JPH05245894A - Method for determining mold-cooling water flow rate in injection molding - Google Patents
Method for determining mold-cooling water flow rate in injection moldingInfo
- Publication number
- JPH05245894A JPH05245894A JP4845792A JP4845792A JPH05245894A JP H05245894 A JPH05245894 A JP H05245894A JP 4845792 A JP4845792 A JP 4845792A JP 4845792 A JP4845792 A JP 4845792A JP H05245894 A JPH05245894 A JP H05245894A
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- temperature
- cooling water
- water flow
- molded product
- 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
Links
Landscapes
- Moulds For Moulding Plastics Or The Like (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】 本発明は、樹脂の成形金型の冷
却水流量を決定するための方法に関する。TECHNICAL FIELD The present invention relates to a method for determining a cooling water flow rate of a resin molding die.
【0002】[0002]
【従来の技術】 溶融状態の樹脂材料を成形金型に射出
して成形する場合、成形品が離型後に変形するという不
良が発生する。これは、成形品の温度分布が全体にわた
って均一でなく、部分的に温度が高かったりあるいは低
かったりするために生じる。このような変形不良が発生
した場合には、従来では、成形技術者が、成形品の変形
量の大きい場所に近い位置の系統の冷却管の冷却水温度
を低く設定するといった調整、あるいは各系統の冷却水
の流量の調整や冷却時間の調整など行うことによって対
処していた。2. Description of the Related Art When a resin material in a molten state is injected into a molding die for molding, the molded product is deformed after being released from the mold. This occurs because the temperature distribution of the molded product is not uniform throughout and the temperature is partially high or low. When such a deformation defect occurs, conventionally, the molding engineer makes an adjustment such as setting the cooling water temperature of the cooling pipe of the system at a position close to a place where the deformation amount of the molded product is large, or It was dealt with by adjusting the flow rate of cooling water and adjusting the cooling time.
【0003】[0003]
【発明が解決しようとする課題】 ところで、上述の対
処法によると、調整作業を経験のある成形技術者が行う
ことが必要で、しかも成形技術者の経験と勘によっての
み調整を行うので、その調整作業を定量的に取り扱うこ
とが困難で、かなりの時間を要する。このため、従来で
は、生産を開始するまでに、冷却水流量の決定のために
相当な時間を割く必要があった。By the way, according to the above countermeasure, it is necessary for the molding engineer with experience to perform the adjustment work, and the adjustment is performed only by the experience and intuition of the molding engineer. It is difficult to handle the adjustment work quantitatively, and it takes a considerable amount of time. Therefore, conventionally, it was necessary to spend a considerable amount of time for determining the cooling water flow rate before starting the production.
【0004】本発明は、上記の従来の問題点を解消すべ
くなされたもので、その目的とするところは、樹脂成形
品の変形が許容範囲内に入るように樹脂成形品の温度分
布を均一化するための冷却水流量を、成形品生産開始前
に決定することが可能な方法を提供することにある。The present invention has been made to solve the above-mentioned conventional problems, and its object is to make the temperature distribution of the resin molded product uniform so that the deformation of the resin molded product falls within an allowable range. It is an object of the present invention to provide a method capable of determining the flow rate of cooling water for realization before starting the production of molded articles.
【0005】[0005]
【課題を解決するための手段】 本発明方法は、実施例
に対応する図1,図2に示すように、成形品の形状モデ
ル1a,1bと前記成形品を作る成形金型の複数系統2
1・・28の冷却管モデル2とを成形金型内での位置関係
となるよう設定し、冷却水流量をパラメータとして所定
時間後の成形品の形状モデル1a,1bの温度分布をシ
ミュレーションする解析手法を用いて、成形金型への冷
却水流量を決定する方法であって、〓設定された冷却水
流量を用いて上記のシミュレーション解析を行って所定
時間後の成形品の形状モデル1a,1bの温度分布を算
出し(ST6 )、次いでその温度分布から最大温度となっ
た部位Pとその温度Tmax および最小温度Tmin を求め
(ST7 )、〓その最大温度Tmax と最小温度Tmin との
温度差を算出してこの差演算値が許容値Tc以下である
か否かを判定し(ST8 )、〓その判定結果が以下でない
ときには、上記の〓の解析(ST6 )で用いる流量データ
のうち、上記の最大温度Tmax となった部位に最も近い
位置の冷却管2の系統25の冷却水流量データのみを、
所定流量Δvだけ上げたデータに変更し(ST9,ST5 )、
これらの手順〓,〓および〓を、上記の〓での判定結果
が許容値Tc以下となるまで順次繰り返して行うことに
よって特徴づけられる。Means for Solving the Problems As shown in FIGS. 1 and 2 corresponding to an embodiment, the method of the present invention includes shape models 1a and 1b of molded products and a plurality of systems 2 of molding dies for making the molded products.
An analysis for simulating the temperature distribution of the shape models 1a and 1b of the molded product after a predetermined time by setting the cooling pipe model 2 of 1 ... 28 to have a positional relationship in the molding die and using the cooling water flow rate as a parameter. A method for determining the cooling water flow rate to a molding die by using a method, wherein the above-mentioned simulation analysis is performed using the set cooling water flow rate, and the shape model 1a, 1b of the molded product after a predetermined time. The temperature distribution is calculated (ST6), and the maximum temperature P, its temperature Tmax and minimum temperature Tmin are calculated from the temperature distribution (ST7), and the temperature difference between the maximum temperature Tmax and the minimum temperature Tmin is calculated. It is determined whether or not the calculated difference value is less than or equal to the allowable value Tc (ST8). If the result of the determination is not less than the following, among the flow rate data used in the above-mentioned analysis (ST6), Maximum temperature Tma Only the cooling water flow rate data of the system 25 of the cooling pipe 2 at the position closest to the part where x becomes
Change to data increased by a predetermined flow rate Δv (ST9, ST5),
It is characterized in that these steps 〓, 〓 and 〓 are sequentially repeated until the judgment result in the above 〓 becomes equal to or less than the allowable value Tc.
【0006】[0006]
【作用】 金型と冷却水との熱移動は熱伝達係数によっ
て決まり、その関係は式1にて示すことができる。[Operation] The heat transfer between the mold and the cooling water is determined by the heat transfer coefficient, and the relationship can be expressed by Equation 1.
【0007】[0007]
【数1】 [Equation 1]
【0008】さらに冷却水が乱流の場合、熱伝達係数は
式2で示される。Further, when the cooling water is turbulent, the heat transfer coefficient is expressed by equation (2).
【0009】[0009]
【数2】 [Equation 2]
【0010】よって、冷却水の速度、つまり、単位時間
当りの流量が増加すれば、熱の移動が大きくなり冷却効
果が増すことになる。したがって、手順〓,〓および〓
を繰り返してゆくと、成形品の形状モデル1a,1bの
温度分布の最大と最小温度との差が小さくなってゆく。
そして、その温度差が許容値Tc以下となった時点で、
成形品温度分布が全体にわたってほぼ均一となる冷却水
流量を得ることができる。Therefore, if the speed of the cooling water, that is, the flow rate per unit time increases, the heat transfer increases and the cooling effect increases. Therefore, steps 〓, 〓 and 〓
By repeating the above, the difference between the maximum and minimum temperatures of the temperature distribution of the shape models 1a and 1b of the molded product becomes smaller.
Then, when the temperature difference becomes equal to or less than the allowable value Tc,
It is possible to obtain a cooling water flow rate in which the temperature distribution of the molded product is almost uniform throughout.
【0011】[0011]
【実施例】 まず、本発明は、基本的にはCAE(Comp
uter Aided Engine-ering )システム等を用いたシミュ
レーションによって成形金型の冷却水流量を決定する方
法であって、その実施例を、以下、図面に基づいて説明
する。First, the present invention is basically a CAE (Comp
uter Aided Engine-ering) system or the like, which is a method for determining the cooling water flow rate of a molding die, and an example thereof will be described below with reference to the drawings.
【0012】図1は本発明方法の実施例の手順を示すフ
ローチャートである。まず、冷却水流量をパラメータと
して境界要素法あるいは差分法などによって所定時間後
の成形品温度分布の解析を行うための、成形品の形状モ
デルおよび複数の系統からなる冷却管モデルを作成する
(ST1 )。この例では、図2に示すように、配管接続部
品のエルボを成形対象とする場合の成形品の形状モデル
1a,1bと複数の系統21・・28からなる冷却管モデ
ル2とを解析モデルとする。FIG. 1 is a flow chart showing the procedure of an embodiment of the method of the present invention. First, a shape model of a molded product and a cooling pipe model consisting of multiple systems are created to analyze the molded product temperature distribution after a predetermined time by the boundary element method or the difference method using the cooling water flow rate as a parameter (ST1 ). In this example, as shown in FIG. 2, the shape models 1a and 1b of the molded product and the cooling pipe model 2 including a plurality of systems 21 ... To do.
【0013】さて、以上の解析モデル作成が完了した後
に、冷却水流量の初期データおよび冷却時間t秒が入力
されると(ST2,ST3 )、これらの入力データに基づいて
まずは1回目の冷却解析を行って成形品の形状モデル1
の温度分布を算出し(ST6 )、この冷却解析によって得
られた成形品温度分布から最大の温度の部位Pとその温
度Tmax ならびに最小の温度の部位Qの温度Tmin を求
める(ST7 )。When the initial data of the cooling water flow rate and the cooling time t seconds are input (ST2, ST3) after the above-mentioned analysis model creation is completed, the first cooling analysis is performed based on these input data. Shape model 1 of the molded product
Is calculated (ST6), and from the temperature distribution of the molded product obtained by this cooling analysis, the maximum temperature portion P and its temperature Tmax and the minimum temperature portion Q temperature Tmin are obtained (ST7).
【0014】次に、最大と最小の温度差(Tmax −Tmi
n )を演算し、この演算結果が許容値Tc以下であるか
否かを判定し(ST8 )、以下でないときには、成形品温
度分布の最大温度となった部位に最も近い位置の冷却管
の系統の冷却水流量データをΔvだけ上げたデータを求
める(ST9 )。例えば図2において、成形品の形状モデ
ル1bの部位Pの温度が最大温度Tmax となった場合に
は、冷却管の系統25の冷却水流量データにΔvを加え
るいった補正を行い、この後、ステップST4 へと戻る。
なお、Δvは、この解析用のシステムにあらかじめ入力
・記憶した値である。Next, the maximum and minimum temperature difference (Tmax-Tmi
n) is calculated, and it is determined whether or not this calculation result is less than or equal to the allowable value Tc (ST8). If not, the system of the cooling pipe closest to the part where the maximum temperature of the molded product temperature distribution is reached. Obtain the data obtained by increasing the cooling water flow rate data by Δv (ST9). For example, in FIG. 2, when the temperature of the part P of the shape model 1b of the molded product reaches the maximum temperature Tmax, correction is performed by adding Δv to the cooling water flow rate data of the cooling pipe system 25, and thereafter, Return to step ST4.
It should be noted that Δv is a value that has been input and stored in advance in this analysis system.
【0015】これ以後の冷却解析つまり2回目以後の解
析については、まずは冷却解析に用いる各系統21・・2
8の冷却水流量データのうち、ステップST9 で演算を行
った系統、例えば系統25の流量データのみを先の演算
後のデータに変更し(ST5 )、この後に、冷却解析と温
度差の演算を行い(ST6 〜ST8 )、この演算後の温度差
が許容値Tc以下でないときにはステップST9 へと移行
して、再度、ステップST5 〜ST9 を順次繰り返してゆ
く。そして、判断ステップST8 に判定結果が許容値Tc
以下となった時点で、冷却管2の各系統21・・28のそ
れぞれの冷却水流量データを採取して、その各流量デー
タをCRT等の画面上への表示やプリントアウトなどを
行う(ST10)。Regarding the cooling analysis after this, that is, the second and subsequent analyzes, first, each system 21 ...
Of the cooling water flow rate data of No. 8, only the flow rate data of the system that was calculated in step ST9, for example system 25, is changed to the data after the previous calculation (ST5), and then the cooling analysis and the calculation of the temperature difference are performed. When the temperature difference after this calculation is not less than the allowable value Tc, the process proceeds to step ST9, and steps ST5 to ST9 are sequentially repeated again. Then, in the judgment step ST8, the judgment result is the allowable value Tc.
When the following occurs, the cooling water flow rate data of each system 21 ... 28 of the cooling pipe 2 is collected, and the flow rate data is displayed on a screen such as a CRT or printed out (ST10). ).
【0016】以上の手順によって、成形品の温度分布を
全体にわたってほぼ均一にできる冷却水流量を、冷却管
2の各系統21・・22ごとにそれぞれ求めることができ
る。そして、求めた冷却水流量となるよう各系統の冷却
管につながるポンプの圧力又はバルブ開度を調節する。
この調整は、作業者が流量計を見ながら調整してもよい
し、自動調整可能な装置があれば、その装置に冷却水流
量を設定してもよい。ここで、判断ステップST8 の許容
値Tcは、生産する成形品の形状寸法の相違や樹脂の種
別等によって異なるため、この例では、特に数値を示さ
ないが、その許容値Tcは、例えば、成形品の温度分布
にばらつきがあっても成形品が変形しない温度範囲を、
成形品の形状寸法、射出する樹脂の種別およびその温度
ならびに冷却時間などの諸条件に基づいて、あらかじめ
計算等によって求めておき、その算出値を採用するよう
にすればよい。By the above procedure, the cooling water flow rate that can make the temperature distribution of the molded product substantially uniform over the whole can be determined for each system 21 ... 22 of the cooling pipe 2. Then, the pressure or valve opening of the pump connected to the cooling pipe of each system is adjusted so that the obtained cooling water flow rate is obtained.
This adjustment may be performed by an operator while looking at the flow meter, or if there is an automatically adjustable device, the cooling water flow rate may be set in that device. Here, since the allowable value Tc of the judgment step ST8 is different due to the difference in the shape and size of the molded product to be produced, the type of resin, etc., no particular numerical value is shown in this example, but the allowable value Tc is, for example, Even if there is variation in the temperature distribution of the product, the temperature range where the molded product does not deform,
Based on various conditions such as the shape and size of the molded product, the type of resin to be injected, its temperature, and the cooling time, it may be obtained in advance by calculation and the calculated value may be adopted.
【0017】[0017]
【発明の効果】 以上説明したように、本発明方法によ
れば、成形品の温度分布を均一化、つまり成形品に変形
不良が発生することを防止できる冷却水流量を、冷却解
析シミュレーションによって決定することができるの
で、従来行われていた、ダミー成形により冷却水流量を
決定する等の作業が不要となって、成形ライン構築後に
すぐに生産を開始することが可能となる。しかも、冷却
水流量の決定を、経験のある成形技術者でなくても容易
に行うことができる。As described above, according to the method of the present invention, the cooling water flow rate that can make the temperature distribution of the molded product uniform, that is, prevent the defective deformation of the molded product from occurring is determined by the cooling analysis simulation. Since it is possible to do so, the work such as determining the flow rate of the cooling water by dummy molding which has been conventionally performed is unnecessary, and it becomes possible to start the production immediately after the molding line is constructed. Moreover, the cooling water flow rate can be easily determined even by an experienced molding engineer.
【図面の簡単な説明】[Brief description of drawings]
【図1】 本発明方法の実施例の手順を示すフローチャ
ートFIG. 1 is a flow chart showing the procedure of an embodiment of the method of the present invention.
【図2】 その実施例で使用する成形品の形状モデルお
よび冷却管モデルの例を示す図FIG. 2 is a diagram showing an example of a shape model of a molded product and a cooling pipe model used in the embodiment.
1a,1b・・・・成形品の形状モデル 2・・・・冷却管モデル 21・・28・・・・冷却管の系統 1a, 1b ・ ・ ・ ・ Shape model of molded product 2 ・ ・ ・ ・ ・ ・ Cooling pipe model 21 ・ ・ 28 ・ ・ ・ ・ System of cooling pipe
Claims (1)
成形金型の複数系統の冷却管モデルとを成形金型内での
位置関係となるよう設定し、冷却水流量をパラメータと
して所定時間後の上記成形品の形状モデルの温度分布を
シミュレーションする解析手法を用いて、成形金型への
冷却水流量を決定する方法であって、〓設定された冷却
水流量を用いて上記シミュレーション解析を行って所定
時間後の上記成形品の形状モデルの温度分布を算出し、
次いでその温度分布から最大温度となった部位とその温
度および最小温度を求め、〓その最大温度と最小温度と
の温度差を算出してこの差演算値が許容値以下であるか
否かを判定し、〓その判定結果が以下でないときには、
上記の〓の解析で用いる流量データのうち、上記の最大
温度となった部位に最も近い位置の系統の上記冷却管の
冷却水流量データのみを、所定流量だけ上げたデータに
変更し、これらの手順〓,〓および〓を、上記の〓での
判定結果が許容値以下となるまで順次繰り返して行うこ
とを特徴とする、射出成形における金型冷却水流量の決
定方法。1. A shape model of a molded product and a plurality of cooling pipe models of a molding mold for forming the molded product are set to have a positional relationship in the molding mold, and a cooling water flow rate is used as a parameter for a predetermined time. A method of determining the cooling water flow rate to the molding die by using an analysis method for simulating the temperature distribution of the shape model of the molded product afterwards, in which the above simulation analysis is performed using the set cooling water flow rate. Calculate the temperature distribution of the shape model of the above molded product after a predetermined time,
Next, from the temperature distribution, find the maximum temperature, its temperature and minimum temperature, and calculate the temperature difference between the maximum temperature and the minimum temperature to determine whether this difference calculation value is below the allowable value. However, if the judgment result is not below,
Of the flow rate data used in the above-mentioned analysis, only the cooling water flow rate data of the cooling pipe of the system closest to the part where the maximum temperature is reached is changed to the data increased by a predetermined flow rate. A method for determining the mold cooling water flow rate in injection molding, characterized in that the steps 〓, 〓 and 〓 are sequentially repeated until the judgment result in the above 〓 becomes less than the allowable value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4845792A JPH05245894A (en) | 1992-03-05 | 1992-03-05 | Method for determining mold-cooling water flow rate in injection molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4845792A JPH05245894A (en) | 1992-03-05 | 1992-03-05 | Method for determining mold-cooling water flow rate in injection molding |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05245894A true JPH05245894A (en) | 1993-09-24 |
Family
ID=12803891
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4845792A Pending JPH05245894A (en) | 1992-03-05 | 1992-03-05 | Method for determining mold-cooling water flow rate in injection molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05245894A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4834508A (en) * | 1985-03-01 | 1989-05-30 | Manchester R & D Partnership | Complementary color liquid crystal display |
US4878741A (en) * | 1986-09-10 | 1989-11-07 | Manchester R & D Partnership | Liquid crystal color display and method |
US5208686A (en) * | 1985-03-01 | 1993-05-04 | Manchester R&D Partnership | Liquid crystal color display and method |
US5345322A (en) * | 1985-03-01 | 1994-09-06 | Manchester R&D Limited Partnership | Complementary color liquid crystal display |
CN103963255A (en) * | 2013-02-04 | 2014-08-06 | 恩格尔奥地利有限公司 | Temperature Control Device For A Shaping Tool And Method Of Controlling The Same |
-
1992
- 1992-03-05 JP JP4845792A patent/JPH05245894A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4834508A (en) * | 1985-03-01 | 1989-05-30 | Manchester R & D Partnership | Complementary color liquid crystal display |
US5208686A (en) * | 1985-03-01 | 1993-05-04 | Manchester R&D Partnership | Liquid crystal color display and method |
US5345322A (en) * | 1985-03-01 | 1994-09-06 | Manchester R&D Limited Partnership | Complementary color liquid crystal display |
US4878741A (en) * | 1986-09-10 | 1989-11-07 | Manchester R & D Partnership | Liquid crystal color display and method |
CN103963255A (en) * | 2013-02-04 | 2014-08-06 | 恩格尔奥地利有限公司 | Temperature Control Device For A Shaping Tool And Method Of Controlling The Same |
AT513872A2 (en) * | 2013-02-04 | 2014-08-15 | Engel Austria Gmbh | Temperature control device for a mold and method for operating the same |
AT513872A3 (en) * | 2013-02-04 | 2016-06-15 | Engel Austria Gmbh | Temperature control device for a mold and method for operating the same |
AT513872B1 (en) * | 2013-02-04 | 2016-06-15 | Engel Austria Gmbh | Temperature control device for a mold and method for operating the same |
US9718219B2 (en) | 2013-02-04 | 2017-08-01 | Engel Austria Gmbh | Temperature control device for a shaping tool and method of controlling same |
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