JPH0446731B2 - - Google Patents

Info

Publication number
JPH0446731B2
JPH0446731B2 JP19804086A JP19804086A JPH0446731B2 JP H0446731 B2 JPH0446731 B2 JP H0446731B2 JP 19804086 A JP19804086 A JP 19804086A JP 19804086 A JP19804086 A JP 19804086A JP H0446731 B2 JPH0446731 B2 JP H0446731B2
Authority
JP
Japan
Prior art keywords
resin
general
temperature
changing
engineering plastics
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
Application number
JP19804086A
Other languages
Japanese (ja)
Other versions
JPS6354226A (en
Inventor
Koji Kubota
Kenichi Terao
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP19804086A priority Critical patent/JPS6354226A/en
Publication of JPS6354226A publication Critical patent/JPS6354226A/en
Publication of JPH0446731B2 publication Critical patent/JPH0446731B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/1753Cleaning or purging, e.g. of the injection unit

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】 (産業上の利用分野) 本発明は射出成形機の樹脂替方法及び装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method and apparatus for changing resin in an injection molding machine.

(従来の技術) 第3図は従来の射出形成機の側断面図を示し、
1は加熱シリンダ、2はスクリユ、3はバンドヒ
ータ、4は熱電対、5はノズル、6はホツパ、7
は温度計を示す。
(Prior art) Figure 3 shows a side sectional view of a conventional injection molding machine.
1 is a heating cylinder, 2 is a screw, 3 is a band heater, 4 is a thermocouple, 5 is a nozzle, 6 is a hopper, 7
indicates a thermometer.

さてホツパ6からの原料は、その自重によつて
加熱シリンダ1の内部1aに落下し、スクリユ2
の回転により混練されつつ、その溝に沿つて加熱
シリンダ1の先端部1bに送られる。この際原料
は加熱シリンダ1の外周に装着されたバンドヒー
タ3によつて加熱されると共に、混練作用によつ
て発生する摩擦熱が加わつて内部からも温度が上
昇して溶融状態となり、加熱シリンダ1の先端部
1bに溶融樹脂が貯えられるにつれて、その反力
(背圧)によりスクリユ2は後方に押戻される。
Now, the raw material from the hopper 6 falls into the interior 1a of the heating cylinder 1 due to its own weight, and the raw material from the hopper 6 falls into the interior 1a of the heating cylinder 1.
While being kneaded by the rotation, the mixture is sent to the tip 1b of the heating cylinder 1 along the groove. At this time, the raw material is heated by the band heater 3 attached to the outer periphery of the heating cylinder 1, and the frictional heat generated by the kneading action is added to the raw material, causing the temperature to rise from the inside and become molten. As the molten resin is stored in the tip 1b of the screw 2, the reaction force (back pressure) pushes the screw 2 back.

この後退量を図示しないリミツトスイツチ等に
より感知し、スクリユ2の回転を設定位置で停止
させることにより射出量をきめる。この後図示し
ない金型が閉じられて射出工程に入る。
The amount of retraction is sensed by a limit switch (not shown) or the like, and the rotation of the screw 2 is stopped at a set position to determine the amount of injection. After this, the mold (not shown) is closed and the injection process begins.

この射出工程では、図示しない油圧シリンダ
(射出シリンダ)によつてスクリユ2に射出力が
加えられ、同スクリユ2は射出プランジヤとなつ
て、加熱シリンダ1の先端部にあるノズル5より
金型内に溶融樹脂を射出する。またバンドヒータ
3は3〜5個のグループに分けられ、各グループ
毎に加熱ゾーンを構成し、各ゾーンに対応して熱
電対4、温度計7がある。
In this injection process, an injection force is applied to the screw 2 by a hydraulic cylinder (injection cylinder) not shown, and the screw 2 acts as an injection plunger and is injected into the mold from the nozzle 5 at the tip of the heating cylinder 1. Inject molten resin. The band heaters 3 are divided into three to five groups, each group forming a heating zone, and a thermocouple 4 and a thermometer 7 are provided corresponding to each zone.

近年、射出成形においても多種小量生産化が進
み、樹脂の種類の変更(以下樹脂替と呼ぶ)の頻
度が増加している。樹脂替は、一般に以下の様な
方法によつている。
In recent years, high-mix, low-volume production has progressed in injection molding, and the frequency of changing the type of resin (hereinafter referred to as resin change) has increased. Resin replacement is generally performed by the following method.

(1) ホツパ6内の樹脂を排出口6aを用いて全て
抜き去る。
(1) Remove all the resin in the hopper 6 using the discharge port 6a.

(2) 加熱シリンダ3内に残つている今までの樹脂
をスクリユ回転、射出を繰り返して抜き去る。
(2) Remove the resin remaining in the heating cylinder 3 by repeating screw rotation and injection.

(3) 新しい樹脂をホツパ6に入れ、樹脂が替るま
でスクリユ回転・射出を繰り返す。
(3) Put new resin into the hopper 6 and repeat the screw rotation and injection until the resin is replaced.

ところでスクリユ及びシリンダ内部に滞留、付
着した樹脂を新しい樹脂の可塑化によつて替える
ためには、新しい樹脂の溶融粘度が旧樹脂のもの
より高いことが必要である。
By the way, in order to replace the resin that has accumulated and adhered inside the screw and cylinder by plasticizing the new resin, it is necessary that the melt viscosity of the new resin is higher than that of the old resin.

従つて一般的には、融点の低い樹脂から融点の
高い樹脂に替えるのが容易となる。これは融点の
高い樹脂が、同一温度において当然ながら溶融粘
度が高いからである。
Therefore, in general, it is easy to change from a resin with a low melting point to a resin with a high melting point. This is because a resin with a high melting point naturally has a high melt viscosity at the same temperature.

射出成形機においては、融点や成形温度が異な
る樹脂が用いられる。ここで樹脂の融点または軟
化温度と、成形温度の関係を第4図について説明
する。一般に結晶性樹脂は融点が存在するが、非
晶性樹脂は融点がないので、剛性が低下し、変形
し易くなる軟化温度が、融点の代りに用いられて
いる。第4図で示す様に、成形温度により高い方
からA,B,Cの3グループに分けられる。
In injection molding machines, resins with different melting points and molding temperatures are used. Here, the relationship between the melting point or softening temperature of the resin and the molding temperature will be explained with reference to FIG. Generally, crystalline resins have a melting point, but amorphous resins do not have a melting point, so the softening temperature at which the rigidity decreases and deformation occurs is used instead of the melting point. As shown in FIG. 4, the molding temperature is divided into three groups, A, B, and C, in descending order of molding temperature.

先ずAは一般に耐熱エンジニアリングプラスチ
ツク、Bは汎用エンジニアリングプラスチツク、
Cは汎用樹脂と呼ばれている。また各樹脂名の下
側に引かれた線は、縦軸の各樹脂の融点又は軟化
温度に対して、成形温度の範囲を示している。成
形温度の下限は、金型内に射出可能となる溶融粘
度の最大値の時の温度であり、上限は、一般に樹
脂が熱劣化する直前の温度となる。この範囲での
樹脂の溶融粘度は、温度の上昇に従つて低下する
が、樹脂の特性により低下の割合が各々異なる。
また第4図において中央に斜に引かれた点線は、
融点又は軟化温度=成形温度の線である。
First, A is generally a heat-resistant engineering plastic, B is a general-purpose engineering plastic,
C is called a general-purpose resin. Further, the line drawn below each resin name indicates the range of molding temperature with respect to the melting point or softening temperature of each resin on the vertical axis. The lower limit of the molding temperature is the temperature at which the melt viscosity reaches its maximum value at which injection into the mold is possible, and the upper limit is generally the temperature immediately before the resin deteriorates thermally. The melt viscosity of the resin in this range decreases as the temperature increases, but the rate of decrease differs depending on the characteristics of the resin.
In addition, the dotted line drawn diagonally in the center in Figure 4 is
This is the line where melting point or softening temperature = molding temperature.

(発明が解決しようとする問題点) 第4図に示す成形温度の高いAグループの耐熱
エンジニアリングプラスチツクから、成形温度の
低いBブループの汎用エンジニアリングプラスチ
ツク、又はCグループの汎用樹脂へ樹脂替を行な
おうとすると、樹脂替時のシリンダ温度におい
て、常にAグループの樹脂の溶融粘度が高いの
で、スクリユ2や、加熱シリンダ1に滞留、付着
したAグループの樹脂を、BやCグループの樹脂
の可塑化・射出の繰り返しでは剥がすことができ
ず、BやCグループの樹脂に替り難いなどの問題
があつた。
(Problems to be Solved by the Invention) The resin is changed from heat-resistant engineering plastics of group A, which have a high molding temperature, to general-purpose engineering plastics of group B, which have a low molding temperature, or general-purpose resins of group C, which have a low molding temperature. However, since the melt viscosity of group A resin is always high at the cylinder temperature when changing the resin, the resin of group A that has accumulated and adhered to the screw 2 and heating cylinder 1 is used to plasticize the resin of group B and C.・There were problems such as it could not be removed by repeated injections and it was difficult to replace it with Group B or C resin.

本発明は前記従来の問題点を解決できる樹脂替
方法及び装置を提供しようとするものである。
The present invention aims to provide a resin replacement method and apparatus that can solve the above-mentioned conventional problems.

(問題点を解決するための手段及び作用) このため本発明は、耐熱エンジニアリングプラ
スチツクから汎用エンジニアリングプラスチツク
又は汎用樹脂に樹脂替を行なう場合に、一旦成形
温度範囲が前記両樹脂の成形温度と重なり合うガ
ラス繊維等の充填材入り低粘度樹脂に樹脂替を行
なつてから、続いて汎用エンジニアリングプラス
チツク又は汎用樹脂に樹脂替するようにしてなる
もので、これを問題点解決のための手段及び作用
とするものである。
(Means and effects for solving the problem) Therefore, when changing the resin from heat-resistant engineering plastics to general-purpose engineering plastics or general-purpose resins, the present invention provides for glass whose molding temperature range overlaps with the molding temperatures of both resins. After changing the resin to a low-viscosity resin containing fillers such as fibers, the resin is then changed to a general-purpose engineering plastic or a general-purpose resin, and this is the means and action to solve the problem. It is something.

また本発明は、耐熱エンジニアリングプラスチ
ツクと汎用エンジニアリングプラスチツク又は汎
用樹脂を貯蔵するホツパと、充填材入り低粘度樹
脂を貯蔵する暫定置換用樹脂貯蔵装置と、耐熱エ
ンジニアリングプラスチツクから汎用エンジニア
リングプラスチツク又は汎用樹脂に切換える際、
各樹脂に対応した加熱シリンダの温度制御及び前
記各樹脂の供給・停止等のシーケンス制御を行な
う制御装置とを有するもので、これを問題点解決
のための手段とするものである。
The present invention also provides a hopper for storing heat-resistant engineering plastics and general-purpose engineering plastics or general-purpose resins, a temporary replacement resin storage device for storing low-viscosity resin containing fillers, and a system for switching from heat-resistant engineering plastics to general-purpose engineering plastics or general-purpose resins. edge,
It has a control device that performs temperature control of a heating cylinder corresponding to each resin and sequence control such as supply and stop of each resin, and this is used as a means for solving the problem.

(実施例) 以下本発明を図面の実施例について説明する
と、第1図は本発明の方法及び装置の実施例を示
す。なお、図中符号1〜6,6aまでの部材は前
記第3図のものと同一であるので、ここではこれ
らについての詳細な説明は省略する。次に第3図
との相違点について説明すると、10は本発明の
樹脂替方法を自動的に行なう様に以下に述べる各
装置を制御する制御装置である。また11はガラ
ス繊維等の充填材入り低粘度樹脂を入れる暫定置
換用樹脂貯蔵装置、12,13は樹脂の落下をオ
ン、オフ制御する電磁弁やフイードスクリユ等か
らなる樹脂供給装置、14は樹脂落下孔である。
(Embodiments) The present invention will now be described with reference to the embodiments shown in the drawings. FIG. 1 shows an embodiment of the method and apparatus of the present invention. Incidentally, since the members numbered 1 to 6 and 6a in the figure are the same as those shown in FIG. 3, detailed explanation thereof will be omitted here. Next, the differences from FIG. 3 will be explained. Reference numeral 10 denotes a control device that controls each device described below so as to automatically carry out the resin changing method of the present invention. 11 is a temporary replacement resin storage device containing a low viscosity resin containing a filler such as glass fiber; 12 and 13 are resin supply devices consisting of solenoid valves and feed screws that control resin dropping on and off; and 14 is a resin dropping device. It is a hole.

制御装置10は第2図に示す構成からなつてお
り、操作パネル20、樹脂供給装置12,13の
動作指令及び温度制御用CPU22及びスクリユ
動作制御用CPU23への動作指令及びデータ転
送を行なうメインCPU21、インタフエース2
4,25,26から構成されている。
The control device 10 has the configuration shown in FIG. 2, and includes an operation panel 20, a main CPU 21 that sends operation commands to the resin supply devices 12 and 13, and transfers operation commands and data to a temperature control CPU 22 and a screw operation control CPU 23. , interface 2
It consists of 4, 25, and 26.

次に作用を説明すると、例えばポリエーテルイ
ミド等の耐熱エンジニアリングプラスチツクの成
形が終了した後、ホツパ6内の同樹脂を排出口6
aより抜き去る。次にガラス繊維等の充填材入り
低粘度樹脂として、例えばポリカーボネートの高
流動グレードにガラス繊維を混入したもの(以下
置換用樹脂と呼ぶ)を用い、同置換用樹脂を暫定
置換用樹脂貯蔵装置11に投入する。
Next, to explain the operation, for example, after the molding of heat-resistant engineering plastic such as polyetherimide is completed, the resin in the hopper 6 is discharged from the discharge port 6.
Remove from a. Next, as a low-viscosity resin containing a filler such as glass fiber, for example, a high-flow grade polycarbonate mixed with glass fiber (hereinafter referred to as replacement resin) is used, and the replacement resin is stored in the temporary replacement resin storage device 11. put it in.

次に制御装置10の操作パネル20より樹脂替
動作時間、樹脂替動作時のスクリユ回転数、背
圧、加熱シリンダ温度(340℃)及び本実施例で
樹脂替の目標樹脂である汎用樹脂の例えばポリエ
チレンの成形温度(260℃)を設定する。
Next, from the operation panel 20 of the control device 10, the resin change operation time, the screw rotation speed during the resin change operation, the back pressure, the heating cylinder temperature (340 degrees Celsius), and the example of the general-purpose resin that is the target resin for resin change in this example. Set the polyethylene molding temperature (260℃).

その後ポリエチレンをホツパ6に入れて、操作
パネル20のスイツチにより樹脂替動作の開始信
号を出力する。そしてこの開始信号をメイン
CPU21が入力すると、温度制御用CPU22に
樹脂替時の加熱シリンダ温度の設定値を指令す
る。
Thereafter, polyethylene is put into the hopper 6, and a switch on the operation panel 20 outputs a signal to start the resin change operation. And use this start signal as the main
When the CPU 21 inputs the input, it instructs the temperature control CPU 22 to set the heating cylinder temperature at the time of resin change.

温度制御用CPU22は、熱電対4の検出温度
と、前記設定温度(340℃)と比較して、加熱シ
リンダ1の温度が、設定温度(340℃)になる様
にバンドヒータ3を制御する。ここで設定温度
(340℃)は、ポリエーテルイミドの成形温度と、
置換樹脂の成形温度が重なり合う範囲から選定さ
れている。
The temperature control CPU 22 compares the temperature detected by the thermocouple 4 with the set temperature (340°C) and controls the band heater 3 so that the temperature of the heating cylinder 1 reaches the set temperature (340°C). Here, the set temperature (340℃) is the molding temperature of polyetherimide,
The molding temperatures of the replacement resins are selected from a range that overlaps with each other.

次に加熱シリンダ1の温度が前記設定温度
(340℃)に到達すると、温度制御用CPU22は、
メインCPU21へ温度変更完了信号を出力する。
メインCPU21は、インターフエース25を介
して樹脂供給装置13に供給開始信号を送ると共
に、スクリユ動作制御用CPU23へ動作指令を
出力する。
Next, when the temperature of the heating cylinder 1 reaches the set temperature (340°C), the temperature control CPU 22
A temperature change completion signal is output to the main CPU 21.
The main CPU 21 sends a supply start signal to the resin supply device 13 via the interface 25, and also outputs an operation command to the screw operation control CPU 23.

次に前記出力により、樹脂供給装置13は、置
換用樹脂を樹脂落下孔14を経て加熱シリンダ1
内部1aへ供給する。これと同時に、スクリユ動
作制御用CPU23の指令により、図示しないス
クリユ駆動装置が制御され、スクリユ2の回転、
射出が繰り返えされる。
Next, according to the output, the resin supply device 13 supplies the replacement resin to the heating cylinder 1 through the resin drop hole 14.
Supplied to the interior 1a. At the same time, a screw driving device (not shown) is controlled by a command from the screw operation control CPU 23 to rotate the screw 2,
The injection is repeated.

置換樹脂は、ポリエーテルイミドより低粘度で
あるが、混入されているガラス繊維は硬度が高い
ので、研摩剤と同様な作用を生じ、スクリユ2及
び加熱シリンダ1内部に付着、滞留した粘度の高
いポリエーテルイミド等の耐熱エンジニアリング
プラスチツクを容易に樹脂替できる。
Although the substituted resin has a lower viscosity than polyetherimide, the glass fibers mixed in it have a high hardness, so it acts similar to an abrasive and removes the high viscosity that adheres and stays inside the screw 2 and heating cylinder 1. Heat-resistant engineering plastics such as polyetherimide can be easily replaced with resin.

対で樹脂替動作の時間が樹脂替動作時間設定値
に到達すると、メインCPU21は、スクリユ動
作制御用CPU23、及び樹脂供給装置13に指
令して、スクリユ動作及び置換樹脂の供給を停止
させる。またメインCPU21は、ポリエチレン
の設定温度(260℃)を温度制御用CPU22へ指
令する。温度制御用CPU22の動作により、加
熱シリンダ1の温度が低下する。
When the resin replacement operation time for each pair reaches the resin replacement operation time setting value, the main CPU 21 instructs the screw operation control CPU 23 and the resin supply device 13 to stop the screw operation and the supply of replacement resin. The main CPU 21 also instructs the temperature control CPU 22 to set the polyethylene temperature (260° C.). The temperature of the heating cylinder 1 decreases due to the operation of the temperature control CPU 22.

次に加熱シリンダ1の温度が設定値(260℃)
に到達すると、温度制御用CPU22はメイン
CPU21へ完了信号を出力する。メインCPU2
1は、樹脂供給装置12へ指令して、ホツパ6の
ポリエチレンを加熱シリンダ1の内部1aへ供給
する。また同時にメインCPU21は、スクリユ
動作制御用CPU23に指令し、CPU23により
スクリユ2の回転、射出が繰り返えされる。
Next, the temperature of heating cylinder 1 is the set value (260℃)
When the temperature control CPU 22 reaches the main
Outputs a completion signal to the CPU 21. Main CPU2
1 instructs the resin supply device 12 to supply the polyethylene in the hopper 6 to the interior 1a of the heating cylinder 1. At the same time, the main CPU 21 commands the screw operation control CPU 23, and the CPU 23 repeats the rotation and injection of the screw 2.

置換樹脂であるポリカーボネートの高流動グレ
ードは、成形温度にわたつて低粘度の為、ポリエ
チレン等の汎用樹脂に容易に樹脂替ができる。こ
の樹脂替は、樹脂替動作時間設定値による時間行
なわれ完了すると、メインCPU21の指令によ
り樹脂供給装置12及びスクリユ2の回転、射出
が停止する。
The high flow grade polycarbonate used as the replacement resin has a low viscosity over the molding temperature, so it can be easily replaced with a general-purpose resin such as polyethylene. This resin change is carried out for a time according to the resin change operation time setting value, and when it is completed, the rotation and injection of the resin supply device 12 and the screw 2 are stopped by a command from the main CPU 21.

なお、以上の実施例では、ポリエーテルイミド
からポリエチレンへの樹脂替を示したが、第4図
に示すAグループの300℃以上の成形温度の耐熱
性エンジニアリングプラスチツクからBグループ
の汎用エンジニアリングプラスチツクや、Cグル
ープの汎用樹脂へ樹脂替も同様に容易に行なえ
る。
In addition, although the above example shows the resin change from polyetherimide to polyethylene, it is possible to change from the heat-resistant engineering plastic of group A shown in FIG. It is also easy to change the resin to a C group general-purpose resin.

ま前記実施例と異なり、樹脂替動作時間を設定
する代りに、暫定置換用樹脂貯蔵装置11及びホ
ツパ6の内部に、図示しないレベル計を設け、樹
脂替においてレベル計の検出する前記内部の樹脂
の高さが予め設定した高さまで減少する時、各樹
脂替動作を停止する樹脂替制御装置としてもよ
い。
Also, unlike the above embodiment, instead of setting the resin change operation time, a level meter (not shown) is provided inside the temporary replacement resin storage device 11 and the hopper 6, and the level meter detects the resin inside the temporary replacement resin storage device 11 and the hopper 6. The resin change control device may stop each resin change operation when the height of the resin decreases to a preset height.

(発明の効果) 以上詳細に説明した如く本発明によると、耐熱
エンジニアリングプラスチツクから汎用エンジニ
アリングプラスチツク又は汎用樹脂への樹脂替が
容易にできる。即ち、置換樹脂としての低粘度樹
脂には、ガラス繊維等の充填剤が入つているた
め、耐熱エンジニアリングプラスチツクを容易に
剥がして排出でき、また置換樹脂は低粘度のた
め、汎用エンジニアリングプラスチツク又は汎用
樹脂へ容易に樹脂替できるので、生産性を向上す
ることができる。
(Effects of the Invention) As described above in detail, according to the present invention, it is possible to easily change the resin from heat-resistant engineering plastic to general-purpose engineering plastic or general-purpose resin. In other words, since the low-viscosity resin used as the replacement resin contains fillers such as glass fibers, heat-resistant engineering plastics can be easily peeled off and discharged, and since the replacement resin has a low viscosity, it can be used as a general-purpose engineering plastic or general-purpose resin. Since the resin can be changed easily, productivity can be improved.

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

第1図は本発明の実施例を示す射出成形機の樹
脂替装置のシステム図、第2図は同制御装置の構
成を示すブロツク図、第3図は従来の射出成形機
の側断面図、第4図は樹脂融点又は軟化温度と成
形温度の関係を示す説明図である。 図の主要部分の説明、10……制御装置、11
……暫定置換用樹脂貯蔵装置、12,13……樹
脂供給装置、14……樹脂落下孔。
FIG. 1 is a system diagram of a resin changing device for an injection molding machine showing an embodiment of the present invention, FIG. 2 is a block diagram showing the configuration of the control device, and FIG. 3 is a side sectional view of a conventional injection molding machine. FIG. 4 is an explanatory diagram showing the relationship between resin melting point or softening temperature and molding temperature. Explanation of main parts of the figure, 10...control device, 11
...Resin storage device for temporary replacement, 12, 13...Resin supply device, 14...Resin drop hole.

Claims (1)

【特許請求の範囲】 1 耐熱エンジニアリングプラスチツクから汎用
エンジニアリングプラスチツク又は汎用樹脂に樹
脂替する場合に、一旦成形温度範囲が前記両樹脂
の成形温度と重なり合うガラス繊維等の充填材入
り低粘度樹脂に樹脂替を行なつてから、続いて汎
用エンジニアリングプラスチツク又は汎用樹脂に
樹脂替することを特徴とする射出成形機の樹脂替
方法。 2 耐熱エンジニアリングプラスチツクと汎用エ
ンジニアリングプラスチツク又は汎用樹脂を貯蔵
するホツパと、充填材入り低粘度樹脂を貯蔵する
暫定置換用の樹脂貯蔵装置と、耐熱エンジニアリ
ングプラスチツクから汎用エンジニアリングプラ
スチツク又は汎用樹脂に切換える際、各樹脂に対
応した加熱シリンダの温度制御及び前記各樹脂の
供給・停止等のシーケンス制御を行なう制御装置
とからなることを特徴とする射出形成機の樹脂替
装置。
[Claims] 1. When changing the resin from a heat-resistant engineering plastic to a general-purpose engineering plastic or a general-purpose resin, the resin is first changed to a low-viscosity resin containing a filler such as glass fiber whose molding temperature range overlaps with the molding temperature of both resins. 1. A method for changing resin in an injection molding machine, which comprises performing the following steps, and then changing the resin to a general-purpose engineering plastic or a general-purpose resin. 2. A hopper for storing heat-resistant engineering plastics and general-purpose engineering plastics or general-purpose resins, a temporary replacement resin storage device for storing low-viscosity resin containing fillers, and a hopper for storing heat-resistant engineering plastics and general-purpose engineering plastics or general-purpose resins, and a A resin changing device for an injection molding machine, comprising a control device that performs temperature control of a heating cylinder corresponding to the resin and sequence control such as supplying and stopping each resin.
JP19804086A 1986-08-26 1986-08-26 Method and apparatus for changing-over resin in injection molder Granted JPS6354226A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19804086A JPS6354226A (en) 1986-08-26 1986-08-26 Method and apparatus for changing-over resin in injection molder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19804086A JPS6354226A (en) 1986-08-26 1986-08-26 Method and apparatus for changing-over resin in injection molder

Publications (2)

Publication Number Publication Date
JPS6354226A JPS6354226A (en) 1988-03-08
JPH0446731B2 true JPH0446731B2 (en) 1992-07-30

Family

ID=16384535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19804086A Granted JPS6354226A (en) 1986-08-26 1986-08-26 Method and apparatus for changing-over resin in injection molder

Country Status (1)

Country Link
JP (1) JPS6354226A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6068389B2 (en) * 2014-05-19 2017-01-25 日精樹脂工業株式会社 Purge method for injection molding machine
JP6563368B2 (en) * 2016-06-17 2019-08-21 日精樹脂工業株式会社 Resin change support method and apparatus for molding machine

Also Published As

Publication number Publication date
JPS6354226A (en) 1988-03-08

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