JPS59217906A - Method of producing high foamable plastic cable - Google Patents
Method of producing high foamable plastic cableInfo
- Publication number
- JPS59217906A JPS59217906A JP58091954A JP9195483A JPS59217906A JP S59217906 A JPS59217906 A JP S59217906A JP 58091954 A JP58091954 A JP 58091954A JP 9195483 A JP9195483 A JP 9195483A JP S59217906 A JPS59217906 A JP S59217906A
- Authority
- JP
- Japan
- Prior art keywords
- foaming
- insulating layer
- foamed
- producing high
- conductor
- 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
- 229920003023 plastic Polymers 0.000 title claims description 10
- 239000004033 plastic Substances 0.000 title claims description 10
- 238000000034 method Methods 0.000 title description 10
- 239000007788 liquid Substances 0.000 claims description 10
- 239000004020 conductor Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 238000009835 boiling Methods 0.000 claims description 6
- 239000004088 foaming agent Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000005187 foaming Methods 0.000 description 23
- -1 polyethylene Polymers 0.000 description 8
- 239000004604 Blowing Agent Substances 0.000 description 7
- 239000004698 Polyethylene Substances 0.000 description 7
- 238000009413 insulation Methods 0.000 description 7
- 229920000573 polyethylene Polymers 0.000 description 7
- 239000006260 foam Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 229920001684 low density polyethylene Polymers 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- 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 2
- 239000005977 Ethylene Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007765 extrusion coating Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- B29C47/92—
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[発明の技術分野]
本発明は低沸点液状発泡剤を使用したガス発泡法による
発泡率75%以上の高発泡プラスチックケーブルの製造
方法に関りる。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for producing a highly foamed plastic cable with a foaming rate of 75% or more by a gas foaming method using a low boiling point liquid foaming agent.
[発明の技術的RM!とその問題点]
近年、同軸ケーブル等においては、絶縁体の発泡率を高
くし、これによって誘電率やtanδの減少おにび漏洩
減衰■の低減を図ったいわゆる高発泡同軸ケーブルの開
発が進められている。 このJ:うな高発泡率の同軸ケ
ーブルコアを製造する方法として、従来からフレオン(
商品名)等の低沸点液状発泡剤を配合したプラチック組
成物を加圧下で押出機に供給して導体上に押出被覆し、
次いeこれを空気中で発泡させた後、冷7JJ固化1−
るガス発泡法が知られており、すでに発泡率60%以上
のものも得られている。[Technical RM of invention! In recent years, in coaxial cables, etc., the development of so-called highly foamed coaxial cables has been progressing, which aims to increase the foaming rate of the insulator, thereby reducing dielectric constant, tan δ, and leakage attenuation. It is being Freon (Freon) has traditionally been used as a method of manufacturing coaxial cable cores with high expansion ratio
A plastic composition containing a low boiling point liquid foaming agent such as (trade name) is fed to an extruder under pressure and extrusion coated onto a conductor.
Next, after foaming this in the air, it is cooled to 7JJ and solidified 1-
A gas foaming method is known, and foaming ratios of 60% or more have already been obtained.
しかしながら、ガス発泡法によって75%以上?3発泡
率の絶縁層を得ようとづると極め”(回動な問題が生じ
る。However, 75% or more by gas foaming method? If you try to obtain an insulating layer with a foaming rate of 3, the problem of rotation will occur.
すなわち、高発泡率を得る方法としく、(イ)導体温度
を上げる方法や、(ロ)発泡剤の配合Φを増加する方法
が一般に行われているが、(イ)の方法では、第1図に
示すように、導体1上にカス化した発泡剤が集まり易く
なり、連結し/、−大きなセル2を生成して、発泡絶縁
層3と導体1との密着が悪くなるという問題が生じる。In other words, methods for obtaining a high foaming rate are (a) increasing the conductor temperature and (b) increasing the foaming agent mixture Φ, but in method (a), the first As shown in the figure, the foaming agent that has become scum tends to collect on the conductor 1, connects, and forms large cells 2, causing a problem of poor adhesion between the foam insulation layer 3 and the conductor 1. .
この問題を解消するには、第2図に承りように、導体上
に例えばポリエチレン組成物からなる充実絶縁層4を設
ければよいが、それで6なお75%という高発泡率を得
ようとすると、充実絶縁層4の周囲に大きなセル2を生
じ、機械的強瓜や伸びが低下づるとい−う問題が生じる
。一方、(ロ)の発泡剤の配合■を11りづ方法におい
ても、高価な発泡剤を効率悪く使用Jることになって非
経済的であるばかりでなく、(イ〉と同様に75%以上
のa1発泡率では、発泡絶縁層3の中層に大きなセル2
を生成しく強度上問題となる。さらに方法(イ)おにび
(LJ)を組合けだ場合にも、第1図や第2図に示づよ
うな状態どなり、上記問題の解消にはならない。In order to solve this problem, as shown in Figure 2, it is possible to provide a solid insulating layer 4 made of, for example, a polyethylene composition on the conductor, but if you try to obtain a high foaming rate of 75% with that, , large cells 2 are formed around the solid insulating layer 4, resulting in a problem of reduced mechanical strength and elongation. On the other hand, even in the 11th method of formulating the blowing agent in (b), it is not only uneconomical because it uses an expensive blowing agent inefficiently, but also 75% With the above a1 foaming rate, the middle layer of the foamed insulation layer 3 has large cells 2.
This is a problem in terms of strength. Furthermore, even if method (a) is used in combination, the situation shown in FIGS. 1 and 2 will occur, and the above-mentioned problem will not be solved.
[発明の目的J
本発明はかかる従来の事情に対処してなされたもので、
ガス発泡法により電気特性に優れ、かつ機械的強度にも
問題のない発泡率75%以上の高発泡プラスチックケー
ブルを得ることのできる製造方法を提供しようと1」−
るものである。[Object of the Invention J The present invention has been made in response to such conventional circumstances,
We aim to provide a manufacturing method that uses gas foaming to produce highly foamed plastic cables with a foaming ratio of 75% or more that has excellent electrical properties and no mechanical strength problems.
It is something that
[発明の概要1
すなわら本発明の高発泡プラスチックケーブルの製造プ
ラ法は、導体外周に充実絶縁層を設【)、この充実絶縁
層の外周に低沸点液状発泡剤を溶解混合したブラヂツク
組成物を押出板Wノシ、これを5)0〜100℃の高温
雰囲気下で発泡さけることを特徴どしている。[Summary of the Invention 1] In other words, the plastic method for manufacturing a highly foamed plastic cable of the present invention is to provide a solid insulating layer around the outer periphery of the conductor. The product is made of an extruded plate W, which is characterized by 5) foaming in a high temperature atmosphere of 0 to 100°C.
本発明に使用するプラスブーツク組成物のI\−スボリ
マーとしては、ポリエチレン、ボリプ11ヒ゛レン、シ
リル変14ポリ土チレン等がdi+す、こねらは充実絶
縁層および発泡絶縁槽のいずれにし使用される。The I\-subolimer of the plastic tank composition used in the present invention includes polyethylene, polypropylene 11-ethylene, silyl-modified polyethylene 14-ethylene, etc. Ru.
J、た低沸点液状発泡剤どしでは、例えば低:J1点炭
化水素費液状のフレオン(商品名)弯公知の低?J1点
液状発泡剤を用いることかでさ、ごの発泡剤の配合量は
、使用するベースポリ7−い発泡剤の種類a3よび目的
とする発泡率ににつで異”fるが、一般にベースポリマ
ー100小崩部当たり15小吊部以下C充分Cある。Among low-boiling point liquid blowing agents, such as low boiling point liquid blowing agents, for example, low: J1 point hydrocarbon cost liquid Freon (trade name) is known as low-boiling point liquid blowing agent. J1 Point When using a liquid blowing agent, the amount of the blowing agent to be mixed depends on the type of foaming agent used and the desired foaming rate, but in general, There are 15 small hanging parts or less C per 100 small broken parts of the polymer.
本発明において押出し後の発泡雰囲′;A記麿を50〜
100℃の範囲としたのは、50℃未イ閃の温度では加
熱の効果がなく、100℃を越えると発泡体中のセルの
被膜が破れたり、表面に凹凸を生ずる等の不都合が生じ
好j、しくないためである。In the present invention, the foaming atmosphere after extrusion;
The range of 100°C was chosen because at a temperature of 50°C, there is no heating effect, and if the temperature exceeds 100°C, problems such as tearing of the cell coating in the foam and unevenness on the surface occur. j. It's because it's not good.
このような雰囲気温度を得るには、例えば押出ヘッド前
方の717通路上に赤外線を熱縁とする温度調節可能な
加熱筒を配置すればよい。In order to obtain such an ambient temperature, for example, a temperature-adjustable heating cylinder having an infrared ray as a heating edge may be disposed on the passage 717 in front of the extrusion head.
[発明の実施例J 次に本発明の実施例について記載する。[Embodiment J of the invention Next, examples of the present invention will be described.
実施例1
Ml3.O1密度0.924g/CI+’(7)低密度
ポリエチレンを第3図に示すように直径2.1鮨の導体
1上に厚さ0.2iIIとなるよう押出被覆して薄い充
実絶縁層4を形成し、次いでこのコア上に、押出機によ
り、上記の低密度ポリエチレンにこのポリエチレン10
0重量部あたり10重量部の液状のフレオン114(商
品名)を混合した組成物を押出し被覆し、これをコアの
発泡領域に配置された雰囲気温度70℃の加熱筒内に案
内して発泡絶縁層3を形成して、絶縁層外径8.0〜8
.2■の同軸ケーブルコアを製造した。Example 1 Ml3. O1 density 0.924g/CI+' (7) As shown in Fig. 3, a thin solid insulating layer 4 is formed by extrusion coating low-density polyethylene onto a conductor 1 having a diameter of 2.1mm to a thickness of 0.2iII. This polyethylene 10 is then added to the above low density polyethylene by an extruder onto this core.
A composition prepared by mixing 10 parts by weight of liquid Freon 114 (trade name) per 0 parts by weight is extruded and coated, and this is guided into a heating cylinder at an ambient temperature of 70°C placed in the foaming region of the core to form foam insulation. Forming layer 3, the outer diameter of the insulating layer is 8.0 to 8.
.. Two coaxial cable cores were manufactured.
次いで得られた同軸ケーブルコアの静電容量を、発泡絶
縁層の外周にアルミ箔を巻回して測定し、さらに発泡絶
縁層の圧縮強さおよび伸び率を測定した。Next, the capacitance of the obtained coaxial cable core was measured by wrapping aluminum foil around the outer periphery of the foamed insulating layer, and the compressive strength and elongation of the foamed insulating layer were also measured.
この同軸ケーブルコアの静電容量は/l 9 +) F
/mであり、セル2は外周部まC゛均一形成びれCい
た。The capacitance of this coaxial cable core is /l 9 +) F
/m, and cell 2 had uniformly formed fins C around the outer periphery.
ここで比較のために、上記実施例の静電容771 /1
9PF/mの±2PF/mを目標に以下の比較例1およ
び2により同軸チーブルニ17を製jもした。Here, for comparison, the capacitance of the above example is 771/1
A coaxial chip 17 was also manufactured according to Comparative Examples 1 and 2 below, aiming at ±2PF/m of 9PF/m.
比較例1
実施例と同じ低密度ポリエチレンに液状フレオン114
を上記ポリエチレン100壬fQ部に3=J L30重
量部となるように混合した組成物を使用し、発泡雰囲気
温度を空温として、実施例1ど11i1拝にして同軸ケ
ーブルコアを製造した。Comparative Example 1 Liquid Freon 114 was added to the same low density polyethylene as in the example.
A coaxial cable core was produced in the same manner as in Example 1, using a composition obtained by mixing 3=JL30 parts by weight with 100 parts of the above polyethylene, and setting the foaming atmosphere temperature to air temperature.
比較例2
発泡雰囲気温度を空温とした以外は実施例1と同様にし
て同軸ケーブルコアを製造した。Comparative Example 2 A coaxial cable core was manufactured in the same manner as in Example 1 except that the temperature of the foaming atmosphere was set to air temperature.
以上の実施例および各比較例のIiJ軸ケーブル−,1
アの特性の測定結果を次表に示す。Ii J axis cable of the above examples and each comparative example -, 1
The measurement results of the characteristics of a are shown in the table below.
*発泡率は畜瓜法りなわら次式により算出した。*The foaming rate was calculated using the following formula.
発泡率−1−発泡体の密度/充実ポリ1チレンの密度(
−0,920>
**圧縮強さは円柱状の試験片く発泡ポリエチレン絶縁
コアを所定長さに切断したもの)を径方向に圧縮し、発
泡絶縁層が2顛圧縮された時の組線荷重で表わした。Foaming ratio - 1 - Density of foam / Density of solid polyethylene (
-0,920> **Compressive strength is measured by compressing a cylindrical test piece (made by cutting a foamed polyethylene insulation core into a predetermined length) in the radial direction, and compressing the foamed insulation layer twice. Expressed as load.
「発明の効果」
以上の実施例からも明らかなように、本発明方法によれ
ば絶縁層の発泡を高い雰囲気温度のもとて行なわせるの
で絶縁層外周部にも均一にセルが形成され、電気特性の
みならず機械的特性にも優れた高い発泡率のプラスチッ
クケーブルを製造することがCきる。"Effects of the Invention" As is clear from the above examples, according to the method of the present invention, the foaming of the insulating layer is carried out at a high ambient temperature, so that cells are uniformly formed on the outer periphery of the insulating layer. It is possible to manufacture a plastic cable with a high foaming rate that has excellent not only electrical properties but also mechanical properties.
第1図は従来法による発泡同軸クープルXjアの横断面
図、第2図は他の従来の方法にJ、る発泡同軸ケーブル
コアの横断面図、第3図は本発明の一実施例により形成
された同軸ケージルー」アの横断面図である。
1・・・・・・・・・・・・導体
2・・・・・・・・・・・・セ ル
3・・・・・・・・・・・・発泡絶縁層4・・・・・・
・・・・・・充実絶縁層代理人弁理士 須 山 仏
−
(ほか1名)FIG. 1 is a cross-sectional view of a foamed coaxial cable core made by a conventional method, FIG. 2 is a cross-sectional view of a foamed coaxial cable core made by another conventional method, and FIG. 3 is a cross-sectional view of a foamed coaxial cable core made by another conventional method. FIG. 3 is a cross-sectional view of the formed coaxial cage luer. 1......Conductor 2...Cell 3...Foam insulation layer 4...・・・
...Full Insulation Layer Patent Attorney Suyama Buddha - (1 other person)
Claims (1)
外周に低沸点液状発泡剤を溶解混合したブラチック相成
物を押出被覆し、これを50〜100℃の^4雰囲気下
C発泡させることを特徴とづる高発泡プラスチックケー
ブルの製造り法。(1) A solid insulating layer is provided on the outer periphery of the conductor, and a plastic phase composition in which a low boiling point liquid foaming agent is dissolved and mixed is extruded and coated on the outer periphery of the solid insulating layer, and this is C-foamed in a ^4 atmosphere at 50 to 100°C. A manufacturing method for highly foamed plastic cables that is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58091954A JPS59217906A (en) | 1983-05-25 | 1983-05-25 | Method of producing high foamable plastic cable |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58091954A JPS59217906A (en) | 1983-05-25 | 1983-05-25 | Method of producing high foamable plastic cable |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59217906A true JPS59217906A (en) | 1984-12-08 |
Family
ID=14040967
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58091954A Pending JPS59217906A (en) | 1983-05-25 | 1983-05-25 | Method of producing high foamable plastic cable |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59217906A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04229903A (en) * | 1990-12-27 | 1992-08-19 | Nippon Unicar Co Ltd | High foam polyethylene insulation cable and manufacture thereof |
-
1983
- 1983-05-25 JP JP58091954A patent/JPS59217906A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04229903A (en) * | 1990-12-27 | 1992-08-19 | Nippon Unicar Co Ltd | High foam polyethylene insulation cable and manufacture thereof |
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