Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0139602B2 - - Google Patents
[go: Go Back, main page]

JPH0139602B2 - - Google Patents

Info

Publication number
JPH0139602B2
JPH0139602B2 JP58162063A JP16206383A JPH0139602B2 JP H0139602 B2 JPH0139602 B2 JP H0139602B2 JP 58162063 A JP58162063 A JP 58162063A JP 16206383 A JP16206383 A JP 16206383A JP H0139602 B2 JPH0139602 B2 JP H0139602B2
Authority
JP
Japan
Prior art keywords
color
crosshead
color change
overflow
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
Application number
JP58162063A
Other languages
Japanese (ja)
Other versions
JPS6054110A (en
Inventor
Akira Matsui
Hideo Eda
Juko Furu
Yasushi Tanaka
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric Co 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP58162063A priority Critical patent/JPS6054110A/en
Publication of JPS6054110A publication Critical patent/JPS6054110A/en
Publication of JPH0139602B2 publication Critical patent/JPH0139602B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Processes Specially Adapted For Manufacturing Cables (AREA)

Description

【発明の詳細な説明】 〔技術分野〕 本発明は、発泡絶縁電線を製造しているときの
発泡絶縁体の色替を行う方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a method for changing the color of a foam insulator during the manufacture of a foam insulated wire.

〔従来技術〕[Prior art]

通信ケーブルの心線等に用いられる発泡絶縁電
線は、銅線を押出機のクロスヘツドに通して、そ
の上に発泡絶縁体を押出被覆することにより製造
される。ケーブル化した場合に個々の発泡絶縁電
線の識別を容易にするため、発泡絶縁電線の製造
に際しては、同一サイズでも何種類かの色の異な
る発泡絶縁体を押出被覆する必要があり、しばし
ば色替が行われている。この色替は、押出機に供
給する樹脂材料をある色のものから他の色のもの
に切替えることによつて行われるが、この色替を
行う時に不良品ができるので、それをできるだけ
少なくすること及び色替のための時間をできるだ
け少なくすることが肝要である。
Foamed insulated wires used as core wires of communication cables are manufactured by passing a copper wire through the crosshead of an extruder and extruding a foamed insulating material thereon. In order to make it easier to identify individual foam-insulated wires when they are made into cables, when manufacturing foam-insulated wires, it is necessary to extrude and cover the foam insulation with several different colors even if they are the same size, and the color is often changed. is being carried out. This color change is performed by switching the resin material supplied to the extruder from one color to another, but since defective products are produced when performing this color change, it is necessary to minimize the number of defective products. It is important to minimize the time required for color changes.

発泡絶縁電線の製造過程における色替は、一般
に線材の走行を停止させ、押出機のクロスヘツド
にあるオーバーフローコツクを開いて押出機内に
残つているこれまでの色の樹脂材料を抜き出し、
新しい色の樹脂材料に切替わつたところで再び運
転を開始するという手順をとつている。
To change the color during the manufacturing process of foam insulated wire, generally, the running of the wire is stopped, the overflow kettle in the crosshead of the extruder is opened, and the resin material of the previous color remaining in the extruder is extracted.
The procedure is to restart operation once the new colored resin material has been used.

ところで、発泡絶縁電線の製造方法には、押出
機に供給する樹脂材料中に熱分解型の化学発泡剤
を混入しておいてそれを加熱発泡させる化学発泡
方式と、押出機内で溶融した樹脂材料中にガスを
注入し、そのガスを発泡剤として用いるガス注入
発泡方式とがある。化学発泡方式では、使用する
着色剤(顔料)の種類によつて一定の発泡率を得
るための押出条件(例えば温度等)が異なるた
め、色替の度に押出条件の変更が必要となり、色
替に例えば30〜40分というような多大の時間を要
するという問題がある。これに比べガス注入発泡
方式では、発泡剤がもともとガスであるため、着
色剤の種類が変わつても押出条件を変更する必要
がないという利点がある。しかしながらガス注入
発泡方式の場合でも、線速を変えたり、オーバー
フローコツクを開閉したりすると発泡率が変化す
るため、運転を再開してから発泡率を安定させる
までに時間がかかり、またこれによる不良品の発
生も少なくないという問題がある。
By the way, there are two methods for manufacturing foam insulated wires: a chemical foaming method in which a pyrolytic chemical foaming agent is mixed into the resin material supplied to an extruder, and the mixture is heated and foamed; There is a gas injection foaming method in which gas is injected into the foam and the gas is used as a foaming agent. In the chemical foaming method, the extrusion conditions (e.g. temperature, etc.) to obtain a constant foaming rate vary depending on the type of colorant (pigment) used, so it is necessary to change the extrusion conditions each time the color is changed. However, there is a problem in that it takes a long time, for example, 30 to 40 minutes. In comparison, the gas injection foaming method has the advantage that, since the foaming agent is originally a gas, there is no need to change the extrusion conditions even if the type of colorant changes. However, even in the case of the gas injection foaming method, the foaming rate changes when the line speed is changed or the overflow tank is opened or closed, so it takes time to stabilize the foaming rate after restarting operation, and this can cause problems. There is a problem in that there are not a small number of non-defective products.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、上記のガス注入発泡方式の利
点を生かし、発泡絶縁電線の製造過程で色替を短
時間で行うことのできる方法を提供せんとするも
のである。
An object of the present invention is to provide a method that takes advantage of the above-mentioned gas injection foaming method and can change colors in a short time during the manufacturing process of foamed insulated wires.

〔発明の構成〕[Structure of the invention]

上記目的を達成すべく本発明は、ガス注入発泡
方式により発泡絶縁電線を製造しているときに押
出される発泡絶縁体の色替を行う方法において、
線速を運転線速から色替線速に下げて色替を行う
と共に、色替開始時又は色替の途中から色替終了
までの間、クロスヘツド内の樹脂圧力が一定とな
るようにオーバーフローコツクの開度を調節する
ことを特徴とするものである。
In order to achieve the above object, the present invention provides a method for changing the color of a foamed insulator extruded when manufacturing a foamed insulated wire using a gas injection foaming method.
The line speed is lowered from the operating line speed to the color change line speed to perform the color change, and an overflow control is applied to keep the resin pressure in the crosshead constant from the start of the color change or from the middle of the color change to the end of the color change. It is characterized by adjusting the opening degree of the opening.

通常、発泡絶縁電線は、1000〜3000m/分程度
の線速で製造されており、これがいわゆる運転線
速であるが、色替を行う場合には、これを例えば
300m/分前後の色替線速に低下させる。そして
色替終了時にはもとの運転線速に戻すようにす
る。また色替を行うときは、当然のことながらク
ロスヘツドに付いているオーバーフローコツクを
開き、これまでの色の樹脂材料を排出することに
なる。このように線速を変えたり、オーバーフロ
ーコツクを開閉したりするとクロスヘツド内の樹
脂圧力が変動する。一般に、線速を低下させると
クロスヘツド内の樹脂圧力は上昇し、オーバーフ
ローコツクを開くと同樹脂圧力は低下する。ガス
注入発泡方式では、このようなクロスヘツド内の
樹脂圧力の変動は発泡率の変動につながる。即
ち、一般には押出量Qは次式で表わされる。
Normally, foam insulated wires are manufactured at a line speed of about 1000 to 3000 m/min, which is the so-called operating line speed, but when changing colors, for example,
Reduce the color change line speed to around 300m/min. Then, at the end of the color change, the original operating line speed is restored. Also, when changing colors, the overflow tank attached to the crosshead must be opened and the resin material of the previous color must be discharged. In this way, changing the linear speed or opening and closing the overflow cock causes the resin pressure in the crosshead to fluctuate. Generally, when the line speed is reduced, the resin pressure in the crosshead increases, and when the overflow stock is opened, the resin pressure decreases. In the gas injection foaming method, such fluctuations in the resin pressure within the crosshead lead to fluctuations in the foaming rate. That is, the extrusion amount Q is generally expressed by the following formula.

Q=αN−βΔP ……(1) N:スクリユー回転数 ΔP;差圧、つまりクロスヘツド内の樹脂圧力と
押出機の軸方向のある位置(例えばガス注入
部)における樹脂圧力との差 α、β:定数 N=一定とした場合、クロスヘツド内の樹脂圧
力が変動するということは、ΔPが変動し、従つ
て押出量Qが変動するということである。一方、
ガス注入発泡方式の場合、注入されるガス量(単
位時間当り)は押出機内の樹脂圧力の変動にかか
わらず一定であるから、押出量が変動すると、樹
脂とガスの比率が変わり、発泡率が変動すること
になる。
Q = αN - βΔP ... (1) N: Screw rotation speed ΔP; Differential pressure, that is, the difference α, β between the resin pressure in the crosshead and the resin pressure at a certain position in the axial direction of the extruder (e.g. gas injection part) :Constant When N=constant, the fact that the resin pressure in the crosshead fluctuates means that ΔP fluctuates, and therefore the extrusion amount Q fluctuates. on the other hand,
In the case of the gas injection foaming method, the amount of gas injected (per unit time) is constant regardless of fluctuations in the resin pressure inside the extruder, so if the extrusion amount changes, the ratio of resin to gas changes and the foaming rate changes. It will change.

このため本発明は、色替中にクロスヘツド内の
樹脂圧力が運転状態と同じ一定の圧力となるよう
にオーバーフローコツクの開度を調節して、色替
終了後はただちに運転状態に入れるようにしたも
のである。
For this reason, the present invention adjusts the opening degree of the overflow cock so that the resin pressure in the crosshead remains at the same constant pressure as in the operating state during the color change, and immediately returns to the operating state after the color change is completed. It is something.

〔実施例〕〔Example〕

第1図は本発明の方法を実施するのに用いる装
置の一例を示している。符号1はスクリユー式押
出機、3は着色剤を混合した樹脂材料を供給する
ホツパー、5はガス注入口、7はガス流量を設定
する弁、9はクロスヘツドである。線材はクロス
ヘツド9内を紙面に垂直な方向に走行する。11
はクロスヘツド9に取付けられた樹脂抜き用のオ
ーバーフローコツク、13はそのオーバーフロー
コツク11の開度を調節するパルスモータ、15
はクロスヘツド9内の樹脂圧力を検出する圧力検
出器、17は色替時に検出した圧力に応じてパル
スモータを駆動する制御器である。
FIG. 1 shows an example of the apparatus used to carry out the method of the invention. 1 is a screw type extruder, 3 is a hopper for supplying a resin material mixed with a colorant, 5 is a gas inlet, 7 is a valve for setting the gas flow rate, and 9 is a crosshead. The wire runs within the crosshead 9 in a direction perpendicular to the plane of the paper. 11
13 is a pulse motor for adjusting the opening degree of the overflow socket 11; 15 is an overflow socket for removing resin attached to the crosshead 9
A pressure detector 17 detects the resin pressure in the crosshead 9, and a controller 17 drives a pulse motor in accordance with the pressure detected at the time of color change.

次にこの装置により色替を行う順序を第2図の
タイムチヤートを参照して説明する。まず色替開
始時t1でオーバーフローコツク11を全開する。
これと同時あるいはこれに先立つてホツパ3から
供給する材料を別の色に切替える。オーバーフロ
ーコツク11を開くとクロスヘツド9内の樹脂圧
力が低下するから、少し時間をおいたt2の時点よ
り線速を低下させる。これまでは運転線速であ
る。線速を漸次低下させ、線速が所定の色替速度
に達したら、その時点t4からt5までの間、線速を
色替線速一定に保つ。色替線速は例えば運転線速
の1/10程度である。t4からt5までの時間は押出機
1及びクロスヘツド9内の樹脂がすべて新しい色
に入れ替わるまでの時間を考慮して定められる。
樹脂の入れ替えが終るとt5の時点から線速を上昇
させ、運転線速に達したならばその時点t6以後は
運転線速一定に保つ。一方、クロスヘツド9内の
樹脂圧力はオーバーフローコツク11の開放によ
り低下するが、その後の適当な時点t3より色替終
了時t6までの間は、運転状態と同じ一定の圧力と
なるように制御される。この制御は、圧力検出器
15によりクロスヘツド9内の樹脂圧力を検出
し、その検出値が制御器17内の設定値より高い
ときはパルスモータ13をオーバーフローコツク
11が開く方向に駆動し、低いときはパルスモー
タ13を逆方向に駆動することにより、行う。こ
のためオーバーフローコツク11はt3からt6まで
の間、開度が細かく変化する。
Next, the order in which color change is performed by this device will be explained with reference to the time chart of FIG. First, at t1 at the start of color change, the overflow cock 11 is fully opened.
At the same time or prior to this, the material supplied from the hopper 3 is switched to another color. When the overflow stock 11 is opened, the resin pressure in the crosshead 9 decreases, so the linear speed is reduced from time t2 after a short delay. Up until now, it has been the operating line speed. The line speed is gradually reduced, and when the line speed reaches a predetermined color change speed, the line speed is kept constant from time t4 to t5 . The color change line speed is, for example, about 1/10 of the operating line speed. The time from t 4 to t 5 is determined by taking into account the time required for all of the resin in the extruder 1 and crosshead 9 to be replaced with new colors.
When the resin replacement is completed, the linear speed is increased from time t 5 , and when the operating linear speed is reached, the operating linear speed is kept constant from that point t 6 onwards. On the other hand, the resin pressure inside the crosshead 9 decreases due to the opening of the overflow cock 11, but from an appropriate time t3 until the color change end time t6 , the pressure is controlled to be the same as the operating state. be done. In this control, the pressure detector 15 detects the resin pressure in the crosshead 9, and when the detected value is higher than the set value in the controller 17, the pulse motor 13 is driven in the direction in which the overflow cock 11 opens; is performed by driving the pulse motor 13 in the opposite direction. Therefore, the opening degree of the overflow socket 11 changes minutely from t 3 to t 6 .

このように色替を行つているうちからクロスヘ
ツド9内の樹脂圧力を一定にしておくと、その間
押出量はぼぼ一定に保たれるから、発泡率もまた
ほぼ一定になる。したがつて運転線速に戻した後
ただちに発泡率の安定した製品を得ることができ
る。
If the resin pressure in the crosshead 9 is kept constant while the color is being changed in this way, the extrusion amount will be kept approximately constant during that time, and the foaming rate will also be approximately constant. Therefore, a product with a stable foaming rate can be obtained immediately after returning to the operating line speed.

上記実施例では、色替の途中t3からクロスヘツ
ド内の圧力制御を行つたが、この圧力制御は色替
開始時t1から行つても差支えない。
In the above embodiment, the pressure inside the crosshead was controlled from t3 during the color change, but this pressure control may also be performed from t1 at the start of the color change.

また上記実施例では、スクリユー式押出機の中
間からガスを注入する場合について説明したが、
押出機を2台接続し、その接続部からガスを注入
する場合についても本発明は同様に適用可能であ
る。
Furthermore, in the above embodiment, a case was explained in which gas was injected from the middle of the screw type extruder.
The present invention is similarly applicable to the case where two extruders are connected and gas is injected from the connection.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明によれば、線速を落
として色替を行つているときからクロスヘツド内
の樹脂圧力を一定に保つように制御しているの
で、色替線速から運転線速に戻した時点ではすで
に発泡率が安定しており、その後ただちに良好な
製品が得られるようになるため、色替に要する時
間が短かくて済むという利点がある。
As explained above, according to the present invention, the resin pressure in the crosshead is controlled to be kept constant even when the color change is performed at a reduced linear speed, so that the linear speed of the color change changes to the operating linear speed. The foaming rate is already stable at the time of return, and a good product can be obtained immediately thereafter, which has the advantage that the time required for color change is short.

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

第1図は本発明の方法を実施するのに用いられ
る装置の一例を示す正面図、第2図は本発明の方
法の一実施例を示すタイムチヤートである。 1……押出機、5……ガス注入口、9……クロ
スヘツド、11……オーバーフローコツク、13
……パルスモータ、15……圧力検出器、17…
…制御器。
FIG. 1 is a front view showing an example of an apparatus used to carry out the method of the present invention, and FIG. 2 is a time chart showing an example of the method of the present invention. 1...Extruder, 5...Gas inlet, 9...Crosshead, 11...Overflow stock, 13
...Pulse motor, 15...Pressure detector, 17...
...Controller.

Claims (1)

【特許請求の範囲】[Claims] 1 ガス注入発泡方式により発泡絶縁電線を製造
しているときに押出される発泡絶縁体の色替を行
う方法において、線速を運転線速から色替線速に
下げて色替を行うと共に、色替開始時又は色替の
途中から色替終了時までの間、クロスヘツド内の
樹脂圧力が一定となるようにオーバーフローコツ
クの開度を調節することを特徴とする発泡絶縁電
線の色替方法。
1. In a method of changing the color of a foamed insulator extruded during the production of foamed insulated wire by a gas injection foaming method, the wire speed is lowered from the operating wire speed to the color changing wire speed and the color is changed, A method for changing the color of a foam insulated wire, characterized by adjusting the opening degree of an overflow socket so that the resin pressure in the crosshead remains constant from the start of color change or from the middle of color change to the end of color change.
JP58162063A 1983-09-05 1983-09-05 Method of replacing color of foamable insulated wire Granted JPS6054110A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58162063A JPS6054110A (en) 1983-09-05 1983-09-05 Method of replacing color of foamable insulated wire

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58162063A JPS6054110A (en) 1983-09-05 1983-09-05 Method of replacing color of foamable insulated wire

Publications (2)

Publication Number Publication Date
JPS6054110A JPS6054110A (en) 1985-03-28
JPH0139602B2 true JPH0139602B2 (en) 1989-08-22

Family

ID=15747380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58162063A Granted JPS6054110A (en) 1983-09-05 1983-09-05 Method of replacing color of foamable insulated wire

Country Status (1)

Country Link
JP (1) JPS6054110A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01307113A (en) * 1988-06-02 1989-12-12 Furukawa Electric Co Ltd:The Manufacture of insulated wire
JPH0787055B2 (en) * 1990-05-28 1995-09-20 藤田エンジニアリング株式会社 Feeder for wire coating
JP2012014911A (en) * 2010-06-30 2012-01-19 Sumitomo Electric Ind Ltd Method for manufacturing electric wire

Also Published As

Publication number Publication date
JPS6054110A (en) 1985-03-28

Similar Documents

Publication Publication Date Title
JPH04219221A (en) Barrier screw
US3986477A (en) Wire coating apparatus
US3300554A (en) Method of making cellular articles
JPH0139602B2 (en)
US5215698A (en) Extrusion tool and method of extrusion coating
US4067554A (en) Method and apparatus for extruding plastic and similar material
JP3348890B2 (en) Wire coating method and device
JPH0721858A (en) Color change control method in wire coating extruder and method for preventing seizure of color change valve in wire coating extruder
JP3542230B2 (en) Color change control device for wire coating equipment
JPH04125123A (en) Operation control method for resin extrusion molding device and its device
FR2565887A1 (en) Continuous vulcanisation and/or crosslinking line, especially for producing insulating synthetic layers on cables
CN119340041B (en) A three-layer co-extrusion cross-linking air extrusion material arrangement method for long-length submarine cables
US20080099942A1 (en) Automatic ramping method and system for extrusion coating wire
JPH08203358A (en) Method for extruding crosslinked-polyethylene admixture
JP2023048722A (en) Extruder and its control method
JPH054271A (en) Flow rate controlling method of extruder
JP3752086B2 (en) Method and apparatus for controlling thickness of plastic sheet, etc.
JPH0467494B2 (en)
JPH06234147A (en) Extraction method for plastic material
JPS6082322A (en) Rising control of extruder
JPS58189912A (en) Method of producing high foamable insulated wire and apparatus therefor
JPS6031939A (en) Extrusion method using a connected extruder
DE2639922A1 (en) Two=stage extruder for high voltage cable insulation - has short initial cooling period above crystallisation temp. for stabilisation
JPS6112605B2 (en)
JPH08300441A (en) Silica dispersion method by screw type kneading extruder