JPS5849172B2 - Plastic injection molding control method - Google Patents
Plastic injection molding control methodInfo
- Publication number
- JPS5849172B2 JPS5849172B2 JP15750278A JP15750278A JPS5849172B2 JP S5849172 B2 JPS5849172 B2 JP S5849172B2 JP 15750278 A JP15750278 A JP 15750278A JP 15750278 A JP15750278 A JP 15750278A JP S5849172 B2 JPS5849172 B2 JP S5849172B2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- cavity
- control method
- injection molding
- molding
- 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.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/76—Measuring, controlling or regulating
- B29C45/77—Measuring, 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)
Description
【発明の詳細な説明】
本発明はプラスチック割出戊形におりる成形条件御制方
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of controlling molding conditions for plastic index molding.
プラスチック躬出成形は第1図に示すように躬出装置3
、型締装置4、材料供給装置5からなる躬出成形機と戊
形型2によって行なわれる。For plastic extrusion molding, as shown in Figure 1, an extrusion device 3 is used.
, a mold clamping device 4 , a material supply device 5 , and an extrusion molding machine and a hollow mold 2 .
従来技術における躬出成形では躬出圧力、保圧力は一義
的に躬出装置3の油圧御制弁6の開閉によって設定して
いるため、樹脂温度、型温、油温、樹脂ロフトの変動に
よるキャビテイ内圧力の変動を生じ、したがって寸法、
重量が均一な成形品が得られなく、また歩留りが低いと
いう欠点があった。In conventional overflow molding, the overflow pressure and holding pressure are primarily set by opening and closing the hydraulic control valve 6 of the overflow device 3, so changes in resin temperature, mold temperature, oil temperature, and resin loft may cause This results in variations in the cavity pressure and therefore the dimensions,
There were disadvantages in that molded products with uniform weight could not be obtained and the yield was low.
本発明の目的は上記した従来技術の欠点をなくして成形
品の寸法、重量精度向上とともに或形歩留りを向上させ
るプラスチック割出或形制御法を提供するにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a plastic indexing or shaping control method that eliminates the above-mentioned drawbacks of the prior art and improves the dimensional and weight accuracy of molded products as well as the production yield.
先ず本発明の原理を説明する。First, the principle of the present invention will be explained.
第2図は成形時における経過時間tとキャビティ内圧力
ps”M出圧力p。Figure 2 shows the elapsed time t during molding and the cavity internal pressure ps''M output pressure p.
、および保圧力p1との関係を模式的に示したものであ
る。, and the relationship between the holding pressure p1 and the holding pressure p1.
第2図においてA点は樹脂がキャビテイに充填しはじめ
た点、B点は充填し終った点、C−D間は成形品のひけ
防止のために保圧力を負荷している工程、D点はゲート
シール点、D−E間は威形品の収縮によってキャビテイ
内圧力が減少していることを示すものである。In Figure 2, point A is the point where the resin has begun to fill the cavity, point B is the point where the filling has finished, and point C and D are the process in which holding pressure is applied to prevent sinking of the molded product, and point D. indicates the gate seal point, and the area between D and E indicates that the pressure inside the cavity is decreasing due to the contraction of the large-sized product.
キャビテイ内圧力プロフィール即ち曲線ABCDEはた
とえ躬出装置の油圧制御弁(第1図の6)の開閉を一定
に設定しても、樹脂温度、型温度、樹脂ロフトの変動に
よって異なりたとえばA’B’C’D’E’のようにな
る(第3図)。Even if the opening/closing of the hydraulic control valve (6 in Fig. 1) of the ejecting device is set constant, the cavity pressure profile, that is, the curve ABCDE, varies depending on changes in resin temperature, mold temperature, and resin loft, for example, A'B'. It will look like C'D'E' (Figure 3).
このキャビテイ内圧力プロフィールの変動が成形品の寸
法精度に影響するわけであるが、本発明者らの研究によ
ればキャビテイ内圧力の寸法におよぼす部分の時間によ
る積分値
ftD
Q(t)− p(t)dt ・・・・・・・
・・・・・ (1)が一定値になるように保圧時間を制
御すればたとえキャビテイ内圧力プロフィールが異なっ
ていても成形品の寸法は同じになることが判った。This variation in the cavity pressure profile affects the dimensional accuracy of the molded product, and according to research by the present inventors, the integral value over time of the portion of the cavity pressure that affects the dimension ftD Q(t)-p (t) dt ・・・・・・・・・
... It was found that if the holding pressure time is controlled so that (1) becomes a constant value, the dimensions of the molded product will be the same even if the cavity pressure profile is different.
このようなQ(t)を一定値になるよう保圧時間を変え
る制御ではゲートシール以前に保圧力を解除することに
なる。In such a control that changes the holding pressure time so that Q(t) becomes a constant value, the holding pressure is released before the gate seals.
この場合の寸法に影響をおよぼすQ(t)は、第4図に
参照すれば、次式のようになる。Q(t), which affects the dimensions in this case, is expressed by the following equation with reference to FIG.
Q(t)= j”:冫t)a t−p( tx) −
( t x−tc )−(2)(2)式においてp(t
x) ・(tx−tc)を差引いている理由は第4図に
おいてXで保圧力を解除するとp(tX)がゲートから
抜けてしまうためで、この場合キャビテイ内圧力の積分
値Q(t)としては口tc−σ・X−txに相当する積
分値を差引いた値を用いるのが良いという実験的事実に
基づいている。Q(t)=j”: t)a t-p(tx) −
(t x - tc) - (2) In equation (2), p(t
x) ・The reason for subtracting (tx - tc) is that when the holding pressure is released at This is based on the experimental fact that it is better to use a value obtained by subtracting the integral value corresponding to tc-σ·X-tx.
第5図は、(2)式で定義した積分値Q(t)と成形品
の寸法との関係を示す一例であって、キャビテイ寸法が
外径φ20mm,高さ14mmの円筒形のものをポリア
セタール樹脂を使って戊形した結果である。Figure 5 is an example showing the relationship between the integral value Q(t) defined by equation (2) and the dimensions of a molded product. This is the result of molding it using resin.
第5図から明らかなように、積分値Q(t)と戒形品寸
法とが強い相関があることが判る。As is clear from FIG. 5, it can be seen that there is a strong correlation between the integral value Q(t) and the dimensions of the precept form.
以下本発明の一実施例を第6図によって説明する。An embodiment of the present invention will be described below with reference to FIG.
或形型2には、第6図に示すように、キャビテイ7内に
設けられたエジエクタピン8の後部にキャビテイ内圧力
を検出するための圧カセンサ9を設ける。As shown in FIG. 6, the certain type mold 2 is provided with a pressure sensor 9 at the rear of an ejector pin 8 provided in the cavity 7 for detecting the pressure inside the cavity.
該キャビテイ内圧力のアナログ信号はA/D変換器10
によってデジタル信号に変えられマイクロコンピュータ
11に入力される。The analog signal of the cavity internal pressure is sent to an A/D converter 10.
is converted into a digital signal and input to the microcomputer 11.
マイクロコンピュータ11は、時刻tにおけるキャビテ
イ内圧力積分値Q(t)を前記(2)式で計算する。The microcomputer 11 calculates the cavity internal pressure integral value Q(t) at time t using the above equation (2).
各成形品に相応しいキャビテイ内圧力積分値Q。Cavity internal pressure integral value Q appropriate for each molded product.
はキャビテイ内圧力積分値設定装置12で設定される。is set by the cavity internal pressure integral value setting device 12.
マイクロコンピュータ11ではQ(t)とQ。とを比較
判定をし、Q(t)がQ。In microcomputer 11, Q(t) and Q. Q(t) is Q.
に等しくなった時にマイクロコンピュータ11から躬出
成形機1への保圧力切断信号を出力する。When it becomes equal to , the microcomputer 11 outputs a holding pressure cut signal to the extrusion molding machine 1.
この出力はD/A変換器13、アンプ14を経て保圧力
切断装置15に至り、或形機の躬出装置を切断し保圧力
を解除する。This output passes through the D/A converter 13 and the amplifier 14 and reaches the holding force cutting device 15, which cuts off the ejection device of a certain type of machine and releases the holding force.
一例として、キャビテイ寸法で外径φ20間内径φ14
ms.,高さ14mπのポリアセタール樹脂円筒或形品
でキャビテイ内圧力積分値Q(t)を5000(kg/
i)・sec4こなるよう制御して或形した場合、各シ
ョット毎の寸法バラツキを高さ寸法で3σ=0.005
mm以内に、重量バラツキで3(7=0.005g以内
にでき歩留りを大巾に向上できた。As an example, the cavity dimensions are between outer diameter φ20 and inner diameter φ14.
ms. , a polyacetal resin cylinder or shaped product with a height of 14 mπ has a cavity internal pressure integral value Q(t) of 5000 (kg/
i)・sec4 When a certain shape is controlled, the dimensional variation for each shot is 3σ = 0.005 in height dimension.
The weight variation was within 3 (7=0.005 g), and the yield was greatly improved.
一方従来の成形法では、躬出圧力600kq/Ci.、
保圧力200一/一、型温60℃、樹脂215℃の設定
条件で前記成形品を戊形じた場合の寸法バラツキは3σ
=0.01關、重量バラツキ3σ=0.012gであっ
た。On the other hand, in the conventional molding method, the ejection pressure is 600 kq/Ci. ,
The dimensional variation when the above molded product is shaped under the setting conditions of holding pressure 2001/1, mold temperature 60℃, and resin 215℃ is 3σ
= 0.01g, weight variation 3σ = 0.012g.
以上詳細に説明したように本発明によれば、キャビテイ
内圧力を時間で積分した値が一定値になるよらに各ショ
ットにおける保圧時間を制御するようにしたので、戒形
品の寸法、重量精度が向上するとともに、成形歩留りも
向上する。As explained in detail above, according to the present invention, the pressure holding time in each shot is controlled so that the value integrated over time of the cavity internal pressure becomes a constant value, so that the dimensions and weight of the shaped product are controlled. Accuracy is improved and molding yield is also improved.
第1図はプラスチック躬出戊形装置の概略を示す説明図
、第2.3.4図は経過時間とキャビテイ内圧力との関
係を示す図、第5図は或形品寸法とキャビテイ内圧力積
分値との関係を示す図、第6図は本発明の一実施例を示
す説明図である。
7・・・・・・キャビテイ。Fig. 1 is an explanatory diagram showing the outline of the plastic protrusion forming device, Fig. 2.3.4 is a diagram showing the relationship between elapsed time and cavity pressure, and Fig. 5 is a diagram showing the relationship between the dimensions of a certain molded product and the cavity pressure. A diagram showing the relationship with the integral value, and FIG. 6 is an explanatory diagram showing one embodiment of the present invention. 7... Cavity.
Claims (1)
を時間で積分した値が一定値になるように各ショットに
おける保圧時間を制御することを特徴とするプラスチッ
ク躬出成形制御法。1. A plastic indexing molding control method, which is characterized by controlling the pressure holding time in each shot so that the value integrated over time of the cavity internal pressure becomes a constant value in plastic indexing molding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15750278A JPS5849172B2 (en) | 1978-12-22 | 1978-12-22 | Plastic injection molding control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15750278A JPS5849172B2 (en) | 1978-12-22 | 1978-12-22 | Plastic injection molding control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5584642A JPS5584642A (en) | 1980-06-26 |
| JPS5849172B2 true JPS5849172B2 (en) | 1983-11-02 |
Family
ID=15651079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15750278A Expired JPS5849172B2 (en) | 1978-12-22 | 1978-12-22 | Plastic injection molding control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5849172B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10621965B2 (en) | 2016-12-04 | 2020-04-14 | Hiroshi Abiko | Acoustic apparatus |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60139422A (en) * | 1983-12-28 | 1985-07-24 | Fanuc Ltd | Injection molding machine |
| DE19524395C1 (en) * | 1995-07-04 | 1996-10-10 | Battenfeld Gmbh | Hydraulic operating system for plastic injection processing machines |
-
1978
- 1978-12-22 JP JP15750278A patent/JPS5849172B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10621965B2 (en) | 2016-12-04 | 2020-04-14 | Hiroshi Abiko | Acoustic apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5584642A (en) | 1980-06-26 |
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