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JP4304183B2 - Foamed coaxial cable - Google Patents
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JP4304183B2 - Foamed coaxial cable - Google Patents

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JP4304183B2
JP4304183B2 JP2005356115A JP2005356115A JP4304183B2 JP 4304183 B2 JP4304183 B2 JP 4304183B2 JP 2005356115 A JP2005356115 A JP 2005356115A JP 2005356115 A JP2005356115 A JP 2005356115A JP 4304183 B2 JP4304183 B2 JP 4304183B2
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foamed
foaming
coaxial cable
mixture
ethylene
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亮 渡部
知久 渡邉
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Fujikura Ltd
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Description

本発明は、高発泡度の発泡絶縁体層を有する発泡同軸ケーブルに関するものである。   The present invention relates to a foamed coaxial cable having a foamed insulating layer having a high foaming degree.

高周波用の発泡同軸ケーブルは、銅等からなる内部導体とその上に設けられる発泡絶縁体層と、その外周に設けられる外部導体等から構成される。そして最近は、使用周波数域がGHz帯域においても減衰量が小さい発泡同軸ケーブルが要求されるため、絶縁体層の高発泡度化が望まれている。例えば特許文献1では、セルが微細かつ均一な高発泡度で、良好な外観を有する同軸ケーブルを得るために、熱溶融押出し可能なポリオレフィン系樹脂と成核剤としてフッ素系樹脂粉末とを含有する組成物を、発泡剤の存在下に発泡押出し成型する同軸ケーブルが記載されている。しかしながら成核剤の改良のみでは、高発泡度化させると発泡絶縁体層に巨大空泡が形成され、高い発泡度の発泡絶縁体層を安定して確実に形成するのは困難であった。また特許文献2には、誘電正接(tanδ)等の絶縁特性や発泡成型性に優れた、同軸ケーブルの絶縁層の形成などに好適な発泡成型用のポリマー組成物が開示されている。すなわち、ポリマー組成物のベースレジンとして、エチレン成分を0.5〜20重量%含有するプロピレン・エチレン共重合体を用いることによって、前記の特性が得られるとしている。しかしながらこのようなポリマー組成物を用いても、安定して確実に高発泡度化させることは困難であった。これは前記ポリマー組成物が、破断時の溶融張力と溶融時の伸長性のバランスが十分ではないために、発泡時にセル壁の破れが生じるため、また発泡セルが十分成長しないためと思われる。さらに特許文献3には、溶融成型におけるポリプロピレンの伸びの低下問題を解決するために、ポリプロピレンとポリプロピレン/ポリエチレンのブロックコポリマーとポリプロピレン/エチレン・プロピレンゴムのブロックコポリマーとのいずれかの材料と、この材料よりもメルトインデックスが大きくかつ10g/10分以下の高密度ポリエチレンとの混合物の発泡体からなる絶縁被覆を有する発泡絶縁電線が記載されている。しかしながら、前記の混合物を用いても破断時の溶融張力または溶融時の伸長性が十分でないために、安定して確実に高発泡度の発泡絶縁電線を得るには十分とは言えなかった。
特許第3227091号公報 特許第2668174号公報 特許第2618464号公報
A high-frequency foamed coaxial cable is composed of an inner conductor made of copper or the like, a foamed insulator layer provided on the inner conductor, and an outer conductor provided on the outer periphery thereof. Recently, a foamed coaxial cable having a small attenuation is required even in the use frequency range of GHz, and therefore, it is desired to increase the degree of foaming of the insulating layer. For example, in Patent Document 1, in order to obtain a coaxial cable having a fine and uniform high foaming degree and a good appearance, a polyolefin resin that can be hot melt extruded and a fluorine resin powder as a nucleating agent are contained. A coaxial cable is described in which the composition is foam extruded in the presence of a blowing agent. However, only by improving the nucleating agent, when the degree of foaming is increased, huge air bubbles are formed in the foamed insulator layer, and it is difficult to stably and reliably form a foamed insulator layer having a high foaming degree. Patent Document 2 discloses a polymer composition for foam molding that is excellent in insulation characteristics such as dielectric loss tangent (tan δ) and foam moldability and suitable for forming an insulating layer of a coaxial cable. That is, as the base resin of the polymer composition, the above characteristics can be obtained by using a propylene / ethylene copolymer containing 0.5 to 20% by weight of an ethylene component. However, even when such a polymer composition is used, it has been difficult to stably and reliably increase the degree of foaming. This is presumably because the polymer composition does not have a sufficient balance between the melt tension at break and the extensibility at melt, so that the cell wall is broken at the time of foaming, and the foamed cells do not grow sufficiently. Further, in Patent Document 3, in order to solve the problem of decrease in the elongation of polypropylene in melt molding, any material of polypropylene, a block copolymer of polypropylene / polyethylene, and a block copolymer of polypropylene / ethylene / propylene rubber, and this material A foam insulated wire having an insulation coating made of a foam of a mixture with a high density polyethylene having a higher melt index and 10 g / 10 min or less is described. However, even if the above mixture is used, the melt tension at break or the extensibility at the time of melting is not sufficient, and it cannot be said that it is sufficient to obtain a foamed insulated wire having a high degree of foaming stably and reliably.
Japanese Patent No. 3227091 Japanese Patent No. 2668174 Japanese Patent No. 2618464

よって本発明が解決しようとする課題は、発泡度が80%以上の発泡絶縁体層が安定して確実に形成され、高周波帯域(1MHz以上)での減衰量が少ない発泡同軸ケーブルを提供することにある。また、前記特性に加えて、低温曲げ特性、耐衝撃性や曲げ白化等の特性を向上させた発泡同軸ケーブルを提供することにある。   Therefore, the problem to be solved by the present invention is to provide a foamed coaxial cable in which a foamed insulation layer having a foaming degree of 80% or more is stably and reliably formed and has a low attenuation in a high frequency band (1 MHz or more). It is in. Another object of the present invention is to provide a foamed coaxial cable having improved properties such as low-temperature bending properties, impact resistance and bending whitening in addition to the above properties.

前記解決しようとする課題は、請求項1に記載されるように、エチレン・プロピレン共重合体を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記エチレン・プロピレン共重合体は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜10.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブルとすることによって、解決される。 The problem to be solved is a foamed coaxial cable in which a foamed insulation layer obtained by foaming an ethylene / propylene copolymer is provided on an inner conductor as defined in claim 1, wherein the ethylene・ Propylene copolymer was measured with a capillary rheometer at 190 ° C using a Φ2.095 mm × 8.03 mm capillary with a piston speed of 10 mm / min, furnace body diameter of 9.55 mm, take-up acceleration of 400 m / min 2 The melt tension at break is 5.0 to 10.0 g, the melt mass flow rate at 190 ° C. and 2.16 kg is 1.0 g / 10 min or more, and the foamed insulating layer has a foaming degree of 80%. This is solved by using a foamed coaxial cable characterized by the above.

また、請求項2に記載されるように、エチレン・プロピレン共重合体とポリエチレンとの混合物を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記混合物は、当該混合物におけるエチレン・プロピレン共重合体の含有量が20質量%以上、100質量%未満であり、前記混合物は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜12.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブルとすることによって、解決される Moreover, as described in claim 2, a foamed coaxial cable in which a foamed insulator layer obtained by foaming a mixture of an ethylene / propylene copolymer and polyethylene is provided on an inner conductor, wherein the mixture is The ethylene / propylene copolymer content in the mixture is 20% by mass or more and less than 100% by mass, and the mixture uses a Φ2.095 mm × 8.03 mm capillary, the piston speed is 10 mm / min, the furnace Melt mass flow at a body diameter of 9.55 mm, take-up acceleration of 400 m / min 2 , melt tension at break as measured with a capillary rheometer at 190 ° C. of 5.0 to 12.0 g, and 190 ° C. and 2.16 kg The rate is 1.0 g / 10 min or more, and the foamed insulating layer has a foaming degree of 80% or more. By the foam coaxial cable, it is solved.

以上の本発明は、エチレン・プロピレン共重合体を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記エチレン・プロピレン共重合体は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜10.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、前記発泡絶縁体層が、発泡度が80%以上であることを特徴とする発泡同軸ケーブルであるから、発泡度が80%以上の発泡絶縁体層を内部導体上に安定して確実に形成することができる。また得られた発泡同軸ケーブルは、高周波帯域(1MHz以上)での減衰量が少なく優れたものである。 The present invention described above is a foamed coaxial cable in which a foamed insulation layer obtained by foaming an ethylene / propylene copolymer is provided on an inner conductor, and the ethylene / propylene copolymer has a diameter of 2.095 mm × 8 A 0.03 mm capillary was used, the piston speed was 10 mm / min, the furnace body diameter was 9.55 mm, the take-up acceleration was 400 m / min 2 , and the melt tension at break measured by a capillary rheometer at 190 ° C. was 5.0 to 10 A foamed coaxial cable having a melt mass flow rate at 190 ° C. and 2.16 kg of 1.0 g / 10 min or more, and the foamed insulating layer has a foaming degree of 80% or more. Therefore, it is possible to stably and reliably form the foamed insulating layer having a foaming degree of 80% or more on the inner conductor. The obtained foamed coaxial cable is excellent in that it has a small amount of attenuation in a high frequency band (1 MHz or more).

また、エチレン・プロピレン共重合体とポリエチレンとの混合物を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記混合物は、当該混合物におけるエチレン・プロピレン共重合体の含有量が20質量%以上、100質量%未満であり、前記混合物は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜12.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、前記発泡絶縁体層は、発泡度が80%以上であるとしたので、前述の特性を有し、発泡同軸ケーブルの低温曲げ特性、さらに耐衝撃性や曲げ白化等を向上させることができる。 Further, the foamed insulation layer by foaming a mixture of ethylene-propylene copolymer and polyethylene, a foamed coaxial cable provided on the inner conductor, said mixture of ethylene-propylene copolymer in the mixture weight Content of coalescence is 20% by mass or more and less than 100% by mass, and the mixture uses a capillary of Φ2.095 mm × 8.03 mm, piston speed is 10 mm / min, furnace body diameter is 9.55 mm, take-up acceleration 400 m / min 2 , the melt tension at break measured by a capillary rheometer at 190 ° C. is 5.0 to 12.0 g, and the melt mass flow rate at 190 ° C. and 2.16 kg is 1.0 g / 10 min or more. There, the foamed insulation layer, since the degree of foaming was Ru der least 80% possess the aforementioned properties, the foam coaxial Cold flexural properties of Buru, it is possible to further improve the impact resistance and bending whitening like.

以下に本発明を詳細に説明する。請求項1に記載される発明は、エチレン・プロピレン共重合体(以下EP共重合体)を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記EP共重合体は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜10.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレート(以下MFR)が1.0g/10min以上であり、前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブルに関するものである。 The present invention is described in detail below. The invention described in claim 1 is a foamed coaxial cable in which a foamed insulating layer obtained by foaming an ethylene / propylene copolymer (hereinafter referred to as an EP copolymer) is provided on an inner conductor, The polymer is a Φ2.095 mm × 8.03 mm capillary, the piston speed is 10 mm / min, the furnace body diameter is 9.55 mm, the take-up acceleration is 400 m / min 2 , and measured at 190 ° C. with a capillary rheometer The melt mass flow rate (hereinafter referred to as MFR) at 190 ° C. and 2.16 kg is 1.0 g / 10 min or more, and the foamed insulating layer has a foaming degree of 80 to 10.0 g. % Or more of the foamed coaxial cable.

図1の一例によって説明する。例えば、無酸素銅線や銀メッキ銅線などのめっき銅線や銅合金線等からなる内部導体1と、その上に設けられる発泡絶縁体層2等からなり、さらにその上には外部導体3、通常保護層としてプラスチック材料からなるシース4が施されている。そして内部導体1としては、通常0.5〜20mm程度の導体径のめっき銅線や銅合金線が使用され、発泡絶縁体層2の厚さは0.5〜15mm程度とされる。また図1に示すように、外部導体3として例えば、銅薄板等を用いてスパイラル状に波型を形成すれば、可とう性をより付与させることができ好ましい。このようなコルゲート加工は、通常行われる方法によって形成すれば良い。   An example will be described with reference to FIG. For example, it comprises an inner conductor 1 made of a plated copper wire such as an oxygen-free copper wire or a silver-plated copper wire, a copper alloy wire, etc., and a foamed insulator layer 2 provided on the inner conductor 1, and further on the outer conductor 3 Usually, a sheath 4 made of a plastic material is provided as a protective layer. And as the internal conductor 1, the plated copper wire and copper alloy wire of a conductor diameter of about 0.5-20 mm are normally used, and the thickness of the foaming insulator layer 2 shall be about 0.5-15 mm. As shown in FIG. 1, it is preferable to form a corrugation in a spiral shape using, for example, a copper thin plate or the like as the external conductor 3, because flexibility can be further imparted. Such corrugating may be formed by a commonly performed method.

そして発泡絶縁体層2には、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0g以上であり、かつ190℃、2.16kgにおけるMFRが1.0g/10min以上のEP共重合体が用いられる。このようなEP共重合体とすることにより、破断時の溶融張力および溶融時の伸長性のバランスが良く、高発泡度の発泡絶縁体層2を安定して確実に形成することができる。すなわちEP共重合体として、破断時の溶融張力が5.0g以上で、190℃、2.16kgにおけるMFRを1.0g/10min以上とすることによって、発泡させた際にセル壁が破れることがなく、十分な溶融時の伸長性を有するので発泡セルを十分に成長させることができ、安定して確実に高発泡度を得ることができる。このことにより、発泡度が80%以上(発泡倍率としては5.0倍以上)の発泡絶縁体層を、安定して確実に形成することができる。また得られた発泡同軸ケーブルは、高周波帯域(1MHz以上)での減衰量が少なく優れた発泡同軸ケーブルとなる。
なお、EP共重合体の好ましい具体例としては、日本ポリプロ社のFB3312が挙げられる。
The foamed insulator layer 2 is a capillary rheometer at 190 ° C. using a Φ2.095 mm × 8.03 mm capillary with a piston speed of 10 mm / min, a furnace diameter of 9.55 mm, a take-up acceleration of 400 m / min 2. An EP copolymer having a melt tension at break of 5.0 g or more as measured in (1) and an MFR of 1.0 g / 10 min or more at 190 ° C. and 2.16 kg is used. By using such an EP copolymer, the balance between the melt tension at the time of fracture and the extensibility at the time of melting is good, and the foam insulation layer 2 having a high foaming degree can be stably and reliably formed. That is, as EP copolymer, the melt tension at break is 5.0 g or more, and the cell wall is torn when foamed by setting MFR at 190 ° C. and 2.16 kg to 1.0 g / 10 min or more. In addition, since it has sufficient extensibility upon melting, the foamed cells can be sufficiently grown, and a high foaming degree can be obtained stably and reliably. This makes it possible to stably and reliably form a foamed insulator layer having a foaming degree of 80% or more (a foaming ratio of 5.0 or more). The obtained foamed coaxial cable is an excellent foamed coaxial cable with little attenuation in a high frequency band (1 MHz or more).
A preferred specific example of the EP copolymer is FB3312 manufactured by Nippon Polypro.

また、請求項2に記載されるように、エチレン・プロピレン共重合体とポリエチレンとの混合物を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、前記混合物は、当該混合物におけるエチレン・プロピレン共重合体の含有量が20質量%以上、100質量%未満であり、前記混合物は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜12.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブルとなる。 Moreover, as described in claim 2, a foamed coaxial cable in which a foamed insulator layer obtained by foaming a mixture of an ethylene / propylene copolymer and polyethylene is provided on an inner conductor , wherein the mixture is The ethylene / propylene copolymer content in the mixture is 20% by mass or more and less than 100% by mass, and the mixture uses a capillary of Φ2.095 mm × 8.03 mm, the piston speed is 10 mm / min, the furnace Melt mass flow at a body diameter of 9.55 mm, take-up acceleration of 400 m / min 2 , melt tension at break as measured with a capillary rheometer at 190 ° C. of 5.0 to 12.0 g, and 190 ° C. and 2.16 kg rate is not less 1.0 g / 10min or more, the foamed insulation layer, characterized in that the foaming degree of 80% or more To the foam coaxial cable.

なお発泡絶縁体層2の形成は、各種発泡剤によって行うことができる。例えば、アゾジカルボンアミド、4、4′−オキシビス(ベンゼンスルホニルヒドラジン)、N、N′−ジニトロソペンタメチレンテトラミン等の化学発泡剤や窒素ガス、アルゴンガス、フロンガス、炭酸ガス等の不活性ガスが、単独で或いは併用して使用できる。特に不活性ガスによる発泡の場合には、化学発泡剤によって発泡させた場合のように発泡残渣が誘電特性に悪影響を与えたり、また発泡度が十分でない等の問題が少なくなる。また、発泡核剤を添加することが好ましい。例えば、タルク、クレイ、ボロンナイトライド(BN)、シリカ等の微粉末、さらにアゾジカルボンアミドやフッ素系樹脂の微粉末或いはフッ素系ゴムの微粉末である。その添加量は、通常ベース樹脂100質量部に対して0.05〜3.0質量部程度である。   The foamed insulator layer 2 can be formed by various foaming agents. For example, chemical blowing agents such as azodicarbonamide, 4,4'-oxybis (benzenesulfonylhydrazine), N, N'-dinitrosopentamethylenetetramine, and inert gases such as nitrogen gas, argon gas, freon gas, and carbon dioxide gas. Can be used alone or in combination. In particular, in the case of foaming with an inert gas, problems such as foaming residues having an adverse effect on dielectric properties as in the case of foaming with a chemical foaming agent and insufficient foaming are reduced. Moreover, it is preferable to add a foam nucleating agent. For example, fine powders such as talc, clay, boron nitride (BN), and silica, fine powders of azodicarbonamide and fluororesin, and fine powders of fluororubber. The addition amount is usually about 0.05 to 3.0 parts by mass with respect to 100 parts by mass of the base resin.

さらに発泡絶縁体層2には、例えば3−(N−サリチロイル)アミノ−1,2,4−トリアゾール(商品名:CDA−1)、2′,3−ビス[3−(3,5−ジ−ターシャリーブチル−4−ヒドロキシフェニル)プロピオニル]プロピオノヒドラジド(商品名:イルガノックスMD1024)等の金属不活性剤、N、N′−ジ−2−ナフチル−p−フェニレンジアミン(商品名:ノクラックWhite)のようなアミン系酸化防止剤、ペンタエリスリトールテトラキス[3−(3、5−ジ−ターシャリーブチル−4−ヒドロキシフェニル)プロピオネート](商品名:イルガノックス1010)などのヒンダードフェノール系酸化防止剤や4、4′−チオビス(3−メチル−6−ターシャリーブチルフェノール)(商品名ノクラック300)などのチオビスフェノール系酸化防止剤を添加することができる。   Further, for example, 3- (N-salicyloyl) amino-1,2,4-triazole (trade name: CDA-1), 2 ′, 3-bis [3- (3,5-diazo) is used as the foamed insulating layer 2. -Tertiarybutyl-4-hydroxyphenyl) propionyl] propionohydrazide (trade name: Irganox MD1024) and other metal deactivators, N, N'-di-2-naphthyl-p-phenylenediamine (trade name: Nocrack) Hindered phenolic oxidations such as amine antioxidants such as White) and pentaerythritol tetrakis [3- (3,5-di-tertiarybutyl-4-hydroxyphenyl) propionate] (trade name: Irganox 1010). Inhibitors, 4,4'-thiobis (3-methyl-6-tertiarybutylphenol) (trade name NOCRACK 300), etc. It can be added o bisphenol-based antioxidant.

表1に記載する実施例および比較例によって、本発明の効果を示す。二段押出機の第2押出機で、発泡絶縁体を形成するペレット材料として表1に示される樹脂ペレット材料(表中、樹脂材料)と、発泡核剤として富士タルク社のタルク微分粉末(LMS−300)をドライブレンドし、これを230℃に調整した第1押出機に供給し、第1押出機の途中から窒素ガスを注入して混合溶融し、第2押出機で170℃程度に温度調整し、Φ9mmの銅線からなる内部導体上に押出すると同時に発泡させて発泡同軸ケーブルを作製した。   The effects of the present invention are shown by the examples and comparative examples described in Table 1. In the second extruder of the two-stage extruder, the resin pellet material (resin material in the table) shown in Table 1 as the pellet material forming the foam insulation, and the talc differential powder (LMS) of Fuji Talc as the foam nucleating agent -300) is dry blended, supplied to a first extruder adjusted to 230 ° C., mixed and melted by injecting nitrogen gas from the middle of the first extruder, and heated to about 170 ° C. in the second extruder. A foamed coaxial cable was prepared by adjusting and extruding onto an inner conductor made of a copper wire with a diameter of 9 mm and simultaneously foaming.

これらの発泡同軸ケーブルについて、発泡絶縁体層の発泡度(%)を[(ベース樹脂の比重−発泡後の比重)/(ベース樹脂の比重)]×100として計算した。発泡度が80%以上のものを合格とした。併せて発泡倍率を、[1/(100−発泡度)]×100として求めて記載した。5倍以上が好ましいものである。また、ネットワークアナライザーを用いて、2.2GHzにおける20Dサイズの発泡同軸ケーブルの減衰量を測定した。減衰量が62dB/km以下を合格とした。なお低温曲げ特性としては、20Dの発泡同軸ケーブル(外径22mm)を−40℃の恒温槽に1時間放置し取出した後、各種径のマンドレルに巻き付け発泡絶縁体層のクラックの状態を調べた。クラックが生じない最小のマンドレルの径(mm)を記載した。さらに、前記各種樹脂の破断時の溶融張力(Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minでの190℃におけるキャピラリーレオメータによって測定。)およびMFRの値を記載した。なおMFRは、190℃、2.16kgで測定した値である。表1に結果を記載した。 For these foamed coaxial cables, the foaming degree (%) of the foamed insulating layer was calculated as [(specific gravity of base resin−specific gravity after foaming) / (specific gravity of base resin)] × 100. A foam having a foaming degree of 80% or more was regarded as acceptable. In addition, the expansion ratio was determined and described as [1 / (100-foaming degree)] × 100. 5 times or more is preferable. Moreover, the attenuation amount of the 20D size foam coaxial cable in 2.2 GHz was measured using the network analyzer. Attenuation was 62 dB / km or less as acceptable. As low-temperature bending characteristics, a 20D foam coaxial cable (outer diameter: 22 mm) was left in a thermostatic bath at -40 ° C. for 1 hour, and then wound around a mandrel of various diameters to examine the state of cracks in the foam insulation layer. . The minimum mandrel diameter (mm) at which no cracks occurred was described. Further, melt tension at break of the various resins (using a capillary of Φ2.095 mm × 8.03 mm, a piston speed of 10 mm / min, a furnace body diameter of 9.55 mm, and a take-up acceleration of 400 m / min 2 at 190 ° C. Measured with a capillary rheometer) and MFR values. MFR is a value measured at 190 ° C. and 2.16 kg. Table 1 shows the results.

表1から明らかなとおり、実施例1〜6に記載されるように、本発明の発泡同軸ケーブルは、発泡度が80%以上(発泡倍率が5.0倍以上)であった。また、高周波帯域(1GHz以上)での減衰量が60dB/km以下と優れたものであることが判る。さらに低温曲げ特性に関しては、20mm以上と十分に実用的なものである。   As is clear from Table 1, as described in Examples 1 to 6, the foamed coaxial cable of the present invention had a foaming degree of 80% or more (a foaming ratio of 5.0 times or more). Moreover, it turns out that the attenuation amount in a high frequency band (1 GHz or more) is excellent with 60 dB / km or less. Furthermore, regarding the low temperature bending characteristics, it is sufficiently practical at 20 mm or more.

すなわち実施例1に示すように、破断時の溶融張力が10.0gでMFRが2.0g/10minのEP共重合体を発泡させて発泡絶縁体層を形成した発泡同軸ケーブルは、発泡度が89%(発泡倍率が9.1倍)、減衰量が56dB/km、低温曲げ特性が80mmと良好なものであった。また、実施例2〜6に示すようにEP共重合体混合物の場合も、EP共重合体の配合量が20質量%以上、99質量%未満であって、破断時の溶融張力が5.0〜12.0g、MFRが1.0〜8.0g/10minとしたものは、発泡度が82〜88%(発泡倍率も5.6〜8.3倍)、減衰量が56〜60dB/km、低温曲げ特性が20〜80mmと良好な発泡同軸ケーブルが得られることが判る。   That is, as shown in Example 1, the foamed coaxial cable formed by foaming an EP copolymer having a melt tension at break of 10.0 g and an MFR of 2.0 g / 10 min to form a foamed insulator layer has a foaming degree. It was as good as 89% (foaming ratio: 9.1 times), attenuation was 56 dB / km, and low-temperature bending characteristics were 80 mm. Further, as shown in Examples 2 to 6, also in the case of an EP copolymer mixture, the blending amount of the EP copolymer is 20% by mass or more and less than 99% by mass, and the melt tension at break is 5.0. ˜12.0 g, MFR of 1.0 to 8.0 g / 10 min, foaming degree is 82 to 88% (foaming ratio is also 5.6 to 8.3 times), attenuation is 56 to 60 dB / km It can be seen that a foamed coaxial cable having a low temperature bending characteristic of 20 to 80 mm can be obtained.

これに対して、比較例1〜7に示す本発明の範囲を外れた発泡絶縁体層の発泡同軸ケーブルは、発泡度(発泡倍率)、減衰量、低温曲げ特性のいずれかに問題があった。すなわち、比較例1のように破断時の溶融張力が2.0gと小さい場合には、発泡度が68%(発泡倍率も3.1倍)、減衰量も72dB/kmと大きくなる。また、比較例2のようにMFRが0.4g/10min(並びに密度が0.91g/cmで230℃、2.16kgのMFRが0.5g/10min)と小さいと、破断時の溶融張力が11.0gであっても発泡度が74%(発泡倍率も3.8倍)であり、減衰量が67dB/kmと大きくなる。さらに比較例6に示すように、EP共重合体とPEの混合物の場合であっても、EP共重合体の含有量が10質量%であると破断時の溶融張力が4.0gと小さくなって、発泡度が79%(発泡倍率は5.3倍)、減衰量も63dB/kmと僅かに目的値を達成できなかった。また比較例7に示すように、EP共重合体とPEの混合物の場合であっても、EP共重合体の含有量が70質量%であると破断時の溶融張力が3.0gと小さくなって、発泡度が76%(発泡倍率は4.2倍)、減衰量も67dB/kmとなった。なお、比較例3および4のように、発泡絶縁体層に破断時の溶融張力が小さいPEを用いた場合は、比較例4のように破断時の溶融張力が0.5gと小さい場合には、発泡度が52%(発泡倍率も2.1倍)と小さく減衰量が90dB/kmと大きくなり、またPEどうしの混合物を用いた場合でも、比較例3のように破断時の溶融張力が3.0gの場合には、発泡度が78%(発泡倍率が4.5倍)で減衰量が64dB/kmとなった。さらに比較例5のように、破断時の溶融張力が大ききものであっても、MFRが0.2g/10minと小さいPEを用いると、発泡度が70%(発泡倍率も3.3倍)、減衰量が71dB/kmと大きくなる。 On the other hand, the foamed coaxial cable of the foamed insulator layer outside the scope of the present invention shown in Comparative Examples 1 to 7 has a problem in any of the degree of foaming (foaming ratio), the amount of attenuation, and the low-temperature bending characteristics. . That is, when the melt tension at break is as small as 2.0 g as in Comparative Example 1, the foaming degree is 68% (foaming ratio is 3.1 times) and the attenuation is as large as 72 dB / km. Also, as in Comparative Example 2, when the MFR is as small as 0.4 g / 10 min (and the density is 0.91 g / cm 3 at 230 ° C. and the 2.16 kg MFR is 0.5 g / 10 min), the melt tension at break Is 11.0 g, the foaming degree is 74% (foaming ratio is also 3.8 times), and the attenuation is as large as 67 dB / km. Furthermore, as shown in Comparative Example 6, even in the case of a mixture of an EP copolymer and PE, when the content of the EP copolymer is 10% by mass, the melt tension at break becomes as small as 4.0 g. The foaming degree was 79% (foaming ratio was 5.3 times), and the attenuation was 63 dB / km. Further, as shown in Comparative Example 7, even in the case of a mixture of EP copolymer and PE, when the content of the EP copolymer is 70% by mass, the melt tension at break becomes as small as 3.0 g. The foaming degree was 76% (foaming ratio was 4.2 times) and the attenuation was 67 dB / km. In addition, when PE having a low melt tension at break is used for the foamed insulator layer as in Comparative Examples 3 and 4, when the melt tension at break is as small as 0.5 g as in Comparative Example 4. The foaming degree is 52% (the foaming ratio is 2.1 times) and the damping amount is as large as 90 dB / km, and even when a mixture of PEs is used, the melt tension at the time of breaking as in Comparative Example 3 is high. In the case of 3.0 g, the foaming degree was 78% (foaming ratio was 4.5 times), and the attenuation was 64 dB / km. Furthermore, even if the melt tension at break is large as in Comparative Example 5, when PE with a small MFR of 0.2 g / 10 min is used, the foaming degree is 70% (the foaming ratio is 3.3 times), The amount of attenuation increases to 71 dB / km.

以上の本発明の発泡同軸ケーブルは、発泡絶縁体層に破断時の溶融張力およびMFRを特定したEP共重合体または、EP共重合体とポリエチレンとの混合物であって、破断時の溶融張力およびMFRを特定した混合物を用いたので、高発泡度の発泡絶縁体層を安定して確実に形成でき、高周波帯域(1GHz以上)での減衰量が少ない種々の用途の発泡同軸ケーブルとして用いることができる。   The above foamed coaxial cable of the present invention is an EP copolymer in which the foamed insulator layer has a melt tension and MFR specified at break, or a mixture of an EP copolymer and polyethylene, and the melt tension at break and Since a mixture with MFR specified is used, it is possible to stably and surely form a foamed insulation layer having a high foaming degree, and to be used as a foamed coaxial cable for various applications with low attenuation in a high frequency band (1 GHz or more). it can.

本発明の発泡同軸ケーブルの一例を示す概略断面斜視図である。It is a schematic sectional perspective view which shows an example of the foaming coaxial cable of this invention.

1 内部導体
2 発泡絶縁体層
3 コルゲート構造の外部導体
4 シース
DESCRIPTION OF SYMBOLS 1 Inner conductor 2 Foam insulator layer 3 Corrugated structure outer conductor 4 Sheath

Claims (2)

エチレン・プロピレン共重合体を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、
前記エチレン・プロピレン共重合体は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜10.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、
前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブル。
A foamed insulation cable in which an ethylene / propylene copolymer is foamed is a foamed coaxial cable provided on an inner conductor,
The ethylene / propylene copolymer uses a capillary of Φ2.095 mm × 8.03 mm, has a piston speed of 10 mm / min, a furnace diameter of 9.55 mm, a take-up acceleration of 400 m / min 2 , and a capillary rheometer at 190 ° C. The melt tension at the time of breaking as measured at 5.0 to 10.0 g, and the melt mass flow rate at 190 ° C. and 2.16 kg is 1.0 g / 10 min or more,
The foamed coaxial cable is characterized in that the foamed insulating layer has a foaming degree of 80% or more.
エチレン・プロピレン共重合体とポリエチレンとの混合物を発泡させた発泡絶縁体層が、内部導体上に設けられた発泡同軸ケーブルであって、
前記混合物は、当該混合物におけるエチレン・プロピレン共重合体の含有量が20質量%以上、100質量%未満であり、
前記混合物は、Φ2.095mm×8.03mmのキャピラリーを用い、ピストンスピードが10mm/min、炉体径が9.55mm、引取加速度が400m/minで、190℃におけるキャピラリーレオメータで測定した破断時の溶融張力が5.0〜12.0gであり、かつ190℃、2.16kgにおけるメルトマスフローレートが1.0g/10min以上であり、
前記発泡絶縁体層は、発泡度が80%以上であることを特徴とする発泡同軸ケーブル。
A foamed coaxial cable in which a foamed insulation layer obtained by foaming a mixture of ethylene / propylene copolymer and polyethylene is provided on an inner conductor,
In the mixture, the content of the ethylene / propylene copolymer in the mixture is 20% by mass or more and less than 100% by mass,
The mixture used was a Φ2.095 mm × 8.03 mm capillary with a piston speed of 10 mm / min, a furnace diameter of 9.55 mm, a take-up acceleration of 400 m / min 2 and a breakage measured with a capillary rheometer at 190 ° C. And melt mass flow rate at 190 ° C. and 2.16 kg is 1.0 g / 10 min or more,
The foamed coaxial cable is characterized in that the foamed insulating layer has a foaming degree of 80% or more.
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