JPH0565334B2 - - Google Patents
Info
- Publication number
- JPH0565334B2 JPH0565334B2 JP58226394A JP22639483A JPH0565334B2 JP H0565334 B2 JPH0565334 B2 JP H0565334B2 JP 58226394 A JP58226394 A JP 58226394A JP 22639483 A JP22639483 A JP 22639483A JP H0565334 B2 JPH0565334 B2 JP H0565334B2
- Authority
- JP
- Japan
- Prior art keywords
- screw
- rotation speed
- extruder
- feeder
- forced feeder
- 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 - Fee Related
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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92019—Pressure
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92085—Velocity
- B29C2948/92095—Angular velocity
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92333—Raw material handling or dosing, e.g. active hopper or feeding device
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92361—Extrusion unit
- B29C2948/9238—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92514—Pressure
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/9259—Angular velocity
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92828—Raw material handling or dosing, e.g. active hopper or feeding device
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/288—Feeding the extrusion material to the extruder in solid form, e.g. powder or granules
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明は熱可塑性樹脂を押出機に強制的に送り
込むようにした、粉体原料用押出機及び射出機に
応用できるフイーダスクリユの回転数制御方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the rotational speed of a feeder screw, which is applicable to extruders and injection machines for powder raw materials, in which a thermoplastic resin is forcibly fed into the extruder.
熱可塑性パウダー状樹脂原料の押出機において
は、原料のくい込み性不良のため押出量の低下、
あるいは押出変動という問題が生じ易く、主押出
機の原料供給用として原料のかさ比重を高め、主
スクリユ基部での粉体圧を増強するため、スクリ
ユ式強制フイーダを押出機原料供給ホツパに設け
たものが第1図に示す如く採用されている。な
お、第1図における1は押出機スクリユ、2は強
制フイーダスクリユ、3は駆動モータである。 In extruders for thermoplastic powder resin raw materials, the amount of extrusion decreases due to poor penetration of the raw materials.
Alternatively, the problem of extrusion fluctuation is likely to occur, and in order to increase the bulk specific gravity of the raw material and increase the powder pressure at the base of the main screw, a screw-type forced feeder was installed at the extruder raw material supply hopper. A device is adopted as shown in FIG. In FIG. 1, 1 is an extruder screw, 2 is a forced feeder screw, and 3 is a drive motor.
この押出装置のスクリユ起動時、あるいはスク
リユ回転数変更時においては、押出機スクリユ回
転数と強制フイーダのスクリユ回転数をバランス
よく設定する必要があり、現状では強制フイーダ
の駆動モータ3の電流がある値となるまで主スク
リユの回転数に応じて強制フイーダのスクリユ回
転数を手動で徐々に増大して行き、所定電流値と
なる様強制フイーダの回転数を決める方法、ある
いは主スクリユ回転数と強制フイーダスクリユ回
転数が常に一定比率となる様な制御方法がとられ
ているのが現状である。 When starting the screw of this extrusion device or changing the screw rotation speed, it is necessary to set the extruder screw rotation speed and the screw rotation speed of the forced feeder in a well-balanced manner.Currently, the current of the drive motor 3 of the forced feeder is A method of manually increasing the screw rotation speed of the force feeder according to the rotation speed of the main screw until the specified current value is reached, or determining the rotation speed of the force feeder so that the specified current value is reached, or At present, a control method is used in which the feeder screw rotation speed is always kept at a constant ratio.
すなわち、定常運転時、所定の押出機スクリユ
回転数に合わせた強制フイーダのスクリユ回転数
をもとに、常にこの一定比率で運転される。また
微粉末原料等の押出しにおいては、押出機スクリ
ユの回転数に対して強制フイーダのスクリユ回転
数は低く、不足気味の原料供給状態となつた場
合、強制フイーダスクリユ下部及び押出機スクリ
ユ基部において粉末原料が空気を含んだ状態で攪
拌される状況となり、流動し易くなつてしまう。 That is, during steady operation, the forced feeder is always operated at a constant ratio based on the screw rotation speed of the forced feeder that matches the predetermined extruder screw rotation speed. In addition, when extruding fine powder raw materials, etc., the screw rotation speed of the forced feeder is low compared to the rotation speed of the extruder screw, and if the raw material supply state is insufficient, the powder raw material is This results in a situation where the liquid is stirred while containing air, making it easier to flow.
一旦この状態をつくり出すと、この状況で強制
フイーダのスクリユ回転数を増大し、供給能力を
増大させようとしても粉末原料がしまつた状態と
ならない為、供給能力が増大しないという現象が
ある。この現象は微粉末原料を攪拌して空気を含
んだものは、手で握つた場合指の間から流出する
が、静止状態でしばらく放置した原料は、手で握
りしめることが可能である事によつて経験するこ
とのできるものである。 Once this condition is created, even if an attempt is made to increase the feed capacity by increasing the screw rotation speed of the forced feeder in this situation, the feed capacity will not increase because the powder raw materials will not be packed together. This phenomenon is due to the fact that when a fine powder raw material is stirred and contains air, it flows out between the fingers when it is held in the hand, but when the raw material is left in a stationary state for a while, it is possible to squeeze it in the hand. It is something that can be experienced.
また逆に、強制フイーダのスクリユ回転数が押
出機スクリユ回転数に対して過度に高い場合は、
強制フイーダの駆動モータのオーバーロードの問
題が生ずる。従つて押出機スクリユ回転数と強制
フイーダの回転数は、強制フイーダ下部及び押出
機スクリユ基部で粉体原料をしまつた状態に保ち
ながら、かつ強制フイーダの駆動モータがオーバ
ーロードしないように連動させる必要がある。押
出機起動時や、押出機スクリユ回転数変更時に
は、この微妙な連動が必要であるが、従来方法で
は十分な調整ができないため供給不可の原料流動
状況、強制フイーダ駆動モータのオーバーロード
の問題を生じてしまう。 Conversely, if the forced feeder screw rotation speed is excessively high compared to the extruder screw rotation speed,
The problem of overloading the drive motor of the forced feeder arises. Therefore, the rotation speed of the extruder screw and the rotation speed of the forced feeder must be linked to keep the powder raw material packed at the bottom of the forced feeder and the base of the extruder screw, and to prevent the drive motor of the forced feeder from overloading. There is. This delicate interlocking is necessary when starting the extruder or changing the extruder screw rotation speed, but conventional methods cannot make sufficient adjustments, which can prevent problems such as material flow conditions that make it impossible to feed and overload of the forced feeder drive motor. It will happen.
また従来法の比率一定方式では、ある押出機ス
クリユ回転数に対して強制フイーダ回転数が設定
された後は、両者の比率が一定にコントロールさ
れるため、押出機シリンダ温度やスクリユ温度の
変化、強制フイーダのホツパ内原料高さの変化等
の外乱が生じた場合、前記のような不具合が発生
する欠点があつた。また一度原料に流動状態を生
じてしまつて供給不足となつた場合は、一旦押出
機と強制フイーダの両スクリユ回転数を低速に落
し、再度正規条件までの再スタートが必要であつ
た。 In addition, in the conventional constant ratio method, after the forced feeder rotation speed is set for a certain extruder screw rotation speed, the ratio between the two is controlled to be constant, so changes in the extruder cylinder temperature and screw temperature, When a disturbance such as a change in the height of the raw material in the hopper of the forced feeder occurs, the above-mentioned problems occur. In addition, once the raw material becomes fluid and there is a shortage of supply, it is necessary to temporarily reduce the screw rotation speed of both the extruder and the forced feeder to a low speed and restart the process to normal conditions again.
最近用途拡大の急な炭カル、タルク等のフイラ
ーの微粉末を含んだ混合原料樹脂を押出機にて押
出す場合、押出機スクリユ回転数及び強制フイー
ダスクリユ回転数を所定の値に設定しても、その
運転経路により押出量が極端に異なるとか、押出
量が安定したり、不安定になつたりするなどの再
現性の乏しい現象を生じた。これを分析してみる
と、押出機基部のシリンダ内樹脂圧力をほぼ一定
値となるように押出機スクリユ回転数と強制フイ
ーダ回転数を連動させながら所定の運転条件へ持
つて行くと、押出量も多く、安定性も良好である
ことが分つた。 When using an extruder to extrude a mixed raw material resin containing fine powder of fillers such as charcoal and talc, whose applications are rapidly expanding recently, even if the extruder screw rotation speed and forced feeder screw rotation speed are set to predetermined values. This resulted in phenomena with poor reproducibility, such as the extrusion rate being extremely different depending on the operating route, and the extrusion rate becoming stable or unstable. Analyzing this, we found that when the extruder screw rotation speed and forced feeder rotation speed are brought to a predetermined operating condition while interlocking the extruder screw rotation speed and forced feeder rotation speed so that the resin pressure in the cylinder at the base of the extruder remains almost constant, the amount of extrusion increases. It was found that the stability was good.
押出機スクリユ回転数をあらかじめ所定の回転
数まで上昇させ、しかるのち強制フイーダのスク
リユ回転数を増大した場合は、押出量が極端に少
なく、安定性も悪かつた。かかる現象は実機採用
に当つて重大な問題であり、両者のスクリユ回転
数、特に強制フイーダのスクリユ回転数制御は重
要であり、この回転数制御を良好に実施するため
に本発明は提案されたものである。 When the extruder screw rotational speed was increased to a predetermined rotational speed in advance and then the screw rotational speed of the forced feeder was increased, the extrusion amount was extremely small and the stability was poor. This phenomenon is a serious problem when adopting an actual machine, and controlling the screw rotation speed of both devices, especially the screw rotation speed of the forced feeder, is important, and the present invention has been proposed in order to effectively implement this rotation speed control. It is something.
すなわち、本発明は強制フイーダ下部、押出機
スクリユ基部における樹脂の状態を流動性のない
しまつた状態に常に保つように、この部分での粉
体圧力を検出し、これが一定となるよう強制フイ
ーダのスクリユ回転数を制御しようとするもの
で、特に微小な粉体圧を測定することは困難であ
るが、これを比較的容易とする強制フイーダのス
クリユのスラスト力検出法、または押出機スクリ
ユ基部の粉体圧が拡大された形で検出できる押出
機フイード部での樹脂圧力の検出を特徴とするも
のであり、熱可塑化樹脂を押出機に強制的に送り
込むスクリユ式強制フイーダをもつ押出装置にお
いて、強制フイーダ下部及び押出機スクリユ基部
での樹脂原料の圧力をセンサで検出し、同センサ
の出力により前記圧力が常に一定となるよう強制
フイーダスクリユの回転数を制御するようにした
フイーダスクリユの回転数制御方法を提供せんと
するものである。 That is, the present invention detects the powder pressure at the lower part of the forced feeder and the base of the extruder screw so as to always maintain the state of the resin in a non-flowable state, and adjusts the pressure of the forced feeder so that this remains constant. This method attempts to control the screw rotation speed, and it is difficult to measure particularly minute powder pressure. However, it is relatively easy to measure the thrust force of the forced feeder screw, or the screw thrust force detection method of the screw base of the extruder It is characterized by the detection of resin pressure at the extruder feed section, which can detect the powder pressure in an enlarged form, and is suitable for extrusion equipment with a screw-type forced feeder that forcibly feeds thermoplastic resin into the extruder. , a feeder screw rotation speed control in which the pressure of the resin raw material at the lower part of the forced feeder and the extruder screw base is detected by a sensor, and the rotation speed of the forced feeder screw is controlled so that the pressure is always constant based on the output of the sensor. The purpose is to provide a method.
以下本発明の実施例を図面について説明する
と、第2図及び第3図は本発明方法を実施する装
置を示し、図中1は押出機スクリユ、2は強制フ
イーダスクリユ、3は強制フイーダスクリユ駆動
モータである。そしてこの装置では、強制フイー
ダ下部及び押出機スクリユ1基部での粉体原料の
圧力を検出し、これが一定となるよう強制フイー
ダのスクリユ回転数の制御を行なう。 Embodiments of the present invention will be described below with reference to the drawings. Figures 2 and 3 show an apparatus for implementing the method of the present invention, in which 1 is an extruder screw, 2 is a forced feeder screw, and 3 is a forced feeder screw drive motor. be. In this device, the pressure of the powder raw material at the lower part of the forced feeder and the base of the extruder screw 1 is detected, and the screw rotation speed of the forced feeder is controlled so that the pressure remains constant.
またa,b,c,dは強制フイーダのスクリユ
回転数を制御するための粉体原料の圧力を検出す
る位置を示す。そしてa位置は、供給粉体圧によ
りフイーダスクリユのスラスト力が決まることか
ら、スクリユのスラスト力を、例えばロードセル
で検知する場合である。またb位置は、供給粉体
圧と押出機フイード部の樹脂圧が比例することか
ら、押出機フイード部の樹脂圧を通常用いられる
隔膜式の歪ゲージ式圧力計や、圧電素子形圧力計
を用いて検出する場合である。一方c位置は、フ
イーダスクリユ先端に圧力計を取付け、直接供給
粉体圧を検出する場合である。またd位置は、原
料供給口の側壁に圧力計を取付け、直接供給粉体
圧を検出する例である。 Further, a, b, c, and d indicate positions for detecting the pressure of the powder raw material for controlling the screw rotation speed of the forced feeder. Since the thrust force of the feeder screw is determined by the pressure of the supplied powder, the position a is used when the thrust force of the feeder screw is detected by, for example, a load cell. In addition, at position b, since the supply powder pressure and the resin pressure at the extruder feed section are proportional, the resin pressure at the extruder feed section can be measured using a normally used diaphragm-type strain gauge pressure gauge or a piezoelectric element pressure gauge. This is a case of detection using On the other hand, at position c, a pressure gauge is attached to the tip of the feeder screw to directly detect the pressure of the supplied powder. Further, position d is an example in which a pressure gauge is attached to the side wall of the raw material supply port to directly detect the pressure of the supplied powder.
さて検出部a,b,c,d等の位置により検出
される粉体原料の圧力が、図示しない制御装置に
より常に一定となるように、強制フイーダスクリ
ユ2の回転数が制御される。 Now, the rotation speed of the forced feeder screw 2 is controlled so that the pressure of the powder raw material detected by the positions of the detection parts a, b, c, d, etc. is always constant by a control device (not shown).
以上詳細に説明した如く本発明は構成されてい
るので、強制フイーダ下部及び押出機スクリユ基
部で粉体原料がある一定の圧力となるよう強制フ
イーダのスクリユ回転数を制御することにより、
粉体原料のかさ比重を高め、押出機スクリユへ常
に安定した量の原料を送り込むことにより、押出
量の低下、押出変動を防ぐことができる。なお、
本発明は、粉体原料の他、粉体と粒子(ペレツ
ト)を混合した原料、フイルム等の破砕した原
料、あるいはこの破砕原料とペレツトを混合した
原料を強制フイーダを用いて主押出機に送り込む
押出装置に適用できる。 Since the present invention is configured as described above in detail, by controlling the screw rotation speed of the forced feeder so that a certain pressure of the powder material is maintained at the lower part of the forced feeder and the base of the extruder screw,
By increasing the bulk specific gravity of the powder raw material and constantly feeding a stable amount of raw material to the extruder screw, it is possible to prevent a decrease in the extrusion rate and fluctuations in the extrusion rate. In addition,
In the present invention, in addition to powder raw materials, raw materials mixed with powder and particles (pellets), crushed raw materials such as films, or raw materials mixed with this crushed raw material and pellets are fed into the main extruder using a forced feeder. Applicable to extrusion equipment.
第1図は従来のスクリユ式強制フイーダを設け
た押出機の側断面図、第2図は本発明の方法を実
施する装置におけるフイーダスクリユ先端部の側
断面図、第3図は第2図における要部の詳細断面
図である。
図の主要部分の説明、1……押出機スクリユ、
2……強制フイーダスクリユ、3……駆動モー
タ、a,b,c,d……粉体原料の圧力検出位
置。
FIG. 1 is a side sectional view of an extruder equipped with a conventional screw-type forced feeder, FIG. 2 is a side sectional view of the tip of the feeder screw in an apparatus for carrying out the method of the present invention, and FIG. FIG. Explanation of the main parts of the figure, 1... Extruder screw,
2...Forced feeder screw, 3...Drive motor, a, b, c, d...Powder raw material pressure detection position.
Claims (1)
クリユ式強制フイーダを持つ押出装置において、
強制フイーダ下部及び押出機スクリユ基部での樹
脂原料の圧力をセンサで検出し、同センサの出力
により前記圧力が常に一定となるよう強制フイー
ダスクリユの回転数を制御することを特徴とする
フイーダスクリユの回転数制御方法。1. In an extrusion device with a screw-type forced feeder that forcibly feeds thermoplastic resin into an extruder,
The rotation speed of the feeder screw, characterized in that the pressure of the resin raw material at the lower part of the forced feeder and the base of the extruder screw is detected by a sensor, and the rotation speed of the forced feeder screw is controlled so that the pressure is always constant based on the output of the sensor. Control method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58226394A JPS60116424A (en) | 1983-11-30 | 1983-11-30 | Controlling method of revolutional number of feeder screw |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58226394A JPS60116424A (en) | 1983-11-30 | 1983-11-30 | Controlling method of revolutional number of feeder screw |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60116424A JPS60116424A (en) | 1985-06-22 |
| JPH0565334B2 true JPH0565334B2 (en) | 1993-09-17 |
Family
ID=16844429
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58226394A Granted JPS60116424A (en) | 1983-11-30 | 1983-11-30 | Controlling method of revolutional number of feeder screw |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60116424A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3545747C2 (en) * | 1985-12-21 | 1994-10-06 | Krupp Ag Hoesch Krupp | Extruder monitoring |
| DE3744193C1 (en) * | 1987-12-24 | 1989-01-26 | Berstorff Gmbh Masch Hermann | Process and extruder for degassing thermoplastic plastic melts over a wide range of viscosities |
| JPH04276418A (en) * | 1991-03-04 | 1992-10-01 | Japan Steel Works Ltd:The | Powder compression apparatus |
| IT1274715B (en) * | 1993-08-24 | 1997-07-24 | Nissei Plastics Ind Co | INJECTION MOLDING METHOD OF POLYETHYLENE TEREPHTHALATE |
| JP2659515B2 (en) * | 1994-01-31 | 1997-09-30 | 帝人株式会社 | Extruder discharge pressure control device |
| DE102016224607A1 (en) * | 2016-12-09 | 2018-06-14 | Raumedic Ag | Silicone extrusion line, process for silicone extrusion and silicone extrudate produced thereby |
| CN113021053A (en) * | 2021-03-15 | 2021-06-25 | 大连理工大学 | Self-healing test device and method for precision of feeding shaft of numerical control machine tool |
| DE102023121312A1 (en) * | 2023-08-09 | 2025-02-13 | Windmöller & Hölscher Kg | Feeding device and method for feeding granules and ground material into a plastic extruder |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50161553A (en) * | 1974-06-21 | 1975-12-27 |
-
1983
- 1983-11-30 JP JP58226394A patent/JPS60116424A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60116424A (en) | 1985-06-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1043444C (en) | Method regulating level of mixture of flowable material in container having outlet | |
| US4209476A (en) | Method and apparatus for fabrication of extruded articles | |
| JP2011500373A (en) | Method and apparatus for processing synthetic resin materials | |
| JPS5947980B2 (en) | Thermoplastic resin extrusion method | |
| JPH0565334B2 (en) | ||
| KR0150503B1 (en) | Method of injection molding polyethylene terephthalate | |
| JP2673491B2 (en) | Amorphous molding material supply method | |
| JP2616635B2 (en) | Dry compression granulation method and apparatus therefor | |
| US4470937A (en) | Size control of extrusion molded articles | |
| JP3217152B2 (en) | Vent extruder | |
| JPS6254654B2 (en) | ||
| JPH074019U (en) | Extrusion amount control device such as plastic molding machine | |
| JPH05212773A (en) | Extruder discharge rate control device | |
| JPS6331731A (en) | Precision control of extruder or the like | |
| JPH069852B2 (en) | Raw material consumption detection device for synthetic resin extrusion device and method for controlling extrusion amount | |
| JPS62246713A (en) | Controlling film thickness in apparatus for manufacturing synthetic resin film | |
| JP3505440B2 (en) | Material supply monitoring method and apparatus for metal injection molding machine | |
| JP2659515B2 (en) | Extruder discharge pressure control device | |
| JP2000094110A (en) | Material supply control method and apparatus for metal injection molding machine | |
| SU910424A1 (en) | Apparatus for automatic control of polymeric material processing in auger machines | |
| JP7738308B1 (en) | Molding method | |
| JPH02269024A (en) | Apparatus for control of emission amount of extruder with gear pump | |
| US5045252A (en) | Method and apparatus for controlling rotary extruder | |
| JP3517902B2 (en) | Discharge stability control method for multi-screw extruder | |
| JPH054271A (en) | Flow rate controlling method of extruder |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |