JPH0976320A - Automatic setting method for injection molding speed condition of injection mold machine - Google Patents

Automatic setting method for injection molding speed condition of injection mold machine

Info

Publication number
JPH0976320A
JPH0976320A JP23707195A JP23707195A JPH0976320A JP H0976320 A JPH0976320 A JP H0976320A JP 23707195 A JP23707195 A JP 23707195A JP 23707195 A JP23707195 A JP 23707195A JP H0976320 A JPH0976320 A JP H0976320A
Authority
JP
Japan
Prior art keywords
injection molding
resin
speed condition
pressure
setting
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.)
Pending
Application number
JP23707195A
Other languages
Japanese (ja)
Inventor
Katsuyuki Suzuki
克之 鈴木
Kazuo Murakawa
和生 村川
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 JP23707195A priority Critical patent/JPH0976320A/en
Publication of JPH0976320A publication Critical patent/JPH0976320A/en
Pending 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
    • B29C45/7693Measuring, controlling or regulating using rheological models of the material in the mould, e.g. finite elements method
    • 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
    • B29C45/77Measuring, controlling or regulating of velocity or pressure of moulding material

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 previously analyze a resin pressure in a mold cavity by flow analysis of a melt resin by a form model of a molding without providing a resin pressure sensor in a mold and computing and correcting an injection speed so as to eliminate a difference between the resin pressure and a previously set pressure. SOLUTION: In an injection mold machine which molds a desired molding by injecting a melting material into a mold cavity 20 by movement of a screw 12, a reference pressure of the melting material to be injected into the cavity is set as a function of an elapsed time from start of injection process or the moved distance of the screw. A form model of a molding is previously divided into elements, and flow analysis of the melting material is performed by a finite element method and a boundary element method so as to analyze the resin pressure in the cavity. Within a range where the resin pressure differs from the reference pressure, from the relationship between the calculated pressure and the reference pressure, the resin pressure in the mold cavity is obtained by computing a correction value of the injection speed so as to eliminate the difference.

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、射出成形機の射出
成形速度条件の自動設定方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of automatically setting an injection molding speed condition of an injection molding machine.

【0002】[0002]

【従来の技術】射出成形機の充填工程において、予め設
定した圧力に対し、検出した金型内樹脂圧力をフィード
バックして射出速度を制御し、成形品の品質向上を図る
制御方法が提案されている。
2. Description of the Related Art In a filling process of an injection molding machine, a control method has been proposed for improving the quality of a molded product by feeding back the detected resin pressure in a mold to a preset pressure to control the injection speed. There is.

【0003】図11は、このような従来の制御方法を実
施する射出成形機の射出成形速度制御装置の概略構成を
示すものである。すなわち、図11において、参照符号
10は射出シリンダ、12はスクリュ、14はバレル、
16はノズル、18はゲート、20は金型キャビティ、
22は前記スクリュ12による射出速度を制御するため
の前記射出シリンダ10に対して設けられた油圧ユニッ
ト、24は前記スクリュ12の移動位置を検出するため
のスクリュ位置検出器、26は前記油圧ユニット22を
制御するための制御装置、28は前記金型キャビティ2
0内の樹脂圧を検出するための樹脂圧センサをそれぞれ
示す。
FIG. 11 shows a schematic construction of an injection molding speed control device of an injection molding machine which carries out such a conventional control method. That is, in FIG. 11, reference numeral 10 is an injection cylinder, 12 is a screw, 14 is a barrel,
16 is a nozzle, 18 is a gate, 20 is a mold cavity,
22 is a hydraulic unit provided for the injection cylinder 10 for controlling the injection speed of the screw 12, 24 is a screw position detector for detecting the moving position of the screw 12, and 26 is the hydraulic unit 22. And a control device 28 for controlling the mold cavity 2
The resin pressure sensor for detecting the resin pressure within 0 is shown respectively.

【0004】このように構成された射出成形速度制御装
置において、金型キャビティ20内における溶融樹脂の
圧力(樹脂圧)を樹脂圧センサ28により検出し、この
検出圧力を制御装置26へフィードバックして、スクリ
ュ12による射出速度を制御するように構成される。こ
の場合、前記樹脂圧センサ28により検出される金型キ
ャビティ20内の樹脂圧が、充填工程中に予め設定した
圧力よりも高い場合、所定の演算によって充填速度を自
動的に下げ、金型内樹脂圧力の過大な上昇を制御する充
填速度の自動減速制御が達成される。このような射出成
形速度制御装置を使用した射出成形機の成形方法によれ
ば、金型サイズの縮小、軽量化、成形機の小形化、成形
品の品質の向上等に有効である。
In the injection molding speed controller thus constructed, the pressure of the molten resin (resin pressure) in the mold cavity 20 is detected by the resin pressure sensor 28, and this detected pressure is fed back to the controller 26. , The injection speed of the screw 12 is controlled. In this case, when the resin pressure in the mold cavity 20 detected by the resin pressure sensor 28 is higher than the pressure set in advance during the filling process, the filling speed is automatically reduced by a predetermined calculation, and An automatic deceleration control of the filling speed that controls an excessive increase in resin pressure is achieved. The molding method of the injection molding machine using such an injection molding speed control device is effective in reducing the size of the mold, reducing the weight of the molding machine, reducing the size of the molding machine, and improving the quality of the molded product.

【0005】[0005]

【発明が解決しようとする課題】しかるに、前述した射
出成形速度制御装置において、金型キャビティ内の樹脂
圧のフィードバックによる充填速度の自動減速制御を行
うに際しては、金型キャビティ内の樹脂圧を検出するた
めに、金型に対して樹脂圧センサを取付ける必要があ
る。
However, in the above-mentioned injection molding speed control device, when performing automatic deceleration control of the filling speed by feedback of the resin pressure in the mold cavity, the resin pressure in the mold cavity is detected. Therefore, it is necessary to attach a resin pressure sensor to the mold.

【0006】従って、このような自動減速制御を行うた
めに対象となる全ての金型に対して樹脂圧センサを取付
けるための加工を行うことは、費用が掛かるばかりでな
く、成形品の形状や金型の形状によっては、樹脂圧セン
サを所望の位置に設けることができない難点がある。ま
た、既存の金型に対し、これを一部加工して樹脂圧セン
サを取付けることは困難な場合が多い。
Therefore, it is not only costly to perform processing for attaching the resin pressure sensor to all the target molds for performing such automatic deceleration control, but also the shape of the molded product and There is a problem that the resin pressure sensor cannot be provided at a desired position depending on the shape of the mold. In addition, it is often difficult to process a part of an existing mold to mount the resin pressure sensor.

【0007】さらに、金型交換を行う場合の段取り作業
においても、金型を射出成形機に着脱させる都度、樹脂
圧センサやその配線を着脱する必要があり、煩雑な作業
となり、作業時間も増大する難点がある。
Further, also in the setup work for exchanging the mold, it is necessary to attach and detach the resin pressure sensor and its wiring every time the mold is attached to and detached from the injection molding machine, which is a complicated work and the working time is increased. There is a difficulty to do.

【0008】そこで、本発明の目的は、金型に対して樹
脂圧センサを設けることなく、予め成形品の形状モデル
による溶融樹脂の流動解析によって金型キャビティ内に
おける樹脂圧を解析し、この樹脂圧と予め設定した圧力
との差異をなくすように射出速度を演算して修正するこ
とができる射出成形機の射出成形速度条件自動設定方法
を提供することにある。
Therefore, an object of the present invention is to analyze the resin pressure in the mold cavity in advance by analyzing the flow of the molten resin according to the shape model of the molded product without providing a resin pressure sensor on the mold. An object of the present invention is to provide an injection molding speed condition automatic setting method for an injection molding machine, which can calculate and correct an injection speed so as to eliminate a difference between a pressure and a preset pressure.

【0009】[0009]

【課題を解決するための手段】前記目的を達成するた
め、本発明に係る射出成形機の射出成形速度条件自動設
定方法は、溶融材料をスクリュの移動により金型キャビ
ティ内に射出して所要の成形品を成形する射出成形機に
おいて、前記キャビティ内に射出される溶融材料の基準
圧力を射出工程開始からの経過時間またはスクリュの移
動距離の関数として設定すると共に、予め成形品の形状
モデルを要素分割し、有限要素法、境界要素法等による
溶融材料の流動解析を行って、前記キャビティ内の樹脂
圧を解析し、この樹脂圧が前記基準圧力を越えている範
囲において計算圧力と基準圧力との関係からその差異を
なくすように射出速度の修正値を演算して求めることを
特徴とする。
In order to achieve the above object, the method for automatically setting the injection molding speed condition of an injection molding machine according to the present invention is performed by injecting a molten material into a mold cavity by moving a screw. In an injection molding machine for molding a molded product, the reference pressure of the molten material injected into the cavity is set as a function of the elapsed time from the start of the injection process or the moving distance of the screw, and the shape model of the molded product is set in advance as an element. Divide and analyze the flow of the molten material by the finite element method, boundary element method, etc., analyze the resin pressure in the cavity, and calculate the calculated pressure and the reference pressure in the range where the resin pressure exceeds the reference pressure. It is characterized in that the correction value of the injection speed is calculated and obtained so as to eliminate the difference from the relationship of.

【0010】この場合、複数の樹脂温度に対応する、前
述した記載の射出成形機の射出成形速度条件自動設定方
法で設定される射出成形速度条件を準備しておき、成形
時の樹脂温度に応じて射出成形速度条件を切換えて使用
することができる。
In this case, an injection molding speed condition corresponding to a plurality of resin temperatures, which is set by the above-mentioned automatic setting method of the injection molding speed condition of the injection molding machine, is prepared, and the resin temperature at the time of molding is adjusted. The injection molding speed conditions can be switched and used.

【0011】また、複数の樹脂粘度に対応する、前述し
た射出成形機の射出成形速度条件自動設定方法で設定さ
れる射出成形速度条件を準備しておき、成形時の樹脂粘
度に応じて射出成形速度条件を切換えて使用することも
できる。
Further, the injection molding speed conditions corresponding to a plurality of resin viscosities, which are set by the above-mentioned automatic setting method of the injection molding speed condition of the injection molding machine, are prepared, and the injection molding is performed according to the resin viscosities at the time of molding. The speed condition can be switched and used.

【0012】さらに、射出成形機の制御プログラムの初
期条件設定ルーチンの中に、入力データとして成形品の
流動解析結果を与えることにより、前述した射出成形機
の射出成形速度条件自動設定方法で設定される射出成形
速度条件を設定するサブルーチンを設けて、前記成形品
の流動解析結果から射出成形速度条件を自動設定するこ
ともできる。
Furthermore, by giving the flow analysis result of the molded product as input data in the initial condition setting routine of the control program of the injection molding machine, the injection molding speed condition automatic setting method of the injection molding machine described above is set. It is also possible to provide a subroutine for setting the injection molding speed condition to automatically set the injection molding speed condition from the flow analysis result of the molded product.

【0013】さらにまた、射出成形機の制御プログラム
の初期条件設定ルーチンの中に、入力データとして成形
品の流動解析結果を与えると共に、成形時の樹脂温度の
検出を行うことにより、前述した射出成形機の射出成形
速度条件自動設定方法で設定される射出成形速度条件を
設定するサブルーチンを設けて、前記成形品の流動解析
結果および成形時の樹脂温度から射出成形速度条件を自
動設定することも可能である。
Furthermore, by giving the flow analysis result of the molded product as input data in the initial condition setting routine of the control program of the injection molding machine and detecting the resin temperature at the time of molding, the above-mentioned injection molding is performed. It is also possible to provide a subroutine to set the injection molding speed condition set by the automatic injection molding speed condition setting method of the machine and automatically set the injection molding speed condition from the flow analysis result of the molded product and the resin temperature during molding. Is.

【0014】そして、射出成形機の制御プログラムの初
期条件設定ルーチンの中に、入力データとして成形品の
流動解析結果を与えると共に、成形時の樹脂粘度の検出
を行うことにより、前述した射出成形機の射出成形速度
条件自動設定方法で設定される射出成形速度条件を設定
するサブルーチンを設けて、前記成形品の流動解析結果
および成形時の樹脂粘度から射出成形速度条件を自動設
定することも可能である。
Then, the flow analysis result of the molded product is given as the input data in the initial condition setting routine of the control program of the injection molding machine, and the resin viscosity at the time of molding is detected, thereby making the injection molding machine described above. It is also possible to provide a subroutine to set the injection molding speed condition set by the method for automatically setting the injection molding speed condition, and to automatically set the injection molding speed condition from the flow analysis result of the molded product and the resin viscosity at the time of molding. is there.

【0015】[0015]

【発明の実施の形態】次に、本発明に係る射出成形機の
射出成形速度条件自動設定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。
BEST MODE FOR CARRYING OUT THE INVENTION Next, an embodiment of an automatic method for setting an injection molding speed condition of an injection molding machine according to the present invention will be described in detail below with reference to the accompanying drawings.

【0016】すなわち、本発明においては、射出成形速
度条件の設定に際し、射出成形型内に射出される溶融材
料の基準圧力を、射出工程開始からの経過時間またはス
クリュの移動距離の関数として設定すると共に、予めス
プル、ランナを含む成形品の形状モデルにより流動解析
を行い、前記型内の樹脂圧の解析結果から、前記基準圧
力との差異がある範囲において、流体力学理論により計
算圧力と基準圧力との差異をなくすように射出速度の修
正値を演算して求め、射出成形速度条件を自動設定する
ものである。
That is, in the present invention, when setting the injection molding speed condition, the reference pressure of the molten material injected into the injection mold is set as a function of the elapsed time from the start of the injection process or the moving distance of the screw. At the same time, a flow analysis is performed in advance using the shape model of the molded product including the sprue and runner, and from the analysis result of the resin pressure in the mold, in the range where there is a difference from the reference pressure, the calculated pressure and the reference pressure are calculated by the fluid dynamic theory. The injection molding speed condition is automatically set by calculating the correction value of the injection speed so as to eliminate the difference between

【0017】なお、樹脂材料による射出成形において、
金型キャビティ内の溶融樹脂の流動解析(シミュレーシ
ョン)を行う場合、成形品の形状モデルを微小要素に分
割して、有限要素法、境界要素法、差分法、FAN法等
の数値解析法を用いて、流体の運動方程式、連続の式お
よびエネルギーの式等を演算する方法が一般に利用され
ている。
In the injection molding of resin material,
When performing a flow analysis (simulation) of the molten resin in the mold cavity, divide the shape model of the molded product into minute elements and use the numerical analysis methods such as the finite element method, the boundary element method, the difference method, and the FAN method. Therefore, a method of calculating a fluid motion equation, a continuity equation, an energy equation, and the like is generally used.

【0018】このような金型キャビティ内での溶融樹脂
の流動解析方法では、使用する樹脂の選択と成形機の運
転条件として、樹脂温度、金型温度、充填速度を入力し
て演算することにより、樹脂の充填の進行状況(時間)
を示すものとして、全充填時間を任意の数に分割し、各
時間毎に充填される樹脂の到達位置を線により結んで作
成した等時間線図、同様に圧力について作成した等圧力
線図、また同様に温度について作成した等温度線図等が
それぞれ所要の計算により求めることができることは公
知である(特公平4−69851号公報等)。
In such a method for analyzing the flow of the molten resin in the mold cavity, the resin temperature, the mold temperature and the filling speed are input and calculated as the selection of the resin to be used and the operating conditions of the molding machine. , Resin filling progress (time)
As shown, the total filling time is divided into an arbitrary number, the isochronous diagram created by connecting the arrival positions of the resin to be filled at each time with a line, the equal pressure diagram created for the pressure, Similarly, it is well known that the isothermal lines and the like created with respect to the temperature can be obtained by required calculations, respectively (Japanese Patent Publication No. 4-69851).

【0019】[0019]

【実施例1】 (A)溶融樹脂の流動解析による型内樹脂圧 図1は、所要の成形品の射出工程におけるバレル14内
におけるスクリュ12の行程(射出動作ステップ)と、
金型キャビティ20内の溶融樹脂の充填の進行状況(充
填進行ステップ)の関係を示すものである。なお、本実
施例においては、前述した図11に示す射出成形速度制
御装置を適用して実施することができるものであり、従
って図1において、前述した図11に示す装置構成と同
一の構成部分については、同一の参照符号を付し、その
詳細な説明は省略する。
EXAMPLE 1 (A) mold resin pressure Figure 1 by flow analysis of the molten resin, the stroke of the screw 12 in the barrel 14 at a required molded article of the injection process (injection process step),
4 shows the relationship of the progress of the filling of the molten resin in the mold cavity 20 (filling progress step). The present embodiment can be implemented by applying the above-mentioned injection molding speed control device shown in FIG. 11, and therefore, in FIG. 1, the same components as the above-described device configuration shown in FIG. Are denoted by the same reference numerals, and detailed description thereof will be omitted.

【0020】この場合、前記金型キャビティ20による
成形品の流動解析により求めた、金型キャビティ20内
における樹脂圧(以下、型内樹脂圧と略称する)の観察
基準点Aおよびそれ以後における型内樹脂圧とスクリュ
12の行程との関係は、例えば図2に示すようになる。
In this case, the resin pressure in the mold cavity 20 (hereinafter, abbreviated as in-mold resin pressure) obtained by the flow analysis of the molded product by the mold cavity 20 and the mold at the observation reference point A and thereafter. The relationship between the internal resin pressure and the stroke of the screw 12 is as shown in FIG. 2, for example.

【0021】(B)金型キャビティ内に射出される溶融
材料の基準圧力 図2においては、型内樹脂圧は、溶融樹脂が型内樹脂圧
の観察基準点Aに到達した時点から立上がり、充填の進
行に伴って増加する状態が示されている。そこで、型内
樹脂圧が過大に上昇すると、金型の型締力が不足して、
成形品にバリを生じたり、中子の損傷を生じたり、ある
いは残留応力による成形品の変形を生じたりする等の不
具合を生じる。例えば、図2に示す場合において、成形
品に前記のような不具合を生じないための限界型内樹脂
圧、すなわち基準圧力を、基準点Aにおいて13Mpa
に設定すると、充填完了に近い6〜10区間における型
内樹脂圧は、基準圧力(13Mpa)を越えていること
になる。
(B) Melt injected into the mold cavity
Reference Pressure of Material In FIG. 2, the resin pressure in the mold rises from the time when the molten resin reaches the observation reference point A of the resin pressure in the mold, and shows a state in which it increases with the progress of filling. Therefore, if the resin pressure in the mold rises excessively, the mold clamping force of the mold will be insufficient,
There are problems such as burrs on the molded product, damage to the core, and deformation of the molded product due to residual stress. For example, in the case shown in FIG. 2, the resin pressure inside the mold for preventing the above-mentioned defects from occurring in the molded product, that is, the reference pressure is 13 MPa at the reference point A.
When set to, the resin pressure in the mold in the 6 to 10 section close to the completion of filling exceeds the reference pressure (13 Mpa).

【0022】(C)型内樹脂圧と射出速度の関係 図1に示すように、射出工程におけるスクリュ12の行
程を所要数の区間に区切り、区間内の射出速度は一定と
する階段状射出速度の設定を行うものとする。すなわ
ち、この場合における階段状射出速度の設定例を、図3
に示す。
(C) Relationship between in-mold resin pressure and injection speed As shown in FIG. 1, the stroke of the screw 12 in the injection process is divided into a required number of sections, and the injection speed in each section is constant. Shall be set. That is, an example of setting the stepwise injection speed in this case is shown in FIG.
Shown in

【0023】一般に、溶融樹脂の流動時の粘度特性は、
いわゆる非ニュートン特性を示し、その剪断応力と剪断
速度との関係は、次式(1) により近似することができ
る。
Generally, the viscosity characteristics of a molten resin when flowing are
It exhibits so-called non-Newtonian characteristics, and the relationship between its shear stress and shear rate can be approximated by the following equation (1).

【0024】[0024]

【数1】 但し、 τ:溶融樹脂の流動に伴う剪断応力 φ(dv/dy,T):樹脂の粘度特性を示す定数 (dv/dy):剪断速度 T:樹脂温度 ここで、通常の成形条件の範囲では、φは次式(2) によ
り近似することができる。
[Equation 1] However, τ: Shear stress due to the flow of molten resin φ (dv / dy, T): A constant indicating the viscosity characteristic of the resin (dv / dy): Shear rate T: Resin temperature Here, in the range of normal molding conditions. , Φ can be approximated by the following equation (2).

【0025】[0025]

【数2】 但し、 A:粘度係数 B:剪断係数 C:温度係数 前記式(1) を式(2) に代入して、次式(3) が得られる。[Equation 2] However, A: viscosity coefficient B: shear coefficient C: temperature coefficient Substituting equation (1) into equation (2), the following equation (3) is obtained.

【0026】[0026]

【数3】 ここで、ある1回の充填工程中の金型内樹脂温度Tの変
化が無視でき、かつ繰り返される成形サイクルにおいて
樹脂温度の変動が無視できる場合には、前記式(3) は次
式(4) により表すことができる。
(Equation 3) Here, when the change of the resin temperature T in the mold during a certain filling step can be ignored and the variation of the resin temperature in the repeated molding cycle can be ignored, the above equation (3) is expressed by the following equation (4) ) Can be represented.

【0027】[0027]

【数4】 但し、 n ,φ:樹脂の粘度特性を示す定数 そこで、溶融樹脂の金型キャビティ内における流動を、
ヘレ−ショウ(Hele−Shaw)流れと仮定する
と、この粘度特性を有する溶融樹脂が、前記金型キャビ
ティ内において、図4に示すように、第q区間を溶融樹
脂の充填が進行するに際し、この時の前記溶融樹脂の流
動方向断面内の流速分布は、図5に示すようになり、流
速分布vおよび区間圧力損失ΔPは、それぞれ次式で示
される。
(Equation 4) However, n and φ are constants indicating the viscosity characteristics of the resin. Therefore, the flow of the molten resin in the mold cavity is
Assuming a Hele-Shaw flow, the molten resin having this viscosity characteristic is filled with the molten resin in the mold cavity in the q-th section as shown in FIG. The flow velocity distribution in the flow direction cross section of the molten resin at this time is as shown in FIG. 5, and the flow velocity distribution v and the section pressure loss ΔP are respectively expressed by the following equations.

【0028】[0028]

【数5】 (Equation 5)

【0029】[0029]

【数6】 (Equation 6)

【0030】[0030]

【数7】 但し、 v:位置yにおける流速 h:キャビティ厚さ y:キャビティ厚さ方向の中心からの距離 ΔP:区間圧力損失 L:区間の流動方向距離 v0 :最大流速(キャビティ厚さ方向の中心での流速) va:平均流速 前記式(6) 、(7) より、次式の関係が得られる。(Equation 7) However, v: flow velocity at position y h: cavity thickness y: distance from center in cavity thickness direction ΔP: section pressure loss L: flow direction distance in section v 0 : maximum flow velocity (at center in cavity thickness direction) Flow velocity) va: Average flow velocity From the equations (6) and (7), the following equation is obtained.

【0031】[0031]

【数8】 すなわち、所要の成形品の成形における所要区間iに着
目した場合、区間圧力損失ΔPi は、次式(6) で示すよ
うに、その区間の平均流速vai の(1/n)乗に比例
する。
(Equation 8) That is, when focusing on the required section i in the molding of the required molded product, the section pressure loss ΔP i is proportional to the (1 / n) th power of the average flow velocity va i in that section, as shown in the following equation (6). To do.

【0032】[0032]

【数9】 また、金型キャビティ内の第p区間にある基準点Aにお
ける第q区間の溶融樹脂の充填時の型内樹脂圧Pq は、
次式(10)で示すように、第p区間から第q区間までの区
間圧力損失を合計したものである。
[Equation 9] Further, the in-mold resin pressure P q when the molten resin is filled in the q-th section at the reference point A in the p-th section in the mold cavity is
As shown in the following equation (10), it is the sum of the section pressure losses from the p-th section to the q-th section.

【0033】[0033]

【数10】 さらに、第q区間における溶融樹脂の充填時の射出速度
q と、各区間の平均流速vai は、次式(11)で示すよ
うに、比例するものと考えられる。
(Equation 10) Furthermore, it is considered that the injection speed Q q at the time of filling the molten resin in the q-th section and the average flow velocity va i in each section are proportional to each other as shown in the following equation (11).

【0034】[0034]

【数11】 従って、金型キャビティ内の第p区間にある基準点Aに
おける第q区間の溶融樹脂の充填時の型内樹脂圧P
q は、次式(12)および(13)で示すように、第q区間の溶
融樹脂の充填時の射出速度Qq の(1/n)乗に比例す
る。
[Equation 11] Therefore, the in-mold resin pressure P at the time of filling the molten resin in the q-th section at the reference point A in the p-th section in the mold cavity
q, as shown by the following equation (12) and (13), is proportional to (1 / n) square of injection speed Q q in filling of the molten resin of the q segment.

【0035】[0035]

【数12】 (D)射出速度の修正値の演算 しかるに、型内樹脂圧について、前述した計算圧力Pc
q が、基準点Aにおける基準圧力Psq と差異がある範
囲における修正射出速度をQ′q とすると、前記式(13)
から、次式の関係が成立する。
(Equation 12) (D) Calculation of the correction value of the injection speed In consideration of the resin pressure in the mold, the above-mentioned calculated pressure Pc
Assuming that the corrected injection speed in the range where q is different from the reference pressure Ps q at the reference point A is Q ′ q , the above equation (13)
Therefore, the relation of the following equation is established.

【0036】[0036]

【数13】 (Equation 13)

【0037】[0037]

【数14】 [Equation 14]

【0038】[0038]

【数15】 従って、前記式(16)から明らかなように、修正射出速度
をQ′q は、元の射出速度Qq を、基準圧力Psq と計
算圧力Pcq との比に対し、これをn乗倍すれば求める
ことができる。
(Equation 15) Therefore, the equation (16) As is apparent from the Q 'q modified injection speed, the original injection speed Q q, with respect to the ratio of the reference pressure Ps q and calculates pressure Pc q, which n th power You can ask for it.

【0039】すなわち、Psq /Pcq が1未満であれ
ば、成形品に不具合を生じないための基準圧力(限界型
内樹脂圧)に向けて減速修正されるし、逆にPsq /P
qが1を越えれば、型内樹脂圧の不足によるショート
ショット等の不具合を解消すべく、基準圧力(限界型内
樹脂圧よりも低い適正型内樹脂圧)に向けて増速修正さ
れる。
That is, if Ps q / Pc q is less than 1, deceleration is corrected toward the reference pressure (resin pressure inside the mold) that does not cause a defect in the molded product, and conversely Ps q / P
If c q exceeds 1, the speed is corrected toward the reference pressure (the proper in-mold resin pressure lower than the limit in-mold resin pressure) in order to eliminate problems such as short shots due to insufficient in-mold resin pressure. .

【0040】(E)射出速度の修正値の計算例 表1は、所要の成形品に関する流動解析および射出速度
の修正計算のための条件を示す。そして、この表1に示
す条件で、流動解析および射出速度の修正計算を行った
結果を、表2に示す。
(E) Calculation Example of Correction Value of Injection Speed Table 1 shows the conditions for flow analysis and injection speed correction calculation for a required molded product. Table 2 shows the results of the flow analysis and the correction calculation of the injection speed under the conditions shown in Table 1.

【0041】[0041]

【表1】 [Table 1]

【0042】[0042]

【表2】 [Table 2]

【0043】(F)成形試験による効果の確認 前記表2に示す当初の射出速度および修正した射出速度
で成形した場合における、基準点Aにおいての型内樹脂
圧の測定結果を、図6に示す。この場合において、当初
の射出速度では、充填の6区間以降において、基準圧力
13Mpaを越えているが、修正した射出速度では、ほ
ぼ基準圧力の範囲内に収まっており、本発明による方法
が有効であることを確認できる。
(F) Confirmation of Effect by Molding Test FIG. 6 shows the measurement results of the resin pressure in the mold at the reference point A when molding was carried out at the initial injection speed and the modified injection speed shown in Table 2 above. . In this case, at the initial injection speed, the reference pressure exceeds 13 Mpa after the 6th section of filling, but at the corrected injection speed, it is almost within the range of the reference pressure, and the method according to the present invention is effective. You can confirm that there is.

【0044】[0044]

【実施例2】繰り返される成形サイクルにおいて、射出
される溶融樹脂の温度が変動すると、前記式(3) のex
p(CT)の値が変化し、樹脂粘度が変動し、同一の射
出速度条件においても、金型キャビティ内の基準点の型
内樹脂圧は、異なった値となる。従って、この場合に
は、前記実施例1における(A)〜(F)に示した方法
により、種々の樹脂温度に対する射出成形速度条件を求
めておき、成形時の樹脂温度に応じて、適宜射出成形速
度条件を切換え設定し、成形を行うことができる。
Example 2 In a repeated molding cycle, when the temperature of the injected molten resin fluctuates, ex of the formula (3)
The value of p (CT) changes, the resin viscosity changes, and even under the same injection speed condition, the in-mold resin pressure at the reference point in the mold cavity has different values. Therefore, in this case, the injection molding speed conditions for various resin temperatures are obtained in advance by the methods shown in (A) to (F) of Example 1, and the injection is appropriately performed according to the resin temperature during molding. Molding can be performed by switching and setting the molding speed conditions.

【0045】この場合、例えばノズル部に樹脂温度セン
サを設けたり、あるいはバレル温度センサを利用し、予
めバレルの検出温度と成形時の樹脂温度との関係を求め
ておくことによる手段等により、それぞれ成形時の樹脂
温度を容易に検知することができる。
In this case, for example, a resin temperature sensor may be provided in the nozzle portion, or a barrel temperature sensor may be used to obtain the relationship between the detected temperature of the barrel and the resin temperature during molding in advance. The resin temperature during molding can be easily detected.

【0046】[0046]

【実施例3】また、原料樹脂の品質のバラツキにより、
繰り返される成形サイクルにおいて、溶融樹脂の粘度が
変動すると、前記式(3) の粘度係数Aが変化し、樹脂粘
度が変動し、同一の射出速度条件においても、金型キャ
ビティ内の基準点の型内樹脂圧は、異なった値となる。
従って、この場合には、前記実施例1における(A)〜
(F)に示した方法により、種々の樹脂粘度に対応する
ノズル部の樹脂圧力を求めておき、成形時のノズル部の
樹脂圧力に応じて適宜射出成形速度条件を切換え設定
し、成形を行うことができる。
Example 3 In addition, due to variations in the quality of the raw resin,
In the repeated molding cycle, when the viscosity of the molten resin changes, the viscosity coefficient A of the above formula (3) changes and the resin viscosity also changes, and even under the same injection speed condition, the mold of the reference point in the mold cavity is changed. The internal resin pressure has different values.
Therefore, in this case, (A) to
By the method shown in (F), the resin pressure of the nozzle portion corresponding to various resin viscosities is obtained in advance, and the injection molding speed condition is appropriately switched and set according to the resin pressure of the nozzle portion at the time of molding, and molding is performed. be able to.

【0047】この場合、例えばノズル部に樹脂圧力セン
サを設けたり、あるいはスクリュ駆動油圧を利用し、予
め射出時のスクリュ駆動油圧とノズル部の樹脂圧力との
関係を求めておくことによる手段等により、それぞれ成
形時の樹脂圧力を容易に検知することができる。
In this case, for example, by providing a resin pressure sensor in the nozzle portion, or by utilizing the screw driving oil pressure, the relationship between the screw driving oil pressure at injection and the resin pressure in the nozzle portion is obtained in advance. The resin pressure at the time of molding can be easily detected.

【0048】[0048]

【実施例4】さらに、射出成形機の制御装置の制御プロ
グラムの初期条件設定ルーチンの中に、入力データとし
て与えられる流動解析結果から、前記実施例1における
(A)〜(F)に示した方法により、射出成形速度条件
を求めるサブルーチンを設けることによって、射出成形
機の制御装置に、溶融樹脂の流動解析結果から射出成形
速度条件を自動設定する機能を付与するように構成する
ことができる。
[Fourth Embodiment] Further, from the flow analysis result given as input data in the initial condition setting routine of the control program of the control device of the injection molding machine, the results are shown in (A) to (F) in the first embodiment. By providing a subroutine for obtaining the injection molding speed condition according to the method, it is possible to provide the control device of the injection molding machine with a function of automatically setting the injection molding speed condition from the flow analysis result of the molten resin.

【0049】この場合、前記実施例2および3に示す機
能をさらに付加することもできる。
In this case, the function shown in the second and third embodiments can be further added.

【0050】[0050]

【実施例5】実施例1における(A)〜(D)により求
められる射出速度条件による型内樹脂圧の抑制効果につ
いて、所要の成形品に関し流動解析し、実機での試験に
より確認した。
[Embodiment 5] The effect of suppressing the resin pressure in the mold under the injection speed conditions obtained in (A) to (D) in Embodiment 1 was subjected to a flow analysis on a required molded product and confirmed by a test using an actual machine.

【0051】(G)流動解析および実機試験の条件 表3は、流動解析および実機試験の条件を示す。なお、
成形品として、図7に示す解析モデルからなる平板を対
象とした。
(G) Conditions for Flow Analysis and Actual Machine Test Table 3 shows conditions for flow analysis and actual machine test. In addition,
As a molded product, a flat plate composed of the analytical model shown in FIG. 7 was used.

【0052】[0052]

【表3】 [Table 3]

【0053】(H)解析結果と型内樹脂圧の抑制効果 前記表3による条件に基づく本発明による射出速度条件
により、射出成形を行った結果、図8ないし図10に示
すように、期待通りの型内樹脂圧の抑制効果を得ること
ができた。なお、解析においては、実機試験結果から樹
脂粘度データの定数項を補正して、樹脂圧を合わせた。
(H) Analytical result and effect of suppressing resin pressure in the mold As a result of injection molding under the injection speed condition according to the present invention based on the conditions shown in Table 3, as shown in FIGS. 8 to 10, as expected, It was possible to obtain the effect of suppressing the resin pressure in the mold. In the analysis, the resin pressure was adjusted by correcting the constant term of the resin viscosity data from the actual machine test result.

【0054】すなわち、試験に使用した樹脂の粘度定数
nは、n=2.74であるが、n=4〜5(図10参
照)にした場合の方が、型内樹脂圧の抑制精度を向上し
得ることが確認された。これは、前記式(16)において、
溶融樹脂の粘度変化を無視しているのに対し、減速によ
り充填時間が延び、粘度が大きくなるためであると考え
られる。
That is, the viscosity constant n of the resin used in the test is n = 2.74, but when n = 4 to 5 (see FIG. 10), the accuracy of suppressing the resin pressure in the mold is higher. It was confirmed that it could be improved. This is in the above formula (16),
It is considered that, while the change in the viscosity of the molten resin is ignored, the filling time is extended and the viscosity is increased due to the deceleration.

【0055】また、粘度定数n=2.74で求めた射出
速度条件を与えて、再度同じ手順を繰り返すと、図8に
示すように、型内樹脂圧の抑制精度は向上し、2回目の
解析でほぼ目標通りの型内樹脂圧に収まる射出速度条件
を得ることができた。
When the injection speed condition determined by the viscosity constant n = 2.74 is given and the same procedure is repeated again, as shown in FIG. Through the analysis, it was possible to obtain injection speed conditions that were within the target mold resin pressure.

【0056】以上、本発明の好適な実施例について説明
したが、本発明は前記実施例に限定されることなく、本
発明の精神を逸脱しない範囲内において種々の設計変更
をすることができる。
Although the preferred embodiments of the present invention have been described above, the present invention is not limited to the above embodiments, and various design changes can be made without departing from the spirit of the present invention.

【0057】[0057]

【発明の効果】前述した実施例から明らかなように、本
発明に係る射出成形機の射出成形速度条件自動設定方法
によれば、金型に対して樹脂圧センサを設けることな
く、予めスプル、ランナを含む成形品の形状モデルによ
る溶融樹脂の流動解析によって金型キャビティ内におけ
る樹脂圧を解析し、この樹脂圧と予め設定した圧力との
差異をなくすように射出速度を演算して修正することに
より、金型サイズの縮小、軽量化、成形機の小形化、成
形品の品質の向上等を容易に達成することができる。
As is apparent from the above-described embodiments, according to the method for automatically setting the injection molding speed condition of the injection molding machine according to the present invention, sprue can be preliminarily set without providing the resin pressure sensor on the mold. Analyze the resin pressure in the mold cavity by the flow analysis of the molten resin using the shape model of the molded product including the runner, and calculate and correct the injection speed so as to eliminate the difference between this resin pressure and the preset pressure. As a result, it is possible to easily achieve a reduction in mold size, a reduction in weight, a downsizing of a molding machine, an improvement in quality of a molded product, and the like.

【0058】従って、本発明によれば、金型に対して樹
脂圧センサを取付けるための加工を行う手間と費用とを
省くことができると共に、金型交換に際しての段取り作
業も複雑化することなく、簡便かつ迅速に達成すること
ができる利点を有する。
Therefore, according to the present invention, it is possible to save the labor and cost for the processing for attaching the resin pressure sensor to the mold, and the setup work for the mold replacement is not complicated. , Has the advantage that it can be achieved simply and quickly.

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

【図1】本発明に係る射出成形機の射出成形速度条件自
動設定方法を実施するスクリュと金型キャビティとの関
係を示す射出成形機の概略説明図である。
FIG. 1 is a schematic explanatory view of an injection molding machine showing a relationship between a screw and a mold cavity for carrying out an injection molding speed condition automatic setting method for an injection molding machine according to the present invention.

【図2】図1に示す金型キャビティ内の基準点における
樹脂圧とスクリュ行程との関係を示す特性線図である。
FIG. 2 is a characteristic diagram showing a relationship between a resin pressure and a screw stroke at a reference point in the mold cavity shown in FIG.

【図3】図1に示すスクリュによる射出速度の設定例を
示すスクリュ位置と射出速度との関係を示す特性線図で
ある。
FIG. 3 is a characteristic diagram showing a relationship between a screw position and an injection speed, which shows an example of setting an injection speed by the screw shown in FIG.

【図4】図1に示す金型キャビティ内における溶融樹脂
の充填が進行する状態を示す説明図である。
FIG. 4 is an explanatory diagram showing a state where the molten resin is being filled in the mold cavity shown in FIG. 1.

【図5】図1に示す金型キャビティ内における溶融樹脂
の流動方向断面内の流速分布および区間圧力損失につい
て示す説明図である。
5 is an explanatory view showing a flow velocity distribution and a section pressure loss in a cross section in the flow direction of the molten resin in the mold cavity shown in FIG.

【図6】図1に示す射出成形機において当初の射出速度
および修正された射出速度で成形した場合の金型キャビ
ティ内における基準点での樹脂圧の測定結果を示す圧力
特性線図である。
6 is a pressure characteristic diagram showing a measurement result of resin pressure at a reference point in a mold cavity when molding is performed at an initial injection speed and a modified injection speed in the injection molding machine shown in FIG.

【図7】流動解析モデルの一実施例を示す説明図であ
る。
FIG. 7 is an explanatory diagram showing an example of a flow analysis model.

【図8】図7に示す流動解析モデルからなる金型キャビ
ティ内においての射出成形時の充填率との関係における
樹脂圧の解析演算結果を示す圧力特性線図である。
8 is a pressure characteristic diagram showing an analysis calculation result of a resin pressure in relation to a filling rate at the time of injection molding in a mold cavity made of the flow analysis model shown in FIG.

【図9】図7に示す流動解析モデルからなる金型キャビ
ティ内においての本発明方法による射出成形時の充填時
間との関係における樹脂圧の測定結果を示す圧力特性線
図である。
9 is a pressure characteristic diagram showing the measurement result of resin pressure in relation to the filling time at the time of injection molding by the method of the present invention in the mold cavity made of the flow analysis model shown in FIG. 7.

【図10】樹脂の粘度条件を変更した場合の図9に示す
と同様の樹脂圧の測定結果を示す圧力特性線図である。
FIG. 10 is a pressure characteristic diagram showing the same resin pressure measurement results as shown in FIG. 9 when the resin viscosity condition is changed.

【図11】金型キャビティ内における樹脂圧のフィード
バックによる充填速度の自動減圧制御を行う射出成形機
の概略説明図である。
FIG. 11 is a schematic explanatory diagram of an injection molding machine that performs automatic pressure reduction control of a filling speed by feedback of resin pressure in a mold cavity.

【符号の説明】[Explanation of symbols]

10 射出シリンダ 12 スクリュ 14 バレル 16 ノズル 18 ゲート 20 金型キャビティ 22 油圧ユニット 24 スクリュ位置検出器 26 制御装置 28 樹脂圧センサ 10 Injection Cylinder 12 Screw 14 Barrel 16 Nozzle 18 Gate 20 Mold Cavity 22 Hydraulic Unit 24 Screw Position Detector 26 Control Device 28 Resin Pressure Sensor

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 溶融材料をスクリュの移動により金型キ
ャビティ内に射出して所要の成形品を成形する射出成形
機において、前記キャビティ内に射出される溶融材料の
基準圧力を射出工程開始からの経過時間またはスクリュ
の移動距離の関数として設定すると共に、予め成形品の
形状モデルを要素分割し、有限要素法、境界要素法等に
よる溶融材料の流動解析を行って、前記キャビティ内の
樹脂圧を解析し、この樹脂圧が前記基準圧力を越えてい
る範囲において計算圧力と基準圧力との関係からその差
異をなくすように射出速度の修正値を演算して求めるこ
とを特徴とする射出成形機の射出成形速度条件自動設定
方法。
1. In an injection molding machine for injecting a molten material into a mold cavity by moving a screw to form a desired molded article, a reference pressure of the molten material injected into the cavity is set from the start of the injection process. In addition to setting as a function of elapsed time or screw movement distance, the shape model of the molded product is divided into elements in advance, and the flow analysis of the molten material is performed by the finite element method, boundary element method, etc. to determine the resin pressure in the cavity. The injection molding machine is characterized by analyzing and calculating a correction value of the injection speed so as to eliminate the difference between the calculated pressure and the reference pressure in the range where the resin pressure exceeds the reference pressure. Injection molding speed condition automatic setting method.
【請求項2】 複数の樹脂温度に対応する、請求項1記
載の射出成形機の射出成形速度条件自動設定方法で設定
される射出成形速度条件を準備しておき、成形時の樹脂
温度に応じて射出成形速度条件を切換えて使用すること
を特徴とする射出成形機の射出成形速度条件自動設定方
法。
2. An injection molding speed condition set by the method for automatically setting an injection molding speed condition of an injection molding machine according to claim 1, which corresponds to a plurality of resin temperatures, is prepared, and the temperature is adjusted according to the resin temperature at the time of molding. A method for automatically setting an injection molding speed condition of an injection molding machine, characterized in that the injection molding speed condition is switched and used.
【請求項3】 複数の樹脂粘度に対応する、請求項1記
載の射出成形機の射出成形速度条件自動設定方法で設定
される射出成形速度条件を準備しておき、成形時の樹脂
粘度に応じて射出成形速度条件を切換えて使用すること
を特徴とする射出成形機の射出成形速度条件自動設定方
法。
3. An injection molding speed condition, which is set by the method for automatically setting an injection molding speed condition of an injection molding machine according to claim 1, corresponding to a plurality of resin viscosities is prepared, and the resin viscosity at the time of molding is adjusted. A method for automatically setting an injection molding speed condition of an injection molding machine, characterized in that the injection molding speed condition is switched and used.
【請求項4】 射出成形機の制御プログラムの初期条件
設定ルーチンの中に、入力データとして成形品の流動解
析結果を与えることにより、請求項1記載の射出成形機
の射出成形速度条件自動設定方法で設定される射出成形
速度条件を設定するサブルーチンを設けて、前記成形品
の流動解析結果から射出成形速度条件を自動設定するこ
とを特徴とする射出成形機の射出成形速度条件自動設定
方法。
4. The automatic injection molding speed condition setting method for an injection molding machine according to claim 1, wherein a flow analysis result of a molded product is given as input data to an initial condition setting routine of a control program of the injection molding machine. A method for automatically setting an injection molding speed condition for an injection molding machine, characterized in that a subroutine for setting an injection molding speed condition set in 1. is provided to automatically set an injection molding speed condition from a flow analysis result of the molded product.
【請求項5】 射出成形機の制御プログラムの初期条件
設定ルーチンの中に、入力データとして成形品の流動解
析結果を与えると共に、成形時の樹脂温度の検出を行う
ことにより、請求項2記載の射出成形機の射出成形速度
条件自動設定方法で設定される射出成形速度条件を設定
するサブルーチンを設けて、前記成形品の流動解析結果
および成形時の樹脂温度から射出成形速度条件を自動設
定することを特徴とする射出成形機の射出成形速度条件
自動設定方法。
5. The method according to claim 2, wherein the flow condition analysis result of the molded product is given as input data to the initial condition setting routine of the control program of the injection molding machine, and the resin temperature at the time of molding is detected. A subroutine for setting the injection molding speed condition set by the injection molding speed automatic setting method of the injection molding machine is provided to automatically set the injection molding speed condition from the flow analysis result of the molded product and the resin temperature at the time of molding. A method for automatically setting an injection molding speed condition of an injection molding machine, characterized by:
【請求項6】 射出成形機の制御プログラムの初期条件
設定ルーチンの中に、入力データとして成形品の流動解
析結果を与えると共に、成形時の樹脂粘度の検出を行う
ことにより、請求項3記載の射出成形機の射出成形速度
条件自動設定方法で設定される射出成形速度条件を設定
するサブルーチンを設けて、前記成形品の流動解析結果
および成形時の樹脂粘度から射出成形速度条件を自動設
定することを特徴とする射出成形機の射出成形速度条件
自動設定方法。
6. The method according to claim 3, wherein the flow analysis result of the molded product is given as input data to the initial condition setting routine of the control program of the injection molding machine, and the resin viscosity at the time of molding is detected. A subroutine for setting the injection molding speed condition set by the injection molding speed automatic setting method of the injection molding machine is provided to automatically set the injection molding speed condition from the flow analysis result of the molded product and the resin viscosity at the time of molding. A method for automatically setting an injection molding speed condition of an injection molding machine, characterized by:
JP23707195A 1995-09-14 1995-09-14 Automatic setting method for injection molding speed condition of injection mold machine Pending JPH0976320A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23707195A JPH0976320A (en) 1995-09-14 1995-09-14 Automatic setting method for injection molding speed condition of injection mold machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23707195A JPH0976320A (en) 1995-09-14 1995-09-14 Automatic setting method for injection molding speed condition of injection mold machine

Publications (1)

Publication Number Publication Date
JPH0976320A true JPH0976320A (en) 1997-03-25

Family

ID=17009993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23707195A Pending JPH0976320A (en) 1995-09-14 1995-09-14 Automatic setting method for injection molding speed condition of injection mold machine

Country Status (1)

Country Link
JP (1) JPH0976320A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004025457A (en) * 2002-06-21 2004-01-29 Toyota Motor Corp Injection molding simulation method
JP2006198796A (en) * 2005-01-18 2006-08-03 Toyota Motor Corp Method and apparatus for calculating molding condition of injection molding machine and molding condition calculating program
JP2014518795A (en) * 2011-05-20 2014-08-07 ザ プロクター アンド ギャンブル カンパニー Method and apparatus for substantially constant pressure injection molding of thin-walled parts
JP2019130860A (en) * 2018-02-02 2019-08-08 株式会社日本製鋼所 Initial condition setting method for molding condition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004025457A (en) * 2002-06-21 2004-01-29 Toyota Motor Corp Injection molding simulation method
JP2006198796A (en) * 2005-01-18 2006-08-03 Toyota Motor Corp Method and apparatus for calculating molding condition of injection molding machine and molding condition calculating program
JP2014518795A (en) * 2011-05-20 2014-08-07 ザ プロクター アンド ギャンブル カンパニー Method and apparatus for substantially constant pressure injection molding of thin-walled parts
US9815233B2 (en) 2011-05-20 2017-11-14 Imflux, Inc. Method and apparatus for substantially constant pressure injection molding of thinwall parts
JP2019130860A (en) * 2018-02-02 2019-08-08 株式会社日本製鋼所 Initial condition setting method for molding condition

Similar Documents

Publication Publication Date Title
EP1439046B1 (en) Automated molding technology for thermoplastic injection molding
EP0749821B1 (en) A low pressure method for injection molding a plastic article
US5898591A (en) Article of manufacture having computer readable program code for molding an article and method of molding an article by providing computer readable program code
JPH05147090A (en) Method and device for controlling fluctuation of rheological properties of resin in injection molding machine
JPH0952269A (en) Optimum molding condition-setting system for injection mold machine
US9044891B2 (en) Control device of an injection molding machine
JPH05507659A (en) Injection molding machine control method and device
JPH0976320A (en) Automatic setting method for injection molding speed condition of injection mold machine
JPH09272145A (en) Injection molding machine
JP3395589B2 (en) Injection molding machine molding condition setting method
JPH10272663A (en) Optimizing method of molding condition of injection molding machine
JPH08174609A (en) Method for controlling speed of injection molding machine
EP3939765A1 (en) Injection molding method and injection molding machine
JP3618452B2 (en) Setting method of injection speed profile in injection molding machine
JPH08281756A (en) Operation control method for injection molding machine
JP3395542B2 (en) Injection molding machine molding condition setting method
JP2006116920A (en) Resin characteristic measuring method of injection molding machine and injection control method
JP2787470B2 (en) Control method of injection molding machine
JP4028563B2 (en) Local pressure pin drive control method
JPH0422130B2 (en)
AU738181B2 (en) Automated molding technology for thermoplastic injection molding
JPH081744A (en) Controlling method for injection molding machine
JP4913924B2 (en) Method for creating injection speed program pattern of injection molding machine and control device for injection molding machine
JP2006116921A (en) Characteristics measuring device and characteristics measuring method for injection molding machine
JP3114110B2 (en) Control method of injection molding machine

Legal Events

Date Code Title Description
A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20040316