JP4238418B2 - Olefin resin foam and method for producing the same - Google Patents

Olefin resin foam and method for producing the same Download PDF

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Publication number
JP4238418B2
JP4238418B2 JP15581099A JP15581099A JP4238418B2 JP 4238418 B2 JP4238418 B2 JP 4238418B2 JP 15581099 A JP15581099 A JP 15581099A JP 15581099 A JP15581099 A JP 15581099A JP 4238418 B2 JP4238418 B2 JP 4238418B2
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weight
foam
resin foam
olefin resin
olefin
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JP2000344923A (en
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基 内藤
宗暁 塚田
史朗 今井
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Toray Industries Inc
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Toray Industries Inc
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Description

【0001】
【発明の属する技術分野】
本発明はオレフィン系樹脂発泡体、特にポリエチレン系樹脂発泡体を製造する際のシート成形時に安定剤のブリードアウトの弊害がなく、また、発泡時の耐熱安定性不足のために発泡温度を一定限界以上に上げることができないという問題を解消でき、さらに、着色がなく長期耐熱安定性にも優れたオレフィン系樹脂発泡体に関するものである。
【0002】
【従来の技術】
オレフィン系樹脂発泡体は、優れたクッション性、緩衝性、耐水性、化学的性質を有することから、クーラー等電化製品の断熱材、高級製品の包装緩衝材、容器のパッキン、粘着テープ、或いは長尺屋根用断熱材、或いは、パイプ形状に加工して調理機器の配管断熱材等幅広く使用されてきている。かかるオレフィン系樹脂発泡体、特にポリエチレン系樹脂発泡体の製造に際しては、一般的に加工時の熱或いは機械的せん断力による熱劣化を防止するため熱安定剤として酸化防止剤が添加されてきている。かかる酸化防止剤としては、その機能面からラジカル連鎖禁止剤と過酸化物分解物とに大別され、長期熱安定性の観点から両者を併用して用いられてきた。
【0003】
【発明が解決しようとする課題】
上述のごとくオレフィン系樹脂発泡体の製造においても、熱安定剤を適用してきているが、シート化時に該熱安定剤がブリードアウトし搬送ロールに付着、ロールを汚すばかりでなく、その付着物に起因してへこみ欠点が発生する問題があった。更に電子線で架橋させる場合、電子線でその安定剤が変成し、所期効果を多くの熱を受ける発泡工程で十分に発揮させることが出来ず、発泡温度を一定限界以上には上げることが出来ない、また、温度を上げると特に端部に熱焼けが生じ着色するといった問題があった。また、上記の多岐に渡る用途分野において種々の加工が施され製品化されるが、熱を受ける場合、耐熱性に劣り成形不良が多くなったり、長期熱安定性に欠けるという欠点があった。
【0004】
本発明は、かかる発泡体の耐熱性を改良し、シート化時のブリードアウト問題を解消し、高温発泡時にも熱焼けすることがなく、着色がなく、長期耐熱性にも優れた発泡体を提供することを目的とする。
【0005】
【課題を解決するための手段】
本発明は、前記課題を達成するため、独立気泡を有するオレフィン系樹脂発泡体であって、融点150℃以上のヒンダードフェノール系酸化防止剤を0.05〜1.0重量%含有するオレフィン系樹脂発泡体からなる。
また、本発明は、独立気泡を有するオレフィン系樹脂発泡体であって、融点150℃以上のヒンダードフェノール系酸化防止剤(A)を0.05〜1.0重量%、及び、分子量500以上のチオエーテル系酸化防止剤(B)を0.05〜1.0重量%含有し、かつ(B)/(A)の比率が0.5〜2.0であるオレフィン系樹脂発泡体からなる。
【0006】
【発明の実施の形態】
以下に本発明の詳細を説明する。
本発明のオレフィン系樹脂発泡体を構成するオレフィン系樹脂としては、ポリエチレン系樹脂単独、ポリエチレン系樹脂に、酢酸ビニルやエチレン・エチルアクリレート等を共重合したポリエチレン系樹脂を配合したポリエスチレン系混合樹脂、あるいは、ポリプロピレン系樹脂単独、ポリプロピレン系樹脂とポリエチレン系樹脂との混合樹脂が例示される。
【0007】
ポリエチレン系樹脂としては、低圧法、中圧法、高圧法により製造された密度0.90〜0.965g/cm3のポリエチレン樹脂、エチレンにブテン、ペンテン、ヘキセン、オクテン、4−メチルペンテン等のαオレフィンが共重合された直鎖状ポリエチレン系樹脂、線状超低密度ポリエチレン、エチレン−酢酸ビニル共重合体、エチレン−エチルアクリレート共重合体等を例示することができる。これらのポリエチレン系樹脂は、そのぞれ単独で用いられてもよいし、2種類以上混合して用いられてもよい。
【0008】
ポリプロピレン系樹脂としては、プロピレンの単独重合体、エチレンやブテン等のαオレフィンとプロピレンとのブロック共重合体、ランダム共重合体、ランダム−ブロック共重合体等を例示することができる。これらのポリプロピレン系樹脂は、そのぞれ単独で用いられてもよいし、2種類以上混合して用いられてもよい。
本発明に用いられるオレフィン系樹脂の好適な用例としては、特に耐寒性が良好なことから、前記ポリエチレン系樹脂からなる発泡体が好ましい。
【0009】
本発明に用いるオレフィン系樹脂発泡体は、耐熱性の改良のために、融点150℃以上のヒンダードフェノール系酸化酸化防止剤を、オレフィン系樹脂に対し0.05〜1.0重量%含有させることが必要である。
【0010】
かかる融点150℃以上のヒンダードフェノール系酸化防止剤としては、1,1,3−トリス(2−メチル−4−ヒドロキシ−5−t−ブチルフェニル)ブタン(融点:186℃)、1,1−ビス(2−メチル−4−ヒドロキシ−5−t−ブチルフェニル)ブタン(融点:210℃)、1,3,5−トリメチル−2,4,6−トリス(3,5−ジ−t−ブチル−4−ヒドロキシベンジル)ベンゼン(融点:244℃)などの分子骨格が炭素、水素のみからなる構造のものを好ましく挙げることができる。これらは、いずれもポリオレフィン等衛生協議会のポジティブリストに登録されており、近年注目される安全性にも優れたものである。
【0011】
かかるヒンダードフェノール系酸化防止剤の発泡体中含有量は、オレフィン系樹脂に対し0.05〜1.0重量%の量が必要である。0.05重量%未満であれは、本発明の目的とする効果が発現困難である。また、1.0重量%を越えて増量しても増量した効果は殆どないので不必要である。
【0012】
また、分子量500以上のチオエーテル系酸化防止剤としては、ジドデシル チオジプロピオネート(分子量:517)、ジテトラデシル チオジプロピオネート(分子量:571)、ジオクタデシル チオジプロピオネート(分子量:683)、ペンタエチリトールテトラキス 3−ドデシルチオプロピオネート(分子量1162)等が挙げられるが、中でもジオクタデシル チオジプロピオネートが好ましい。かかるチオエーテル系酸化防止剤の発泡体中の含有量は、オレフィン系樹脂に対し0.05〜1.0重量%が好ましい。
【0013】
本発明においては、ヒンダードフェノール系酸化防止剤単独でも十分本発明の効果が発現されるが、チオエーテル系酸化防止剤と併用することにより、長期熱安定性がさらに高まるので好ましい。かかるチオエーテル系酸化防止剤の含有量が1.0重量%を越えると発泡体製造時にブリードアウトしやすく、製造工程中のロールに転写し、汚れ欠点等を生じやすくなるので好ましくない。なお、ヒンダードフェノール系抗酸化剤(A)とチオ系抗酸化剤(B)の混合割合(B)/(A)としては、0.5〜2.0の範囲が好ましい。
【0014】
本発明のオレフィン系樹脂発泡体は、上記樹脂に発泡剤、顔料等の添加剤、及び上述のヒンダードフェノール系酸化防止剤、或いはさらにチオエーテル系酸化防止剤とを併用するかたちで、所定量混合し、押出機でシート状に押出し、電子線で架橋した後、前記発泡剤を発泡させることにより、所望の形状の発泡体を製造することができる。発泡剤としては、例えばアゾジカルボンアミド等の熱分解型発泡剤を用いることができる。
【0015】
なお、発泡に先立って、或いは発泡と同時に、ポリオレフィン系樹脂を電離性放射線架橋法、ジクミルパーオキサイド等の過酸化物を用いた化学架橋法、または、ビルニメトキシシラン等を用いシラノール縮合させるいわゆるシラン架橋法、或いは、紫外線照射による紫外線架橋等の手段により架橋させることができるが、電子線照射による架橋法が工程管理の容易さの点から望ましい。
なお、架橋性のために、適宜、ジビニルヘンゼン、ジアリルフタレート、ヒドロキノンジメタクリレート等を架橋助剤として樹脂組成物中に配合して使用してもよい。
【0016】
本発明のオレフィン系樹脂発泡体の見掛け密度は、使用目的に合わせ適宜選択することができるが、各種パッキンとして用いる場合、特に0.05〜0.25g/cm3の範囲が強度面、取扱い上の点で好ましい。見掛け密度が小さい場合には、発泡体の強度が小さくなり、かかる目的とする用途には使い勝手が良好とは言い難く、適宜引張強度との兼ね合いで密度、言い換えれば発泡倍率を選定すればよい。
【0017】
なお、発泡体の厚みとしては、0.2〜5mmの範囲のものが好ましく用いられるが、特に限定されたものではなく、使用態様に応じ適宜設定すればよい。
本発明のオレフィン系樹脂発泡体の気泡構造は高い剪断強度が得られることから独立気泡構造であり、かかる独立気泡構造を有する発泡体は、熱分解型発泡剤を用いる上述の方法で製造することができる。
【0018】
【実施例】
以下実施例によって本発明を詳細に説明する。
なお、オレフィン系樹脂発泡体の特性はJIS K6767に準拠し測定したものである。
【0019】
[実施例1、比較例1]
樹脂密度0.92g/cm3の低密度ポリエチレン樹脂100重量部に対し、発泡剤としてアゾジカルボンアミドを10.5重量部添加した組成物を2つ準備し、一方には、熱安定剤として1,1−ビス(2−メチル−4−ヒドロキシ−5−ブチルフェニル)ブタン(融点:210℃)(旭電化製 マークAO−40)を0.3重量部、添加し(実施例1)、他方には、テトラキス[メチレン−3−(3,5−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオネート]メタン(融点:120℃)(チバガイギー製Irganox1010)を0.3重量部添加し(比較例1)、押出機を用いて厚さ1.8mmのシートを作成した。次いで、かかる2枚のシートに電子線照射を施し、樹脂を架橋せしめた後、小型発泡炉の温度を245℃に設定し発泡させたところ、実施例1のシートは5分間の発泡炉中において熱劣化、変色とも認められず耐熱性に優れたものであった。これに対し比較例1のシートは発泡開始後2分30秒あたりから端部が熱劣化をし始め変色が認められた。
さらに、実施例1のシートを発泡炉の温度を270℃と高く設定して発泡させたが、5分間の発泡炉中において熱劣化、変色とも認められず耐熱性に優れたものであった。
【0020】
[実施例2]
樹脂密度0.92g/cm3の低密度ポリエチレン樹脂50重量部、ブチレンを共重合した直鎖状ポリエチレン樹脂50重量部に対し、発泡剤としてアゾジカルボンアミドを2.5重量部、着色剤として酸化チタン熱安定剤として1,1−ビス(2−メチル−4−ヒドロキシ−5−ブチルフェニル)ブタン(融点:210℃)(旭電化製 マークAO−40)を0.2重量部、ジオクタデシル チオジプロピオネート(分子量:683)(商標:シーノックス DS)、を0.2重量部添加して発泡体用樹脂組成物を作成した。
【0021】
得られた発泡体用樹脂組成物を、ヘンシェルミキサーにて混合した後、押出機を用いてT‐ダイ法により押出し、厚み1.4mmのシート状物を得た。かかるシート化時に安定剤がロールにブリードアウトしてくることはなかった。しかる後、このシート状物に電子線を照射し、あらかじめ樹脂に架橋を施した後、280℃の熱風発泡炉内で発泡させ、シート状の発泡体を製造した。
得られた発泡体は、独立気泡構造を有する架橋発泡体であり、厚みは2.0mmで、見掛け密度は0.20g/cm3であり、架橋度を表すゲル分率は35%であり、端部が熱焼けして黄色に着色することもなく、綺麗な白色発泡シートが得られた。
【0022】
次に、該発泡シートを50mmφの円形状に打ち抜きパッキン部材を作成した。
しかる後、キャップ部材として線状ポリエチレン樹脂を用い、金型内に上記パッキン部材を装着した後、射出温度180℃にて該樹脂を射出するインサート成形方法にてパッキン部材が一体成形された小型ポリタンクのキャップ部品を作成した。得られたキャップ部品のパッキン部分は熱によって溶けたり、形状が欠けたり、面が粗れたりすることはなく、良好な仕上がり状態であった。また、成形不良も全くみられなかった。
【0023】
[比較例2]
実施例2の酸化防止剤に代えて、テトラキス[メチレン−3(3,5−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオネート]メタン(融点:120℃)(チバガイギー製Irganox1010)を0.5重量%添加する以外は実施例1と全く同様にしてシート状の発泡体を製造した。シート化時には安定剤がブリードアウトし、ロール清掃しつつ製造しなければならなかった。
また、得られた比較例2の発泡体は端部が熱焼けし黄変したばかりでなく、中央部もところどころ面があれ、黄味を帯び商品価値として劣るものであった。
【0024】
【発明の効果】
本発明のオレフィン系樹脂発泡体は以下の効果を有するものである。
(1)発泡体製造過程におけるシート成形時のブリードアウトが解消される。
(2)発泡体は、熱焼けによる黄変もなく綺麗な表面品位を有することが出来る。
(3)発泡体は長期耐熱性に優れ、各種の成形加工における成形不良率を低減することが出来る。
[0001]
BACKGROUND OF THE INVENTION
The present invention has no adverse effect of bleed out of the stabilizer during sheet molding when producing olefin resin foam, particularly polyethylene resin foam, and the foaming temperature is limited to a certain limit due to insufficient heat stability during foaming. The present invention relates to an olefin-based resin foam that can solve the problem that it cannot be raised more than that, and further has no coloring and excellent long-term heat stability.
[0002]
[Prior art]
Olefin-based resin foam has excellent cushioning properties, cushioning properties, water resistance, and chemical properties, so it can be used as insulation for electrical appliances such as coolers, packaging cushioning materials for high-end products, packing for containers, adhesive tape, or long. It has been widely used as a heat insulating material for a scale roof or a pipe heat insulating material processed into a pipe shape. In the production of such an olefin resin foam, particularly a polyethylene resin foam, an antioxidant has generally been added as a heat stabilizer to prevent thermal degradation due to heat during processing or mechanical shearing force. . Such antioxidants are roughly classified into radical chain inhibitors and peroxide decomposition products in terms of their functions, and have been used in combination from the viewpoint of long-term thermal stability.
[0003]
[Problems to be solved by the invention]
As described above, heat stabilizers have also been applied in the production of olefin-based resin foams. However, the heat stabilizer bleeds out and adheres to the transport roll when it is made into a sheet. As a result, there was a problem that a dent defect occurred. Furthermore, when cross-linking with an electron beam, the stabilizer is modified by the electron beam, and the desired effect cannot be fully exhibited in the foaming process receiving a lot of heat, and the foaming temperature can be raised to a certain limit or more. In addition, there was a problem that when the temperature was raised, the edge portion was particularly hot and colored. In addition, various processes are performed in the above-mentioned various application fields to produce products. However, when heat is applied, there are disadvantages that heat resistance is poor, molding defects are increased, and long-term thermal stability is lacking.
[0004]
The present invention improves the heat resistance of such a foam, eliminates the bleed-out problem at the time of forming a sheet, does not burn even at high temperature foaming, has no color, and has excellent long-term heat resistance. The purpose is to provide.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, the present invention provides an olefin resin foam having closed cells, which contains 0.05 to 1.0% by weight of a hindered phenol antioxidant having a melting point of 150 ° C. or higher. It consists of a resin foam.
Further, the present invention is an olefin resin foam having closed cells, 0.05 to 1.0% by weight of a hindered phenol antioxidant (A) having a melting point of 150 ° C. or higher, and a molecular weight of 500 or higher. The thioether-based antioxidant (B) is contained in an amount of 0.05 to 1.0% by weight, and the ratio of (B) / (A) is 0.5 to 2.0.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
Details of the present invention will be described below.
Examples of the olefin resin constituting the olefin resin foam of the present invention include a polyethylene resin alone, and a polyethylene-based resin blended with a polyethylene resin obtained by copolymerizing vinyl acetate, ethylene / ethyl acrylate, or the like with a polyethylene resin. Alternatively, a polypropylene resin alone or a mixed resin of a polypropylene resin and a polyethylene resin is exemplified.
[0007]
Examples of the polyethylene resin include polyethylene resins having a density of 0.90 to 0.965 g / cm 3 manufactured by a low pressure method, a medium pressure method, and a high pressure method, ethylene, butene, pentene, hexene, octene, 4-methylpentene, and the like. Illustrative examples include linear polyethylene resins copolymerized with olefins, linear ultra-low density polyethylene, ethylene-vinyl acetate copolymers, ethylene-ethyl acrylate copolymers, and the like. These polyethylene resins may be used alone or in combination of two or more.
[0008]
Examples of polypropylene resins include propylene homopolymers, block copolymers of α-olefins such as ethylene and butene with propylene, random copolymers, random-block copolymers, and the like. These polypropylene resins may be used alone or in combination of two or more.
A preferred example of the olefin resin used in the present invention is a foam made of the polyethylene resin because of its particularly good cold resistance.
[0009]
In order to improve heat resistance, the olefin resin foam used in the present invention contains 0.05 to 1.0% by weight of a hindered phenol antioxidant having a melting point of 150 ° C. or higher based on the olefin resin. It is necessary.
[0010]
Examples of the hindered phenol antioxidant having a melting point of 150 ° C. or higher include 1,1,3-tris (2-methyl-4-hydroxy-5-tert-butylphenyl) butane (melting point: 186 ° C.), 1,1. -Bis (2-methyl-4-hydroxy-5-t-butylphenyl) butane (melting point: 210 ° C.), 1,3,5-trimethyl-2,4,6-tris (3,5-di-t- Preferable examples include those having a molecular skeleton composed of only carbon and hydrogen such as butyl-4-hydroxybenzyl) benzene (melting point: 244 ° C.). These are all registered on the positive list of the Sanitation Council for Polyolefins, etc., and are excellent in safety that has been attracting attention in recent years.
[0011]
The content of the hindered phenol antioxidant in the foam needs to be 0.05 to 1.0% by weight with respect to the olefin resin. If it is less than 0.05% by weight, it is difficult to achieve the intended effect of the present invention. Further, even if the amount exceeds 1.0% by weight, there is almost no effect of increasing the amount.
[0012]
Examples of thioether antioxidants having a molecular weight of 500 or more include didodecyl thiodipropionate (molecular weight: 517), ditetradecyl thiodipropionate (molecular weight: 571), dioctadecyl thiodipropionate (molecular weight: 683), pentae. Examples include thylitol tetrakis 3-dodecyl thiopropionate (molecular weight 1162), among which dioctadecyl thiodipropionate is preferable. The content of the thioether antioxidant in the foam is preferably 0.05 to 1.0% by weight with respect to the olefin resin.
[0013]
In the present invention, even if the hindered phenolic antioxidant alone is used, the effect of the present invention is sufficiently exhibited. However, the combined use with a thioether antioxidant is preferable because long-term thermal stability is further enhanced. If the content of the thioether-based antioxidant exceeds 1.0% by weight, it tends to bleed out during the production of the foam and is transferred to a roll during the production process, which tends to cause stain defects and the like. In addition, as a mixing ratio (B) / (A) of a hindered phenol type antioxidant (A) and a thio type antioxidant (B), the range of 0.5-2.0 is preferable.
[0014]
The olefin resin foam of the present invention is mixed with a predetermined amount in the above resin in combination with a foaming agent, an additive such as a pigment, and the above-mentioned hindered phenol antioxidant, or further a thioether antioxidant. And after extruding into a sheet form with an extruder and bridge | crosslinking with an electron beam, the foam of a desired shape can be manufactured by making the said foaming agent foam. As the foaming agent, for example, a thermally decomposable foaming agent such as azodicarbonamide can be used.
[0015]
Prior to or simultaneously with foaming, polyolefin resin is subjected to silanol condensation using an ionizing radiation crosslinking method, a chemical crosslinking method using a peroxide such as dicumyl peroxide, or bilnimethoxysilane. Crosslinking can be performed by means such as a so-called silane crosslinking method or ultraviolet crosslinking by ultraviolet irradiation, but the crosslinking method by electron beam irradiation is desirable from the viewpoint of ease of process control.
For crosslinkability, divinyl hensen, diallyl phthalate, hydroquinone dimethacrylate, and the like may be appropriately blended and used in the resin composition as a crosslinking aid.
[0016]
The apparent density of the olefin resin foam of the present invention can be appropriately selected according to the purpose of use. However, when used as various packings, the range of 0.05 to 0.25 g / cm 3 is particularly in strength and handling. This is preferable. When the apparent density is small, the strength of the foam is small, and it is difficult to say that it is easy to use for the intended application, and the density, in other words, the expansion ratio may be selected in consideration of the tensile strength.
[0017]
In addition, as a thickness of a foam, the thing of the range of 0.2-5 mm is used preferably, However It does not specifically limit and should just set suitably according to a use aspect.
The cell structure of the olefin resin foam of the present invention is a closed cell structure because high shear strength is obtained, and the foam having such a closed cell structure is produced by the above-described method using a pyrolytic foaming agent. Can do.
[0018]
【Example】
Hereinafter, the present invention will be described in detail by way of examples.
In addition, the characteristic of an olefin resin foam is measured based on JISK6767.
[0019]
[Example 1, Comparative Example 1]
Two compositions prepared by adding 10.5 parts by weight of azodicarbonamide as a foaming agent to 100 parts by weight of a low density polyethylene resin having a resin density of 0.92 g / cm 3 were prepared. , 1-bis (2-methyl-4-hydroxy-5-butylphenyl) butane (melting point: 210 ° C.) (Asahi Denka Mark AO-40) was added in an amount of 0.3 part by weight (Example 1). Was added 0.3 parts by weight of tetrakis [methylene-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate] methane (melting point: 120 ° C.) (Irganox 1010 manufactured by Ciba Geigy) (Comparative Example) 1) A sheet having a thickness of 1.8 mm was prepared using an extruder. Next, the two sheets were irradiated with an electron beam to crosslink the resin, and then the temperature of a small foaming furnace was set to 245 ° C., and foaming was performed. The sheet of Example 1 was placed in a foaming furnace for 5 minutes. Neither thermal deterioration nor discoloration was observed, and the heat resistance was excellent. On the other hand, the sheet of Comparative Example 1 started to thermally deteriorate at about 2 minutes and 30 seconds after the start of foaming, and discoloration was recognized.
Furthermore, the sheet of Example 1 was foamed by setting the temperature of the foaming furnace as high as 270 ° C., but it was excellent in heat resistance without any thermal deterioration or discoloration in the foaming furnace for 5 minutes.
[0020]
[Example 2]
50 parts by weight of low-density polyethylene resin with a resin density of 0.92 g / cm 3 and 50 parts by weight of linear polyethylene resin copolymerized with butylene, 2.5 parts by weight of azodicarbonamide as a foaming agent, and oxidation as a colorant 0.21 parts by weight of 1,1-bis (2-methyl-4-hydroxy-5-butylphenyl) butane (melting point: 210 ° C.) (Mark AO-40, manufactured by Asahi Denka) as a titanium heat stabilizer, dioctadecylthio 0.2 parts by weight of dipropionate (molecular weight: 683) (trademark: Cynox DS) was added to prepare a resin composition for a foam.
[0021]
The obtained resin composition for foam was mixed with a Henschel mixer and then extruded by a T-die method using an extruder to obtain a sheet-like product having a thickness of 1.4 mm. During the sheet formation, the stabilizer did not bleed out to the roll. Thereafter, the sheet-like material was irradiated with an electron beam, the resin was previously crosslinked, and then foamed in a hot air foaming furnace at 280 ° C. to produce a sheet-like foam.
The obtained foam is a crosslinked foam having a closed cell structure, the thickness is 2.0 mm, the apparent density is 0.20 g / cm 3 , the gel fraction representing the degree of crosslinking is 35%, A beautiful white foam sheet was obtained without the end portion being heated and colored yellow.
[0022]
Next, the foamed sheet was punched into a circular shape of 50 mmφ to prepare a packing member.
Thereafter, a linear polyethylene resin is used as a cap member, and after the packing member is mounted in a mold, the packing member is integrally molded by an insert molding method in which the resin is injected at an injection temperature of 180 ° C. A cap part was created. The packing part of the obtained cap part was in a good finished state without being melted by heat, lacking in shape, or roughening the surface. Also, no molding defects were observed.
[0023]
[Comparative Example 2]
Instead of the antioxidant of Example 2, tetrakis [methylene-3 (3,5-di-t-butyl-4-hydroxyphenyl) propionate] methane (melting point: 120 ° C.) (Irganox 1010 manufactured by Ciba Geigy) was 0.5. A sheet-like foam was produced in the same manner as in Example 1 except that the addition by weight was added. At the time of sheeting, the stabilizer bleeded out and had to be manufactured with roll cleaning.
Further, the obtained foamed product of Comparative Example 2 was not only burnt and yellowed at the ends, but also had a smooth surface at the center and was yellowish and inferior in commercial value.
[0024]
【The invention's effect】
The olefin resin foam of the present invention has the following effects.
(1) Bleed-out at the time of sheet molding in the foam production process is eliminated.
(2) The foam can have a clean surface quality without yellowing due to heat burn.
(3) The foam is excellent in long-term heat resistance and can reduce the molding defect rate in various molding processes.

Claims (4)

独立気泡を有するオレフィン系樹脂発泡体であって、融点150℃以上のヒンダードフェノール系酸化防止剤を0.05〜1.0重量%含有するオレフィン系樹脂発泡体。An olefin resin foam having closed cells and containing 0.05 to 1.0% by weight of a hindered phenol antioxidant having a melting point of 150 ° C. or higher. 独立気泡を有するオレフィン系樹脂発泡体であって、融点150℃以上のヒンダードフェノール系酸化防止剤(A)を0.05〜1.0重量%、及び、分子量500以上のチオエーテル系酸化防止剤(B)を0.05〜1.0重量%含有し、かつ(B)/(A)の比率が0.5〜2.0であるオレフィン系樹脂発泡体。An olefin resin foam having closed cells, 0.05 to 1.0% by weight of a hindered phenol antioxidant (A) having a melting point of 150 ° C. or higher, and a thioether antioxidant having a molecular weight of 500 or higher An olefin-based resin foam containing 0.05 to 1.0% by weight of (B) and having a ratio of (B) / (A) of 0.5 to 2.0. オレフィン系樹脂発泡体が電子線架橋された発泡体であることを特徴とする請求項1又は2記載のオレフィン系樹脂発泡体。The olefin resin foam according to claim 1 or 2, wherein the olefin resin foam is an electron beam crosslinked foam. オレフィン系樹脂100重量部に対し、熱分解型発泡剤1〜20重量部、及び融点150℃以上のヒンダードフェノール系酸化防止剤0.05〜1.0重量部添加して混合した後、シート状に押出し、電子線を照射せしめた後、200℃以上の高温下で発泡剤を分解せしめて発泡させることを特徴とするオレフィン系樹脂発泡体の製造方法。After adding and mixing 1 to 20 parts by weight of a heat decomposable foaming agent and 0.05 to 1.0 parts by weight of a hindered phenol antioxidant having a melting point of 150 ° C. or more with respect to 100 parts by weight of the olefin resin, a sheet A process for producing an olefin-based resin foam, which is extruded into a shape and irradiated with an electron beam, and then the foaming agent is decomposed and foamed at a high temperature of 200 ° C. or higher.
JP15581099A 1999-06-02 1999-06-02 Olefin resin foam and method for producing the same Expired - Lifetime JP4238418B2 (en)

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