JPH0475127B2 - - Google Patents
Info
- Publication number
- JPH0475127B2 JPH0475127B2 JP58190358A JP19035883A JPH0475127B2 JP H0475127 B2 JPH0475127 B2 JP H0475127B2 JP 58190358 A JP58190358 A JP 58190358A JP 19035883 A JP19035883 A JP 19035883A JP H0475127 B2 JPH0475127 B2 JP H0475127B2
- Authority
- JP
- Japan
- Prior art keywords
- extruder
- value
- resin
- temperature
- time
- 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 - Lifetime
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
- B29C2948/92504—Controlled parameter
- B29C2948/9258—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
- B29C2948/92504—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
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- 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
- B29C2948/92885—Screw or gear
-
- 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
- B29C2948/92933—Conveying, transporting or storage of articles
-
- 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
- B29C2948/9298—Start-up, shut-down or parameter setting phase; Emergency shut-down; Material change; Test or laboratory equipment or studies
-
- 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
- B29C48/06—Rod-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/04—Condition, form or state of moulded material or of the material to be shaped cellular or porous
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
- Processes Specially Adapted For Manufacturing Cables (AREA)
Description
【発明の詳細な説明】
(発明の技術分野)
本発明は、押出機特に発泡プラスチツク被覆押
出機の立ち上がり(始動)状態を制御する方法に
関する。TECHNICAL FIELD OF THE INVENTION The present invention relates to a method for controlling the start-up conditions of an extruder, particularly a foamed plastic coating extruder.
(発明の技術的背景とその問題点)
一般に発泡プラスチツク絶縁電線においては、
規格の仕上り外径や静電容量等の絶縁特性を持つ
ために絶縁体が所定の発泡率で発泡されているこ
とが要求されている。(Technical background of the invention and its problems) Generally, in foamed plastic insulated wires,
Insulators are required to be foamed at a predetermined foaming rate in order to have insulation properties such as standard finished outer diameter and capacitance.
而して被覆押出機を用いて発泡剤を配合した樹
脂を混練し押出発泡させる方法においては、押出
機内の樹脂温度を適正値に保たないと所定の発泡
率が得られない。 In the method of kneading and extruding foaming a resin containing a blowing agent using a coating extruder, a predetermined foaming rate cannot be obtained unless the resin temperature in the extruder is maintained at an appropriate value.
従つて従来から押出機の始動後混練時に発生す
る剪断熱により上昇した樹脂温度が安定した後に
初めて製品の引取りを行なつていた。 Conventionally, therefore, the product was not collected until the resin temperature, which had risen due to the shear heat generated during kneading after starting the extruder, had stabilized.
すなわち第1図に示されるように、定常値に加
熱温度が設定された押出機の始動後、押出体の引
取速度およびスクリユーの回転数が定常値に達
し、
樹脂温度が適正値まで上昇して安定した時点
T′から製品取りを開始していた。 In other words, as shown in Figure 1, after the extruder is started with the heating temperature set to a steady value, the take-up speed of the extruded body and the rotational speed of the screw reach the steady value, and the resin temperature rises to the appropriate value. stable point
We started picking up products from T′.
そのため押出機の始動から製品取りまでに時間
がかかり、この間に押出された多量の樹脂や導体
などの材料が無駄になるという問題があつた。 Therefore, there was a problem in that it took a long time from starting the extruder to taking out the product, and a large amount of materials such as resin and conductors extruded during this time were wasted.
また押出機を一旦停止して再始動する場合に
は、まず発泡温度以上の温度に長時間さらされ過
発泡状態になつた残留樹脂を出しきらなければな
らずこの場合にも従来からの立ち上がり制御方法
では材料ロスが大きかつた。 In addition, when the extruder is stopped and restarted, the residual resin that has been exposed to temperatures above the foaming temperature for a long period of time and has become overfoamed must be removed. This method resulted in a large amount of material loss.
(発明の目的)
本発明はこれらの問題を解決するためになされ
たもので、始動から製品取りまでの時間を短縮し
材料ロスを低減することができる押出機の立ち上
がり制御方法を提供することを目的とする。(Object of the Invention) The present invention was made to solve these problems, and an object of the present invention is to provide a start-up control method for an extruder that can shorten the time from startup to product removal and reduce material loss. purpose.
(発明の概要)
本発明は、予め押出機の加熱温度を定常値より
やや高めに設定しておき、この設定温度信号によ
り押出機内の樹脂温度を急激に上昇させると同時
に、スクリユーの回転数を押出体の引取速度の上
昇率より高い上昇率で定常値まで上昇させつつ押
出しを続け、前記スクリユーの回転数が定常値に
達したら直ちに前記押出機の設定温度を定常値に
戻し、樹脂温度を適正値に保持することを特徴と
する押出機の立ち上がり制御方法である。(Summary of the invention) In the present invention, the heating temperature of the extruder is set in advance to a slightly higher value than the steady value, and the resin temperature in the extruder is rapidly raised by this set temperature signal, and at the same time, the rotation speed of the screw is increased. Extrusion is continued while increasing to a steady value at a higher rate of increase than the rate of increase in the take-up speed of the extruded body, and as soon as the rotational speed of the screw reaches the steady value, the set temperature of the extruder is returned to the steady value, and the resin temperature is This is a method for controlling the start-up of an extruder, which is characterized by maintaining the start-up at an appropriate value.
(発明の実施例)
以下本発明の実施例を図面を参照しながら説明
する。(Embodiments of the invention) Examples of the invention will be described below with reference to the drawings.
実施例においてはまず第2図Cに示されるよう
に、押出機の加熱温度設定値を樹脂が過発泡とな
らない範囲で定常値よりやや高めに設定してお
き、この設定温度信号を押出機の加熱混練部に出
力しつつ押出機を始動させる。始動後前記設定温
度信号により押出機内の樹脂温度は第2図Dに示
されるように急激に上昇し、しかも加熱混練の際
に発生する剪断熱により、さらに上昇する。この
樹脂温度が適正値を越えないように、適正値に近
くなつた時点で加熱設定温度を定常値に戻す。 In the example, first, as shown in Figure 2C, the heating temperature setting value of the extruder is set slightly higher than the steady value within a range that does not cause over-foaming of the resin, and this set temperature signal is used to control the extruder heating temperature. The extruder is started while outputting to the heating kneading section. After startup, the temperature of the resin in the extruder rises rapidly in response to the set temperature signal, as shown in FIG. 2D, and further rises due to the shear heat generated during heating and kneading. In order to prevent this resin temperature from exceeding an appropriate value, the heating set temperature is returned to a steady value when it approaches the appropriate value.
また始動後の押出体の引取速度は第2図Aに示
されるように一定の速さで上昇するように制御さ
れているが、このときスクリユーの回転数を、内
部の樹脂圧力が過大にならない範囲で第2図Bに
示されるように、定常値まで引取速度より速やか
に上昇させる。こうして前記剪断熱の発生により
樹脂温度はいつそう速かに適正値まで上昇するこ
とになる。 In addition, the take-up speed of the extruded body after startup is controlled so that it increases at a constant speed as shown in Figure 2A, but at this time, the rotation speed of the screw is controlled so that the internal resin pressure does not become excessive. As shown in FIG. 2B in the range, the take-up speed is increased more quickly than the steady-state value. In this way, the resin temperature quickly rises to an appropriate value due to the generation of the shear heat.
尚、スクリユーの回転数は第2図Bの破線で示
すように、一旦定常値より高い値にまで上げた
後、引取速度が定常値に達した時点で定常値まで
下げるように制御することもできる。 In addition, as shown by the broken line in Figure 2B, the screw rotation speed can be controlled so that it is once raised to a value higher than the steady value and then lowered to the steady value when the take-up speed reaches the steady value. can.
このように制御される実施例においては引取速
度が定常値に到達した時点と樹脂温度が適正値に
達して製品取りを開始することができる時点T2
をほぼ一致させることができ、始動から製品取り
までの時間を大幅に短縮することができる。 In the embodiment controlled in this way, the time point T2 when the take-up speed reaches a steady value and the time point T2 when the resin temperature reaches an appropriate value and product taking can be started.
can be made almost the same, and the time from startup to product removal can be significantly shortened.
(発明の効果)
以上の記載から明らかなように、本発明によれ
ば押出機の始動から製品取りまでの立ち上がり時
間を従来に比べて大幅に短縮することができ、立
ち上がり時に押出される樹脂等の材料のロス分を
減少させることができる。(Effects of the Invention) As is clear from the above description, according to the present invention, the start-up time from the start of the extruder to the product removal can be significantly shortened compared to the conventional method, and the resin extruded at the time of start-up can be greatly reduced. can reduce material loss.
第1図は従来の方法により制御された場合の引
取速度、スクリユー回転数、加熱設定温度および
樹脂温度の経時変化を示すタイムチヤート、第2
図は本発明の実施例の方法により制御されたとき
の同一量の経時変化を示すタイムチヤートであ
る。
Figure 1 is a time chart showing changes over time in take-up speed, screw rotation speed, heating set temperature, and resin temperature when controlled by the conventional method;
The figure is a time chart showing the change over time of the same amount when controlled by the method of the embodiment of the present invention.
1 繊維板等の吸音板表面に適宜厚さの棒状スペ
ーサ部材を複数本、適宜間隔毎に平行に配設、固
着し、これらの棒状スペーサ部材に表面化粧板の
裏面を一体に接着し、該表面化粧板に棒状スペー
サ部材と交叉する方向にスリツト状開口部を表裏
面間に貫通させて穿設していることを特徴とする
吸音化粧材。
2 繊維板等の吸音板表面に適宜厚さの棒状スペ
ーサ部材を複数本、適宜間隔毎に平行に配設して
装着する工程と、これらの棒状スペーサ部材表面
に架設するようにして表面化粧板を配設してその
裏面を棒状スペーサ部材表面に一体に接着する工
程と、表面化粧板にルーター或いはノコ等によつ
て前記棒状スペーサ部材に交叉する方向に沿つて
複数個のスリツト状開口部を表裏面間に貫通して
穿設する工程と必要に応じて表面化粧材を適数に
分別する工程とからなる吸音化粧材の製造方法。
1 Arrange and fix a plurality of rod-shaped spacer members of an appropriate thickness in parallel at appropriate intervals on the surface of a sound-absorbing board such as a fiberboard, and integrally adhere the back side of the surface decorative board to these rod-shaped spacer members. A sound-absorbing decorative material characterized in that a slit-shaped opening is formed in a surface decorative board in a direction intersecting with a rod-shaped spacer member so as to penetrate between the front and back surfaces. 2. A process of installing a plurality of rod-shaped spacer members of appropriate thickness in parallel at appropriate intervals on the surface of a sound-absorbing board such as a fiberboard, and installing a surface decorative board on the surface of these rod-shaped spacer members. and integrally bonding the back side thereof to the surface of the rod-shaped spacer member, and forming a plurality of slit-shaped openings in the surface decorative board along the direction intersecting the rod-shaped spacer member using a router, a saw, etc. A method for producing a sound-absorbing decorative material, which comprises the steps of drilling a hole between the front and back surfaces, and separating the surface decorative material into an appropriate number of parts as necessary.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58190358A JPS6082322A (en) | 1983-10-12 | 1983-10-12 | Rising control of extruder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58190358A JPS6082322A (en) | 1983-10-12 | 1983-10-12 | Rising control of extruder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6082322A JPS6082322A (en) | 1985-05-10 |
| JPH0475127B2 true JPH0475127B2 (en) | 1992-11-30 |
Family
ID=16256856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58190358A Granted JPS6082322A (en) | 1983-10-12 | 1983-10-12 | Rising control of extruder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6082322A (en) |
-
1983
- 1983-10-12 JP JP58190358A patent/JPS6082322A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6082322A (en) | 1985-05-10 |
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