JPH08300427A - Resin supply device and resin supply method - Google Patents
Resin supply device and resin supply methodInfo
- Publication number
- JPH08300427A JPH08300427A JP10843195A JP10843195A JPH08300427A JP H08300427 A JPH08300427 A JP H08300427A JP 10843195 A JP10843195 A JP 10843195A JP 10843195 A JP10843195 A JP 10843195A JP H08300427 A JPH08300427 A JP H08300427A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- resin supply
- screw
- molding machine
- opening
- 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
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
(57)【要約】
【目的】 均一化された樹脂の溶融状態を保持して、安
定した優れた品質を有する成形品を得ることを目的とす
る。
【構成】 射出成形機またはブロー成形機の射出装置へ
樹脂を供給する装置であって、スクリュ軸方向に略1ス
クリュピッチほど離間して配列された複数の樹脂供給口
30を備え、樹脂供給口30を連通遮断する開閉弁60
とこれに接続するホッパ40を備えたものである。
(57) [Summary] [Purpose] The object is to obtain a molded article having stable and excellent quality by maintaining the molten state of the homogenized resin. A device for supplying resin to an injection device of an injection molding machine or a blow molding machine, comprising a plurality of resin supply ports 30 arranged at intervals of approximately one screw pitch in the screw axis direction, and the resin supply port An on-off valve 60 that shuts off 30
And a hopper 40 connected to this.
Description
【0001】[0001]
【産業上の利用分野】本発明は、射出成形機やブロー成
形機に使用されるスクリュインライン式射出装置におけ
る樹脂の供給装置および樹脂の供給方法に関し、特に、
可塑化計量中の樹脂の溶融状態を均一に保って成形品の
品質を向上させることを企図している。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a resin supplying device and a resin supplying method in a screw in-line type injection device used in an injection molding machine or a blow molding machine, and more particularly,
It is intended to maintain the molten state of the resin during plasticizing and to improve the quality of the molded product.
【0002】[0002]
【従来の技術】射出成形機やブロー成形機におけるスク
リュインライン式射出装置は、図7に示すように、先端
部にノズル3を有し、外周部に温度調節装置(ヒータ1
1)を有するバレル1を備えている。このバレル1は、
金型4の材料注入口へノズル3を臨ませうるようにして
配設されている。ホッパ10からバレル1内へ送り込ま
れた樹脂は、油圧モータ5により回転駆動されるスクリ
ュ2により材料供給部より圧縮部へ移送され、圧縮部に
おいてねじ溝の溝深さが漸減するために徐々に圧縮作用
を受ける。この過程でスクリュ2のフライト20間の樹
脂はヒータ11によるバレル1の内壁面からの熱伝達
と、前記スクリュ2の回転作用による樹脂自身、およ
び、樹脂とバレル1もしくは前記スクリュ2との間で生
じる摩擦熱(剪断エネルギにより発生する)により、バ
レル1の内壁面に溶融したメルトフィルムが形成され、
さらに前記フライト20により掻集され、フライト20
にメルトプールが形成される。このように、可塑化が促
進される過程におけるバレル1内の樹脂はメルトフィル
ム、メルトプールおよびまだ溶融点に達していないソリ
ッドベッドの3つの部分から構成され、これらがスクリ
ュ2の回転に伴い、さらに前方に移送される間に連続的
にヒータ11からの加熱とスクリュ2による回転作用と
で未溶融部分(ソリッドベッド)を溶融部分(メルト)
に変換し、前記スクリュ2の計量部では未溶融部分をな
くして均質な溶融可塑化樹脂を得ようとするものであ
る。2. Description of the Related Art A screw-in-line type injection device in an injection molding machine or a blow molding machine has a nozzle 3 at its tip and a temperature control device (heater 1) at its outer periphery, as shown in FIG.
It comprises a barrel 1 with 1). This barrel 1
It is arranged so that the nozzle 3 can face the material injection port of the die 4. The resin fed from the hopper 10 into the barrel 1 is transferred from the material supply section to the compression section by the screw 2 which is rotationally driven by the hydraulic motor 5, and the groove depth of the screw groove is gradually reduced in the compression section. Receives compression. In this process, the resin between the flights 20 of the screw 2 transfers heat from the inner wall surface of the barrel 1 by the heater 11 and the resin itself due to the rotating action of the screw 2, and between the resin and the barrel 1 or the screw 2. The generated frictional heat (generated by shearing energy) forms a molten melt film on the inner wall surface of the barrel 1,
Furthermore, it is collected by the flight 20, and the flight 20
A melt pool is formed on the surface. Thus, the resin in the barrel 1 in the process of promoting plasticization is composed of three parts, a melt film, a melt pool, and a solid bed which has not yet reached the melting point, and as the screw 2 rotates, While being transferred further forward, the unmelted portion (solid bed) is continuously melted by the heating from the heater 11 and the rotating action of the screw 2.
In order to obtain a homogeneous molten plasticized resin by removing the unmelted portion in the measuring section of the screw 2.
【0003】[0003]
【発明が解決しようとする課題】上述のような従来の射
出装置においては、樹脂の供給口が1箇所しかなく樹脂
の可塑化計量工程においてスクリュが後退することによ
り、供給口より前方にあるスクリュ長さが次第に短かく
なるのでスクリュ有効長さが減少する。このため供給さ
れる樹脂の予熱時間やスクリュとバレル内周面との間で
実施される剪断発熱量が少なくなり、可塑化計量初期と
可塑化計量終期の間で樹脂温度や樹脂物性値が変化する
こととなり均一な溶融樹脂の供給が困難となり、その結
果、金型やダイス内へ射出される樹脂の溶融状態が不均
一となり、成形される製品の物性が製品全体で均一性を
保持できないので良好な品質の製品が得られないという
難点があった。In the conventional injection apparatus as described above, since there is only one resin supply port, the screw is retracted in the plasticizing and measuring step of the resin, so that the screw located in front of the supply port. Since the length gradually becomes shorter, the effective screw length decreases. As a result, the preheating time of the supplied resin and the amount of heat generated by shearing between the screw and the inner peripheral surface of the barrel are reduced, and the resin temperature and resin physical property values change between the beginning of plasticization measurement and the end of plasticization measurement. As a result, it becomes difficult to uniformly supply the molten resin, and as a result, the molten state of the resin injected into the mold or die becomes non-uniform, and the physical properties of the molded product cannot be kept uniform throughout the product. However, there is a problem that a product of good quality cannot be obtained.
【0004】[0004]
【課題を解決するための手段】このような課題を解決し
て均一な溶融状態を有する樹脂を可塑化計量できるよう
にするため、本発明の装置(第1の発明)では、射出成
形機またはブロー成形機のスクリュインライン式射出装
置における樹脂の供給装置であって、該供給装置はスク
リュ軸方向に略スクリュピッチほど離間して配列された
複数個の樹脂供給口を備え、該各々の樹脂供給口にそれ
ぞれ該樹脂供給口を連通遮断できる開閉弁を配設し、か
つ、該各々の樹脂供給口へ樹脂を供給するホッパを接続
してなる構成とした。また、本発明の装置(第2の発
明)では、開閉弁の開閉手段を油圧シリンダまたは空気
圧シリンダとし、さらに、本発明の方法(第3の発明)
では、第1の発明における供給装置の複数の樹脂供給口
を備えた射出成形機またはブロー成形機のスクリュイン
ライン式射出装置における樹脂の供給方法であって、可
塑化計量開始時には複数の樹脂供給口のうち最前列の樹
脂供給口のみ開閉弁を開いて樹脂を供給するとともに、
可塑化計量中にスクリュ後退量を計測し、該スクリュ後
退量がスクリュピッチ分に達する毎に順次それまで連通
され樹脂供給していた樹脂供給口の開閉弁を閉じ、該樹
脂供給口に後続する樹脂供給口の開閉弁を開いて樹脂供
給することとした。In order to solve such problems and enable plasticizing and metering of a resin having a uniform molten state, the apparatus of the present invention (first invention) uses an injection molding machine or A resin supply device for a screw in-line type injection device of a blow molding machine, the supply device comprising a plurality of resin supply ports arranged at a distance of approximately a screw pitch in the screw axial direction, each of the resin supply ports being provided. An opening / closing valve capable of shutting off the communication between the resin supply ports is arranged at each of the ports, and a hopper for supplying the resin to each of the resin supply ports is connected. In the device of the present invention (second invention), the opening / closing means of the opening / closing valve is a hydraulic cylinder or a pneumatic cylinder, and the method of the present invention (third invention).
A method of supplying a resin in a screw-in-line type injection device of an injection molding machine or a blow molding machine having a plurality of resin supply ports of the supply device according to the first aspect of the present invention, wherein a plurality of resin supply ports are provided at the start of plasticization measurement. Open the on-off valve only at the resin supply port on the front row to supply the resin,
The amount of screw retreat is measured during plasticization metering, and each time the amount of screw retreat reaches the screw pitch, the on / off valve of the resin supply port, which has been communicating until then and is supplying resin, is closed, and the resin supply port is followed. It was decided to supply the resin by opening the on-off valve of the resin supply port.
【0005】[0005]
【作用】本発明の樹脂の供給装置や供給方法では、可塑
化計量初期にはスクリュ軸方向に複数個配列されている
樹脂供給口のうち最前方の樹脂供給口以外を閉じておき
最前方の樹脂供給口のみから樹脂を供給し、可塑化計量
を行なう。そして、可塑化計量中にスクリュ後退量を検
出しておき、スクリュ後退量がスクリュ1ピッチ分にな
ったとき最前方の樹脂供給口を閉じて供給をストップす
るとともに、後続の樹脂供給口を開いて樹脂を供給す
る。以上のようにして、スクリュ後退量がスクリュ1ピ
ッチ分に達する毎に順次それまで樹脂を供給していた樹
脂供給口からの供給を止め、後続する次位の樹脂供給口
からの樹脂供給に切替えていく。このように行なうこと
により、現実に樹脂を供給している樹脂供給口から前方
にあるスクリュ長さはほぼ同一の長さに保持され、樹脂
に加えられる熱量が一定化されるから樹脂溶融状態はほ
ぼ一定に保たれ、樹脂温度は均一化される。In the resin feeding apparatus and feeding method of the present invention, at the initial stage of plasticization measurement, all the resin feeding ports arranged in the axial direction of the screw are closed except the foremost resin feeding port. The resin is supplied only from the resin supply port, and plasticization is measured. Then, the amount of screw retreat is detected during plasticization measurement, and when the amount of screw retreat reaches one screw pitch, the foremost resin supply port is closed to stop the supply and the subsequent resin supply port is opened. Supply the resin. As described above, every time the screw retreat amount reaches one pitch of the screw, the supply from the resin supply port, which has been supplying resin until then, is stopped, and the resin supply is switched to the resin supply port from the next succeeding resin supply port. To go. By doing in this way, the length of the screw in front of the resin supply port that actually supplies the resin is maintained at approximately the same length, and the amount of heat applied to the resin is made constant, so that the molten state of the resin is It is kept almost constant and the resin temperature is made uniform.
【0006】[0006]
【実施例】以下図面に基づいて本発明の実施例について
詳細に説明する。図1〜図5は本発明に係り、図1は樹
脂の供給装置の縦断面図(可塑化計量初期の状態を示
す)、図2は樹脂の供給装置の縦断面図(可塑化計量終
期の状態を示す)、図3は図1のA−A視の横断面図、
図4〜図5はスクリュ位置と樹脂温度との相関を示すグ
ラフで、図4は樹脂供給口が2個の場合、図5は樹脂供
給口が3個の場合を示す。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. 1 to 5 relate to the present invention, FIG. 1 is a vertical cross-sectional view of a resin supply device (in the initial state of plasticization measurement), and FIG. 2 is a vertical cross-sectional view of a resin supply device (at the end of plasticization measurement). FIG. 3 is a cross-sectional view taken along line AA of FIG. 1,
4 to 5 are graphs showing the correlation between the screw position and the resin temperature, FIG. 4 shows the case where there are two resin supply ports, and FIG. 5 shows the case where there are three resin supply ports.
【0007】図1〜図3は樹脂供給口30が2個の場合
の樹脂供給装置100を示したもので、バレル1にスク
リュ2の軸方向に複数個の樹脂供給口30がほぼ1スク
リュピッチ分だけ離間して配設され、各々の樹脂供給口
30には射出ハウジング1Aを介してホッパハウジング
50が立設され、その内部には油圧シリンダ62の操作
により上下動して樹脂供給口30を開閉する開閉弁60
が配設される。また、隣り合うホッパハウジング50、
50の間には図3に示すようなホッパ40およびシュー
ト42が連結されるとともに、側面に油圧シリンダ62
のピストンロッド62aに固結され連動して上下動する
シャッタ70が設けられ、開閉弁60の閉動作と同時
に、ホッパ40ならびにシュート42の樹脂経路を遮断
する構成となっている。図1〜図3の場合には、樹脂供
給口30は2個とした実施例を示したが、一般に計量中
における全スクリュ後退量はスクリュピッチの約6倍程
度あるから、樹脂供給口30、30同志の間隔が1スク
リュピッチ分とした場合には、樹脂供給口30は6個あ
ることが最も望ましいが、少なくとも3〜4個布設する
のが望ましい。図1の実施例のように、樹脂供給口3
0、30同志の間隔は1スクリュピッチより若干大きめ
にし、スクリュピッチの1.5〜2.0倍とした。1 to 3 show a resin supply device 100 in the case of two resin supply ports 30, wherein a plurality of resin supply ports 30 are arranged in the barrel 1 in the axial direction of the screw 2 at approximately one screw pitch. A hopper housing 50 is erected at each of the resin supply ports 30 via the injection housing 1A, and the hopper housing 50 is vertically moved by the operation of the hydraulic cylinder 62 inside the resin supply ports 30 so that the resin supply ports 30 can be opened. Open / close valve 60 to open / close
Is arranged. In addition, adjacent hopper housings 50,
A hopper 40 and a chute 42 as shown in FIG.
A shutter 70 that is fixed to the piston rod 62a and moves up and down in conjunction therewith is provided, and the resin path of the hopper 40 and the chute 42 is shut off at the same time when the opening / closing valve 60 is closed. In the case of FIGS. 1 to 3, an example in which the number of the resin supply ports 30 is two is shown. However, since the total screw retreat amount during measurement is about 6 times the screw pitch, the resin supply ports 30, When the distance between the 30 members is one screw pitch, it is most preferable that the number of resin supply ports 30 is 6, but it is preferable that at least 3 to 4 be provided. As in the embodiment of FIG. 1, the resin supply port 3
The spacing between 0 and 30 was set to be slightly larger than one screw pitch, and was 1.5 to 2.0 times the screw pitch.
【0008】このように構成された本発明の樹脂供給装
置100の作動について説明する。図1〜図2は樹脂供
給口30が2個設けられた場合であり、可塑化計量を開
始する場合には図1に示すように、後方の樹脂供給口3
0の開閉弁60を閉じ、前方の樹脂供給口30のみ開い
て樹脂を供給する。そして、計量中計量の進行とともに
樹脂供給口30より供給された樹脂はスクリュ2の回転
による摩擦熱とバレル1の周囲のヒータ11の熱伝達に
より溶融しつつ前方の樹脂溜りへ貯溜されるとともに、
スクリュ2は後退する。そして、計量中に測定するスク
リュ後退量があらかじめ設定された値に達したとき、前
方の樹脂供給口30を油圧シリンダ62のピストンロッ
ド62aの下降によりシャッタ70と開閉弁60を閉
じ、後方の樹脂供給口30を開いて樹脂の供給位置をス
クリュ後退量ほど後方に移動させる。この場合の供給位
置を切替える設定値は2つの樹脂供給口30、30の離
間距離程度とし、2供給口を有する図1〜図2の場合に
はスクリュピッチの1.5〜2.0倍ほど2つの樹脂供
給口を離しているので、スクリュ後退量がこの値に達し
たときに樹脂供給を前方から後方に切替えるのがよい。
図2は計量終期における状態を示している。また、樹脂
供給口30が3個以上の複数個スクリュ軸方向に配列さ
れている樹脂供給装置100では、その個数が多くなる
ほど隣り合う樹脂供給口30、30間の距離を短かく
し、ほぼ1スクリュピッチ分程度とし、その切替はスク
リュ後退量が1スクリュピッチ分に達する毎に順次後方
の樹脂供給口30の供給に切替えていく。The operation of the resin supply apparatus 100 of the present invention thus constructed will be described. 1 and 2 show a case where two resin supply ports 30 are provided, and when starting the plasticizing measurement, as shown in FIG.
The on-off valve 60 of 0 is closed, and only the front resin supply port 30 is opened to supply the resin. During the measurement, the resin supplied from the resin supply port 30 is melted by the frictional heat generated by the rotation of the screw 2 and the heat transfer of the heater 11 around the barrel 1, and is accumulated in the resin reservoir in the front.
The screw 2 retracts. Then, when the screw retreat amount measured during measurement reaches a preset value, the shutter 70 and the opening / closing valve 60 are closed by lowering the piston rod 62a of the hydraulic cylinder 62 from the front resin supply port 30 to close the rear resin supply port 30. The supply port 30 is opened and the resin supply position is moved backward by the screw retreat amount. In this case, the set value for switching the supply position is about the distance between the two resin supply ports 30 and 30, and in the case of FIGS. 1 and 2 having two supply ports, about 1.5 to 2.0 times the screw pitch. Since the two resin supply ports are separated, it is preferable to switch the resin supply from the front to the rear when the screw retreat amount reaches this value.
FIG. 2 shows the state at the end of measurement. Further, in the resin supply device 100 in which the resin supply ports 30 are arranged in the axial direction of a plurality of screws of three or more, the distance between the resin supply ports 30 and 30 adjacent to each other is shortened as the number of the resin supply devices 100 increases, and the resin supply ports 30 are almost one screw. The pitch is set to about the pitch, and the switching is sequentially switched to the supply of the resin supply port 30 on the rear side every time the screw retreat amount reaches one screw pitch.
【0009】このような複数の樹脂供給口30を有する
樹脂供給装置100で射出装置へ供給される樹脂温度を
温度計80で測定し、樹脂温度の分布を見ると、2個の
場合には図4のようになり、図6の従来の1個の樹脂供
給口30によって供給されるものに比べてピーク温度に
達する樹脂温度のスクリュ位置による変化が平準化され
ているのがわかる。さらに、樹脂供給口30が3個の場
合の図5に示すグラフでは一層スクリュ位置による温度
変化が少なくなり、均一な樹脂の溶融化が図られること
が検証された。なお、図4〜図6のグラフの樹脂温度は
スクリュヘッド2aが各々P1、P2、P3、P4の位
置にあるときの温度計80で計測された樹脂温度を示し
ている。The temperature of the resin supplied to the injection device is measured by the thermometer 80 in the resin supply device 100 having such a plurality of resin supply ports 30, and the distribution of the resin temperature is examined. 4, it can be seen that the change in the resin temperature reaching the peak temperature depending on the screw position is leveled as compared with the conventional one supplied by one resin supply port 30 in FIG. Further, in the graph shown in FIG. 5 in the case where the number of the resin supply ports 30 is three, it was verified that the temperature change due to the screw position is further reduced and the uniform resin melting is achieved. The resin temperatures in the graphs of FIGS. 4 to 6 represent the resin temperatures measured by the thermometer 80 when the screw head 2a is at the positions P1, P2, P3, and P4, respectively.
【0010】このようなデータから推察すると、樹脂溶
融化の均一化のためには、樹脂供給口30がなるべく多
いことが望まれ、有効スクリュピッチが通常約6ピッチ
であることを考えると樹脂供給口30は3〜5個程度配
設するのが望まれる。Inferring from such data, it is desired that the number of resin supply ports 30 is as large as possible in order to make the resin melt uniform, and considering that the effective screw pitch is usually about 6 pitches, the resin supply is It is desirable to arrange about 3 to 5 mouths 30.
【0011】[0011]
【発明の効果】以上述べたように、本発明においては、
樹脂の溶融状態が可塑化計量中常にほぼ均一となり、均
質な安定した成形品品質が確保される。また、射出成形
の場合には、樹脂の溶融状態が均質化されているので成
形条件の条件出しが容易で運転操作性が向上し、ブロー
成形ではダイスの貯溜槽を上記の均一溶融樹脂が通過す
るため均一なパリソンを吐出することができ、品質が向
上する。As described above, according to the present invention,
The molten state of the resin is almost uniform during the plasticization measurement, and a homogeneous and stable molded product quality is secured. In addition, in the case of injection molding, since the molten state of the resin is homogenized, it is easy to set the molding conditions and the operability is improved.In blow molding, the above-mentioned homogeneous molten resin passes through the storage tank of the die. Therefore, a uniform parison can be discharged, and the quality is improved.
【図1】本発明の実施例を示す樹脂の供給装置(可塑化
計量初期)の縦断面図を示す。FIG. 1 is a vertical sectional view of a resin supply device (initial stage of plasticization measurement) showing an embodiment of the present invention.
【図2】本発明の実施例を示す樹脂の供給装置(可塑化
計量終期)の縦断面図を示す。FIG. 2 is a vertical cross-sectional view of a resin supply device (end of plasticization measurement) showing an embodiment of the present invention.
【図3】図1のA−A視の横断面図である。FIG. 3 is a cross-sectional view taken along the line AA of FIG.
【図4】本発明の実施例を示すスクリュ位置と樹脂温度
との相関を示すグラフである。FIG. 4 is a graph showing a correlation between a screw position and a resin temperature showing an example of the present invention.
【図5】本発明の実施例を示すスクリュ位置と樹脂温度
との相関を示すグラフである。FIG. 5 is a graph showing a correlation between a screw position and a resin temperature showing an example of the present invention.
【図6】従来の実施例におけるスクリュ位置と樹脂温度
との相関を示すグラフである。FIG. 6 is a graph showing a correlation between a screw position and a resin temperature in a conventional example.
【図7】従来の射出成形機の全体縦断面図である。FIG. 7 is an overall vertical sectional view of a conventional injection molding machine.
【図8】従来の射出成形機の全体縦断面図である。FIG. 8 is an overall vertical sectional view of a conventional injection molding machine.
1 バレル 1A 射出ハウジング 2 スクリュ 2a スクリュヘッド 3 ノズル 4 金型 5 油圧モータ 10 ホッパ 11 ヒータ 20 フライト 30 樹脂供給口 40 ホッパ 42 シュート 50 ホッパハウジング 60 開閉弁 62 油圧シリンダ(または空気圧シリンダ) 62a ピストンロッド 70 シャッタ 80 温度計 100 樹脂供給装置 1 barrel 1A injection housing 2 screw 2a screw head 3 nozzle 4 mold 5 hydraulic motor 10 hopper 11 heater 20 flight 30 resin supply port 40 hopper 42 chute 50 hopper housing 60 on-off valve 62 hydraulic cylinder (or pneumatic cylinder) 62a piston rod 70 Shutter 80 Thermometer 100 Resin supply device
Claims (3)
ュインライン式射出装置における樹脂の供給装置であっ
て、該供給装置はスクリュ軸方向に略スクリュピッチほ
ど離間して配列された複数個の樹脂供給口を備え、該各
々の樹脂供給口にそれぞれ該樹脂供給口を連通遮断でき
る開閉弁を配設し、かつ、該各々の樹脂供給口へ樹脂を
供給するホッパを接続してなる樹脂の供給装置。1. A resin supply device for a screw in-line type injection device of an injection molding machine or a blow molding machine, wherein the supply device is a plurality of resin supply devices arranged at a distance of approximately screw pitch in the screw axial direction. An apparatus for supplying resin, which is provided with an opening, an opening / closing valve for arranging each of the resin supply openings to cut off the resin supply opening, and a hopper for supplying the resin to each of the resin supply openings is connected. .
空気圧シリンダとする請求項1記載の樹脂の供給装置。2. The resin supply device according to claim 1, wherein the opening / closing means of the opening / closing valve is a hydraulic cylinder or a pneumatic cylinder.
た射出成形機またはブロー成形機のスクリュインライン
式射出装置における樹脂の供給方法であって、可塑化計
量開始時には複数の樹脂供給口のうち最前列の樹脂供給
口のみ開閉弁を開いて樹脂を供給するとともに、可塑化
計量中にスクリュ後退量を計測し、該スクリュ後退量が
スクリュピッチ分に達する毎に順次それまで連通され樹
脂供給していた樹脂供給口の開閉弁を閉じ、該樹脂供給
口に後続する樹脂供給口の開閉弁を開いて樹脂供給する
ことを特徴とする樹脂の供給方法。3. A method of supplying resin in a screw in-line type injection apparatus of an injection molding machine or a blow molding machine comprising a plurality of resin supply ports according to claim 1, wherein the plurality of resin supply ports are provided at the start of plasticizing and weighing. The resin is supplied by opening the open / close valve only at the resin supply port in the front row of the above, and the screw retreat amount is measured during plasticizing and the resin is communicated in sequence until the screw retreat amount reaches the screw pitch. A resin supply method characterized in that the on-off valve of the resin supply port that has been supplied is closed, and the on-off valve of the resin supply port subsequent to the resin supply port is opened to supply the resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10843195A JPH08300427A (en) | 1995-05-02 | 1995-05-02 | Resin supply device and resin supply method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10843195A JPH08300427A (en) | 1995-05-02 | 1995-05-02 | Resin supply device and resin supply method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08300427A true JPH08300427A (en) | 1996-11-19 |
Family
ID=14484609
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10843195A Pending JPH08300427A (en) | 1995-05-02 | 1995-05-02 | Resin supply device and resin supply method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08300427A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115302661A (en) * | 2022-10-12 | 2022-11-08 | 四川航天拓达玄武岩纤维开发有限公司 | Basalt fiber reinforced resin matrix composite material storage device and method |
-
1995
- 1995-05-02 JP JP10843195A patent/JPH08300427A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115302661A (en) * | 2022-10-12 | 2022-11-08 | 四川航天拓达玄武岩纤维开发有限公司 | Basalt fiber reinforced resin matrix composite material storage device and method |
| CN115302661B (en) * | 2022-10-12 | 2022-12-02 | 四川航天拓达玄武岩纤维开发有限公司 | Basalt fiber reinforced resin matrix composite material storage equipment and method |
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