JPH04319212A - Manufacture of extra-fine high forming wire - Google Patents

Manufacture of extra-fine high forming wire

Info

Publication number
JPH04319212A
JPH04319212A JP3085044A JP8504491A JPH04319212A JP H04319212 A JPH04319212 A JP H04319212A JP 3085044 A JP3085044 A JP 3085044A JP 8504491 A JP8504491 A JP 8504491A JP H04319212 A JPH04319212 A JP H04319212A
Authority
JP
Japan
Prior art keywords
extruder
fine
wire
ultra
extra
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.)
Granted
Application number
JP3085044A
Other languages
Japanese (ja)
Other versions
JP3050627B2 (en
Inventor
Yukio Komura
幸夫 香村
Toshihiro Mikami
三上 俊宏
Sadanori Ishida
禎則 石田
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 JP3085044A priority Critical patent/JP3050627B2/en
Publication of JPH04319212A publication Critical patent/JPH04319212A/en
Application granted granted Critical
Publication of JP3050627B2 publication Critical patent/JP3050627B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)
  • Processes Specially Adapted For Manufacturing Cables (AREA)

Abstract

PURPOSE:To stably manufacture a lengthy extra-fine high foaming wire. CONSTITUTION:When a foaming fluorinated carbon resin is extruded from an extruder and to the outer periphery of an extra-fine core wire, the diameter of which is no more than 0.3mm, and which is coated thereby, so as to manufacture an extra-fine high foaming wire, teh rotational number of a screw 2 of the extruder will be not les than 0.5rpm. The extra-fine high foaming wire is manufactured while the temperature of a cylinder 1 of an extruder in proximity of a hopper 3 of the extruder is maintained not more then the melting point of the fluovinated carbon resin.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、芯線外径0.3 mm
以下の極細高発泡線を製造する極細高発泡線の製造方法
に関するものである。
[Industrial Application Field] The present invention applies to core wires with an outer diameter of 0.3 mm.
The present invention relates to a method for producing an ultra-fine, highly foamed wire as described below.

【0002】0002

【従来の技術】コンピュータ等の情報伝送路として、情
報を高速で大量に処理する必要から、情報の伝搬遅延時
間が小さい高密度電線が要求されている。この要求を満
すものとして、外径0.3 mm以下の極細芯線の外周
に押出機から誘電率の小さい発泡テトラフロロエチレン
樹脂の如き発泡ふっ素樹脂を押出し被覆した極細高発泡
線が用いられている。
2. Description of the Related Art High-density electric wires with low information propagation delay time are required as information transmission paths for computers and the like because of the need to process a large amount of information at high speed. To meet this requirement, an ultra-fine highly foamed wire is used, in which the outer periphery of an ultra-fine core wire with an outer diameter of 0.3 mm or less is extruded from an extruder and coated with a foamed fluororesin such as foamed tetrafluoroethylene resin, which has a low dielectric constant. There is.

【0003】この極細発泡線は、熱溶融できるテトラフ
ロロエチレンにフロンの如き発泡ガスを押出機内で注入
し、混練した後、クロスヘッドで発泡ふっ素樹脂を極細
芯線上に押出し被覆した後、発泡させることにより製造
している。この場合、芯線径が小さいと、押出機からの
発泡ふっ素樹脂の押出し量も小さくなる。従来は、シリ
ンダ内径25mmの押出機、又はシリンダ内径30mm
の押出機を低速回転させて、極細芯線に押出し被覆を行
っていた。なお、テトラフロロエチレンの押出しは、剪
断率を大きくすると、被覆表面の肌荒れが起こるため、
剪断率には制限がある。
[0003] This ultra-fine foam wire is made by injecting a foaming gas such as chlorofluorocarbon into heat-meltable tetrafluoroethylene in an extruder, kneading it, and then extruding foamed fluororesin onto the ultra-fine core wire using a crosshead to coat the ultra-fine core wire, followed by foaming. Manufactured by In this case, if the core wire diameter is small, the amount of foamed fluororesin extruded from the extruder will also be small. Conventionally, an extruder with a cylinder inner diameter of 25 mm or a cylinder inner diameter of 30 mm was used.
The extruder was rotated at low speed to extrude and coat the ultra-fine core wire. In addition, when extruding tetrafluoroethylene, increasing the shear rate causes roughening of the coated surface.
There are limits to the shear rate.

【0004】0004

【発明が解決しようとする課題】このような従来の極細
高発泡線の製造方法では、次に示すような種々の問題点
がある。
Problems to be Solved by the Invention The conventional method for producing ultra-fine, highly foamed wires has various problems as shown below.

【0005】(ア)シリンダ内径25mmの押出機で0
.35g/minの押出し量を得るには、スクリュー回
転数は0.4rpm以下にする必要がある。この回転数
では、押出し量が安定しないため、被覆径が不安定にな
る。
(a) 0 in an extruder with a cylinder inner diameter of 25 mm
.. In order to obtain an extrusion rate of 35 g/min, the screw rotation speed needs to be 0.4 rpm or less. At this rotation speed, the extrusion amount is not stable, so the coating diameter becomes unstable.

【0006】(イ)テトラフロロエチレンとフロンは押
出機内で反応するが、押出し量が小さいので、押出機内
で滞留時間が長くなるため、反応が進み、被覆前にテト
ラフロロエチレンが劣化する。例えばシリンダ内径25
mmの押出機で0.35g/min を押出すと、ホッ
パーからダイスまでの押出し材料の滞留時間は5時間以
上となる。
(a) Tetrafluoroethylene and Freon react in the extruder, but since the extrusion rate is small, the residence time in the extruder becomes long, so the reaction progresses and the tetrafluoroethylene deteriorates before coating. For example, cylinder inner diameter 25
When extruding 0.35 g/min with a 1.0 mm extruder, the residence time of the extruded material from the hopper to the die will be more than 5 hours.

【0007】(ウ)シリンダ内径10mm以下の押出機
を用いると、スクリューシャフトの強度が小さく、テト
ラフロロエチレンは融点近傍(300 ℃)で急激に粘
度が変わるため、スクリューに大きな捩りモーメントが
加わり、スクリューが破損する。
(c) If an extruder with a cylinder inner diameter of 10 mm or less is used, the strength of the screw shaft is low and the viscosity of tetrafluoroethylene changes rapidly near its melting point (300°C), so a large torsional moment is applied to the screw. The screw will be damaged.

【0008】本発明の目的は、芯線外径0.3mm 以
下の極細高発泡線の製造を長尺にわたって安定して行う
ことができる極細高発泡線の製造方法を提供することに
ある。
An object of the present invention is to provide a method for producing an ultra-fine, highly foamed wire that can stably produce an ultra-fine, highly foamed wire having a core outer diameter of 0.3 mm or less over a long length.

【0009】[0009]

【課題を解決するための手段】上記の目的を達成するた
めの本発明の手段を説明すると、本発明は外径0.3 
mm以下の極細芯線の外周に押出機から発泡ふっ素樹脂
を押出し被覆して極細高発泡線を製造する極細高発泡線
の製造方法において、前記押出機のスクリュー回転数が
0.5rpm以上となるように、且つ前記押出機のホッ
パーに近い該押出機のシリンダの温度をふっ素樹脂の融
点以下に維持しつつ前記極細高発泡線の製造を行うこと
を特徴とする。
[Means for Solving the Problems] To explain the means of the present invention for achieving the above object, the present invention has an outer diameter of 0.3
In the method for producing an ultra-fine highly foamed wire, in which the outer periphery of an ultra-fine core wire of mm or less is coated with a foamed fluororesin by extrusion from an extruder to produce an ultra-fine, highly foamed wire, the screw rotation speed of the extruder is set to 0.5 rpm or more. Further, the ultrafine highly foamed wire is produced while maintaining the temperature of the cylinder of the extruder near the hopper of the extruder below the melting point of the fluororesin.

【0010】0010

【作用】このように、押出機のスクリュー回転数が0.
5rpm以上となるように、且つ該押出機のホッパーに
近い該押出機のシリンダの温度をふっ素樹脂の融点以下
に維持しつつ極細高発泡線の製造を行うと、スクリュー
を安定して回転させることができ、所期の発泡率,外径
を持ち、外観の良い極細高発泡線を長尺にわたって安定
して製造することができる。
[Operation] In this way, the screw rotation speed of the extruder is 0.
The screw can be rotated stably by manufacturing an ultra-fine, highly foamed wire at a speed of 5 rpm or more while maintaining the temperature of the extruder cylinder near the extruder hopper below the melting point of the fluororesin. This makes it possible to stably produce long lengths of ultra-fine, highly foamed wires that have the desired foaming rate, outer diameter, and good appearance.

【0011】[0011]

【実施例】図1(A)は本実施例で用いる押出機を示し
たものである。図において、1はシリンダ、2は該シリ
ンダ1内で回転するスクリュー、3はシリンダ1の基端
側でシリンダ1内にペレット状の押出し材料4を供給す
るホッパー、5はシリンダ1の先端に設けられているク
ロスヘッド、6はシリンダ1の外周に設けられているヒ
ータ、7a〜7dはシリンダ1の温度測定点、8はシリ
ンダ1に設けられている発泡剤注入口、9は発泡剤を収
容したタンク、10はタンク9から発泡剤を発泡剤注入
口8を経てシリンダ1内に注入する注入ポンプ,11は
ホッパー3に対応したシリンダ1を冷却している冷却ジ
ャケットである。
EXAMPLE FIG. 1(A) shows an extruder used in this example. In the figure, 1 is a cylinder, 2 is a screw that rotates within the cylinder 1, 3 is a hopper that supplies pellet-shaped extruded material 4 into the cylinder 1 on the base end side of the cylinder 1, and 5 is provided at the tip of the cylinder 1. 6 is a heater provided on the outer periphery of the cylinder 1, 7a to 7d are temperature measurement points of the cylinder 1, 8 is a foaming agent inlet provided in the cylinder 1, and 9 is a housing for storing the foaming agent. 10 is an injection pump for injecting the foaming agent from the tank 9 into the cylinder 1 through the foaming agent inlet 8, and 11 is a cooling jacket for cooling the cylinder 1 corresponding to the hopper 3.

【0012】図1(B)は図1(A)におけるシリンダ
1のフィードゾーン,コンプレッションゾーン,メータ
リングゾーンの温度分布を示したものである。
FIG. 1(B) shows the temperature distribution of the feed zone, compression zone, and metering zone of the cylinder 1 in FIG. 1(A).

【0013】本発明者は、芯線外径0.3mm 以下の
極細高発泡線の最適な製造条件を決定するため、被覆材
としてテトラフロロエチレン(融点300℃)を用いて
各線種に対して実験を行ったところ、表1に示す結果が
得られた。
[0013] In order to determine the optimal manufacturing conditions for ultrafine, highly foamed wires with a core wire outer diameter of 0.3 mm or less, the present inventor conducted experiments on each wire type using tetrafluoroethylene (melting point: 300°C) as a coating material. As a result, the results shown in Table 1 were obtained.

【0014】[0014]

【表1】[Table 1]

【0015】線種が90Ωの極細高発泡線については、
最初表1の条件で製造したが、その表面に凹凸が多く、
外観が悪いのでシリンダ内径25mmの押出機を用いて
試作したところ、良品が得られた。このとき、スクリュ
ー回転数は2rpm 、ホッパー3下近傍のヒータ6の
設定温度は290 ℃とした。
Regarding the ultra-fine highly foamed wire with a wire type of 90Ω,
Initially, it was manufactured under the conditions shown in Table 1, but the surface had many irregularities.
Since the appearance was poor, a prototype was produced using an extruder with a cylinder inner diameter of 25 mm, and a good product was obtained. At this time, the screw rotation speed was 2 rpm, and the set temperature of the heater 6 near the bottom of the hopper 3 was 290°C.

【0016】また、線種が65Ω×3.8ns/m (
1) ,65Ω×3.8ns/m (2) ,65Ω×
3.8ns/m (3)の極細高発泡線については、表
1の条件で製造を行ったところ、所期の発泡率,外径を
長尺にわたって安定して得ることができた。 更に、外観も良いものができた。
[0016] Furthermore, the line type is 65Ω×3.8ns/m (
1) ,65Ω×3.8ns/m (2) ,65Ω×
When the ultrafine highly foamed wire of 3.8 ns/m (3) was manufactured under the conditions shown in Table 1, the desired foaming rate and outer diameter could be stably obtained over a long length. Furthermore, we were able to create a product with a good appearance.

【0017】フィードゾーンにあるヒータ6の温度はふ
っ素樹脂の融点以下となるように加熱し、コンプレッシ
ョンゾーン(シリンダとスクリュー間の断面積比が急激
に圧縮する側に変わる点)でふっ素樹脂の融点以上とな
り、メータリングゾーンで340 ℃以上となるように
している。
The temperature of the heater 6 in the feed zone is heated to be below the melting point of the fluororesin, and in the compression zone (the point where the cross-sectional area ratio between the cylinder and the screw suddenly changes to the compression side), the melting point of the fluororesin is lowered. As a result, the temperature in the metering zone is 340°C or higher.

【0018】発泡剤の注入は、メータリングゾーンで行
なった。そのときの注入圧力は、40〜60kg/cm
2 である。
The blowing agent injection was carried out in the metering zone. The injection pressure at that time was 40 to 60 kg/cm.
It is 2.

【0019】線種が65Ω×3.8ns/m (3) 
の押出機として、シリンダ内径15mmの押出機を用い
た。ホッパーからは外径1.5mm 、長さ1.5mm
 以下の微細ペレットを供給した。この微細ペレット状
のテトラフロロエチレン剤としては、発泡核剤を混入し
た全練りペレットを用いた。スクリュー回転数は1.5
rpm、押出し量は2.2g/min として、被覆を
行なった。その結果、得られた極細高発泡線は、発泡率
73%、伝搬遅延時間3.8 ns/m ±0.12n
s/m を達成した。ダイスから出た直後の極細高発泡
線を直接水冷することによって、滑らかな外観を得た。 このとき、ホッパー近傍のヒータは280 ℃で温調し
た。
[0019] Line type is 65Ω×3.8ns/m (3)
An extruder with a cylinder inner diameter of 15 mm was used as the extruder. From the hopper, the outer diameter is 1.5 mm and the length is 1.5 mm.
The following fine pellets were supplied. As the tetrafluoroethylene agent in the form of fine pellets, fully kneaded pellets mixed with a foaming nucleating agent were used. Screw rotation speed is 1.5
Coating was performed at rpm and extrusion rate of 2.2 g/min. As a result, the obtained ultra-fine highly foamed wire had a foaming rate of 73% and a propagation delay time of 3.8 ns/m ±0.12n.
Achieved s/m. A smooth appearance was obtained by directly cooling the ultra-fine, highly foamed wire with water immediately after it came out of the die. At this time, the temperature of the heater near the hopper was controlled at 280°C.

【0020】[0020]

【発明の効果】以上説明したように、本発明に係る極細
高発泡線の製造方法では、押出機のスクリュー回転数が
0.5 rpm 以上となるように、且つ該押出機のホ
ッパーに近い該押出機のシリンダの温度をふっ素樹脂の
融点以下に維持しつつ極細高発泡線の製造を行うので、
スクリューを安定して回転させることができ、所期の発
泡率,外径を持ち、外観の良い極細高発泡線を長尺にわ
たって安定して製造することができる。
Effects of the Invention As explained above, in the method for producing ultra-fine highly foamed wire according to the present invention, the screw rotation speed of the extruder is set to 0.5 rpm or more, and the The temperature of the extruder cylinder is maintained below the melting point of the fluororesin while producing ultra-fine, highly foamed wire.
The screw can be rotated stably, and it is possible to stably produce long lengths of ultra-fine, highly foamed wires that have the desired expansion rate and outer diameter and have a good appearance.

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

【図1】(A)は本発明に係る極細高発泡線の製造方法
を実施する押出機の概略構成を示す縦断面図、(B)は
該押出機のシリンダの温度分布図である。
FIG. 1 (A) is a vertical cross-sectional view showing a schematic configuration of an extruder for carrying out the method for producing an ultra-fine, highly foamed wire according to the present invention, and (B) is a temperature distribution diagram of a cylinder of the extruder.

【符号の説明】[Explanation of symbols]

1…シリンダ、2…スクリュー、3…ホッパー、4…ペ
レット状押出し材料、5…クロスヘッド、6…ヒータ、
7a〜7d…シリンダ1の温度測定点、8…発泡剤注入
口、9…発泡剤収容タンク、10…注入ポンプ。
1... Cylinder, 2... Screw, 3... Hopper, 4... Pellet-shaped extrusion material, 5... Crosshead, 6... Heater,
7a to 7d... Temperature measuring point of cylinder 1, 8... Foaming agent inlet, 9... Foaming agent storage tank, 10... Injection pump.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  外径0.3 mm以下の極細芯線の外
周に押出機から発泡ふっ素樹脂を押出し被覆して極細高
発泡線を製造する極細高発泡線の製造方法において、前
記押出機のスクリュー回転数が0.5rpm以上となる
ように、且つ前記押出機のホッパーに近い該押出機のシ
リンダの温度をふっ素樹脂の融点以下に維持しつつ前記
極細高発泡線の製造を行うことを特徴とする極細高発泡
線の製造方法。
1. A method for manufacturing an ultra-fine high-foam wire, in which the outer periphery of an ultra-fine core wire with an outer diameter of 0.3 mm or less is extruded and coated with a foamed fluororesin from an extruder to produce an ultra-fine high-foam wire, wherein the screw of the extruder The ultra-fine highly foamed wire is manufactured while maintaining the rotation speed at 0.5 rpm or more and the temperature of the cylinder of the extruder near the hopper of the extruder to be below the melting point of the fluororesin. A method for manufacturing ultra-fine, highly foamed wire.
JP3085044A 1991-04-17 1991-04-17 Production method of ultra-fine high foam wire Expired - Fee Related JP3050627B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3085044A JP3050627B2 (en) 1991-04-17 1991-04-17 Production method of ultra-fine high foam wire

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3085044A JP3050627B2 (en) 1991-04-17 1991-04-17 Production method of ultra-fine high foam wire

Publications (2)

Publication Number Publication Date
JPH04319212A true JPH04319212A (en) 1992-11-10
JP3050627B2 JP3050627B2 (en) 2000-06-12

Family

ID=13847683

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3085044A Expired - Fee Related JP3050627B2 (en) 1991-04-17 1991-04-17 Production method of ultra-fine high foam wire

Country Status (1)

Country Link
JP (1) JP3050627B2 (en)

Also Published As

Publication number Publication date
JP3050627B2 (en) 2000-06-12

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