effects 0.000 claims description 9
- 238000012545 processing Methods 0.000 claims description 9
- 230000005856 abnormality Effects 0.000 claims description 6
- 238000012544 monitoring process Methods 0.000 abstract description 2
- 230000001360 synchronised effect Effects 0.000 abstract 1
- 230000007423 decrease Effects 0.000 description 11
- 238000005259 measurement Methods 0.000 description 8
- 230000001276 controlling effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 230000000875 corresponding effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はスクリュを内蔵し、かつ後部に材料供給機構を
有する加熱筒を備えてなる射出成形機の制御方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method of controlling an injection molding machine equipped with a heating cylinder incorporating a screw and having a material supply mechanism at the rear thereof.
射出成形機における加熱筒内の樹脂状態(樹脂温度、樹
脂量、流動性等)を常に最適な状態に維持することは、
成形品質を高める上でも重要である。Maintaining the optimal resin condition (resin temperature, resin amount, fluidity, etc.) inside the heating cylinder of an injection molding machine is
It is also important for improving molding quality.
ところで、樹脂は加熱筒内においてスクリュの回転によ
り移送されるため、上述した樹脂状態を正確に把握し、
かつ的確に制御することは容易でない。例えば、加熱筒
の加熱ゾーンは前後方向に複数に分割され、また、各加
熱ゾーン毎に異なる温度が設定されるが、温度の検出は
各加熱ゾーンの位置に対応して付設した温度センサによ
り個別に行われるため、実際の樹脂温度を把握しにくい
とともに、各加熱ゾーンの温度は一義的に定まらない。By the way, since the resin is transferred inside the heating cylinder by the rotation of the screw, it is necessary to accurately grasp the state of the resin as described above.
And it is not easy to control accurately. For example, the heating zone of a heating tube is divided into multiple sections in the front and back direction, and a different temperature is set for each heating zone, but the temperature is detected individually by a temperature sensor attached to the position of each heating zone. Since the heating is carried out at different times, it is difficult to grasp the actual resin temperature, and the temperature of each heating zone cannot be uniquely determined.
結局、従来は作業者(オペレータ)が全体の成形状態等
を頼りに、専ら経験と勘によって調節しているのが実情
であり、正確な設定を行うことができないばかりでなく
、多大な時間と労力が費やされ、しかも、樹脂温度は加
熱筒落下前の材料温度、樹脂量、スクリュ回転数等の他
の各種制御要素にも左右されるため、樹脂温度、さらに
は樹脂状態を最適な状態に維持することが困難であると
いう問題があった。In the end, in the past, operators relied on the overall molding condition and made adjustments based solely on their experience and intuition, which not only made it impossible to make accurate settings, but also took a lot of time and effort. This requires a lot of effort, and since the resin temperature also depends on various other control factors such as the material temperature before the heating tube falls, the amount of resin, and the number of screw rotations, it is difficult to keep the resin temperature and even the resin condition at the optimum state. The problem was that it was difficult to maintain the
本発明はこのような従来技術に存在する課題を解決した
もので、加熱筒内における最適な樹脂状態を容易かつ確
実に設定できる射出成形機の制御方法の提供を目的とす
るものである。The present invention solves the problems that exist in the prior art, and aims to provide a control method for an injection molding machine that can easily and reliably set the optimum resin condition within the heating cylinder.
本発明に係る射出成形機の制御方法は、スクリュ2を内
蔵し、かつ後部に材料供給機構6を有する加熱筒3を備
えてなる射出成形機lを制御するに際して、加熱筒3に
臨む材料供給機構6の材料落下ロア付近の温度状態を検
出し、検出した温度状態に基づいて、樹脂状態に影響を
与える制御要素、例えば材料供給機構6における材料供
給量、加熱筒3における複数の加熱ゾーンの加熱温度、
材料供給機構6における加熱温度、スクリュ2の回転数
及び/又は背圧等を可変制御するようにしたことを特徴
とする。この場合、複数の制御要素に対して優先順位を
設定し、優先順位に従って順次制御することができる。The method for controlling an injection molding machine according to the present invention is to supply material facing the heating cylinder 3 when controlling an injection molding machine 1 comprising a heating cylinder 3 having a built-in screw 2 and a material supply mechanism 6 at the rear. The temperature state near the material dropping lower of the mechanism 6 is detected, and based on the detected temperature state, control elements that affect the resin state, such as the amount of material supplied in the material supply mechanism 6 and the number of heating zones in the heating cylinder 3, are controlled. Heating temperature,
It is characterized in that the heating temperature in the material supply mechanism 6, the rotation speed of the screw 2, the back pressure, etc. are variably controlled. In this case, it is possible to set priorities for a plurality of control elements and sequentially control them according to the priorities.
本発明に係る射出成形機1の制御方法によれば、温度セ
ンサ5等によって加熱筒3内に臨む材料供給機構6の材
料落下ロア付近の温度状態を検出する。材料落下ロア付
近の温度特性は、正常時には成形サイクルに同期して周
期的に昇降、即ち、計量時に上昇し、計量時以外に下降
する温度変化を繰返す。したがって、例えば、変動する
温度変化の振幅の大きさ等の温度状態を監視すれば、温
度特性の異常を検出できることになる。この場合、可塑
化の初期状態を検出するため、樹脂状態を早期に検出で
きる。According to the control method for the injection molding machine 1 according to the present invention, the temperature state near the material dropping lower of the material supply mechanism 6 facing into the heating cylinder 3 is detected by the temperature sensor 5 or the like. Under normal conditions, the temperature characteristics near the material drop lower periodically rise and fall in synchronization with the molding cycle, that is, the temperature repeats changes in which it rises during measurement and falls at times other than measurement. Therefore, for example, by monitoring the temperature state such as the magnitude of the amplitude of a fluctuating temperature change, it is possible to detect an abnormality in the temperature characteristics. In this case, since the initial state of plasticization is detected, the state of the resin can be detected early.
よって、得られた温度状態は、例えば、予め設定した目
標値或はモニタ範囲と比較し、この比較偏差に基づいて
樹脂状態に影響を与える制御要素、例えば材料供給機構
6における材料供給量、加熱筒3における複数の加熱ゾ
ーンの加熱温度、材料供給機構6における加熱温度、ス
クリュ2の回転数及び/又は背圧等を可変し、最適な樹
脂状態となるように予め設定した優先順位に従って各制
御要素を順次制御する。Therefore, the obtained temperature state is compared with, for example, a preset target value or a monitor range, and based on this comparison deviation, control elements that affect the resin state, such as the material supply amount in the material supply mechanism 6, heating The heating temperature of the plurality of heating zones in the cylinder 3, the heating temperature in the material supply mechanism 6, the rotation speed and/or back pressure of the screw 2, etc. are varied, and each control is performed according to preset priorities to achieve the optimal resin state. Control elements sequentially.
以下には、本発明に係る好適な実施例を挙げ、図面に基
づき詳細に説明する。Hereinafter, preferred embodiments of the present invention will be described in detail based on the drawings.
まず、本発明に係る制御方法を実施できるベント式射出
成形機及びその制御系の構成について第1図を参照して
説明する。First, the configuration of a vent type injection molding machine and its control system that can implement the control method according to the present invention will be explained with reference to FIG.
1はベント式射出成形機であり、金型側を除く射出装置
Isを示す。射出装置Isは前端に射出ノズル11を有
する加熱筒3を備え、加熱筒3にはその後端に設けたス
クリュ駆動機構部12により回転制御及び進退移動制御
されるスクリュ2を内蔵する。また、加熱筒3の軸方向
中間位置であって、その上部にはベント孔4を設ける。1 is a vent type injection molding machine, and shows the injection device Is excluding the mold side. The injection device Is includes a heating cylinder 3 having an injection nozzle 11 at its front end, and the heating cylinder 3 houses a screw 2 whose rotation and movement are controlled by a screw drive mechanism 12 provided at its rear end. Further, a vent hole 4 is provided at an axially intermediate position of the heating cylinder 3 and at an upper portion thereof.
このベント孔4により加熱筒3の内部と外部が連通し、
スクリュ2の回転により可塑化溶融された樹脂から発生
する水蒸気やガス成分は外部に排出される。This vent hole 4 communicates the inside and outside of the heating cylinder 3,
As the screw 2 rotates, water vapor and gas components generated from the plasticized and melted resin are discharged to the outside.
さらにまた、加熱筒3は前後方向五つに分割した加熱ゾ
ーンを備え、各加熱ゾーンに対応する加熱筒3の外周に
は、当該加熱筒3を加熱するバンドヒータ13a、13
bS 13c113d、13eを取付ける。一方、加熱
筒3の後部には材料供給機構6を設ける。この材料供給
機構6は加熱筒3の内部に連通ずる供給管14と、この
供給管14に連通ずるホッパー15と、このホッパー1
5の下方に設けた移送スクリュ16a及び同スクリュ1
6aを回転制御する移送スクリュ駆動部16bからなる
材料供給制御装置16を備えるとともに、供給管14の
外周には当該供給管14を加熱するバンドヒータ17a
、17b・・・を設ける。Furthermore, the heating tube 3 is provided with heating zones divided into five in the front and back direction, and band heaters 13a and 13 are provided on the outer periphery of the heating tube 3 corresponding to each heating zone to heat the heating tube 3.
bS Install 13c113d and 13e. On the other hand, a material supply mechanism 6 is provided at the rear of the heating cylinder 3. This material supply mechanism 6 includes a supply pipe 14 that communicates with the inside of the heating cylinder 3, a hopper 15 that communicates with this supply pipe 14, and this hopper 1.
Transfer screw 16a provided below 5 and the same screw 1
A material supply control device 16 is provided that includes a transfer screw drive unit 16b that controls the rotation of the supply pipe 6a, and a band heater 17a that heats the supply pipe 14 is provided on the outer periphery of the supply pipe 14.
, 17b... are provided.
また、加熱筒3に臨む材料供給機構6の材料落下ロアの
近傍(前方)には温度センサ5を付設する。Further, a temperature sensor 5 is attached near (in front of) the material dropping lower of the material supply mechanism 6 facing the heating cylinder 3.
そして、温度センサ5は温度処理部21に接続し、同処
理部21は演算部22に接続するとともに、演算部22
は直接及び異常判定回路25を介してコントローラ23
に接続する。The temperature sensor 5 is connected to the temperature processing section 21, and the processing section 21 is connected to the calculation section 22.
controller 23 directly and via the abnormality determination circuit 25
Connect to.
一方、加熱筒3の所定位置には各加熱ゾーンにおける加
熱温度を検出する温度センサ24a、24b、24c・
・・を取付けるとともに、その出力側はコントローラ2
3に接続する。また、コントローラ23には前記バンド
ヒータ13a・・・ 17a・・・、スクリュ駆動機構
部12、移送スクリュ駆動部16bもそれぞれ接続する
。On the other hand, temperature sensors 24a, 24b, 24c, and
..., and its output side is connected to controller 2.
Connect to 3. Further, the band heaters 13a, . . . , 17a, . . . , the screw drive mechanism section 12, and the transfer screw drive section 16b are also connected to the controller 23, respectively.
次に、本発明に係るベント式射出成形機lの制御方法に
ついて、第1図〜第6図を参照して説明する。Next, a method of controlling the vent type injection molding machine 1 according to the present invention will be explained with reference to FIGS. 1 to 6.
まず、所定の成形サイクル中において、材料落下ロア付
近の温度は、温度センサ5により検出される。この場合
、検出温度は第4図に示すように正常時には成形サイク
ルに同期して周期的に昇降を繰返す。即ち、計量時には
成形材料の摩擦発熱により温度が上昇し、計量時以外に
は発熱要素が無くなり温度は下降する。なお、第4図に
おいて、8点は成形開始点、Cは一成形サイクル、Pは
温度変化の振幅をそれぞれ示す。First, during a predetermined molding cycle, the temperature near the material dropping lower is detected by the temperature sensor 5. In this case, as shown in FIG. 4, under normal conditions, the detected temperature repeatedly rises and falls in synchronization with the molding cycle. That is, at the time of measurement, the temperature rises due to frictional heat generation of the molding material, and at times other than the time of measurement, there is no heat generating element and the temperature decreases. In FIG. 4, 8 points indicate the starting point of molding, C indicates one molding cycle, and P indicates the amplitude of temperature change.
一方、温度センサ5により検出された検出信号は、温度
処理部21に付与され、例えば、成形サイクル毎におけ
る温度変化の振幅Pが求められる。On the other hand, the detection signal detected by the temperature sensor 5 is provided to the temperature processing section 21, and, for example, the amplitude P of the temperature change in each molding cycle is determined.
そして、温度処理部21の出力は演算部22に付与され
る。演算部22は温度変化の振幅P(或は検出された温
度T等)と予め設定した目標値(或はモニタ範囲、限界
値等)と比較し、得られた比較偏差により、所定の制御
要素、即ち、加熱筒3における各加熱ゾーンの加熱温度
、材料供給機構6の材料供給量及び供給管14の加熱温
度、スクリュ2の回転数及び/又は背圧に対する制御情
報を演算し、コントローラ23に付与する。よって、コ
ントローラ23は当該制御情報に基づいて、所定の制御
信号を加熱筒3の各バンドヒータ13a、13b・・・
、材料供給機構6における材料供給制御袋4116及び
バンドヒータ17a・・・、スクリュ駆動機構部12に
供給する。The output of the temperature processing section 21 is then given to the calculation section 22. The calculation unit 22 compares the amplitude P of the temperature change (or detected temperature T, etc.) with a preset target value (or monitor range, limit value, etc.), and uses the obtained comparison deviation to control a predetermined control element. That is, the control information for the heating temperature of each heating zone in the heating cylinder 3, the material supply amount of the material supply mechanism 6 and the heating temperature of the supply pipe 14, the rotation speed and/or back pressure of the screw 2 is calculated, and the control information is sent to the controller 23. Give. Therefore, the controller 23 sends a predetermined control signal to each band heater 13a, 13b, . . . of the heating tube 3 based on the control information.
, the material supply control bag 4116 and the band heater 17a in the material supply mechanism 6, and the screw drive mechanism section 12.
ところで、この場合、演算部22では第2図又は第3図
に示す制御パターンに従って制御要素の決定、制御量の
演算を行う。まず、第2図のように、温度処理部21か
ら得る温度変化の振幅Pの大きさが、目標値と比較して
、「■振幅が小さい」、「■振幅が大きい」、「■振幅
がばらつく」の各態様となった場合、これに対応して、
「&加熱筒の温度を上げる」、「b加熱筒の温度を下げ
る」、「C計量時のスクリュ回転数を上げる」、「d計
量時のスクリュ回転数を下げる」、「e背圧を上げる」
、「f背圧を下げる」、「g材料供給量を多くする」、
「h材料供給量を少なくする」、[i材料供給温度を上
げる」、「j材料供給温度を下げる」の各制御を第2図
中の接続線と優先順位に従って実行するための制御情報
をコントローラ23に付与する。これにより、例えば、
温度変化の振幅Pが第5図中、E2で示すように小さい
場合(Eoが正常)、第2図中、「■振幅が小さい」に
該当し、この場合には、まず、「b加熱筒の温度を下げ
る」ように制御する(優先順位1)。また、この制御に
よっても改善されずに温度変化の振幅が大きくならない
場合、次に、「g材料供給量を多くする」ように制御す
る(優先順位2)。このような制御は改善されるまで、
優先順位にしたがって順次行われる。なお、予め設定し
た制御要素を全て制御した後、所定時間経過しても改善
されない場合には、異常処理、即ち、警報の発生、運転
の停止等の制御を行う。Incidentally, in this case, the calculation section 22 determines the control elements and calculates the control amount according to the control pattern shown in FIG. 2 or 3. First, as shown in FIG. 2, the magnitude of the amplitude P of the temperature change obtained from the temperature processing unit 21 is compared to the target value, "■ amplitude is small", "■ amplitude is large", "■ amplitude is In response to this,
"& Raise the temperature of the heating cylinder", "b Decrease the temperature of the heating cylinder", "C Increase the screw rotation speed during measurement", "d Decrease the screw rotation speed during measurement", "e Increase the back pressure ”
, "f lower back pressure", "g increase material supply amount",
The controller provides control information for executing the following controls: "h Decrease the material supply amount,""i Increase the material supply temperature," and "j Decrease the material supply temperature" according to the connection lines and priorities in Figure 2. Granted to 23. This allows, for example,
If the amplitude P of the temperature change is small as shown by E2 in Fig. 5 (Eo is normal), it corresponds to "■ amplitude is small" in Fig. 2, and in this case, first, "b heating cylinder (Priority 1) Furthermore, if this control does not improve the situation and the amplitude of the temperature change does not increase, then control is performed to "increase the amount of g material supplied" (priority order 2). Until such controls are improved,
They are performed in order of priority. Note that if the problem is not improved even after a predetermined period of time has elapsed after all preset control elements have been controlled, abnormality processing, that is, control such as generation of an alarm and stopping of operation, is performed.
一方、第3図に示すように、検出された温度Tの大きさ
が、第5図に示すようにモニター範囲Mに比較して、「
■モニタ範囲より上昇」、「■モニタ範囲より下降」、
「■上限を越え振幅が上に大きい」の各態様となった場
合、これに対応して、「a加熱筒の温度を上げる」、「
b加熱筒の温度を下げる」、「C計量時のスクリュ回転
数を上げる」、「d計量時のスクリュ回転数を下げる」
、「e背圧を上げる」、「f背圧を下げる」、「g材料
供給量を多くする」、「h材料供給量を少なくする」、
「i材料供給温度を上げる」、「j材料供給温度を下げ
る」の各制御を第3図中の接続線と優先順位に従って実
行するための制御情報をコントローラ23に付与する。On the other hand, as shown in FIG. 3, the magnitude of the detected temperature T is "
■Rising above the monitor range", "■Lowering below the monitor range",
In the case of "■ The amplitude exceeds the upper limit and the amplitude is larger than the upper limit", corresponding actions such as "a raise the temperature of the heating cylinder" and "
b. Decrease the temperature of the heating cylinder", "C. Increase the screw rotation speed during measurement", "d. Decrease the screw rotation speed during measurement".
, "e increase back pressure", "f decrease back pressure", "g increase material supply amount", "h decrease material supply amount",
The controller 23 is provided with control information for executing each control of "i increase the material supply temperature" and "j decrease the material supply temperature" according to the connection lines and priorities in FIG. 3.
なお、「モニタ範囲より上昇」とは第5図中、E3で示
すように、温度Tかモニタ範囲Mの上限よりも大きくな
った場合、「モニタ範囲より下降」とは第5図中、E4
で示すように、温度Tがモニタ範囲Mの下限よりも小さ
くなった場合、「上限を越え振幅が上に大きい」とは、
第6図中、E5で示すように、振幅が大きくなり、限界
値りを超え、制御を継続しても下降しない場合である。In addition, "rising above the monitor range" means that when the temperature T becomes larger than the upper limit of the monitor range M, as shown by E3 in FIG. 5, "falling below the monitor range" means E4 in FIG.
As shown in , when the temperature T becomes smaller than the lower limit of the monitor range M, "the upper limit is exceeded and the amplitude is larger than the upper limit" means that
As shown by E5 in FIG. 6, this is a case where the amplitude becomes large, exceeds the limit value, and does not decrease even if the control is continued.
よって、例えば、「■モニタ範囲より上昇」した場合に
は、まず、「b加熱筒の温度を下げる」ように制御する
(優先順位1)。また、この制御によっても改善されず
に温度変化の振幅が大きくならない場合、次に、「h材
料供給量を少くする」ように制御する(優先順位2)。Therefore, for example, when the temperature rises above the monitor range (■), the control is first performed to "lower the temperature of the heating cylinder b" (priority order 1). If the amplitude of the temperature change does not increase even with this control, the control is then performed to "reduce the amount of material h supplied" (priority order 2).
このような制御は改善されるまで、優先順位にしたがっ
て順次行う。なお、「■上限を越え振幅が上に大きい」
場合には、所定時間経過した後、異常判定回路25によ
り異常処理、即ち、警報の発生、運転の停止等の制御を
行う。Such control is performed sequentially in priority order until improvements are made. In addition, "■The amplitude is larger than the upper limit"
In this case, after a predetermined period of time has elapsed, the abnormality determination circuit 25 performs abnormality processing, that is, controls such as issuing an alarm and stopping operation.
よって、樹脂状態に密接に関係する温度として、材料落
下ロア付近の温度状態を検出するようにしたため、早期
検出と適確な検出を行え、かつ演算処理によって最適な
樹脂状態となるように制御される。なお、演算部22で
は必要に応じてAI制御等を行わせることもできる。Therefore, by detecting the temperature near the material falling lower as a temperature closely related to the resin condition, early detection and accurate detection can be performed, and the resin condition can be controlled to the optimum resin condition through calculation processing. Ru. Note that the calculation unit 22 can also perform AI control, etc., if necessary.
以上、実施例について詳細に説明したが本発明はこのよ
うな実施例に限定されるものではない。Although the embodiments have been described in detail above, the present invention is not limited to these embodiments.
例えば、第2図と第3図の制御パターンを組み合わせて
同時に行ってもよいし、制御要素も例示以外の各種制御
要素を加えることができる。また、制御に際しては樹脂
温度を表示等し、これに従って制御要素を手動で操作し
てもよい。さらにまた、ベント式射出成形機を例示した
が、ベント孔の無い一般的な射出成形機でも制御パター
ンを若干変更するのみで同様に適用できる。その他、細
部の構成、手法等において、本発明の要旨を逸脱しない
範囲で任意に変更できる。For example, the control patterns shown in FIG. 2 and FIG. 3 may be combined and performed simultaneously, and various control elements other than those illustrated may be added. Further, during control, the resin temperature may be displayed, and the control elements may be manually operated in accordance with the display. Furthermore, although a vent type injection molding machine is illustrated, the present invention can be similarly applied to a general injection molding machine without a vent hole by only slightly changing the control pattern. In addition, the detailed structure, method, etc. may be arbitrarily changed without departing from the gist of the present invention.
このように、本発明に係る射出成形機の制御方法は、加
熱筒内に臨む材料供給機構の材料落下口付近の温度状態
を検出し、検出した温度状態に基づいて、樹脂状態に影
響を与える制御要素を可変制御するようにしたため、次
のような顕著な効果を奏する。As described above, the injection molding machine control method according to the present invention detects the temperature state near the material drop port of the material supply mechanism facing into the heating cylinder, and influences the resin state based on the detected temperature state. Since the control elements are variably controlled, the following remarkable effects are achieved.
■ 樹脂状態に密接に関係する温度を早期、かつ正確に
検出できるため、最適な樹脂温度、さらには最適な樹脂
状態を容易かつ確実に設定でき、成形品質向上を達成で
きる。■ Since the temperature closely related to the resin condition can be detected early and accurately, the optimum resin temperature and even the optimum resin condition can be easily and reliably set, and molding quality can be improved.
■ 最適な樹脂状態が自動的に設定されるため、省力化
及び生産性向上を達成できる。■ Since the optimal resin condition is automatically set, labor savings and productivity improvements can be achieved.
第1N:本発明に係る制御方法を実施できる射出成形機
の制御系を示すブロック系統
図、
第2図、第3図:同制御系における演算部の制御パター
ンの一例を示すパターン図、
第4N:本発明方法により検出した温度状態を示す温度
特性図、
第5図、第6図:温度状態の変化を示す説明図。
尚図面中、
1:射出成形機 2:スクリュ
3:加熱筒 4:ベント孔
:材料供給機構
:材料落下口1N: A block system diagram showing a control system of an injection molding machine that can carry out the control method according to the present invention. FIGS. 2 and 3: A pattern diagram showing an example of a control pattern of the calculation unit in the control system. 4N : A temperature characteristic diagram showing the temperature state detected by the method of the present invention. FIGS. 5 and 6: An explanatory diagram showing changes in the temperature state. In the drawing, 1: Injection molding machine 2: Screw 3: Heating tube 4: Vent hole: Material supply mechanism: Material dropping port
Claims (9)
する加熱筒を備えてなる射出成形機の制御方法において
、加熱筒内に臨む材料供給機構の材料落下口付近の温度
状態を検出し、検出した温度状態に基づいて、樹脂状態
に影響を与える制御要素を可変制御することを特徴とす
る射出成形機の制御方法。(1) In a method for controlling an injection molding machine equipped with a heating cylinder having a built-in screw and a material supply mechanism at the rear, detecting the temperature state near the material drop port of the material supply mechanism facing into the heating cylinder, A method for controlling an injection molding machine, comprising variably controlling control elements that affect a resin state based on a detected temperature state.
する温度変化の振幅の大きさであることを特徴とする請
求項1記載の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 temperature state is the amplitude of a temperature change that periodically fluctuates in synchronization with a molding cycle.
の大きさであることを特徴とする請求項1記載の射出成
形機の制御方法。(3) The method for controlling an injection molding machine according to claim 1, wherein the temperature state is a temperature level relative to a preset monitor range.
変制御した後、所定時間経過しても限界値内に入らない
場合には、異常処理を行うことを特徴とする請求項1記
載の射出成形機の制御方法。(4) After setting a limit value for the temperature state and variably controlling the control element, if the temperature does not fall within the limit value even after a predetermined period of time has elapsed, abnormality processing is performed. The method for controlling the injection molding machine described.
順位に従って順次制御することを特徴とする請求項1記
載の射出成形機の制御方法。(5) A method for controlling an injection molding machine according to claim 1, characterized in that priorities are set for a plurality of control elements and the control is performed sequentially according to the priorities.
ることを特徴とする請求項1記載の射出成形機の制御方
法。(6) The method for controlling an injection molding machine according to claim 1, wherein the control element is the amount of material supplied in the material supply mechanism.
特徴とする請求項1記載の射出成形機の制御方法。(7) The method for controlling an injection molding machine according to claim 1, wherein the control element is the heating temperature in the heating cylinder.
ことを特徴とする請求項1記載の射出成形機の制御方法
。(8) The method for controlling an injection molding machine according to claim 1, wherein the control element is a heating temperature in the material supply mechanism.
ることを特徴とする請求項1記載の射出成形機の制御方
法。(9) The method for controlling an injection molding machine according to claim 1, wherein the control element is the rotational speed of the screw and/or the back pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21205990A JPH0494915A (en) | 1990-08-10 | 1990-08-10 | Control method for injection molding machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21205990A JPH0494915A (en) | 1990-08-10 | 1990-08-10 | Control method for injection molding machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0494915A true JPH0494915A (en) | 1992-03-27 |
JPH0581421B2 JPH0581421B2 (en) | 1993-11-12 |
Family
ID=16616188
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21205990A Granted JPH0494915A (en) | 1990-08-10 | 1990-08-10 | Control method for injection molding machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0494915A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61235120A (en) * | 1985-04-12 | 1986-10-20 | Mitsubishi Heavy Ind Ltd | Temperature regulating device |
-
1990
- 1990-08-10 JP JP21205990A patent/JPH0494915A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61235120A (en) * | 1985-04-12 | 1986-10-20 | Mitsubishi Heavy Ind Ltd | Temperature regulating device |
Also Published As
Publication number | Publication date |
---|---|
JPH0581421B2 (en) | 1993-11-12 |
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