JPH0440379B2 - - Google Patents

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Publication number
JPH0440379B2
JPH0440379B2 JP57057031A JP5703182A JPH0440379B2 JP H0440379 B2 JPH0440379 B2 JP H0440379B2 JP 57057031 A JP57057031 A JP 57057031A JP 5703182 A JP5703182 A JP 5703182A JP H0440379 B2 JPH0440379 B2 JP H0440379B2
Authority
JP
Japan
Prior art keywords
parts
foaming
polyethylene
weight
azodicarbonamide
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
Application number
JP57057031A
Other languages
Japanese (ja)
Other versions
JPS58174423A (en
Inventor
Osamu Saito
Osamu Shimizu
Masahiro Kato
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.)
SWCC Corp
Original Assignee
Showa Electric Wire and Cable Co
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 Showa Electric Wire and Cable Co filed Critical Showa Electric Wire and Cable Co
Priority to JP5703182A priority Critical patent/JPS58174423A/en
Publication of JPS58174423A publication Critical patent/JPS58174423A/en
Publication of JPH0440379B2 publication Critical patent/JPH0440379B2/ja
Granted legal-status Critical Current

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Description

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

〔発明の技術分野〕 本発明は高発泡性のポリエチレン組成物に係わ
り、特に電気特性や押出成形後の形状安定性に優
れ、かつ導体変色等を起こさない、同軸ケーブル
の絶縁体として好適する、発泡率が65%以上のポ
リエチレン組成物に関する。 〔発明の技術的背景とその問題点〕 従来からテレビ共聴用システムでは、絶縁体と
して発泡プラスチツクを被覆した同軸ケーブルが
使用されているが、このような発泡同軸ケーブル
においては、近時漏洩減衰量をできるだけ小さく
しケーブルの接続距離を延ばすため、より高い発
泡率のものが要求されている。 このような要求に応えるため種々の研究がなさ
れ、その結果フツ素系の溶剤やガスを発泡剤とし
て用いた物理発泡法は、いわゆるガス発泡法によ
り、70%以上の発泡率の同軸ケーブルが製造され
ている。しかるにこの方法においては、高価なフ
ツ素系化合物が使用されるため材料コストが高く
なるばかりでなく、これらの発泡剤を高温高圧で
ベースプラスチツクと混合しなければならず、通
常の押出機以外にこのための付帯設備を必要とす
るという難点があつた。 これに対して化学発泡剤を用い通常の押出機に
より行なう化学発泡法の場合には、特別な付帯設
備を必要とせず製造コストの軽減がはかれるとい
う利点を有するが、ガス発泡法にみられる、溶存
ガスの蒸発気化の際うばわれる気化熱に起因する
プラスチツクの固化現象が期待できず、また多量
のガス(6重量部以上)をプラスチツク中に含有
させることが難しく、高い発泡率のものを製造す
ることが困難とされていた。 さらに化学発泡剤を多量に配合し高発泡ケーブ
ルを製造する方法も考えられているが、この場合
は発泡剤の分解残渣によりtanδの上昇などケーブ
ルの電気特性の低下がもたらされ、また導体変色
も見られるという問題があつた。 〔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、通常の押出機に供給することにより電
気特性に優れ高い発泡率(65%以上)のケーブル
絶縁体を製造することができる、高発泡性ポリエ
チレン組成物を提供することを目的とする。 〔発明の概要〕 低密度ポリエチレン(以下LDPEと略称する)
或いはLDPEと高密度ポリエチレン(以下HDPE
と略称する)との混合物であつて、メルトインデ
ツクス(以下M.Iと略称する)が1〜7のベース
ポリエチレン100重量部に対して、アゾジカルボ
ンアミド(以下ADCAと略称する)とp,p′−オ
キシビス(ベンゼンスルホニルヒドラジト)(以
下OBSHと略称する)とを、重量比で1:1〜
4:1の割合で混合してなる発泡剤1.0〜5.0重量
部と、アゾジカルボンアミドの配合量の10〜100
重量部%のアゾジカルボンアミドの分解を促進さ
せる発泡助剤とを配合して成ることを特徴とする
高発泡性ポリエチレン組成物に関する。 ここで本発明の組成物において、ベースポリエ
チレンのM.Iの値を1〜7の範囲に限定したのは
次の実験結果に基づくものである。 すなわち、M.Iが0.2から20までの種々の値を有
するLDPEに、その100部当りADCA1部、
OBSH0.5部および発泡助剤としてステアリン酸
亜鉛0.5部を配合して成る組成物を、公知の方法
で直径1.8mmの軟銅線上に押出被覆して自然発泡
させ、得られた発泡絶縁線心の発泡率測定および
断面形状の観察を行なつたところ、以下の第1表
に示す結果が得られた。
[Technical Field of the Invention] The present invention relates to a highly foamable polyethylene composition, which has excellent electrical properties and shape stability after extrusion molding, does not cause conductor discoloration, and is suitable as an insulator for coaxial cables. It relates to a polyethylene composition with a foaming rate of 65% or more. [Technical background of the invention and its problems] Conventionally, coaxial cables coated with foamed plastic as an insulator have been used in television public viewing systems. In order to minimize the volume and extend the cable connection distance, higher foaming ratios are required. In order to meet these demands, various studies have been conducted, and as a result, coaxial cables with a foaming rate of 70% or more have been manufactured using the so-called gas foaming method, which uses fluorine-based solvents and gases as foaming agents. has been done. However, this method not only increases material costs due to the use of expensive fluorine-based compounds, but also requires mixing these blowing agents with the base plastic at high temperature and pressure, which requires a machine other than an ordinary extruder. The problem was that additional equipment was required for this purpose. On the other hand, chemical foaming using a chemical foaming agent and using an ordinary extruder has the advantage of not requiring special incidental equipment and reducing production costs, but The solidification phenomenon of plastic due to the heat of vaporization that is released during evaporation of dissolved gas cannot be expected, and it is difficult to incorporate a large amount of gas (more than 6 parts by weight) into plastic, making it difficult to manufacture products with a high foaming rate. It was considered difficult to do so. Furthermore, a method of manufacturing highly foamed cables by blending a large amount of chemical foaming agents has been considered, but in this case, the decomposition residue of the foaming agents causes deterioration of the cable's electrical properties such as an increase in tanδ, and the discoloration of the conductors. There was a problem that I could also see it. [Purpose of the Invention] The present invention was made to solve these problems, and it is possible to manufacture a cable insulator with excellent electrical properties and a high foaming rate (65% or more) by feeding it into an ordinary extruder. The purpose of the present invention is to provide a highly foamable polyethylene composition that can be used. [Summary of the invention] Low density polyethylene (hereinafter abbreviated as LDPE)
Or LDPE and high density polyethylene (HDPE)
It is a mixture of azodicarbonamide (hereinafter referred to as ADCA) and p, p' based on 100 parts by weight of base polyethylene having a melt index (hereinafter referred to as MI) of 1 to 7. -oxybis(benzenesulfonyl hydrazide) (hereinafter abbreviated as OBSH) in a weight ratio of 1:1 to
1.0 to 5.0 parts by weight of a blowing agent mixed in a ratio of 4:1 and 10 to 100 parts by weight of azodicarbonamide
The present invention relates to a highly foamable polyethylene composition characterized in that it contains a foaming aid that promotes the decomposition of azodicarbonamide in an amount of % by weight. Here, in the composition of the present invention, the MI value of the base polyethylene was limited to a range of 1 to 7 based on the following experimental results. That is, 1 part ADCA per 100 parts of LDPE with various MI values from 0.2 to 20;
A composition consisting of 0.5 parts of OBSH and 0.5 parts of zinc stearate as a foaming aid is extruded and coated onto an annealed copper wire of 1.8 mm in diameter by a known method and allowed to foam naturally, resulting in a foamed insulated wire core. When the foaming rate was measured and the cross-sectional shape was observed, the results shown in Table 1 below were obtained.

【表】 この試験結果からも明らかなように、ベースポ
リエチレンのM.Iが小さすぎると発泡率を高くす
ることができず、反対にM.Iが大きすぎると断面
の真円形状を保つことができない。 従つてベースポリエチレンのM.Iは1〜7の範
囲とすることが必要であり、さらには2〜4の範
囲のものを用いるのがより好ましい。 本発明においては、化学発泡剤としてADCA
とOBSHとを併用するがこれらの発泡剤の配合
量は合計で上記ベースポリエチレン100部に対し
て1.0〜5.0部の範囲とする。 発泡剤の配合量をこのような範囲に限定したの
は以下の理由による。 すなわち高い発泡率のケーブルを得るためには
発泡剤の配合量を多くすることが必要であるが、
発泡剤の配合量が増すほどケーブルの誘電正接
(tanδ)などの電気特性が低下する傾向がある。 そこで発泡剤配合量を変えてその場合の発泡率
およびtanδを測定したところ、図面に示すグラフ
が得られた。 このグラフから高い発泡率が達成され、なおか
つ電気特性(tanδ)が良好な発泡剤配合量を求め
たところ、ベースポリエチレン100部に対して1.0
〜5.0部という最適範囲が得られた。 また本発明において発泡剤としてADCAと
OBSHとを混合して用い、その混合比を1:1
〜4:1の範囲にしたのは次に示す理由による。 すなわちADCAとOBSHはいずれも分解温度、
ガス発生量、分解速度分布等がポリエチレンの加
工条件とうまくマツチしており、取扱いが容易で
価格も安いためポリエチレンの発泡剤として広く
用いられているが、配合量を多くし高い発泡率の
同軸ケーブルを製造する場合には、ADCAの単
独使用では分解ガス中に含まれる多量のアンモニ
アの作用により、導体(銅)が加速度的に腐食
(黒変)してしまうという問題があり、OBSHを
単独で用いたときには、ケーブルの断面形状が扁
平化してしまい丸い仕上り形状のものが得られな
いという問題があつた。 従つてOBSHの分解中間生成物である酸性化
合物によりADCAの分解ガス中のアンモニアを
中和させ、なおかつ断面真円形状のケーブルを得
るためにADCAとOBSHの混合系発泡剤が必要
とされる。 またM.Iが1.0、密度0.92のベースポリエチレン
100部に対し種々の割合でADCAとOBSHを配合
し、直径1.8mmの軟銅線上に押出して得られたケ
ーブル(絶縁体外径73mm)の絶縁体外径長短の差
や発泡率等を測定したところ第2表に示す結果が
得られた。
[Table] As is clear from the test results, if the MI of the base polyethylene is too small, the foaming rate cannot be increased, and on the other hand, if the MI is too large, the cross-sectional shape cannot be maintained. Therefore, the MI of the base polyethylene must be in the range of 1 to 7, and more preferably in the range of 2 to 4. In the present invention, ADCA is used as a chemical blowing agent.
and OBSH are used in combination, and the total amount of these blowing agents is in the range of 1.0 to 5.0 parts based on 100 parts of the base polyethylene. The reason why the amount of the blowing agent is limited to this range is as follows. In other words, in order to obtain a cable with a high foaming rate, it is necessary to increase the amount of foaming agent blended.
As the amount of foaming agent added increases, the electrical properties of the cable, such as the dielectric loss tangent (tan δ), tend to decrease. Therefore, when the foaming rate and tan δ were measured by varying the amount of foaming agent mixed, the graph shown in the drawing was obtained. From this graph, we determined the amount of blowing agent that would achieve a high foaming rate and have good electrical properties (tanδ), and found that it was 1.0 parts per 100 parts of base polyethylene.
An optimal range of ~5.0 parts was obtained. In addition, in the present invention, ADCA is used as a blowing agent.
Use a mixture of OBSH and the mixing ratio of 1:1.
The reason for setting the ratio to 4:1 is as follows. In other words, both ADCA and OBSH have a decomposition temperature,
It is widely used as a foaming agent for polyethylene because its gas generation amount, decomposition rate distribution, etc. match well with the processing conditions of polyethylene, and it is easy to handle and inexpensive. When manufacturing cables, there is a problem that when using ADCA alone, the conductor (copper) corrodes (blackens) at an accelerated rate due to the action of a large amount of ammonia contained in the decomposed gas, so OBSH is not used alone. When used in , there was a problem that the cross-sectional shape of the cable became flattened, making it impossible to obtain a round finished shape. Therefore, a mixed blowing agent of ADCA and OBSH is required to neutralize ammonia in the ADCA decomposition gas with an acidic compound that is a decomposition intermediate product of OBSH, and to obtain a cable with a perfectly circular cross section. Base polyethylene with MI of 1.0 and density of 0.92
ADCA and OBSH were mixed in various proportions per 100 parts and extruded onto an annealed copper wire with a diameter of 1.8 mm. The difference in the outer diameter of the insulator and the foaming rate of the obtained cable (insulator outer diameter of 73 mm) were measured. The results shown in Table 2 were obtained.

〔発明の実施例〕[Embodiments of the invention]

次に本発明の実施例について記載する。 実施例 1、2 第3表に示す配合のポリエチレン組成物を90mm
φの押出機に供給し、直径1.8mmの軟銅線上に押
出被覆し自然発泡させて発泡絶縁線心を得た。 得られた絶縁線心の特性を同表下欄に示す。
Next, examples of the present invention will be described. Examples 1 and 2 A polyethylene composition having the composition shown in Table 3 was
The mixture was supplied to a φ extruder, extrusion coated onto annealed copper wire having a diameter of 1.8 mm, and allowed to foam naturally to obtain a foamed insulated wire core. The properties of the obtained insulated wire core are shown in the lower column of the same table.

〔発明の効果〕〔Effect of the invention〕

以上の説明から明らかなように、本発明の組成
物は、通常の押出機により導体上に押出被覆する
ことにより、発泡率が高く電気特性に優れた発泡
同軸ケーブルを得ることができる。 またこうして得られたケーブルは、内部の導体
の変色がなく断面形状も真円形で仕上り外観が良
好である。
As is clear from the above description, the composition of the present invention can be extruded and coated onto a conductor using an ordinary extruder to obtain a foamed coaxial cable with a high foaming rate and excellent electrical properties. In addition, the cable thus obtained has a perfectly circular cross-sectional shape without any discoloration of the internal conductor, and has a good finished appearance.

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

図面は、実験的に求められた発泡剤の配合量と
得られるケーブルの発泡率およびtanδの関係を示
すグラフである。
The drawing is a graph showing the relationship between the experimentally determined blending amount of the foaming agent and the foaming rate and tan δ of the resulting cable.

Claims (1)

【特許請求の範囲】 1 低密度ポリエチレン或いは低密度ポリエチレ
ンと高密度ポリエチレンとの混合物であつて、メ
ルトインデツクスが1〜7のベースポリエチレン
100重量部に対して、アゾジカルボンアミドとp,
p′−オキシビス(ベンゼンスルホニルヒドラジ
ド)とを、重量比で1:1〜4:1の割合で混合
してなる発泡剤1.0〜5.0重量部と、アゾジカルボ
ンアミドの配合量の10〜100重量部%のアゾジカ
ルボンアミドの分解を促進させる発泡助剤とを配
合して成ることを特徴とする高発泡性ポリエチレ
ン組成物。 2 発泡助剤がステアリン酸亜鉛であることを特
徴とする特許請求の範囲第1項記載の高発泡性ポ
リエチレン組成物。
[Scope of Claims] 1. A base polyethylene that is low density polyethylene or a mixture of low density polyethylene and high density polyethylene, and has a melt index of 1 to 7.
With respect to 100 parts by weight, azodicarbonamide and p,
1.0 to 5.0 parts by weight of a blowing agent made by mixing p'-oxybis(benzenesulfonyl hydrazide) in a weight ratio of 1:1 to 4:1 and 10 to 100 parts by weight of azodicarbonamide. % of azodicarbonamide. 2. The highly foamable polyethylene composition according to claim 1, wherein the foaming aid is zinc stearate.
JP5703182A 1982-04-06 1982-04-06 Highly expandable polyethylene composition Granted JPS58174423A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5703182A JPS58174423A (en) 1982-04-06 1982-04-06 Highly expandable polyethylene composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5703182A JPS58174423A (en) 1982-04-06 1982-04-06 Highly expandable polyethylene composition

Publications (2)

Publication Number Publication Date
JPS58174423A JPS58174423A (en) 1983-10-13
JPH0440379B2 true JPH0440379B2 (en) 1992-07-02

Family

ID=13044066

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5703182A Granted JPS58174423A (en) 1982-04-06 1982-04-06 Highly expandable polyethylene composition

Country Status (1)

Country Link
JP (1) JPS58174423A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63501698A (en) * 1980-01-20 1988-07-14 ヘルタ−,ハインツ Method for the separation of SO↓2− and NOx− from flue gas in a wet process in one or multiple steps, especially simultaneously
JPH02222425A (en) * 1989-02-25 1990-09-05 Ube Ind Ltd Expandable powdery resin composition
US5564623A (en) * 1993-06-11 1996-10-15 American Trading And Production Corporation Durable case formed from an expanded high-density polyethylene

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5821432A (en) * 1981-07-31 1983-02-08 Sumitomo Electric Ind Ltd Foam manufacturing method

Also Published As

Publication number Publication date
JPS58174423A (en) 1983-10-13

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