JPH03102706A - Manufacture of high-forming polyolefin small-diameter wire - Google Patents
Manufacture of high-forming polyolefin small-diameter wireInfo
- Publication number
- JPH03102706A JPH03102706A JP24146189A JP24146189A JPH03102706A JP H03102706 A JPH03102706 A JP H03102706A JP 24146189 A JP24146189 A JP 24146189A JP 24146189 A JP24146189 A JP 24146189A JP H03102706 A JPH03102706 A JP H03102706A
- Authority
- JP
- Japan
- Prior art keywords
- foaming
- conductor
- agent
- surface active
- active agent
- 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.)
- Pending
Links
- 229920000098 polyolefin Polymers 0.000 title claims description 8
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 238000005187 foaming Methods 0.000 claims abstract description 18
- 239000004020 conductor Substances 0.000 claims abstract description 12
- 239000004094 surface-active agent Substances 0.000 claims abstract description 11
- 239000004088 foaming agent Substances 0.000 claims abstract description 5
- 239000011347 resin Substances 0.000 claims abstract description 5
- 229920005989 resin Polymers 0.000 claims abstract description 5
- 238000001125 extrusion Methods 0.000 claims description 10
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 239000002667 nucleating agent Substances 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims 1
- 239000012212 insulator Substances 0.000 abstract description 8
- 239000006260 foam Substances 0.000 abstract description 6
- 238000007906 compression Methods 0.000 abstract description 5
- 230000006835 compression Effects 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract 3
- 238000010276 construction Methods 0.000 abstract 1
- 230000005540 biological transmission Effects 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- DDMOUSALMHHKOS-UHFFFAOYSA-N 1,2-dichloro-1,1,2,2-tetrafluoroethane Chemical compound FC(F)(Cl)C(F)(F)Cl DDMOUSALMHHKOS-UHFFFAOYSA-N 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000000689 upper leg Anatomy 0.000 description 1
Landscapes
- Organic Insulating Materials (AREA)
- Processes Specially Adapted For Manufacturing Cables (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野」
本発明は、例えば発泡絶縁体の外径が1.0fi以下と
いった極めて細径な発泡絶縁電線の発泡倍率を3倍以上
の高発泡状態に押出形成し、特にその際の機械的耐圧縮
強度を従来例に比較して大巾に向上させることのできる
高発泡ポリオレフィン細径電線の製造方法に関するもの
である.[従来の技術1
高周波伝送用ゲーブルやコンピューターのような精密電
子m器用ゲープルなどにおいては、絶縁体を低誘電率化
し伝送信号の高速化を図りあるいは誘電体損を低減させ
る目的で発泡化させており、最近は発泡倍率3倍以上の
高発泡化が実現されている.
このような絶縁体の高発泡化は、例えばCATV用同軸
ケーブルのように比較的線径の大きい場合には、ほぼ確
立されている従来技術によって比較的容易に形成させる
ことができる.近年、通信機器類や精、密電子機器類は
小型化あるいは高密度実装化の傾向が著しく、その要請
に対応するために、ケーブル線心もまずます細径化され
る傾向にあり、外径がl.oam以下といった細径高発
泡絶縁電線も使用されるようになった.[発明が解決し
ようとする課題1
電線の細径化はとりもなおさず発泡絶縁休の薄肉化と同
義であり、このような薄肉絶縁体を発泡倍率3倍以上(
発泡度67%以上)といった高発泡層に形成しようとす
る場合、上記従来技術においては考えられなかった様々
なa問に遭遇することになった.
例示すれば、絶縁体が薄肉化するに伴い高発泡化が困難
となること、細径化し絶縁体が薄肉化されると、線速を
上げ生産性を確保しようとした場合に被膜切れが生ずる
こと、などが主要な問題点であり、発明者らはこれらの
難問解決に鋭意取組み、その解決方法を見出し、先にそ
の詳細について提案を行なった。(特願平1−1041
92)しかし、上記提案において尚残されている課題と
して、発泡絶縁体の耐圧縮強度を向上させるという問題
がある.
発泡押出によって高線速で′!MRされた発泡度70%
以上の高発泡ポリオレフィン細径電線は、一般に機械的
強度が弱いという共通した欠点をイfしている.これに
は材質的要因と気泡構造的要因およびコア梢遺的要因が
原因していると考えられる.
これらの中で、高線速による発泡押出という製遣方式に
共通する本質的要因として気泡楕造の特異性を挙げるこ
とができる。Detailed Description of the Invention [Industrial Field of Application] The present invention is directed to a highly foamed state in which the foamed insulated wire has an extremely small diameter, for example, the outer diameter of the foamed insulator is 1.0 fi or less, and the foaming ratio is 3 times or more. The present invention relates to a method for producing a small-diameter highly foamed polyolefin electric wire that can be formed by extrusion, and in particular, the mechanical compressive strength at that time can be greatly improved compared to conventional examples. [Conventional technology 1] In cables for high-frequency transmission and cables for precision electronic devices such as computers, insulators are foamed to lower the dielectric constant, increase the speed of transmission signals, or reduce dielectric loss. Recently, high foaming ratios of more than 3 times have been achieved. Such highly foamed insulators can be formed relatively easily using almost established conventional techniques when the wire diameter is relatively large, such as for example in coaxial cables for CATV. In recent years, there has been a remarkable trend toward miniaturization and high-density packaging of communication equipment and precision electronic equipment. is l. Small diameter highly foamed insulated wires with a diameter of less than OAM have also come into use. [Problem to be solved by the invention 1 Reducing the diameter of electric wires is synonymous with reducing the thickness of foamed insulation, and such thin insulators are made with a foaming ratio of 3 times or more (
When trying to form a highly foamed layer (with a foaming degree of 67% or more), various problems that could not be considered with the above-mentioned conventional techniques were encountered. For example, as the insulator becomes thinner, it becomes difficult to achieve high foaming, and when the diameter of the insulator becomes thinner, coating breakage occurs when trying to increase the line speed and ensure productivity. These are the main problems, and the inventors have worked hard to solve these difficult problems, found a solution, and first proposed the details. (Patent application Hei 1-1041
92) However, an issue that remains unsolved in the above proposal is the problem of improving the compressive strength of the foamed insulator. ′′ at high linear speed by foam extrusion! MR foaming degree 70%
The above-mentioned highly foamed polyolefin small-diameter electric wires generally have a common drawback of low mechanical strength. This is thought to be caused by material factors, bubble structure factors, and core root remains factors. Among these, the uniqueness of cell elliptical structure can be mentioned as an essential factor common to the manufacturing method of foam extrusion using high linear speed.
.すなわち、高い線速で製造すれば、発泡剤ガスを溶解
したポリマメルトがダイス部に於で高い剪断を受けるこ
とになり、流れの方向に対して垂直な断面に於ける流れ
の放物線状の速度分布が生じ、流れの方向に長く伸びた
気泡を成長させる結果となる.この特異な気泡構造は、
コアの導体方向に対して垂直な方向からの圧縮強度を低
下させる大きな原因となるものである.
本発明の目的は、従来技術に本質的に内在する上記の欠
点を解消し、導体方向に対して垂直な方向の耐圧縮性を
大巾に向上させることができる新規な高発泡ポリオレフ
ィン細径電線の製造方法を提供しようとするものである
.
[課題を解決するための手段]
本発明は、細径の導体に高発泡ポリオレフィン絶縁体層
を押出法により成形被覆する場合において、ベースレジ
ンと発泡核剤及び発泡剤からなる系に対して界面活性剤
を0.01〜2 phr配合することを要旨とするもの
である.
ここにいう界面活性剤には、水溶液φで電離して生ずる
イオンの種類により陽イオン界面活性剤(陽イオン系)
、陰イオン界面活性剤(陰イオン系)およびそのように
電離しない非イオン界面活性/fl (ノニオン系)の
3種類があるが、本発明に適用するに当ってはそのいず
れを選択使用してもモ支えはない.
第4級アンモニウム塩のように電気特性を低下させる可
能性のあるものもあるが、本発明の配合量の範囲では実
際に問題となる場合は少ない.しかして、界面活性剤の
配合量を0。01〜2 phrの範囲とするのは、0。.. In other words, if manufactured at a high linear velocity, the polymer melt in which the blowing agent gas is dissolved will be subjected to high shear at the die section, resulting in a parabolic velocity distribution of the flow in the cross section perpendicular to the flow direction. This results in the growth of bubbles that are elongated in the direction of flow. This unique bubble structure is
This is a major cause of decreasing the compressive strength in the direction perpendicular to the conductor direction of the core. The object of the present invention is to provide a novel highly foamed polyolefin small-diameter electric wire that can eliminate the above-mentioned drawbacks essentially inherent in the prior art and can greatly improve the compression resistance in the direction perpendicular to the conductor direction. The aim is to provide a manufacturing method for . [Means for Solving the Problems] The present invention provides an interface to a system consisting of a base resin, a foaming nucleating agent, and a foaming agent when forming and coating a thin conductor with a highly foamed polyolefin insulating layer by an extrusion method. The gist is to incorporate 0.01 to 2 phr of an active agent. The surfactants mentioned here include cationic surfactants (cationic) depending on the type of ions generated by ionization in aqueous solution φ.
There are three types of surfactants: anionic surfactants (anionic) and nonionic surfactants/fl (nonionic), which do not ionize, and which of them should be selected for use in the present invention. There is no thigh support. There are some substances, such as quaternary ammonium salts, that may deteriorate electrical properties, but within the range of the amount used in the present invention, there are few cases in which this actually becomes a problem. Therefore, setting the amount of surfactant to be in the range of 0.01 to 2 phr is zero.
o t phrより少ないと気泡構造に影皆を及ぼす効
果が少なく、また2 phrを越えるようになると発泡
押出が具合よく行なわれなくなり、好ましくないためで
ある.[作用]
上記配合範囲において界面活性剤を添加し発泡押出を行
なうと、高線速によってダイスと樽体の間隙に生じてい
るけわしいIJI断速度場での気泡と気泡の接合を当該
界而活性剤が防止し、流れの方向への気泡成長を抑制し
て、樽体の゛長手方向に対し重直方向への気泡の成長が
促進され、それによって発泡絶縁体層の導体に対し垂直
方向における耐圧縮強度が大巾に向上される.
[実施例]
以下に、本発明について実施例を参照し説明する.
実施例
発泡押出用40m+押出111(L/D=29)のシリ
ンダの中央部に注入用ノズルを設評し、これを通じて発
泡剤として液体フロン(フロンl14)を定量ポンプに
よって加圧注入し、フロンガスが溶解したポリマメルト
を、クロスヘッド部で、走行する導体上に押出披覆して
、高発泡ポリオレフィン細径電線を試作した。This is because if it is less than ot phr, there will be little effect on the cell structure, and if it exceeds 2 phr, foam extrusion will not be carried out properly, which is not preferable. [Function] When a surfactant is added in the above formulation range and foaming extrusion is performed, the bonding between the bubbles in the severe IJI breaking velocity field that occurs in the gap between the die and the barrel due to high linear velocity is activated. The agent prevents and suppresses bubble growth in the direction of flow, promoting bubble growth in the direction perpendicular to the longitudinal direction of the barrel, thereby increasing the Compressive strength is greatly improved. [Examples] The present invention will be described below with reference to Examples. Example: An injection nozzle was installed in the center of a cylinder of 40 m + extrusion 111 (L/D = 29) for foam extrusion, and through this, liquid fluorocarbon (Freon 114) was injected under pressure as a foaming agent using a metering pump, and the fluorocarbon gas The melted polymer melt was extruded onto a running conductor using a crosshead section to fabricate a highly foamed polyolefin small-diameter electric wire.
押出温度は約200℃、ヘッド部はダイスをボリマの融
点近く迄下げるため、シリンダ部からa′tかな温度勾
配をもたせた。高発泡細径化はダイス温度を低下させ高
発泡化か生じて膨張したメルトドロ一部を線速でコント
ロールして細径化した。The extrusion temperature was about 200°C, and the head part had a temperature gradient of about a't from the cylinder part in order to lower the die to near the melting point of the bolymer. To achieve high foaming and reducing the diameter, the die temperature was lowered and a part of the melt dross that expanded due to high foaming was controlled by the line speed to reduce the diameter.
線速は約50m/II!nであった.
ベースレジンとしてショウレックスC4309(密度0
.944g/cs3.MI 0.9g/10iin;
昭和電工製品)、核剤として粉末シリカ0.51)hr
、本発明において添加する界面活性剤として、非イオン
系のアルキルフェノール型のノニオンHS(日本油脂製
品)をO,0.01,0.05,0.1.0.5,1.
0,2.0,3.Ophr各々配合したコンパウンドを
調整し、細粒化して供試材とした.
このコンパウンドを用いて前記の押出機により、導体径
0.18−の導体,Lに発泡押出して、コア径0.8m
、発泡度約80%の高発泡細径電線を得た.
このコア試料について、コアの耐潰れ性、つまり導体方
向に対して乗直な耐圧縮性を調べた.試験機としては、
a厚計を改良して、上部に荷重を載せられるようにした
ものを用い、荷重tooarの時の変形率および荷重を
取去った後30分経過した時の永久変形率を室温で測定
した.結果を第1表に示した.
第1表より明らかなように、界面活性剤を添加しないN
0.1は、荷重変形量および永久変形量ともに大きな値
を示しているが、界面活性剤0.ON+hrの添加(N
o.2>により、その変形量には顕著な改首が認められ
、以下2 phrの添加(No.7)まで、その圧縮変
形の改首効果は著しい
NO,8ずなわち3.Ollhr添加した試料では圧縮
変形量は一層小さくなっているが、遅延時間が4.2n
s/mと大r1Jに増大しており、発泡度においても十
分な発泡が行なわれていないことがわかる.
IIII杼化した場合に困難性の大きい高発泡化を実現
させることの本来の理由は、それによって遅延時間の短
縮化を図り、送信信号の高速化(Tdが3.8nS/m
以下)を達成しようとすることにある.従って、このよ
うな遅延時間の増大を考慮するとき、界面活性剤の添加
量の上限は2 phr程度のところにあるということが
できる.
[発明の効果1Linear speed is approximately 50m/II! It was n. Shorex C4309 (density 0) as base resin
.. 944g/cs3. MI 0.9g/10iin;
Showa Denko products), powdered silica as a nucleating agent 0.51) hr
As a surfactant to be added in the present invention, nonionic alkylphenol type nonionic HS (NOF products) was used at O, 0.01, 0.05, 0.1, 0.5, 1.
0, 2.0, 3. The compound containing each Ophr was adjusted and finely granulated to prepare a test material. This compound was foamed and extruded into a conductor L with a conductor diameter of 0.18 mm using the extruder described above, and the core diameter was 0.8 m.
A highly foamed small diameter electric wire with a degree of foaming of approximately 80% was obtained. For this core sample, we investigated the core's crushing resistance, that is, its compression resistance perpendicular to the conductor direction. As a test machine,
Using a modified A-thickness gauge so that a load could be placed on the top, the deformation rate when the load was tooar and the permanent deformation rate 30 minutes after the load was removed were measured at room temperature. The results are shown in Table 1. As is clear from Table 1, N
0.1 shows large values for both the amount of deformation under load and the amount of permanent deformation. Addition of ON+hr (N
o. 2>, a remarkable change in the amount of deformation was observed, and from then on up to the addition of 2 phr (No. 7), the effect of compression deformation was remarkable as NO, 8, that is, 3. In the sample with Ollhr added, the amount of compressive deformation is even smaller, but the delay time is 4.2n.
s/m and increased to a large r1J, indicating that sufficient foaming was not performed in terms of foaming degree. The original reason for achieving high foaming, which is extremely difficult when using a III-type shuttle, is to shorten the delay time and increase the speed of the transmission signal (Td is 3.8 nS/m).
(below). Therefore, when considering this increase in delay time, it can be said that the upper limit of the amount of surfactant added is about 2 phr. [Effects of the invention 1
Claims (1)
押出法により成形被覆する場合において、ベースレジン
と発泡核剤及び発泡剤からなる系に対して界面活性剤を
0.01〜2phr配合する高発泡ポリオレフィン細径
電線の製造方法。(1) When molding and coating a small-diameter conductor with a highly foamed polyolefin insulating layer by extrusion, 0.01 to 2 phr of a surfactant is added to the system consisting of the base resin, foaming nucleating agent, and foaming agent. A method for producing a highly foamed polyolefin small diameter electric wire.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24146189A JPH03102706A (en) | 1989-09-18 | 1989-09-18 | Manufacture of high-forming polyolefin small-diameter wire |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24146189A JPH03102706A (en) | 1989-09-18 | 1989-09-18 | Manufacture of high-forming polyolefin small-diameter wire |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03102706A true JPH03102706A (en) | 1991-04-30 |
Family
ID=17074664
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24146189A Pending JPH03102706A (en) | 1989-09-18 | 1989-09-18 | Manufacture of high-forming polyolefin small-diameter wire |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03102706A (en) |
-
1989
- 1989-09-18 JP JP24146189A patent/JPH03102706A/en active Pending
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