JP5294129B2 - Metallocene-ethylenepropylene diene copolymer rubber-based open cell body and method for producing the same - Google Patents

Metallocene-ethylenepropylene diene copolymer rubber-based open cell body and method for producing the same Download PDF

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JP5294129B2
JP5294129B2 JP2009520270A JP2009520270A JP5294129B2 JP 5294129 B2 JP5294129 B2 JP 5294129B2 JP 2009520270 A JP2009520270 A JP 2009520270A JP 2009520270 A JP2009520270 A JP 2009520270A JP 5294129 B2 JP5294129 B2 JP 5294129B2
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浩司 吉村
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Sanwa Kako Co Ltd
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Description

本発明は、メタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体及びその製造方法に関するものである。   The present invention relates to a metallocene-ethylenepropylenediene copolymer rubber-based open cell body and a method for producing the same.

周知の通り、エチレンプロピレンジエン共重合体ゴム(以下、「EPDM」ともいう。)系連続気泡体製品は、その優れたクッション性やシール性、防音性によりクッション材や断熱材、吸音材等として家電製品や自動車、建築等の用途に使用されている。また、ポリエチレン系連続気泡体は、断熱性、吸音性、耐薬品性に優れているため、エアコン内の断熱材、自動車のドアミラー内の吸音材、バクテリアの担体、塗布材等の各種用途に広く利用されている。
また、重合触媒としてメタロセン化合物を用いて得られたポリエチレン系樹脂に、4,4’−オキシビス(ベンゼンスルホニルヒドラジド)を添加した発泡性組成物を整形し、次いで常圧下で加熱発泡して発泡体を成形し、該発泡体に機械的変形を加えて気泡を連通化するメタロセン系ポリエチレン連続気泡体の製造方法が提案されている(日本国特開2001−226511号公報参照)。
しかしながら、前記EPDM系連続気泡体は表面ブルーム(析出現象)が発生しやすく、耐油、耐屈曲げ裂性が悪く、架橋剤に有機過酸化物を使用し、2−メルカプトベンズイミダゾール系スコーチ防止剤を使用するEPDM発泡体にあっては、架橋調整が難しく、独立気泡が連続気泡に成りにくいという問題点があった。また、前記ポリエチレン系連続気泡体は、EPDM系連続気泡体に比べて柔軟性、弾力性、圧縮時の回復性に劣るという問題点があった。
また、前記メタロセン系ポリエチレン連続気泡体は、発泡剤に4,4’−オキシビス(ベンゼンスルホニルヒドラジド)を使用する必要があり、厚みのある発泡体が得られないという問題点があった。
そこで、本発明は、有機過酸化物による架橋に適したメタロセン系ポリエチレン樹脂と柔軟性、回復性に優れているエチレンプロピレンジエン共重合体ゴムとを混合した組成物を必須成分として発泡すれば、架橋と発泡とのバランスがとれ、メタロセン系ポリエチレン樹脂とエチレンプロピレンジエン共重合体ゴムが各々単独に有している連続気泡体の問題点を克服してスコーチのない柔軟性、回復性に優れる連続気泡体を得ることができるという刮目すべき知見を得、当該技術的課題を達成したものである。
As is well known, an ethylene propylene diene copolymer rubber (hereinafter also referred to as “EPDM”) type open cell product is used as a cushioning material, heat insulating material, sound absorbing material, etc. due to its excellent cushioning properties, sealing properties, and soundproofing properties. It is used for home appliances, automobiles, buildings, and other applications. In addition, polyethylene-based open cells are excellent in heat insulation, sound absorption, and chemical resistance, so they are widely used in various applications such as heat insulation materials in air conditioners, sound absorption materials in automobile door mirrors, bacteria carriers, and coating materials. It's being used.
Further, a foamed composition obtained by adding 4,4′-oxybis (benzenesulfonylhydrazide) to a polyethylene resin obtained using a metallocene compound as a polymerization catalyst is shaped, and then foamed by heating and foaming under normal pressure. A process for producing a metallocene polyethylene open-celled body is proposed in which the foam is subjected to mechanical deformation to make the bubbles communicate with each other (see Japanese Patent Application Laid-Open No. 2001-226511).
However, the above-mentioned EPDM-based open cell body is prone to surface bloom (precipitation phenomenon), has poor oil resistance and bending crack resistance, uses an organic peroxide as a cross-linking agent, and a 2-mercaptobenzimidazole-based scorch inhibitor. In the case of EPDM foams using the above, there is a problem that it is difficult to adjust the cross-linking, and the closed cells are difficult to become open cells. Further, the polyethylene-based open cell body has a problem that it is inferior in flexibility, elasticity, and recoverability at the time of compression compared to the EPDM open-cell body.
In addition, the metallocene polyethylene open-cell body has a problem that it is necessary to use 4,4′-oxybis (benzenesulfonylhydrazide) as a foaming agent, and a foam having a thickness cannot be obtained.
Therefore, the present invention is to foam a composition comprising a metallocene polyethylene resin suitable for crosslinking with an organic peroxide and an ethylene propylene diene copolymer rubber excellent in flexibility and recoverability as an essential component. A continuous structure that balances crosslinking and foaming, and overcomes the problems of open-cell bodies that each of the metallocene polyethylene resin and the ethylene propylene diene copolymer rubber has independently. The remarkable knowledge that a foam can be obtained has been obtained, and the technical problem has been achieved.

本発明に係るメタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体は、メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部とからなる組成物100重量部に対してポリエチレン樹脂(メタロセン系ポリエチレン樹脂を除く)及び/又は酢酸ビニル樹脂を0〜40重量部及び充填剤を20〜150重量部配合した組成物を加熱発泡させて独立気泡を形成した後当該独立気泡を連通化した連続気泡を形成してなる見掛け密度84〜89kg/m のメタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体である。
また、本発明に係るメタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体の製造方法は、メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部とからなる組成物100重量部に対してポリエチレン樹脂(メタロセン系ポリエチレン樹脂を除く)及び/又は酢酸ビニル樹脂を0〜40重量部及び充填剤を20〜150重量部配合した組成物に有機過酸化物、発泡剤、発泡助剤、軟化剤及び充填剤を添加し、次いで、プレス中の金型に充填して加圧下で加熱し、さらに、常圧にて発泡させた後当該気泡を連続化するものである。
本発明によれば、メタロセン系ポリエチレン樹脂とエチレンプロピレンジエン共重合体ゴムとを混合した組成物を必須成分とし、該組成物に充填剤を添加した混和物を発泡させたので、架橋と発泡とのバランスがとれ、スコーチのない柔軟性、回復性に優れる連続気泡体を得ることができる。
The metallocene-ethylenepropylene diene copolymer rubber open-cell body according to the present invention is composed of 100 parts by weight of a composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of ethylene propylene diene copolymer rubber. On the other hand, a composition containing 0 to 40 parts by weight of a polyethylene resin (excluding a metallocene polyethylene resin) and / or vinyl acetate resin and 20 to 150 parts by weight of a filler is heated and foamed to form closed cells, which are then independent. It is a metallocene-ethylenepropylene diene copolymer rubber-based open cell having an apparent density of 84 to 89 kg / m 3 formed by forming open cells in which bubbles are connected .
The metallocene-ethylenepropylene diene copolymer rubber-based open cell manufacturing method according to the present invention comprises a composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of an ethylene propylene diene copolymer rubber. Organic peroxide and foaming agent in a composition in which 0 to 40 parts by weight of polyethylene resin (excluding metallocene polyethylene resin) and / or vinyl acetate resin and 20 to 150 parts by weight of filler are blended with 100 parts by weight of the product , Adding foaming aids, softeners and fillers, then filling the mold during pressing, heating under pressure, and further foaming at normal pressure and then making the bubbles continuous .
According to the present invention, the composition in which the metallocene-based polyethylene resin and the ethylene propylene diene copolymer rubber are mixed is an essential component, and the mixture obtained by adding a filler to the composition is foamed. Can be obtained, and an open cell body excellent in flexibility and recoverability without scorch can be obtained.

実施の形態1.
本実施の形態に係るメタロセン−EPDM系連続気泡体は、メタロセン系ポリエチレン樹脂30〜70重量部とEPDM70〜30重量部とからなる組成物を必須成分とし、当該組成物に有機過酸化物、発泡剤、発泡助剤、軟化剤及び充填剤を添加してなる混和物を加熱発泡させ、生成した気泡を連続させたものである。
メタロセン系ポリエチレン樹脂とEPDMとの配合割合はメタロセン系ポリエチレン樹脂30〜70重量部に対してEPDM70〜30重量部とするのが良く、さらに好ましいのはメタロセン系ポリエチレン樹脂40〜60重量部に対してEPDM60〜40重量部である。
前記メタロセン系ポリエチレン樹脂は、重合触媒としてメタロセン化合物を用いて得られたポリエチレン系樹脂である。
前記EPDMには、第3成分としてエチリデンノルボルネン、1,4−ヘキサジエン及びジクロペンタジエン等があるが、特に限定されない。
また、さらに必須成分組成物100重量部に対して通常のポリエチレン樹脂(LDPE)及び酢酸ビニル樹脂(EVA)から選ばれる少なくとも一種を0〜40重量部配合してもよい。40重量部以下の添加量であれば、発泡体の柔軟性及び回復性に優れ、40重量部を超えて添加すれば、発泡体の柔軟性及び回復性に悪影響を与えるので好ましくない。
前記有機過酸化物は、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若しくは分子内に架橋結合を生じさせるラジカル発生剤としての有機過酸化物を用いる。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−3,3,5−トリメチルシクロヘキサン、2,5−ジメチル−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−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、及び、ターシャリーブチルパーオキシベンゾエート等を使用することができる。
前記発泡剤としては、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のアゾ系化合物や、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のニトロソ系化合物や、p,p’−オキシビスベンゼンスルホニルヒドラジット等のヒドラジット系化合物や、p,p’−オキシビスベンゼンスルホニルセミカルバジット、トリエンスルホニルセミカルバジット等のスルホニルセミカルバジット系化合物等を使用すればよい。
前記発泡助剤としては、尿素を主成分とする化合物、酸化亜鉛や酸化鉛等の金属酸化物、サリチル酸やステアリン酸等を主成分とする化合物、即ち、高級脂肪酸或いは高級脂肪酸の金属化合物を用いればよく、当該発泡助剤を発泡剤の種類に応じて添加すればよい。
前記軟化剤は、プロセスオイル、可塑剤、パラフィンワックス、流動性パラフィン等のゴムとの相溶性が良いものを使用すればよい。
前記充填剤としては、クレー、タルク、酸化チタン、水酸化アルミニウム、水酸化マグネシウム、炭酸カルシウム、シリカ、その他、常用のゴム配合剤等を用いればよい。当該充填剤を必要に応じて添加すればよく、充填剤の添加量は、メタロセン系ポリエチレン樹脂とEPDMとからなる組成物100重量部に対して20〜150重量部とするのが好ましい。充填剤の添加量が150重量部を超える場合には、発泡成形が阻害され、満足な発泡体が得られないので好ましくなく、20重量部未満の添加量では出来高が少なすぎてコスト的に合わないので好ましくない。さらに好ましくは30〜80重量部である。
実施の形態2.
本実施の形態に係るメタロセン−EPDM系連続気泡体の製造方法は、メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部とからなる組成物に有機過酸化物、発泡剤、発泡助剤、軟化剤及び充填剤を添加して混和物とし、次いで、当該混和物をプレス中の金型に充填して加圧下で加熱し、さらに、常圧にて発泡させた後、当該気泡を機械的に連続化する。
前記製造方法は、用いた有機過酸化物や発泡剤等の発泡温度や架橋開始温度等により、公知の発泡方法及び適宜の発泡条件にて行うことができ、特に好適な製造方法を具体的に説明する。
メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部からなる組成物に充填剤30〜80重量部とその外、ポリエチレン樹脂、酢酸ビニル樹脂、有機過酸化物、軟化剤、発泡剤、発泡助剤を添加して混和物とし、当該混和物をミキシングロール、加圧式ニーダー、押出機等によって練和する。次いで、得られた発泡性樹脂組成物をプレス中の金型に充填し、一定時間加圧下に115〜150℃で加熱し、発泡剤を一部分解し、発泡倍率1.00〜1.05の中間発泡体を生成させる。次いで、該中間発泡体を常圧下にて密閉系でない直方体型などの所望の形状の型内に入れ、140〜180℃で加熱し、有機過酸化物及び発泡剤を完全に分解させて発泡体を得る。
そして、前記発泡体(独立気泡体)を例えば等速二本ロール等により圧縮変形して気泡膜を破壊することにより、機械的に気泡を連通化して連続気泡体を得る。なお、等速二本ロールの表面に無数の小さい針を設けるか、又は等速二本ロールの前及び/又は後に無数の小さい針を設けたロールを配置して、独立気泡体の表面に無数の小孔を開けるようにすれば、気泡の連通化を促進させることができる。
Embodiment 1 FIG.
The metallocene-EPDM open-cell body according to the present embodiment has a composition composed of 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of EPDM as an essential component, and an organic peroxide or foam is added to the composition. A mixture obtained by adding an agent, a foaming aid, a softening agent and a filler is heated and foamed, and the generated bubbles are made continuous.
The blending ratio of the metallocene polyethylene resin and EPDM is preferably 70 to 30 parts by weight of EPDM with respect to 30 to 70 parts by weight of the metallocene polyethylene resin, more preferably 40 to 60 parts by weight of the metallocene polyethylene resin. EPDM is 60 to 40 parts by weight.
The metallocene polyethylene resin is a polyethylene resin obtained using a metallocene compound as a polymerization catalyst.
The EPDM includes ethylidene norbornene, 1,4-hexadiene, dichloropentadiene and the like as the third component, but is not particularly limited.
Furthermore, 0 to 40 parts by weight of at least one selected from ordinary polyethylene resin (LDPE) and vinyl acetate resin (EVA) may be blended with 100 parts by weight of the essential component composition. If the amount is 40 parts by weight or less, the flexibility and recoverability of the foam is excellent, and if it exceeds 40 parts by weight, the flexibility and recoverability of the foam will be adversely affected.
The organic peroxide is decomposed by heating to generate an organic radical as a radical generator that generates free radicals and generates crosslinks between or within the molecules. For example, dicumyl peroxide, 1,1-ditertiary butyl peroxide, 1,1-ditertiary butyl peroxy-3,3,5-trimethylcyclohexane, 2,5-dimethyl-2,5-ditertiary butyl peroxide Oxyhexane, 2,5-dimethyl-2,5-ditertiary butyl peroxyhexine, α, α-ditertiary butyl peroxyisopropylbenzene, tertiary butyl peroxyketone, tertiary butyl peroxybenzoate, etc. Can be used.
Examples of the foaming agent include azo compounds such as azodicarbonamide and barium azodicarboxylate, nitroso compounds such as dinitrosopentamethylenetetramine and trinitrotrimethyltriamine, and p, p′-oxybisbenzenesulfonyl hydragit. Etc., and sulfonyl semicarbadidate compounds such as p, p′-oxybisbenzenesulfonyl semicarbadiate and trienesulfonyl semicarbadi may be used.
As the foaming aid, a compound containing urea as a main component, a metal oxide such as zinc oxide or lead oxide, a compound containing salicylic acid or stearic acid as a main component, that is, a higher fatty acid or a higher fatty acid metal compound is used. What is necessary is just to add the said foaming adjuvant according to the kind of foaming agent.
As the softening agent, those having good compatibility with rubber such as process oil, plasticizer, paraffin wax, and fluid paraffin may be used.
As the filler, clay, talc, titanium oxide, aluminum hydroxide, magnesium hydroxide, calcium carbonate, silica, and other conventional rubber compounding agents may be used. What is necessary is just to add the said filler as needed, and it is preferable that the addition amount of a filler shall be 20-150 weight part with respect to 100 weight part of compositions which consist of a metallocene polyethylene resin and EPDM. When the added amount of the filler exceeds 150 parts by weight, the foam molding is hindered and a satisfactory foam cannot be obtained. This is not preferable, and the added amount of less than 20 parts by weight is too small to meet the cost. Since it is not, it is not preferable. More preferably, it is 30-80 weight part.
Embodiment 2. FIG.
The method for producing a metallocene-EPDM open cell body according to the present embodiment includes an organic peroxide in a composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of ethylene propylene diene copolymer rubber. , Adding a foaming agent, a foaming aid, a softening agent and a filler to make a mixture, then filling the mixture in a mold in a press and heating under pressure, and further foaming at normal pressure After that, the bubbles are mechanically continuous.
The production method can be carried out under a known foaming method and appropriate foaming conditions depending on the foaming temperature, crosslinking initiation temperature, etc. of the organic peroxide and foaming agent used, and a particularly suitable production method is specifically described. explain.
A composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of an ethylene propylene diene copolymer rubber, and 30 to 80 parts by weight of a filler, in addition, a polyethylene resin, a vinyl acetate resin, an organic peroxide, A softener, a foaming agent, and a foaming aid are added to form a blend, and the blend is kneaded by a mixing roll, a pressure kneader, an extruder, or the like. Next, the obtained foamable resin composition is filled in a mold during pressing, heated at 115 to 150 ° C. under pressure for a certain period of time, partially decomposes the foaming agent, and has an expansion ratio of 1.00 to 1.05. An intermediate foam is produced. Next, the intermediate foam is put in a mold having a desired shape such as a rectangular parallelepiped mold which is not a closed system under normal pressure, and heated at 140 to 180 ° C. to completely decompose the organic peroxide and the foaming agent, thereby obtaining a foam. Get.
Then, the foam (closed cell) is compressed and deformed by, for example, a constant-velocity two-roll to break the bubble film, thereby mechanically connecting the bubbles to obtain an open cell. An infinite number of small needles are provided on the surface of the constant-velocity two-roll, or a roll provided with innumerable small needles is arranged before and / or after the constant-speed two-roll, and the surface of the closed cell body is innumerable. If the small holes are opened, the communication of bubbles can be promoted.

実施例1〜13、比較例1〜9
メタロセン系ポリエチレン樹脂としてアフィニティーEG8150(商品名:密度:0.868g/cm、MFR:0.5g/10分、ダウケミカル日本株式会社製)及びアフィニティーEG8200(商品名:密度:0.870g/cm、MFR:5.0g/10分:ダウケミカル日本株式会社製)と、EPDM樹脂としてエスプレン514F(商品名:ムーニー粘度:35ML(1+4)100℃、エチレン含有:70%、ジエン含有:5.5%、住友化学株式会社製)とを表1(実施例)及び表2(比較例)に示す配合割合にて各組成物を得、該各組成物にポリエチレン樹脂としてYF−30(商品名:低密度ポリエチレン、密度:0.920g/cm、MFR:1.1g/10分、日本ポリエチレン株式会社製)、酢酸ビニル樹脂としてLV540(商品名:エチレン−酢酸ビニル共重合体、密度:0.942g/cm、MFR:2.5g/10分:日本ポリエチレン株式会社製)、有機過酸化物としてジクミルパーオキサイド、軟化剤としてプロセスオイル、充填剤としてタルク、発泡剤としてアゾジカルボンアミド及び発泡助剤として酸化亜鉛を表1及び表2に示す配合割合にて添加して各混和物を得、当該各混和物を130℃に加熱されたプレス内の金型(32×160×160mm)に充填し、100kg/cmの圧力で80分間加熱し、各中間発泡体(32×160×160mm)を生成した。
次いで、前記中間発泡体を気密でない金型(90×300×300mm)の略中央に載置し、160℃で180分間加熱して取り出し、各発泡体(90×300×300mm)を得た(実施例1〜13、比較例2,3,5〜8)。
得られた各発泡体をロール間隔20mmに設定した等速二本ロールの間を5回通過させて気泡膜を破壊させ、気泡を連通化させて各連続気泡体(実施例1〜13、比較例2,3,5〜8)を得た。
得られた各連続気泡体の見掛け密度と圧縮応力と圧縮永久歪を表3(実施例)及び表4(比較例)に示す。
表3及び表4によれば、実施例1〜13の連続気泡体は、柔軟性、弾力性、回復性に優れていることを確認できた。比較例1,4及び9 ではスコーチがひどく、満足な発泡体を得ることができなかった。比較例2,3,5〜8では発泡体は得られたが、柔軟性、回復性に劣っていた。なお、気泡体の見掛け密度、引張強度、伸び、圧縮応力及び圧縮永久歪の物性はJIS K6767に準拠して測定した。また、圧縮応力(25%)5kPa未満のものが柔軟性に優れ、圧縮永久歪(24hr)5%未満のものが回復性に優れていた。
比較例10
エチレン−酢酸ビニル共重合体(LV540:商品名)50重量部及びメタロセン系ポリエチレン樹脂(KS240:商品名:密度:0.880g/cm、MFR:2.2g/10分:日本ポリエチレン株式会社製)50重量部からなる組成物にジクミルパーオキサイド0.7重量部とアゾジカルボンアミド9.5重量部とを添加して得られる従来発泡体LC−150G(商品名:三和化工株式会社製)は、見掛け密度50kg/m、引張強度0.17MPa、伸び300%、10%圧縮応力3kPa,25%圧縮応力5kPa,50%圧縮応力8kPa、30min圧縮永久歪5.6%,24hr圧縮永久歪2.9%であった。
本発明における発泡倍率は約11倍(見掛け密度84〜89kg/m)であるから、前記従来発泡体が本発明における柔軟性と同等の柔軟性を得るには、20倍(見掛け密度50kg/m:計算式:樹脂密度÷見掛け密度×1000)の発泡倍率が必要になることを確認できた。
本発明によれば、メタロセン系ポリエチレン樹脂とエチレンプロピレンジエン共重合体ゴム(EPDM)をブレンドした連続気泡体を得ることができ、当該メタロセン−EPDM樹脂系連続気泡体は、柔軟性、弾力性、回復性に優れているから、クッション材や断熱材、吸音材等の用途に適用できる。
Examples 1-13, Comparative Examples 1-9
Affinity EG8150 (trade name: density: 0.868 g / cm 3 , MFR: 0.5 g / 10 min, manufactured by Dow Chemical Japan Co., Ltd.) and affinity EG8200 (trade name: density: 0.870 g / cm) as metallocene polyethylene resins 3 , MFR: 5.0 g / 10 min: manufactured by Dow Chemical Japan Co., Ltd., and Esprene 514F (trade name: Mooney viscosity: 35 ML (1 + 4) 100 ° C., ethylene content: 70%, diene content: 5. 5%, manufactured by Sumitomo Chemical Co., Ltd.) was obtained at a blending ratio shown in Table 1 (Example) and Table 2 (Comparative Example), and YF-30 (trade name) was used as the polyethylene resin in each composition. : low density polyethylene, density: 0.920g / cm 3, MFR: 1.1g / 10 minutes, manufactured by Japan polyethylene Corporation), acetic bi LV540 as Le resin (trade name: ethylene - vinyl acetate copolymer, density: 0.942g / cm 3, MFR: 2.5g / 10 min: manufactured by Japan Polyethylene Corporation), dicumyl peroxide as the organic peroxide , Process oil as a softening agent, talc as a filler, azodicarbonamide as a foaming agent, and zinc oxide as a foaming aid are added at the blending ratios shown in Tables 1 and 2 to obtain respective blends. Was filled in a mold (32 × 160 × 160 mm) in a press heated to 130 ° C., and heated at a pressure of 100 kg / cm 2 for 80 minutes to produce each intermediate foam (32 × 160 × 160 mm).
Next, the intermediate foam was placed in the approximate center of a non-airtight mold (90 × 300 × 300 mm), and was taken out by heating at 160 ° C. for 180 minutes to obtain each foam (90 × 300 × 300 mm) ( Examples 1 to 13, Comparative Examples 2, 3, 5 to 8).
Each foam obtained was passed 5 times between two constant-velocity rolls set at a roll interval of 20 mm to break the bubble film, and the bubbles were connected to each open cell (Examples 1 to 13, comparison). Examples 2, 3, 5-8) were obtained.
Table 3 (Example) and Table 4 (Comparative Example) show the apparent density, compressive stress, and compression set of each open cell body obtained.
According to Table 3 and Table 4, it has confirmed that the open-cell body of Examples 1-13 was excellent in a softness | flexibility, elasticity, and recoverability. In Comparative Examples 1, 4 and 9, the scorch was so bad that a satisfactory foam could not be obtained. In Comparative Examples 2, 3, 5 to 8, foams were obtained, but the flexibility and recoverability were poor. The apparent density, tensile strength, elongation, compression stress and compression set of the foam were measured according to JIS K6767. Also, those having a compression stress (25%) of less than 5 kPa were excellent in flexibility, and those having a compression set (24 hr) of less than 5% were excellent in recoverability.
Comparative Example 10
50 parts by weight of an ethylene-vinyl acetate copolymer (LV540: trade name) and a metallocene polyethylene resin (KS240: trade name: density: 0.880 g / cm 3 , MFR: 2.2 g / 10 minutes: manufactured by Nippon Polyethylene Co., Ltd.) ) Conventional foam LC-150G obtained by adding 0.7 parts by weight of dicumyl peroxide and 9.5 parts by weight of azodicarbonamide to a composition comprising 50 parts by weight (trade name: manufactured by Sanwa Kako Co., Ltd.) ), Apparent density 50 kg / m 3 , tensile strength 0.17 MPa, elongation 300%, 10% compression stress 3 kPa, 25% compression stress 5 kPa, 50% compression stress 8 kPa, 30 min compression set 5.6%, 24 hr compression permanent The strain was 2.9%.
Since the expansion ratio in the present invention is about 11 times (apparent density 84 to 89 kg / m 3 ), in order for the conventional foam to obtain the same flexibility as that in the present invention, 20 times (apparent density 50 kg / m). It was confirmed that an expansion ratio of m 3 : calculation formula: resin density ÷ apparent density × 1000) was required.
According to the present invention, an open cell body obtained by blending a metallocene-based polyethylene resin and an ethylene propylene diene copolymer rubber (EPDM) can be obtained, and the metallocene-EPDM resin-based open cell body has flexibility, elasticity, Since it has excellent recoverability, it can be applied to uses such as cushioning materials, heat insulating materials, and sound absorbing materials.

Claims (2)

メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部とからなる組成物100重量部に対してポリエチレン樹脂(メタロセン系ポリエチレン樹脂を除く)及び/又は酢酸ビニル樹脂を0〜40重量部及び充填剤を20〜150重量部配合した組成物を加熱発泡させて独立気泡を形成した後当該独立気泡を連通化した連続気泡を形成してなる見掛け密度84〜89kg/mのメタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体。 A polyethylene resin (excluding a metallocene polyethylene resin) and / or a vinyl acetate resin is added to 100 parts by weight of a composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of an ethylene propylene diene copolymer rubber. An apparent density of 84 to 89 kg / m is formed by heating and foaming a composition containing 0 to 40 parts by weight of a filler and 20 to 150 parts by weight of a filler to form closed cells and then forming open cells that communicate with the closed cells. 3. Metallocene-ethylene propylene diene copolymer rubber-based open cell body. メタロセン系ポリエチレン樹脂30〜70重量部とエチレンプロピレンジエン共重合体ゴム70〜30重量部とからなる組成物100重量部に対してポリエチレン樹脂(メタロセン系ポリエチレン樹脂を除く)及び/又は酢酸ビニル樹脂を0〜40重量部及び充填剤を20〜150重量部配合した組成物に有機過酸化物、発泡剤、発泡助剤、軟化剤及び充填剤を添加し、次いで、プレス中の金型に充填して加圧下で加熱し、さらに、常圧にて発泡させた後当該気泡を連続化することを特徴とするメタロセン−エチレンプロピレンジエン共重合体ゴム系連続気泡体の製造方法。 A polyethylene resin (excluding a metallocene polyethylene resin) and / or a vinyl acetate resin is added to 100 parts by weight of a composition comprising 30 to 70 parts by weight of a metallocene polyethylene resin and 70 to 30 parts by weight of an ethylene propylene diene copolymer rubber. An organic peroxide, a foaming agent, a foaming aid, a softening agent and a filler are added to a composition containing 0 to 40 parts by weight and 20 to 150 parts by weight of a filler, and then filled into a mold during pressing. A method for producing a metallocene-ethylenepropylene diene copolymer rubber-based open cell body, characterized by heating under pressure and further foaming at normal pressure and then making the bubbles continuous.
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