JP2005264005A - Method for producing flame-retardant conductive crosslinked polyolefin foam - Google Patents

Method for producing flame-retardant conductive crosslinked polyolefin foam Download PDF

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JP2005264005A
JP2005264005A JP2004079461A JP2004079461A JP2005264005A JP 2005264005 A JP2005264005 A JP 2005264005A JP 2004079461 A JP2004079461 A JP 2004079461A JP 2004079461 A JP2004079461 A JP 2004079461A JP 2005264005 A JP2005264005 A JP 2005264005A
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Choji Obara
長二 小原
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Sanwa Kako Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a highly flame-retardant nonhalogen/nonphosphorus conductive crosslinked polyolefin foam. <P>SOLUTION: The method for producing the nonhalogen/nonphosphorus flame-retardant conductive crosslinked polyolefin foam comprises putting a foamable crosslinkable composition prepared by mixing and kneading a polyolefin resin with conductive carbon, a blowing agent, and a crosslinking agent into a press mold, heating the composition in the mold under pressure to yield an intermediate foam, and heating and foaming the intermediate foam in a non-airtight mold to form a crosslinked polyolefin foam, wherein 2 to 30 pts. wt. melamine cyanurate is added to 100 pts. wt. polyolefin resin. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、ポリオレフィン系樹脂を基材とするノンハロゲン・ノンリン難燃性導電性架橋ポリオレフィン系発泡体の製造方法に関するものである。     The present invention relates to a method for producing a non-halogen / non-phosphorus flame retardant conductive crosslinked polyolefin foam based on a polyolefin resin.

本出願人は、ポリオレフィンにカーボン、発泡剤及び架橋剤を添加混練し、加圧下金型中にて架橋させ、次いで常圧下にて加熱発泡させる導電性架橋ポリオレフィン気泡体の製造方法(特公平2−29095号公報)を開発した。しかしながら、上記の製造方法では難燃性の付与を示唆していなかった。     The present applicant has added and kneaded carbon, a foaming agent and a crosslinking agent to polyolefin, crosslinked in a mold under pressure, and then heated and foamed under normal pressure (Japanese Patent Publication No. 2). -29095). However, the above production method did not suggest imparting flame retardancy.

また、従来から行われている難燃性発泡体の製造方法としては、ポリオレフィンに無機系充填剤を添加したものを加熱発泡する方法(特公昭60−26500号公報)、あるいはハロゲン系又はリン系難燃剤を添加したものを加熱発泡する方法(特公昭48−9587号公報、特公昭48−29857号公報及び特公昭58−5930号公報)等がある。しかしながら、上記従来技術の難燃性発泡体は、ハロゲン系難燃剤を使用しているため、燃焼時に有害なハロゲンガスが発生し、人体や環境に悪影響を及ぼした。     Further, as a conventional method for producing a flame-retardant foam, a method of heating and foaming a polyolefin to which an inorganic filler is added (Japanese Patent Publication No. 60-26500), or a halogen-based or phosphorus-based foam is used. There is a method in which a flame retardant added is heated and foamed (Japanese Examined Patent Publication Nos. 48-9857, 48-29857 and 58-5930). However, since the flame retardant foam of the above prior art uses a halogen-based flame retardant, harmful halogen gas is generated at the time of combustion, which adversely affects the human body and the environment.

ノンハロゲンの技術としては、エチレン−酢酸ビニル共重合体単独又は50重量%以上のエチレン−酢酸ビニル共重合体と1種以上の他のポリオレフィン系樹脂との混合物よりなり、かつ、酢酸ビニルの含有量が5〜20重量%のポリオレフィン系樹脂マトリックス100重量部、無機系難燃剤50〜200重量部、赤リン5〜50重量部、メラミン化合物5〜50重量部、多価アルコール1〜15重量部及び発泡剤15〜30重量部からなる発泡性難燃性樹脂組成物が提案されている(特許第3308633号)。
特公平2−29095号公報 特公昭60−26500号公報 特公昭48−9587号公報 特公昭48−29857号公報 特公昭58−5930号公報 特許第3308633号
Non-halogen technology includes ethylene-vinyl acetate copolymer alone or a mixture of 50% by weight or more of ethylene-vinyl acetate copolymer and one or more other polyolefin resins, and the content of vinyl acetate. Is 5 to 20% by weight of polyolefin resin matrix 100 parts by weight, inorganic flame retardant 50 to 200 parts by weight, red phosphorus 5 to 50 parts by weight, melamine compound 5 to 50 parts by weight, polyhydric alcohol 1 to 15 parts by weight and A foamable flame retardant resin composition comprising 15 to 30 parts by weight of a foaming agent has been proposed (Japanese Patent No. 3308633).
Japanese Patent Publication No. 2-29095 Japanese Patent Publication No. 60-26500 Japanese Patent Publication No. 48-9487 Japanese Patent Publication No. 48-29857 Japanese Patent Publication No.58-5930 Japanese Patent No. 3308633

しかし、上記ノンハロゲン難燃化技術は、赤リンを添加している為、電子機器に悪影響を及ぼすことと、難燃剤の添加量が多いため、導電性カーボンを多量に添加し、発泡条件の狭い導電性発泡体の製造方法には適用出来ないことが問題であった。従って、本発明の目的は、十分な難燃性を有しながら、燃焼時には有害なハロゲンガスを発生せず、電子機器にも悪影響を及ぼさないノンハロゲン・ノンリン難燃性導電性架橋ポリオレフィン系発泡体の製造方法を提供することにある。     However, since the above non-halogen flame retardant technology adds red phosphorus, it has an adverse effect on electronic equipment, and the amount of flame retardant added is large, so a large amount of conductive carbon is added and the foaming conditions are narrow. It has been a problem that it cannot be applied to a method for producing a conductive foam. Accordingly, an object of the present invention is a non-halogen / non-phosphorus flame-retardant conductive cross-linked polyolefin foam that has sufficient flame retardancy, does not generate harmful halogen gas during combustion, and does not adversely affect electronic equipment. It is in providing the manufacturing method of.

前記目的を達成するため、本発明の第一の方法は、ポリオレフィン系樹脂100重量部にメラミンシアヌレート2〜30重量部、導電カーボン、発泡剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下に加熱した後、除圧し、発泡体を生成させることを特徴とする難燃性導電性架橋ポリオレフィン系発泡体の製造方法である。 In order to achieve the above object, the first method of the present invention is to add 2 to 30 parts by weight of melamine cyanurate, conductive carbon, a foaming agent and a cross-linking agent to 100 parts by weight of a polyolefin resin, and to obtain the cross-linkability obtained. A method for producing a flame-retardant conductive cross-linked polyolefin-based foam, wherein the foamable composition is heated under pressure and then decompressed to form a foam.

本発明の第二の方法は、ポリオレフィン系樹脂100重量部にメラミンシアヌレート2〜30重量部、導電カーボン、発泡剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下で発泡剤が実質的に分解しない温度に加熱することによって、該組成物を架橋せしめ、次いで得られた架橋性発泡性組成物を金型から取り出して急激に発泡もしくは膨張させないように常圧下で加熱し、発泡剤させることを特徴とする難燃性導電性架橋ポリオレフィン系発泡体の製造方法である。 The second method of the present invention is to add and knead 2 to 30 parts by weight of melamine cyanurate, conductive carbon, a foaming agent and a crosslinking agent to 100 parts by weight of a polyolefin resin, and pressurize the resulting crosslinkable foamable composition. The composition is cross-linked by heating to a temperature at which the foaming agent does not substantially decompose, and then the resulting crosslinkable foamable composition is removed from the mold under normal pressure so as not to expand or expand rapidly. A method for producing a flame-retardant conductive cross-linked polyolefin foam characterized by heating to a foaming agent.

本発明の製造方法において、メラミンシアヌレート及び水酸化アルミニウムが上記範囲未満である場合、十分な難燃性が得られず、上記範囲を越えて添加する場合、発泡成形を阻害し、満足な発泡体が得られない。 In the production method of the present invention, when the melamine cyanurate and aluminum hydroxide are less than the above range, sufficient flame retardancy cannot be obtained, and when added beyond the above range, foam molding is inhibited and satisfactory foaming is achieved. I can't get a body.

本発明の方法によれば、十分な導電性及び難燃性を有し、且つ、人体や環境に悪影響を及ぼすハロゲンや、電子機器に悪影響を及ぼすリンを含有しない。さらに、難燃性能が高く、本発明の方法により得られた発泡体は、UL94HBFに適合することができる。     According to the method of the present invention, it has sufficient conductivity and flame retardancy, and does not contain halogen that adversely affects the human body or the environment, or phosphorus that adversely affects electronic equipment. Furthermore, the flame retardant performance is high, and the foam obtained by the method of the present invention can conform to UL94HBF.

本発明においてポリオレフィンとは、例えば、ポリエチレン、エチレン−酢酸ビニル共重合体、ポリプロピレン、ポリテトラフルオロエチレン、エチレン−プロピレン共重合体、ポリ−4−メチル−1−ペンテン、ポリビニルクロライド、ポリビニリデンクロライド、ポリビニリデンフルオライド、テトラフルオロエチレン、エチレン共重合体を挙げることができる。     In the present invention, polyolefin is, for example, polyethylene, ethylene-vinyl acetate copolymer, polypropylene, polytetrafluoroethylene, ethylene-propylene copolymer, poly-4-methyl-1-pentene, polyvinyl chloride, polyvinylidene chloride, Examples thereof include polyvinylidene fluoride, tetrafluoroethylene, and an ethylene copolymer.

本発明でいう導電性カーボンとは、ファーネス系カーボンブラック、アセチレン系カーボンブラック、チャンネル系カーボンブラック等であり、これらは単独で用いても2種以上を併用しても良い。特にカーボンブラックの中でも表面積(窒素吸着方法)900m/g以上のファーネスブラックが好ましい導電性カーボンブラックである。 The conductive carbon referred to in the present invention is furnace carbon black, acetylene carbon black, channel carbon black and the like, and these may be used alone or in combination of two or more. In particular, among carbon blacks, furnace black having a surface area (nitrogen adsorption method) of 900 m 2 / g or more is a preferable conductive carbon black.

本発明でいう架橋剤とは、ポリオレフィン系樹脂中において少なくともポリオレフィン樹脂の流動開始温度以上の分解温度を有するものであって、加熱により分解され、遊離ラジカルを発生してその分子間もしくは分子内に架橋結合を生じせしめるラジカル発生剤であるところの有機過酸化物、例えばジクミルパーオキサイド、1,1−ジターシャリーブチルパーオキサイド、1,1−ジターシャリーブチルパーオキシー3,3,5−トリメチルシクロヘキサン、2,5−ジメチルー2,5−ジターシャリーブチルパーオキシヘキサン、2,5−ジメチルー2,5−ジターシャリーブチルパーオキシヘキシン、α、α―ジターシャリーブチルパーオキシイソプロピルベンゼン、ターシャリーブチルパーオキシケトン、ターシャリーブチルパーオキシベンゾエートなどがあるが、その時に使用される樹脂によって最適な有機過酸化物を選択しなければならない。     The cross-linking agent as used in the present invention has a decomposition temperature at least equal to or higher than the flow start temperature of the polyolefin resin in the polyolefin-based resin, and is decomposed by heating to generate free radicals between or within the molecules. Organic peroxides that are radical generators that cause cross-linking, such as dicumyl peroxide, 1,1-ditertiary butyl peroxide, 1,1-ditertiary butyl peroxy-3,3,5-trimethylcyclohexane 2,5-dimethyl-2,5-ditertiary butyl peroxyhexane, 2,5-dimethyl-2,5-ditertiary butyl peroxyhexyne, α, α-ditertiary butyl peroxyisopropylbenzene, tertiary butyl per Oxyketone, tertiary butyl peru Although there are xylbenzoate, etc., the optimum organic peroxide must be selected according to the resin used at that time.

本発明でいう発泡剤とは、ポリオレフィン系樹脂の溶融温度以上の分解温度を有する化学発泡剤であり、例えばアゾ系化合物のアゾジカルボンアミド、バリウムアゾジカルボキシレート等;ニトロソ系化合物のジニトロソペンタメチレンテトラミン、トリニトロトリメチルトリアミン等;ヒドラジッド系化合物のp,p‘−オキシビスベンゼンスルホニルヒドラジッド等;スルホニルセミカルバジッド系化合物のp,p‘−オキシビスベンゼンスルホニルセミカルバジッド、トルエンスルホニルセミカルバジッド等がある。 The foaming agent referred to in the present invention is a chemical foaming agent having a decomposition temperature equal to or higher than the melting temperature of the polyolefin resin. For example, azo compounds such as azodicarbonamide and barium azodicarboxylate; nitroso compounds such as dinitrosopenta Methylenetetramine, trinitrotrimethyltriamine, etc .; p, p′-oxybisbenzenesulfonyl hydrazide, etc. of hydrazide compounds; p, p′-oxybisbenzenesulfonyl semicarbazide, toluenesulfonyl semicarbazide of sulfonyl semicarbazide compounds, etc. There are Jid etc.

本発明において、発泡助剤を発泡剤の種類に応じて添加することができる。発泡助剤としては尿素を主成分とした化合物、酸化亜鉛、酸化鉛等の金属酸化物、サリチル酸、ステアリン酸等を主成分とする化合物、即ち高級脂肪酸あるいは高級脂肪酸の金属化合物などがある。 In the present invention, a foaming aid can be added depending on the type of foaming agent. Examples of the foaming aid include compounds mainly composed of urea, metal oxides such as zinc oxide and lead oxide, compounds mainly composed of salicylic acid and stearic acid, that is, higher fatty acids or higher fatty acid metal compounds.

本発明においては、使用する組成物の物性の改良或いは価格の低下を目的として、架橋結合に著しい悪影響を与えない配合剤(充填剤)、例えば酸化亜鉛、酸化チタン、酸化カルシウム、酸化マグネシウム、酸化ケイ素等の金属酸化物、炭酸マグネシウム、炭酸カルシウム等の炭酸塩、あるいはパルプ等の繊維物質、又は各種染料、顔料並びに蛍光物質、その他常用のゴム配合剤等を必要に応じて添加することができる。 In the present invention, for the purpose of improving the physical properties of the composition to be used or reducing the price, a compounding agent (filler) that does not significantly adversely affect the cross-linking, such as zinc oxide, titanium oxide, calcium oxide, magnesium oxide, oxidation Metal oxides such as silicon, carbonates such as magnesium carbonate and calcium carbonate, fiber materials such as pulp, various dyes, pigments, fluorescent materials, and other conventional rubber compounding agents can be added as necessary. .

次に、本発明のノンハロゲン・ノンリン難燃性導電性架橋ポリオレフィン系発泡体の製造方法について説明する。 Next, a method for producing the non-halogen / non-phosphorus flame retardant conductive crosslinked polyolefin foam of the present invention will be described.

まず、第一の方法は、ポリオレフィン100重量部に対して導電性カーボンを好ましくは13〜30重量部、メラミンシアヌレート2〜30重量部、発泡剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下に140〜170℃で一定時間加熱した後除圧し、発泡体を生成させる方法である。 First, in the first method, conductive carbon is preferably added in an amount of 13 to 30 parts by weight, melamine cyanurate 2 to 30 parts by weight, a foaming agent and a cross-linking agent are added to and kneaded with 100 parts by weight of polyolefin, and the obtained cross-linkage is obtained. The foamable composition is heated at 140-170 ° C. for a certain period of time under pressure and then depressurized to produce a foam.

第二の方法は、ポリオレフィン100重量部に対して、導電性カーボン5〜25重量部、メラミンシアヌレート2〜30重量部、発泡剤、発泡助剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下金型中にて発泡剤が実質的に分解しない温度に加熱することによって該組成物を架橋せしめ、次いで得られた発泡性架橋性組成物を金型から取り出して急激に発泡もしくは膨張させないように常圧下にて加熱することにより発泡させることを特徴とするものである。   In the second method, 5 to 25 parts by weight of conductive carbon, 2 to 30 parts by weight of melamine cyanurate, a foaming agent, a foaming aid and a crosslinking agent are added and kneaded with respect to 100 parts by weight of polyolefin, and the obtained crosslinking is performed. The foamable composition is crosslinked by heating to a temperature at which the foaming agent does not substantially decompose in a mold under pressure, and then the resulting foamable crosslinkable composition is removed from the mold. It is characterized by foaming by heating under normal pressure so as not to foam or expand rapidly.

常圧下での加熱手段は、発泡性架橋組成物を、密閉系でない直方体型などの所望の形状の型内に入れ、ローゼ合金、ウッド合金等を用いるメタルバス、オイルバス、硝酸ナトリウム、硝酸カリウム、亜硝酸カリウム等の塩の1種又は2種以上の溶融塩を用いる塩浴中、窒素気流中で、または直方体型がその外壁に加熱用熱媒体導管(熱媒:スチーム等)が設けられてなるものでその中で、あるいは伸長可能な鉄板等により覆われた状態で、所定時間加熱した後、冷却して発泡体を得る。加熱温度は使用するポリオレフィンの種類に応じて145〜210℃、好ましくは160〜190℃であり、加熱時間は60〜210分、好ましくは90〜180分である。   The heating means under normal pressure includes placing the foamable cross-linking composition in a mold of a desired shape such as a rectangular parallelepiped type that is not a closed system, a metal bath using a rose alloy, a wood alloy, an oil bath, sodium nitrate, potassium nitrate, In a salt bath using one or more molten salts of potassium nitrite or the like, in a nitrogen stream, or a rectangular parallelepiped is provided with a heating medium conduit (heating medium: steam, etc.) on its outer wall After being heated for a predetermined time in a state covered with an expandable iron plate or the like, a foam is obtained by cooling. The heating temperature is 145 to 210 ° C., preferably 160 to 190 ° C., depending on the type of polyolefin used, and the heating time is 60 to 210 minutes, preferably 90 to 180 minutes.

本発明の製造方法によって得られる導電性発泡体は、米国UL(Underwriters Laboratories)94HBFに定められた水平燃焼試験に合格するものであった。従って、得られるノンハロゲン難燃性導電性架橋ポリオレフィン系発泡体は、電子機器の緩衝材、電波吸収体等に適用できる     The conductive foam obtained by the production method of the present invention passed the horizontal combustion test defined in the United States UL (Underwriters Laboratories) 94HBF. Therefore, the obtained non-halogen flame-retardant conductive crosslinked polyolefin-based foam can be applied to a buffer material of an electronic device, a radio wave absorber and the like

低密度ポリエチレン(商品名:ノバテックLC−520、密度0.9226 g/cm、メルトフローレート3.8g/10min、三菱化学株式会社製)100重量部と、ファーネス系カーボンブラック(商品名:ケッチェンブラックEC、三菱化学株式会社製)10重量部、メラミンシアヌレート(商品名:MC−610、日産化学工業株式会社製)20重量部、アゾジカルボンアミド(商品名:ビニホールAC#3、永和化成工業株式会社製)4重量部、亜鉛華2重量部、α,α’−ビス(t−ブチルパーオキシ)ジイソプロピルベンゼン(商品名:パーカドックス−14/P40、化薬ヌーリー株式会社製)1重量部からなる組成物を110℃のニーダーにて混練し、160℃に加熱されたプレス内の金型(18×300×300)に練和物を充填し、50分間加圧下で加熱し、発泡体を得た。 Low-density polyethylene (trade name: Novatec LC-520, density 0.9226 g / cm 3 , melt flow rate 3.8 g / 10 min, manufactured by Mitsubishi Chemical Corporation) and 100 parts by weight of furnace carbon black (trade name: Ketsu Chen Black EC, manufactured by Mitsubishi Chemical Corporation) 10 parts by weight, melamine cyanurate (trade name: MC-610, manufactured by Nissan Chemical Industries, Ltd.) 20 parts by weight, azodicarbonamide (trade name: VINYHALL AC # 3, Eiwa Kasei) Kogyo Nouri Co., Ltd.) 4 parts by weight, zinc white 2 parts by weight, α, α′-bis (t-butylperoxy) diisopropylbenzene (trade name: Perkadox-14 / P40, manufactured by Kayaku Nouri Co., Ltd.) The composition consisting of parts is kneaded with a kneader at 110 ° C., and kneaded into a mold (18 × 300 × 300) in a press heated to 160 ° C. And heated under pressure for 50 minutes to obtain a foam.

得られた発泡体の見掛け密度は80kg/mであり、表面抵抗値を測定したところ3×10Ωであった。また、得られた発泡体について前記のUL94HBFの水平燃焼試験を行った結果、すべての要求を満たし合格した。 The apparent density of the obtained foam was 80 kg / m 3 , and when the surface resistance value was measured, it was 3 × 10 3 Ω. Moreover, as a result of conducting the horizontal combustion test of said UL94HBF about the obtained foam, all the requirements were satisfied and passed.

低密度ポリエチレン(商品名:ノバテックLC−520、密度0.9226 g/cm、メルトフローレート3.8g/10min、三菱化学株式会社製)100重量部と、ファーネス系カーボンブラック(商品名:ケッチェンブラックEC、三菱化学株式会社製)10重量部、メラミンシアヌレート20重量部、アゾジカルボンアミド(商品名:ビニホールAC#3、永和化成工業株式会社製)9重量部、α,α’−ビス(t−ブチルパーオキシ)ジイソプロピルベンゼン(商品名:パーカドックス−14/P40、化薬ヌーリー株式会社製)0.8重量部からなる組成物を110℃のニーダーにて混練し、140℃に加熱されたプレス内の金型(33×500×1025)に練和物を充填し、50分間加圧下で加熱後、発泡性架橋組成物を取り出した。 Low-density polyethylene (trade name: Novatec LC-520, density 0.9226 g / cm 3 , melt flow rate 3.8 g / 10 min, manufactured by Mitsubishi Chemical Corporation) and 100 parts by weight of furnace carbon black (trade name: Ketsu CHENBLACK EC, manufactured by Mitsubishi Chemical Corporation) 10 parts by weight, melamine cyanurate 20 parts by weight, azodicarbonamide (trade name: VINYHALL AC # 3, manufactured by Eiwa Kasei Kogyo Co., Ltd.) 9 parts by weight, α, α′-bis A composition comprising 0.8 parts by weight of (t-butylperoxy) diisopropylbenzene (trade name: Parkadox-14 / P40, manufactured by Kayaku Nouri Co., Ltd.) is kneaded with a 110 ° C. kneader and heated to 140 ° C. The mold (33 × 500 × 1025) in the pressed press is filled with the kneaded product, heated under pressure for 50 minutes, and then the foamable crosslinked composition is taken out. did.

次いで、該一次発泡体を加熱水蒸気の流路を周囲に設けた気密でない開閉式金属金型(90×1070×2130mm)の略中央に載置し、7.0kg/cmの加熱水蒸気を該流路に流して180分間加熱して残存する発泡剤及び架橋剤を分解して冷却後、発泡体を得た。 Next, the primary foam is placed in the approximate center of a non-airtight openable metal mold (90 × 1070 × 2130 mm) provided with a flow path of heated steam, and 7.0 kg / cm 2 of heated steam is added to the primary foam. The foam was obtained after flowing through the channel and heating for 180 minutes to decompose and cool the remaining foaming agent and crosslinking agent.

得られた発泡体の見掛け密度は60kg/mであり、表面抵抗値を測定したところ8×10Ωであった。また、得られた発泡体について前記のUL94HBFの水平燃焼試験を行った結果、すべての要求を満たし合格した。 The apparent density of the obtained foam was 60 kg / m 3 , and the measured surface resistance value was 8 × 10 3 Ω. Moreover, as a result of conducting the horizontal combustion test of said UL94HBF about the obtained foam, all the requirements were satisfied and passed.

低密度ポリエチレン(商品名:ノバテックLC−520、密度0.9226 g/cm、メルトフローレート3.8g/10min、三菱化学株式会社製)100重量部と、ファーネス系カーボンブラック(商品名:ケッチェンブラックEC、三菱化学株式会社製)16重量部、メラミンシアヌレート2重量部に変えた以外は、実施例1と同じ配合及び発泡条件で発泡体を得た。 Low-density polyethylene (trade name: Novatec LC-520, density 0.9226 g / cm 3 , melt flow rate 3.8 g / 10 min, manufactured by Mitsubishi Chemical Corporation) and 100 parts by weight of furnace carbon black (trade name: Ketsu A foam was obtained under the same formulation and foaming conditions as in Example 1 except that the amount was changed to 16 parts by weight (Chen Black EC, manufactured by Mitsubishi Chemical Corporation) and 2 parts by weight of melamine cyanurate.

得られた発泡体の見掛け密度55kg/mであり、表面抵抗値を測定したところ500Ωであった。また、得られた発泡体について前記のUL94HBFの水平燃焼試験を行った結果、すべての要求を満たし合格した。
比較例1
The apparent density of the obtained foam was 55 kg / m 3 , and the surface resistance value measured was 500Ω. Moreover, as a result of conducting the horizontal combustion test of said UL94HBF about the obtained foam, all the requirements were satisfied and passed.
Comparative Example 1

実施例1において、メラミンシアヌレートを1重量部に変えた以外は、実施例1と同じ配合及び発泡条件で発泡体を得、UL94HBFの水平燃焼試験を行った結果、不合格であった。
比較例2
In Example 1, except that melamine cyanurate was changed to 1 part by weight, a foam was obtained under the same composition and foaming conditions as in Example 1, and the result of a horizontal combustion test of UL94HBF was rejected.
Comparative Example 2

実施例1において、メラミンシアヌレートを40重量部に変えた以外は、実施例1と同じ配合及び発泡条件で発泡体を成形しようとしたが、難燃剤の添加部数が多すぎて満足な気泡体を得ることが出来なかった。
比較例3
In Example 1, except that the melamine cyanurate was changed to 40 parts by weight, an attempt was made to mold a foam with the same composition and foaming conditions as in Example 1, but there were too many flame retardants added and a satisfactory foam Could not get.
Comparative Example 3

実施例2において、メラミンシアヌレートを1重量部に変えた以外は、実施例1と同じ配合及び発泡条件で発泡体を得、UL94HBFの水平燃焼試験を行った結果、不合格であった。
比較例4
In Example 2, except that melamine cyanurate was changed to 1 part by weight, a foam was obtained with the same formulation and foaming conditions as in Example 1, and the result of a horizontal combustion test of UL94HBF was rejected.
Comparative Example 4

実施例2において、メラミンシアヌレートを40重量部に変えた以外は、実施例1と同じ配合及び発泡条件で発泡体を成形しようとしたが、難燃剤の添加部数が多すぎて満足な気泡体を得ることが出来なかった。 In Example 2, except that melamine cyanurate was changed to 40 parts by weight, an attempt was made to mold a foam with the same composition and foaming conditions as in Example 1, but there were too many flame retardants added and a satisfactory foam Could not get.

Figure 2005264005
Figure 2005264005

Figure 2005264005
Figure 2005264005

以上のように、本発明の方法によれば、難燃性、導電性に優れたノンハロゲン・ノンリンの導電性架橋ポリオレフィン系発泡体を製造できる。本発明の方法によって製造されたノンハロゲン・ノンリン難燃性導電性架橋ポリオレフィン系発泡体は、電子機器の緩衝材、電波吸収体等に適用できる
As described above, according to the method of the present invention, a non-halogen / non-phosphorus conductive cross-linked polyolefin-based foam excellent in flame retardancy and conductivity can be produced. The non-halogen / non-phosphorus flame-retardant conductive cross-linked polyolefin foam produced by the method of the present invention can be applied to a buffer material of an electronic device, a radio wave absorber, etc.

Claims (2)

ポリオレフィン系樹脂100重量部にメラミンシアヌレート2〜30重量部、導電性カーボン、発泡剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下に加熱した後、除圧し、発泡体を生成させることを特徴とする難燃性導電性架橋ポリオレフィン系発泡体の製造方法。 Adding and kneading 2 to 30 parts by weight of melamine cyanurate, conductive carbon, a foaming agent and a crosslinking agent to 100 parts by weight of a polyolefin-based resin, heating the resulting crosslinkable foamable composition under pressure, then depressurizing, A method for producing a flame-retardant conductive cross-linked polyolefin-based foam characterized by producing a foam. ポリオレフィン系樹脂100重量部にメラミンシアヌレート2〜30重量部、導電カーボン、発泡剤及び架橋剤を添加混練し、得られた架橋性発泡性組成物を加圧下で発泡剤が実質的に分解しない温度に加熱することによって、該組成物を架橋せしめ、次いで得られた架橋性発泡性組成物を金型から取り出して急激に発泡もしくは膨張させないように常圧下で加熱し、発泡剤させることを特徴とする難燃性導電性架橋ポリオレフィン系発泡体の製造方法。
Add and knead 2 to 30 parts by weight of melamine cyanurate, conductive carbon, foaming agent and crosslinking agent to 100 parts by weight of polyolefin resin, and the foaming agent does not substantially decompose under pressure in the resulting crosslinkable foamable composition. The composition is crosslinked by heating to a temperature, and then the resulting crosslinkable foamable composition is removed from the mold and heated under normal pressure so as not to expand or expand suddenly, thereby forming a foaming agent. A method for producing a flame-retardant conductive cross-linked polyolefin foam.
JP2004079461A 2004-03-19 2004-03-19 Method for producing flame retardant conductive cross-linked polyolefin foam Expired - Fee Related JP4774199B2 (en)

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JP2013053233A (en) * 2011-09-02 2013-03-21 Furukawa Electric Co Ltd:The Polyolefinic resin foam
KR101246677B1 (en) * 2010-11-30 2013-03-21 한국신발피혁연구소 Polymer foams with low hardness having an electrically conductivity
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KR101135429B1 (en) * 2010-08-13 2012-04-13 영보화학 주식회사 Manufacturing method of conductive form using carbon nano tube and conductive form
KR101246677B1 (en) * 2010-11-30 2013-03-21 한국신발피혁연구소 Polymer foams with low hardness having an electrically conductivity
JP2013053233A (en) * 2011-09-02 2013-03-21 Furukawa Electric Co Ltd:The Polyolefinic resin foam
EP3012287A4 (en) * 2013-06-21 2017-01-25 Kaneka Corporation Polypropylene resin foamed particles having excellent flame resistance and conductivity and polypropylene resin-type in-mold foam molded body
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