JPH04348926A - Resin changing method of injection molder - Google Patents

Resin changing method of injection molder

Info

Publication number
JPH04348926A
JPH04348926A JP3084536A JP8453691A JPH04348926A JP H04348926 A JPH04348926 A JP H04348926A JP 3084536 A JP3084536 A JP 3084536A JP 8453691 A JP8453691 A JP 8453691A JP H04348926 A JPH04348926 A JP H04348926A
Authority
JP
Japan
Prior art keywords
resin
supply
color change
raw material
amount
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.)
Withdrawn
Application number
JP3084536A
Other languages
Japanese (ja)
Inventor
Hideo Kuroda
英夫 黒田
Chikatsu Saito
斉藤 千勝
Masayoshi Kasai
笠井 昌義
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.)
Churyo Engineering Co Ltd
Mitsubishi Heavy Industries Ltd
Original Assignee
Churyo Engineering Co Ltd
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Churyo Engineering Co Ltd, Mitsubishi Heavy Industries Ltd filed Critical Churyo Engineering Co Ltd
Priority to JP3084536A priority Critical patent/JPH04348926A/en
Publication of JPH04348926A publication Critical patent/JPH04348926A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To carry out quick color change by a method wherein feed ratio and stroke ratio are specified. CONSTITUTION:In order to perform quick color change and stock feeding for normal running in an alternative way, a stock resin feeding selecting means 21, the detecting means 30 of the start of color changing resin feeding, the detecting means 40 of the completion of discharging and the detecting means 50 of the completion of color change. In this case, let X1 be a feed ratio and X3 be a stroke ratio, then conditions: 0.7<=X1<=1.8 and 1<=X3<=1.7 are satisfied when the amount of resin consumed for resin change is minimum, where X1=P1 V1/(PCV1+PFVF), X3=stroke/screw diameter, V1 represents intermittent feed (m<3>), VF represents the volume (m3) of a feeding section, VC represents the volume (m<3>) of a compression section, VM represents the volume (m<3>) of a metering section, VO represents the volume (m<3>) per one shot of injection and P1, PF and PC represent the densities at the respective sections.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は射出成形機の樹脂替え方
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 for changing resin in an injection molding machine.

【0002】0002

【従来の技術】射出成形機や押出成形機の色替性能を改
良した原料供給装置としては、その一例が特公昭62−
41450号公報に開示されており、同装置は図12に
示す如く原料供給装置11の原料通路9の途中にシャッ
タ12を設けて、これを開閉制御することにより原料樹
脂を間欠供給するものである。同図において、1はスク
リュ、2はシリンダ、3はエンドキャップ、4は射出ノ
ズル、5はスクリュ回転用油圧モータ、6は原料樹脂供
給用ホッパ、7は射出シリンダであり、同射出シリンダ
7の原料通路9の途中には図示しない制御装置によりタ
イミングを合わせて原料通路9を開閉するシャッタ8が
設けられている。なお、図中10はトーピードである。
[Prior Art] One example of a raw material supply device that improves the color changing performance of injection molding machines and extrusion molding machines is
This device is disclosed in Japanese Patent No. 41450, and as shown in FIG. 12, a shutter 12 is provided in the middle of a raw material passage 9 of a raw material supply device 11, and raw resin is intermittently supplied by controlling opening and closing of the shutter 12. . In the figure, 1 is a screw, 2 is a cylinder, 3 is an end cap, 4 is an injection nozzle, 5 is a hydraulic motor for rotating the screw, 6 is a hopper for supplying raw resin, and 7 is an injection cylinder. A shutter 8 is provided in the middle of the raw material passage 9 to open and close the raw material passage 9 in accordance with the timing by a control device (not shown). In addition, 10 in the figure is a torpedo.

【0003】スクリュ1はその基端側から順にフィード
部a、コンプレッション部b、メータリング部cを構成
する。色替え時に最も旧樹脂が残り滞留し易い個所は、
トーピードの外周面d、エンドキャップ3の内壁面e及
びノズル4の内壁面fである。ここで原料供給装置とは
、ホッパ6、シャッタ8、原料通路9及び図示しないシ
ャッタ開閉機構を含む部分を意味する。但し、原料通路
9はシリンダ2側のみでなく、ホッパ6の筒状出口部を
も含んでいる。
[0003] The screw 1 constitutes a feed section a, a compression section b, and a metering section c in order from its base end side. The areas where old resin is most likely to remain when changing colors are:
These are the outer peripheral surface d of the torpedo, the inner wall surface e of the end cap 3, and the inner wall surface f of the nozzle 4. The raw material supply device herein means a portion including the hopper 6, the shutter 8, the raw material passage 9, and a shutter opening/closing mechanism (not shown). However, the raw material passage 9 includes not only the cylinder 2 side but also the cylindrical outlet portion of the hopper 6.

【0004】さて図において原料供給装置11の原料通
路9をシャッタ12により閉塞して旧原料の供給を止め
、この状態でスクリュ1の回転と射出を繰り返して、少
なくともスクリュ1のフィード部a及びコンプレッショ
ン部bを空洞状態(これを飢餓状態ともいう)にすると
共に、ホッパ6内の原料を新原料に交換する。次にシャ
ッタ12を開いてスクリュ1を回転させる。この時前記
空洞部には新しい未溶融の樹脂が充満することになる。 この状態で更にスクリュ1の回転を継続すると、スクリ
ュ1の先端部の樹脂滞留部d、e、fには定常運転状態
の時より高粘度の溶融樹脂が供給され、樹脂圧が高くな
ってスクリュ1は後退する。
Now, as shown in the figure, the raw material passage 9 of the raw material supply device 11 is closed by the shutter 12 to stop the supply of the old raw material, and in this state, the rotation and injection of the screw 1 are repeated, and at least the feed section a of the screw 1 and the compression The part b is brought into a hollow state (this is also called a starvation state), and the raw material in the hopper 6 is replaced with a new raw material. Next, the shutter 12 is opened and the screw 1 is rotated. At this time, the cavity is filled with new unmelted resin. When the screw 1 continues to rotate in this state, molten resin with a higher viscosity than in the steady operating state is supplied to the resin retention parts d, e, and f at the tip of the screw 1, and the resin pressure increases, causing the screw to 1 retreats.

【0005】スクリュ1が計量ストロークまで後退する
と、スクリュ1の回転を止め、シリンダ7の背圧側に油
圧が供給されてスクリュ1が前進し射出工程に移る。こ
のとき高粘度の溶融樹脂が樹脂滞留部d、e、fを流れ
、樹脂流路壁面に大きな剪断力が働き、壁面に付着して
いる旧樹脂の掻き取り効果が生ずる。このスクリュ回転
と射出を繰り返すことにより、チェックリング11を境
にして、樹脂の流れの上流部は主としてソリッドベッド
による剪断による掻き取り作用によって、下流部は高粘
度の溶融樹脂流動による高い剪断力によって掻き取り作
用が働き、樹脂流路に付着した旧樹脂の除去、即ち色替
えが進行し、やがて定常状態に達する。
When the screw 1 is retracted to the metered stroke, the rotation of the screw 1 is stopped, hydraulic pressure is supplied to the back pressure side of the cylinder 7, and the screw 1 moves forward to proceed to the injection process. At this time, the highly viscous molten resin flows through the resin retention parts d, e, and f, and a large shearing force acts on the wall surface of the resin flow path, producing an effect of scraping off the old resin adhering to the wall surface. By repeating this screw rotation and injection, the upstream part of the resin flow with the check ring 11 as a border is mainly affected by the scraping action due to shearing by the solid bed, and the downstream part is affected by the high shearing force caused by the flow of high-viscosity molten resin. The scraping action works, and the removal of the old resin adhering to the resin flow path, that is, the color change progresses, and eventually a steady state is reached.

【0006】しかしこの定常状態になった状態では、各
部の温度が上昇して樹脂の粘度は低下するので、壁面に
作用する剪断力は小さくなって前述の作用が小さくなる
ため、シャッタ12を閉じて再度前記の各操作を行ない
、更にこれを繰り返して行なう。このようにホッパ内の
原料樹脂供給を一旦停止し、シリンダ内の溶融樹脂を抜
き取った所へ、未溶融樹脂を送り込む操作による色替え
の効果は、単に樹脂を交替した後にスクリュの回転と射
出を繰り返しながら色替えを行なう従来方式に比して、
樹脂消費量で60%減という格別の効果を得ている。
However, in this steady state, the temperature of each part increases and the viscosity of the resin decreases, so the shearing force acting on the wall becomes smaller and the above-mentioned effect becomes smaller, so the shutter 12 is closed. Then, perform each of the above operations again, and then repeat this process again. In this way, the effect of color change by temporarily stopping the supply of raw resin in the hopper and feeding unmolten resin into the place where the molten resin in the cylinder has been extracted is simply to change the resin and then turn the screw and inject it. Compared to the conventional method of changing colors repeatedly,
An exceptional effect has been achieved, with a 60% reduction in resin consumption.

【0007】しかしながら前記の色替方法では、色替え
の所要時間が従来と余り変わらないという点で改善の余
地が残されている。その主な原因は前述の樹脂替え操作
1サイクル当りの樹脂充填量が過大であるため、定常状
態に達した後、未溶融樹脂充填のために空洞を生成する
こと、即ち樹脂排出のための所要時間が短縮されないこ
とにある。この問題解決のために、樹脂充填量を掻き取
り効果が最大限に発揮される最小量にして、色替え時間
の短縮を図ることを目的とした原料樹脂供給装置を、本
発明の発明者等は先に特願平1−254865号にて提
案した。
However, the color changing method described above leaves room for improvement in that the time required for color changing is not much different from the conventional method. The main reason for this is that the amount of resin filled per cycle of the resin change operation described above is excessive, and after reaching a steady state, a cavity is created to fill the unmolten resin, that is, the amount required for resin discharge is The reason is that time is not shortened. In order to solve this problem, the inventors of the present invention developed a raw resin supply device that aims to shorten the color change time by reducing the resin filling amount to the minimum amount that maximizes the scraping effect. was previously proposed in Japanese Patent Application No. 1-254865.

【0008】即ち、前記先願の原料樹脂供給装置は、射
出成形機又は押出機に用いられる原料樹脂供給装置であ
って、色替対象の原料を用いて色替運転を行なうにあた
り、樹脂通路を間欠開閉して原料樹脂をフィード部に間
欠供給する原料供給装置において、樹脂通路の途中に設
けられ、原料樹脂のフィード部への供給を、特定量の間
欠的供給と連続供給を択一的に選択する原料樹脂供給選
択手段と、前記特定量の供給開始時期を検出する色替樹
脂供給開始検出手段と、特定量の原料樹脂相当分の排出
完了を検出する排出完了検出手段と、色替完了検出手段
とを具備し、迅速な色替えと通常運転のための原料供給
を択一的に行なうようにしたものである。
That is, the raw resin supply device of the prior application is a raw resin supply device used for an injection molding machine or an extruder, and when performing a color change operation using the raw material to be color changed, the resin passage is In a raw material supply device that opens and closes intermittently to intermittently supply raw resin to the feed section, it is installed in the middle of the resin passage and selectively supplies a specific amount of raw resin to the feed section between intermittent supply and continuous supply. A raw material resin supply selection means to select, a color change resin supply start detection means for detecting the supply start time of the specified amount, a discharge completion detection means for detecting completion of discharge corresponding to the specified amount of raw resin, and a color change completion detection means. The apparatus is equipped with a detection means, and is configured to selectively perform a quick color change and supply raw materials for normal operation.

【0009】前記特定の樹脂充填量の制御は、原料通路
を開閉する1個の開閉手段の開時間制御によって、或い
は2個の開閉手段を間隔を置いて設け、これを交互に開
閉することにより一定容積の原料を計量することによっ
て行なうことができ、掻き取り効果が最大限に発揮され
る最小量を充填するようにする。要するに小量の未溶融
樹脂を多数回スクリュの空洞部に充填して、掻き取り効
果の大きい状態を維持しながら色替え作業を行ない、色
替えのための樹脂の損失低減と、所要時間を短縮するこ
とである。
The specific resin filling amount can be controlled by controlling the opening time of one opening/closing means for opening and closing the raw material passage, or by providing two opening/closing means at a distance and opening and closing them alternately. This can be done by weighing a certain volume of raw material, ensuring that the minimum amount is filled to maximize the scraping effect. In short, a small amount of unmelted resin is filled into the screw cavity many times, and the color change operation is performed while maintaining a high scraping effect, reducing the loss of resin and shortening the time required for color change. It is to be.

【0010】前記原料樹脂供給装置において、制御装置
のメインサイクルから色替え指令が出ると、色替完了検
出手段の判断部で比較され、未だ色替えがなされていな
いため、当然に色替完了検出手段からの初期値は0であ
るから、NOの信号が出力され、原料樹脂供給選択手段
は原料供給を停止する。しかし原料供給が停止された後
も、射出サイクルはシリンダ内の空洞部が所定長に達す
るまで続行する。空洞部の長さが所定長に達したことは
、色替樹脂供給開始検出手段にて判断され、ここで最初
の色替原料樹脂が特定量供給されて射出が繰り返され、
シリンダ内樹脂を排出する。この排出分が特定量供給分
に達したか否かを特定充填量排出検出手段によって判断
され、条件が満足するまでこの排出サイクルが続く。
In the raw material resin supply device, when a color change command is issued from the main cycle of the control device, it is compared in the judgment section of the color change completion detection means, and since the color change has not yet been performed, it is natural that the color change completion is detected. Since the initial value from the means is 0, a NO signal is output, and the raw material resin supply selection means stops supplying the raw material. However, even after the feedstock supply is stopped, the injection cycle continues until the cavity within the cylinder reaches a predetermined length. It is determined by the color change resin supply start detection means that the length of the cavity has reached a predetermined length, and the first color change raw material resin is supplied in a specific amount and injection is repeated.
Drain the resin inside the cylinder. The specific filling amount discharge detection means determines whether or not this discharge amount has reached the specified amount supplied, and this discharge cycle continues until the condition is satisfied.

【0011】前記の排出完了は、例えば射出回数が所定
の設定数に達したかどうかで判断される。この排出サイ
クルが完了する毎に色替条件、完了条件の入力値は1だ
け増加し、その値が設定値に達するまで、即ち原料樹脂
の特定量が所定回数充填され、排出されるまでこのサイ
クルは続行する。前記入力値が設定値に達すると色替え
は完了し、以後は通常運転状態にリセットされて通常の
成形サイクルに戻る。
[0011] The above-mentioned ejection completion is determined based on, for example, whether the number of injections has reached a predetermined set number. Each time this discharge cycle is completed, the input values for the color change condition and completion condition increase by 1, and the cycle continues until the values reach the set values, that is, until the specified amount of raw resin is filled and discharged a predetermined number of times. continues. When the input value reaches the set value, the color change is completed, and thereafter the normal operating state is reset and the normal molding cycle is resumed.

【0012】前記先願の原料樹脂供給装置を図6につい
て説明すると、1はスクリュ、2はシリンダ、3はエン
ドキャップ、4は射出ノズル、5はスクリュ回転用油圧
モータ、6は原料樹脂供給用ホッパ、7は射出用油圧シ
リンダ、9は原料通路、10はトーピード、11はチェ
ックリングである。また20は原料樹脂供給装置で、原
料樹脂供給用ホッパ6、原料通路9を含む次の各部分(
符号21、30、40、50)から構成される。即ち、
21は原料樹脂選択供給手段であり、原料樹脂供給用ホ
ッパ6とシリンダ2の内部を連絡する原料通路9の途中
に設けられている。例えば、制御装置60からの指令で
原料通路9を開閉するシャッタなどから成る。
[0012] The raw resin supply device of the prior application will be explained with reference to Fig. 6. 1 is a screw, 2 is a cylinder, 3 is an end cap, 4 is an injection nozzle, 5 is a hydraulic motor for rotating the screw, and 6 is for supplying raw resin. Hopper, 7 is a hydraulic cylinder for injection, 9 is a raw material passage, 10 is a torpedo, and 11 is a check ring. Further, 20 is a raw resin supply device, which includes the following parts (
21, 30, 40, 50). That is,
Reference numeral 21 denotes a raw material resin selective supply means, which is provided in the middle of the raw material passage 9 that communicates the raw material resin supplying hopper 6 and the inside of the cylinder 2 . For example, it includes a shutter that opens and closes the raw material passage 9 based on commands from the control device 60.

【0013】また30は空洞長が所定量に達したかどう
かを判断する色替樹脂供給開始検出手段であり、例えば
公知のスクリュ回転数計数器80で計数されたスクリュ
1の回転数が予め設定されたスクリュ回転数に達したこ
とを検出し、制御装置60に出力するものである。40
は樹脂の特定充填量分が、射出の繰り返しにより排出さ
れたかどうかを検出する排出完了検出手段であり、例え
ばスクリュ1のストローク回数を計測器で計測し、予め
設定されたストローク数に達すると制御装置に出力する
ものである。また50は色替完了検出手段であり、これ
は原料樹脂による特定量の充填回数が、予め設定された
回数に達すると制御装置に出力し、通常運転等に切換え
るための検出手段である。
Further, 30 is a color change resin supply start detection means for determining whether the cavity length has reached a predetermined amount. It detects that the specified screw rotation speed has been reached and outputs it to the control device 60. 40
is an ejection completion detection means that detects whether a specific amount of filled resin has been ejected through repeated injections. For example, the number of strokes of the screw 1 is measured with a measuring device, and when the number of strokes set in advance is reached, the control is performed. This is what is output to the device. Further, 50 is a color change completion detection means, which outputs an output to the control device when the number of times of filling a specific amount of raw material resin reaches a preset number of times, and switches to normal operation or the like.

【0014】図7は前記原料樹脂供給装置をもつ射出成
形機における動作フローチャートを示す。図7において
、N1 はスクリュ回転数、N2 は射出回数、N3 
は原料樹脂の特定充填量供給回数を示し、N1S、N2
S、N3Sはそれぞれに対応する予め設定された値であ
り、次に示す意義をもつ。 N1S…色替樹脂の供給開始時期を決定する判断基準で
あって、設定時間又はスクリュ回転の総回転数設定値。 N2S…原料樹脂の特定充填量分の排出完了を決定する
判定基準であって、射出回数設定値。 N3S…色替完了を検出判断する基準値となるものであ
って、原料樹脂特定充填量の供給回数設定値。
FIG. 7 shows an operation flowchart of an injection molding machine having the raw resin supply device. In Fig. 7, N1 is the screw rotation speed, N2 is the number of injections, and N3 is the number of injections.
indicates the number of times the specified filling amount of raw resin is supplied, N1S, N2
S and N3S are preset values corresponding to each, and have the following meanings. N1S: Criteria for determining the time to start supplying color change resin, which is a set time or a set value for the total number of rotations of the screw. N2S: A criterion for determining the completion of discharging a specific filling amount of raw material resin, and a set value for the number of injections. N3S: This is a reference value for detecting and judging the completion of color change, and is a set value for the number of times a specific filling amount of raw resin is supplied.

【0015】次に前記従来装置の作用について説明する
。先ず制御装置60のメインサイクルから色替え運転信
号が出力されると、原料樹脂供給装置20の原料樹脂供
給選択手段21は旧原料の供給を停止する。一般に原料
の供給を停止した状態で射出運転を継続すると、スクリ
ュ1のねじ溝mとシリンダ2の内壁面で形成される原料
樹脂移送溝空間h′内の樹脂は、スクリュ1の基部から
先端部にかけて減少し、空洞部h(又は飢餓部)を形成
し、徐々に先端部へと発達する。
Next, the operation of the conventional device will be explained. First, when a color change operation signal is output from the main cycle of the control device 60, the raw resin supply selection means 21 of the raw resin supply device 20 stops supplying the old raw material. Generally, when the injection operation is continued with the supply of raw materials stopped, the resin in the raw resin transfer groove space h' formed by the thread groove m of the screw 1 and the inner wall surface of the cylinder 2 is transferred from the base of the screw 1 to the tip. It decreases over time, forms a cavity h (or starvation region), and gradually develops to the tip.

【0016】スクリュ1の先端(トーピード10側)に
設けられたチェックリング11により、溶融樹脂の流れ
は堰き止められ、これに作用するスクリュ1のねじ山の
有効押し力と、チェックリング11の内壁面とスクリュ
1の外壁面との間に形成される隙間gを流れる溶融樹脂
の流動抵抗とがバランスする位置まで、前記空洞が発達
し、その位置(これを樹脂の供給口から測って飢餓長さ
という)で空洞の成長は停止し、所謂残留樹脂lを形成
する。残留樹脂l以後ノズル4に向かう樹脂流の後流側
の溶融樹脂との接触面、例えばトーピード10の外周面
d、ヘッドカバー3の内壁面e、ノズル4の内壁面f及
びチェックリング隙間gの表面には溶融樹脂が残留する
The flow of the molten resin is dammed by the check ring 11 provided at the tip of the screw 1 (on the torpedo 10 side), and the effective pushing force of the screw thread of the screw 1 acting on this and the inner part of the check ring 11 are The cavity develops to a position where the flow resistance of the molten resin flowing through the gap g formed between the wall surface and the outer wall surface of the screw 1 is balanced. The growth of the cavity is stopped at the point 1), and the so-called residual resin 1 is formed. Contact surfaces with the molten resin on the downstream side of the resin flow flowing toward the nozzle 4 after the residual resin l, for example, the outer peripheral surface d of the torpedo 10, the inner wall surface e of the head cover 3, the inner wall surface f of the nozzle 4, and the surface of the check ring gap g Molten resin remains.

【0017】またスクリュ1のコンプレッション部b部
は、ねじ溝底面が先端に開く角度で傾斜していることか
ら、同部の溝壁面でも樹脂の付着が多く見られる。原料
供給停止後にスクリュ1のねじ溝内に発達する空洞部の
最成長状態、或いはそれに近い状態は、時間又はスクリ
ュの回転総数を実験、或いはシミュレーションによって
求めておくことにより知ることができる。これを限時設
定手段乃至スクリュ回転数計数手段で設定し、色替樹脂
供給開始検出手段30で検出する。また色替樹脂供給開
始検出手段30の出力により、制御装置60は原料樹脂
供給選択手段21に原料の供給指令を行ない、原料樹脂
供給選択手段21は特定量の新原料樹脂を供給した後、
原料供給を停止する。
Furthermore, since the compression portion b of the screw 1 is inclined at an angle where the bottom surface of the thread groove opens toward the tip, a lot of resin is observed to adhere to the wall surface of the groove in the same portion. The maximum growth state of the cavity that develops in the thread groove of the screw 1 after the raw material supply is stopped, or a state close to it, can be determined by determining the time or the total number of screw rotations by experiment or simulation. This is set by the time limit setting means or screw rotation speed counting means, and detected by the color change resin supply start detection means 30. Further, based on the output of the color change resin supply start detection means 30, the control device 60 issues a raw material supply command to the raw material resin supply selection means 21, and after the raw material resin supply selection means 21 supplies a specific amount of new raw material resin,
Stop raw material supply.

【0018】スクリュ1の空洞状態の溝部hには、原料
通路9から前記残留樹脂部に向け、空洞長さを充満する
には不十分な量の未溶融樹脂が送り込まれ、ソリッドベ
ッド状態となってねじ溝内を図9の如く移動し、ねじ溝
表面には極めて大きな剪断力が図10の如く作用し、旧
溶融樹脂が多く付着するスクリュのコンプレッション部
bの樹脂膜の掻き取りを行なう。そしてそのままスクリ
ュ回転を継続すると、スクリュ1の先端部の残留樹脂l
が、チェックリング11を介してノズル4側に押し出さ
れると共に、ソリッドベッド状で送られた原料樹脂も溶
解してチェックリング11の隙間gを通って押し出され
、同時にその背圧でスクリュ1は後退する。
An insufficient amount of unmelted resin to fill the length of the cavity is fed into the hollow groove h of the screw 1 from the raw material passage 9 toward the residual resin portion, forming a solid bed. The screw moves within the screw groove as shown in FIG. 9, and an extremely large shearing force acts on the surface of the screw groove as shown in FIG. 10, thereby scraping off the resin film on the compression part b of the screw where a large amount of old molten resin adheres. Then, if the screw continues to rotate, the residual resin l at the tip of screw 1
is pushed out to the nozzle 4 side via the check ring 11, and the raw material resin sent in the form of a solid bed is also melted and pushed out through the gap g of the check ring 11, and at the same time, the screw 1 is retracted by the back pressure. do.

【0019】スクリュ1が射出位置まで後退すると、制
御装置60はスクリュ1の回転を停止して射出を指令し
、スクリュ1を前進させて射出を行なう。以後原料供給
を停止したままこれを繰り返す。先に充填された旧樹脂
の射出による排出が完了し、新しい溶融樹脂の特定量が
充填されて射出される時には、樹脂温度は連続射出運転
時よりヒータ入力が下げられているので、高粘度の樹脂
が射出され、前記樹脂滞留部d、e、f、gの表面には
高粘度の溶融樹脂による高い剪断力が図11の如く作用
し、掻き取り効果により使用済樹脂膜の除去が進行する
When the screw 1 is retracted to the injection position, the control device 60 stops the rotation of the screw 1, commands injection, and moves the screw 1 forward to perform injection. Thereafter, this process is repeated while the raw material supply is stopped. When the injection discharge of the old resin filled earlier is completed and a specific amount of new molten resin is filled and injected, the resin temperature is lower than that during continuous injection operation, so the high viscosity The resin is injected, and a high shearing force due to the high viscosity molten resin acts on the surfaces of the resin retention parts d, e, f, and g as shown in FIG. 11, and the removal of the used resin film progresses due to the scraping effect. .

【0020】特定量が充填された樹脂分の排出によるス
クリュ1の空洞成長が飽和に達した段階を、特定充填量
に相当する射出回数を予め設定しておき、射出回数がこ
の設定数に達したことをカウンタ等の特定充填量排出検
出手段40により検出して、特定量充填分が排出された
ことを検出する。以後前記操作を繰り返し、その繰り返
し数が設定値に達したことをカウンタ等の色替完了検出
手段50で検出し、色替完了信号を制御装置60に送り
、以後メインサイクルの通常成形サイクルに移る。なお
、図中ηは粘度を示す。
[0020] The stage at which the cavity growth of the screw 1 reaches saturation due to the discharge of the resin filled in a specific amount is determined in advance by setting the number of injections corresponding to the specific filling amount, and when the number of injections reaches this set number. This is detected by a specific filling amount discharge detection means 40 such as a counter, and it is detected that the specific amount of filling has been discharged. Thereafter, the above operation is repeated, and the color change completion detection means 50 such as a counter detects that the number of repetitions has reached the set value, and a color change completion signal is sent to the control device 60, and the process then proceeds to the normal molding cycle of the main cycle. . Note that η in the figure indicates viscosity.

【0021】次に前記色替えにあたって供給樹脂の特定
量を測定する方法を、図8を例にとって具体的に説明す
ると、この例では、原料樹脂供給装置20のホッパ6の
下部原料通路9の途中に、間隔を置いて設けた2個のシ
ャッタ21−1、21−2より成る原料樹脂選択供給手
段21によって行なわれる。先ず下側のシャッタ21−
2を閉とし、次いで上側のシャッタ21−1を開にする
と、原料樹脂は原料通路9を落下するホッパ6からの原
料樹脂量は常時一定高さに保たれ、ここで上側のシャッ
タ21−1を閉にすれば、両シャッタ21−1、21−
2間に閉じ込められる原料樹脂量jは特定量となる。こ
の状態で原料樹脂供給指令を受けると、下側のシャッタ
21−2が開となり、原料樹脂の特定量はスクリュ1の
フィード部aへ供給される。
Next, a method of measuring a specific amount of supplied resin for the color change will be specifically explained using FIG. 8 as an example. This is carried out by means of raw resin selective supply means 21 consisting of two shutters 21-1 and 21-2 provided at an interval. First, the lower shutter 21-
2 is closed, and then the upper shutter 21-1 is opened, the amount of raw resin falling from the hopper 6 down the raw material passage 9 is always kept at a constant height, and the upper shutter 21-1 is closed. If you close both shutters 21-1, 21-
The amount j of the raw material resin trapped between the two is a specific amount. When a raw resin supply command is received in this state, the lower shutter 21-2 is opened, and a specific amount of raw resin is supplied to the feed section a of the screw 1.

【0022】原料供給が完了すると(この検出は光電ス
イッチ等で行なえば良い)、下側のシャッタ21−2が
閉となり、その後上側のシャッタ21−1が開となり、
所定の供給回数以内なら計量状態でこのまま待機してい
ても良く、制御装置60からの供給指令が出てから閉動
作させ、その後前記特定量の供給動作を行なう。一方連
続供給の指令に対しては、双方のシャッタ21−1、2
1−2ともに開状態を保持させるようにする。
When the supply of raw materials is completed (this detection may be performed using a photoelectric switch, etc.), the lower shutter 21-2 is closed, and then the upper shutter 21-1 is opened.
As long as the number of times of supply is within a predetermined number, it may stand by in the metering state, and after a supply command is issued from the control device 60, the closing operation is performed, and then the supply operation of the specified amount is performed. On the other hand, in response to a continuous supply command, both shutters 21-1 and 21-1
Both 1 and 2 are kept open.

【0023】射出成形機において、特定の供給量を1射
出時の吐出量相当と決め、特定量が供給される毎に射出
サイクルを行なえば、色替作業は極限状態で進行し、色
替えによる損失樹脂量、損失時間ともに極小となる。勿
論、この特定量を複数回の射出量に相当する量として決
めても良い。またスクリュの射出開始は、後退位置検出
手段としてのポテンショメータ出力、又はスクリュが射
出して前進端に達すると計時を開始し、所定時間後にO
N信号を出力する限時手段を併用して、その何れかの信
号により射出がなされる。そして特定量が射出1回で吐
出される程度に設定されている場合には、射出毎のバラ
ツキはあるものの、射出時の粘度が適正範囲に納まるよ
うに特定量と時間を選んでおけば、色替運転による機械
的損傷がなく色替操作が進行し、射出数又は特定量供給
回数を計数して、これを設定値と比較し判別することに
より、色替完了が検出される。
In an injection molding machine, if a specific supply amount is determined to be equivalent to the discharge amount for one injection, and an injection cycle is performed each time a specific amount is supplied, the color change operation will proceed at the limit, and the color change will Both the amount of resin lost and the time lost are minimal. Of course, this specific amount may be determined as an amount corresponding to the amount of multiple injections. In addition, the start of screw injection is determined by the potentiometer output as a backward position detection means, or by starting time measurement when the screw is injected and reaches the forward end, and after a predetermined time, the output is
A time limit means for outputting an N signal is also used, and injection is performed by one of the signals. If the specific amount is set to be ejected in one injection, the specific amount and time should be selected so that the viscosity at the time of injection will be within the appropriate range, although there will be variations from injection to injection. The color change operation progresses without any mechanical damage caused by the color change operation, and the completion of the color change is detected by counting the number of injections or the number of times a specific amount is supplied and comparing this with a set value.

【0024】[0024]

【発明が解決しようとする課題】以上述べた従来装置に
よる利点は、図5に示す色替え時間の感度分析結果によ
って裏付けされる。即ち、
The advantages of the conventional apparatus described above are supported by the results of sensitivity analysis of color change time shown in FIG. That is,

【数2】   ln(t×γW )=−a×ηR /ηW +b 
               (1)但し、 a、b:正の定数 t:色替え時間(色替えショット数に平均サイクルを掛
けた値)〔sec〕 γW :見掛け上の剪断速度(壁面)〔sec−1〕η
R :樹脂粘度(樹脂温度と剪断速度の交点を粘度曲線
から換算した値)〔Pa.s〕 ηW :壁面の樹脂粘度(壁面設定温度と剪断速度の交
点を粘度曲線から換算した値)〔Pa.s〕上式から次
の結論が得られる。 〔色替え迅速化の結論〕樹脂温度を低く(ηR を大き
く)し、壁面温度を高く(ηW を小さく)し、更に高
速で樹脂を流す(γW を大きくする)と、色替え迅速
化に繋がる。
[Formula 2] ln(t×γW)=−a×ηR/ηW +b
(1) However, a, b: positive constant t: color change time (number of color change shots multiplied by average cycle) [sec] γW: apparent shear rate (wall surface) [sec-1] η
R: Resin viscosity (value calculated from the viscosity curve at the intersection of resin temperature and shear rate) [Pa. s] ηW: Resin viscosity on the wall (value calculated from the viscosity curve at the intersection of the wall surface temperature setting and shear rate) [Pa. s] The following conclusion can be obtained from the above equation. [Conclusion for speeding up color change] Lowering the resin temperature (increasing ηR), increasing the wall surface temperature (reducing ηW), and flowing the resin at a higher speed (increasing γW) will lead to faster color change. .

【0025】しかしながら(1)式は射出成形機の主要
諸元であるVI 、VF 、VC 、VO 、D、L(
記号の意味は後述)等と直結しておらず、これ等の間の
関連を明瞭にする必要があった。
However, equation (1) is based on the main specifications of the injection molding machine: VI, VF, VC, VO, D, L(
(The meanings of the symbols will be explained later), etc., and it was necessary to clarify the relationship between them.

【0026】本発明は前記従来の課題を解決するために
提案されたものである。
The present invention has been proposed to solve the above-mentioned conventional problems.

【0027】[0027]

【課題を解決するための手段】このため本発明は、射出
成形機又は押出機に用いられる原料樹脂供給方法であっ
て、色替対象の原料を用いて色替運転を行なうにあたり
、樹脂通路を間欠開閉して原料樹脂をフィード部に間欠
供給する原料供給方法において、樹脂通路の途中に設け
られ、原料樹脂のフィード部への供給を、特定量の間欠
的供給と連続供給を択一的に選択する原料樹脂供給選択
手段と、前記特定量の供給開始時期を検出する色替樹脂
供給開始検出手段と、特定量の原料樹脂相当分の排出完
了を検出する排出完了検出手段と、色替完了検出手段と
を具備し、迅速な色替えと通常運転のための原料供給を
択一的に行なうと共に、送り量比X1 、ストローク比
X3 とした時、樹脂替えに消費される樹脂量最小条件
の時0.7≦X1 ≦1.8、1≦X3 ≦1.7の条
件を満たすようにしてなるもので、これを課題解決のた
めの手段とするものである。
[Means for Solving the Problems] Therefore, the present invention provides a method for supplying raw resin for use in an injection molding machine or an extruder, in which a resin passage is connected when performing a color change operation using a raw material to be changed. In a raw material supply method in which raw resin is intermittently supplied to the feed section by opening and closing intermittently, a valve is installed in the middle of the resin passage and selectively supplies a specific amount of raw resin to the feed section between intermittent supply and continuous supply. A raw material resin supply selection means to select, a color change resin supply start detection means for detecting the supply start time of the specified amount, a discharge completion detection means for detecting completion of discharge corresponding to the specified amount of raw resin, and a color change completion detection means. It is equipped with a detection means to selectively supply raw materials for quick color change and normal operation, and to detect the minimum amount of resin consumed for resin change when the feed rate ratio is X1 and the stroke ratio is X3. It is designed to satisfy the following conditions: 0.7≦X1≦1.8 and 1≦X3≦1.7, and is used as a means to solve the problem.

【数3】 VI :間欠供給量(m3 ) VF :フィード部容積(m3 ) VC :圧縮部容積(m3 ) VM :メータリング部容積(m3 )VO :射出1
ショット容積(m3 )ρI ,ρF ,ρC :各部
の密度(kg/m3 )
[Equation 3] VI: Intermittent supply amount (m3) VF: Feed section volume (m3) VC: Compression section volume (m3) VM: Metering section volume (m3) VO: Injection 1
Shot volume (m3) ρI, ρF, ρC: Density of each part (kg/m3)

【0028】[0028]

【作用】I.所要樹脂量最小化の条件 後述する送り能力化X1 を独立変数、所要樹脂量Y1
 を従属変数とした時、計量比率X3 をパラメータと
する所要樹脂量Y1 の特性は図1の様に表わされる。 これより(1)X3 を決めると、Y1 最小となるX
1 が存在する。 (2)X3 を約1から1.7にすれば、X1 が0.
7〜1.8の広い範囲で変わっても、Y1 が従来の7
0%程度以下となる範囲とすることができる。 (3)X3 が約0.5の時、X1 を0.6〜1.5
に選べば、Y1 が従来の70%以下とすることができ
る。 (4)特に0.8≦X1 ≦1.7に対し1≦X≦1.
5に選択すればY≦0.6とすることができる。 II.所要時間最短の条件
[Effect] I. Conditions for minimizing the required resin amount
When Y1 is the dependent variable, the characteristic of the required resin amount Y1 with the metering ratio X3 as a parameter is expressed as shown in FIG. From this, (1) When determining X3, Y1 is the minimum X
1 exists. (2) If X3 is set from about 1 to 1.7, X1 becomes 0.
Even if it varies over a wide range of 7 to 1.8, Y1 is still the same as the conventional 7.
It can be set to a range of about 0% or less. (3) When X3 is about 0.5, set X1 to 0.6 to 1.5
If selected, Y1 can be reduced to 70% or less of the conventional value. (4) Especially when 0.8≦X1≦1.7 and 1≦X≦1.
If 5 is selected, Y≦0.6 can be satisfied. II. Conditions for shortest time required

【0029】後述する所要時間比Y2 のX3 をパラ
メータとするX1 に対する特性は図2の様に表わされ
る。Y2 にも極小値がある。これより (1)X3 を約1〜1.5に選べば、X1 が1.2
〜1.8の広い範囲に変わっても、Y2 は従来の70
%以下となる範囲とすることができる。 (2)X3 ≧0.5に対し1.0≦X1 ≦1.7に
すれば、Y2 ≦0.7にすることができる。 (3)特に1.0≦X3 ≦1.5に対し、1.3≦X
1 ≦1.7とすれば、Y2 ≦0.6にすることがで
きる。 III.樹脂量、所定時間共に70%以下の条件1≦X
3 ≦1.5に対し1.2≦X1 ≦1.8に選べばY
1 もY2 も同様に従来の70%以下とすることがで
きる。
The characteristic of the required time ratio Y2, which will be described later, with respect to X1 with X3 as a parameter is expressed as shown in FIG. Y2 also has a minimum value. From this, (1) If you choose X3 to be approximately 1 to 1.5, then X1 will be 1.2
Even if it changes to a wide range of ~1.8, Y2 remains the same as the conventional 70
% or less. (2) By setting 1.0≦X1≦1.7 for X3≧0.5, Y2≦0.7 can be achieved. (3) Especially for 1.0≦X3≦1.5, 1.3≦X
If 1≦1.7, then Y2≦0.6. III. Condition 1≦X where both resin amount and predetermined time are 70% or less
3 ≦1.5, if you choose 1.2≦X1≦1.8, Y
1 and Y2 can be similarly reduced to 70% or less of the conventional values.

【0030】極小値が存在する理由は、X3 =1の条
件の下で間欠送り量X1 ×VI を変えて行ったテス
ト結果(図3)から次の様に説明される。図3において
Y1 、Y2 が極小値を示す時のX1 の値は、X1
 =1.0であり、この時シリンダ内の樹脂圧のピーク
値が最大となっており、掻き取り効果が増したものと考
える。これは間欠供給量が最適値より少ないと、圧縮部
でソリッドベッドが圧縮される際、緩やかに圧縮され(
見掛け比重が小さい状態)るため、ソリッドベッドに掛
かる有効圧が小さく、クリーニング作用が小さいものと
考える。また間欠供給量が多過ぎると、連続供給の状態
に近づき、溶融が促進されてスクリュ壁面での剪断応力
が小さくなり、クリーニング作用が低下するものと考え
られる。またX3 を変えると、Y1 、Y2 の極小
値を与えるX1 の値が変わる理由は、現状では充分分
かってはいないが、極小値を与えるX1 が存在するこ
とは事実が示す通りである。
The reason why the minimum value exists is explained as follows based on the test results (FIG. 3) conducted under the condition that X3 = 1 and varying the intermittent feed amount X1 x VI. In FIG. 3, the value of X1 when Y1 and Y2 show minimum values is
= 1.0, and at this time, the peak value of the resin pressure in the cylinder is at its maximum, and it is considered that the scraping effect has increased. This is because if the intermittent supply amount is less than the optimum value, when the solid bed is compressed in the compression section, it will be compressed slowly (
Since the apparent specific gravity is small, the effective pressure applied to the solid bed is small and the cleaning effect is considered to be small. Moreover, if the intermittent supply amount is too large, it approaches a state of continuous supply, which promotes melting and reduces the shear stress on the screw wall surface, which reduces the cleaning effect. Furthermore, the reason why the value of X1 that gives the minimum value of Y1 and Y2 changes when X3 is changed is not fully understood at present, but the facts show that there is a value of X1 that gives the minimum value.

【0031】[0031]

【実施例】以下本発明を図面の実施例について説明する
と、間欠供給量の最適量を検討すするため、次の無次元
数を定義し、この無次元数を説明変数に色替えし、所要
樹脂量比Y1 を特性値に採り、重回帰分析を実施した
[Example] The present invention will be described below with reference to the embodiments shown in the drawings. In order to examine the optimal amount of intermittent supply, the following dimensionless number is defined, and this dimensionless number is colored as an explanatory variable. Multiple regression analysis was performed using the resin amount ratio Y1 as a characteristic value.

【数4】 但し、n×ρO VO ≒ρI VI[Math 4] However, n×ρO VO ≒ρI VI

【数5】 ここでそれぞれの記号の意味は次の通りである。 VI :間欠供給量(m3 ) VF :フィード部容積(m3 ) VC :圧縮部容積(m3 ) VO :射出1ショット容積(m3 )ρI ,ρF 
,ρC :各部の密度(kg/m3 )q:射出率(m
3 /s) L:射出ストローク(m) D:スクリュ外径(m) n:間欠供給1回当りのショット数 またX3 をパラメータとしてX1 を変え、Y1 、
Y2 を重回帰分析した結果を、図1及び図2並びに図
3に示す。
[Equation 5] Here, the meaning of each symbol is as follows. VI: Intermittent supply amount (m3) VF: Feed section volume (m3) VC: Compression section volume (m3) VO: Injection 1 shot volume (m3) ρI, ρF
, ρC: Density of each part (kg/m3) q: Injection rate (m
3/s) L: Injection stroke (m) D: Screw outer diameter (m) n: Number of shots per intermittent supply Also, by changing X1 with X3 as a parameter, Y1,
The results of multiple regression analysis of Y2 are shown in FIGS. 1, 2, and 3.

【0032】[0032]

【発明の効果】以上詳細に説明した如く本発明によれば
、機械の諸元に対し、最適送り量比X1 と最適ストロ
ーク比X3 の関係が明らかになると共に、X1 、X
3 を選択することにより、Y≦0.7、Y2 ≦0.
7、更にはY1 ≦0.6等大幅な改善ができる。
As described in detail above, according to the present invention, the relationship between the optimum feed rate ratio X1 and the optimum stroke ratio X3 is clarified with respect to the specifications of the machine, and
3, Y≦0.7, Y2≦0.
7, and furthermore, a significant improvement such as Y1≦0.6 can be achieved.

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

【図1】本発明の実施例に係る所要樹脂量特性線図であ
る。
FIG. 1 is a required resin amount characteristic diagram according to an example of the present invention.

【図2】本発明の実施例に係る所要時間比特性線図であ
る。
FIG. 2 is a required time ratio characteristic diagram according to an embodiment of the present invention.

【図3】X3 =1におけるY1 、Y2 、シリンダ
内圧特性線図である。
FIG. 3 is a characteristic diagram of Y1, Y2 and cylinder internal pressure when X3=1.

【図4】スクリュ各部の容積と樹脂温度との関係を示す
線図である。
FIG. 4 is a diagram showing the relationship between the volume of each part of the screw and the resin temperature.

【図5】本発明の実施例を示す色替え感度特性線図であ
る。
FIG. 5 is a color change sensitivity characteristic diagram showing an example of the present invention.

【図6】従来の成形機の原料樹脂供給装置のシステム図
である。
FIG. 6 is a system diagram of a raw resin supply device for a conventional molding machine.

【図7】図6における制御フロー図である。FIG. 7 is a control flow diagram in FIG. 6;

【図8】図6と相違する成形機の原料樹脂制御装置のシ
ステム図である。
FIG. 8 is a system diagram of a raw resin control device of the molding machine, which is different from FIG. 6;

【図9】従来のソリッドベッドの流れを示す説明図であ
る。
FIG. 9 is an explanatory diagram showing the flow of a conventional solid bed.

【図10】同ソリッドベッドの剪断応力分布を示す説明
図である。
FIG. 10 is an explanatory diagram showing the shear stress distribution of the solid bed.

【図11】同溶融樹脂の剪断応力分布を示す説明図であ
る。
FIG. 11 is an explanatory diagram showing the shear stress distribution of the molten resin.

【図12】従来の射出成形機の1例を示す側断面図であ
る。
FIG. 12 is a side sectional view showing an example of a conventional injection molding machine.

【符号の説明】[Explanation of symbols]

1  スクリュ 2  シリンダ 4  射出ノズル 5  スクリュ回転用油圧モータ 6  原料樹脂供給ホッパ 20  原料樹脂供給装置 21  原料樹脂供給選択手段 30  色替樹脂供給開始検出手段 40  排出完了検出手段 50  色替完了検出手段 60  制御装置 1 Screw 2 Cylinder 4 Injection nozzle 5 Hydraulic motor for screw rotation 6 Raw resin supply hopper 20 Raw resin supply device 21 Raw resin supply selection means 30 Color change resin supply start detection means 40 Ejection completion detection means 50 Color change completion detection means 60 Control device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  射出成形機又は押出機に用いられる原
料樹脂供給方法であって、色替対象の原料を用いて色替
運転を行なうにあたり、樹脂通路を間欠開閉して原料樹
脂をフィード部に間欠供給する原料供給方法において、
樹脂通路の途中に設けられ、原料樹脂のフィード部への
供給を、特定量の間欠的供給と連続供給を択一的に選択
する原料樹脂供給選択手段と、前記特定量の供給開始時
期を検出する色替樹脂供給開始検出手段と、特定量の原
料樹脂相当分の排出完了を検出する排出完了検出手段と
、色替完了検出手段とを具備し、迅速な色替えと通常運
転のための原料供給を択一的に行なうと共に、送り量比
X1 、ストローク比X3 とした時、樹脂替えに消費
される樹脂量最小条件の時0.7≦X1 ≦1.8、1
≦X3 ≦1.7の条件を満たすようにしたことを特徴
とする射出成形機の樹脂替え方法。但し、 【数1】 VI :間欠供給量(m3 ) VF :フィード部容積(m3 ) VC :圧縮部容積(m3 ) VM :メータリング部容積(m3 )VO :射出1
ショット容積(m3 )ρI ,ρF ,ρC :各部
の密度(kg/m3 )
Claim 1: A raw material resin supply method used in an injection molding machine or an extrusion machine, which comprises intermittently opening and closing a resin passage to supply raw resin to a feed section when performing a color change operation using a raw material to be changed. In an intermittent raw material supply method,
A raw resin supply selection means is provided in the middle of the resin passage and selectively selects between intermittent supply and continuous supply of a specific amount of raw resin to the feed section, and detects the timing at which the supply of the specific amount starts. The system is equipped with a color change resin supply start detection means for detecting the start of supply of color change resin, a discharge completion detection means for detecting the completion of discharge corresponding to a specific amount of raw material resin, and a color change completion detection means. When supplying is performed selectively, and the feed rate ratio is X1 and the stroke ratio is X3, the minimum amount of resin consumed for resin replacement is 0.7≦X1≦1.8, 1
A method for changing resin in an injection molding machine, characterized in that the condition of ≦X3≦1.7 is satisfied. However, [Equation 1] VI: Intermittent supply amount (m3) VF: Feed section volume (m3) VC: Compression section volume (m3) VM: Metering section volume (m3) VO: Injection 1
Shot volume (m3) ρI, ρF, ρC: Density of each part (kg/m3)
JP3084536A 1991-03-26 1991-03-26 Resin changing method of injection molder Withdrawn JPH04348926A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3084536A JPH04348926A (en) 1991-03-26 1991-03-26 Resin changing method of injection molder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3084536A JPH04348926A (en) 1991-03-26 1991-03-26 Resin changing method of injection molder

Publications (1)

Publication Number Publication Date
JPH04348926A true JPH04348926A (en) 1992-12-03

Family

ID=13833368

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3084536A Withdrawn JPH04348926A (en) 1991-03-26 1991-03-26 Resin changing method of injection molder

Country Status (1)

Country Link
JP (1) JPH04348926A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096227A (en) * 2010-10-08 2012-05-24 Kakuno Seisakusho:Kk Pellet manufacturing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096227A (en) * 2010-10-08 2012-05-24 Kakuno Seisakusho:Kk Pellet manufacturing apparatus

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