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JPH0776284B2 - Method for producing olefin resin foam - Google Patents
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JPH0776284B2 - Method for producing olefin resin foam - Google Patents

Method for producing olefin resin foam

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Publication number
JPH0776284B2
JPH0776284B2 JP2019891A JP1989190A JPH0776284B2 JP H0776284 B2 JPH0776284 B2 JP H0776284B2 JP 2019891 A JP2019891 A JP 2019891A JP 1989190 A JP1989190 A JP 1989190A JP H0776284 B2 JPH0776284 B2 JP H0776284B2
Authority
JP
Japan
Prior art keywords
olefin resin
crosslinking
weight
foaming agent
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2019891A
Other languages
Japanese (ja)
Other versions
JPH03221542A (en
Inventor
栄一 高橋
倉之輔 山本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP2019891A priority Critical patent/JPH0776284B2/en
Publication of JPH03221542A publication Critical patent/JPH03221542A/en
Publication of JPH0776284B2 publication Critical patent/JPH0776284B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はオレフィン系樹脂発泡体の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for producing an olefin resin foam.

〔従来の技術〕[Conventional technology]

独立気泡を有するオレフィン系樹脂発泡体は、柔軟で断
熱性及び機械的強度が大きいため、断熱材や緩衝材とし
て各種の分野で広く使用されている。
Olefin resin foams having closed cells are widely used in various fields as heat insulating materials and cushioning materials because they are flexible and have high heat insulating properties and mechanical strength.

この種のオレフィン系樹脂発泡体を製造するためには、
公知の化学架橋剤を使用するか、又は電離放射線(例え
ば電子線)架橋方法により、架橋させるのが、一般的で
ある。また、例えば特開昭51−66334号公報及び特開昭5
5−75432号公報に記載されているように、有機過酸化物
の存在下にオレフィン系樹脂にアルコキシシラン化合物
をグラフト結合させ、次いでこのグラフト結合された樹
脂と発泡剤その他の添加物とを混合し、架橋・発泡させ
る方法が用いられている。
In order to produce this kind of olefin resin foam,
It is common to crosslink using known chemical crosslinking agents or by ionizing radiation (eg electron beam) crosslinking methods. Further, for example, Japanese Patent Laid-Open Nos. 51-66334 and 5
As described in JP-A-5-75432, an olefinic resin is graft-bonded with an alkoxysilane compound in the presence of an organic peroxide, and then the graft-bonded resin is mixed with a blowing agent and other additives. However, a method of crosslinking and foaming is used.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

既知方法においては、通常の化学架橋剤による架橋方法
は、熱成形時の部分架橋が生じやすい。電離放射線によ
る架橋方法は、架橋構造が発泡前に決定されるため架橋
度に上下とも限定があり、最終架橋度を高めることが困
難で、熱寸法安定性が劣る傾向がある。また上記の公報
に記載の方法では、一般に有機過酸化物の分解温度が発
泡剤の分解温度より高いために、a)まず、有機過酸化
物を用いてオレフィン系樹脂にアルコキシシラン化合物
をグラフト結合させ、b)得られたグラフト樹脂に発泡
剤を混練して成形し、c)発泡に必要な適度の架橋度を
与えたのち、加熱発泡させる、という煩雑な工程を経る
必要があり、生産性が極めて低く、この点の解決が望ま
れていた。
In the known method, the conventional crosslinking method using a chemical crosslinking agent tends to cause partial crosslinking during thermoforming. In the cross-linking method using ionizing radiation, since the cross-linking structure is determined before foaming, the cross-linking degree is limited both above and below, it is difficult to increase the final cross-linking degree, and the thermal dimensional stability tends to be poor. Further, in the method described in the above publication, since the decomposition temperature of the organic peroxide is generally higher than the decomposition temperature of the foaming agent, a) first, an alkoxysilane compound is graft-bonded to the olefin resin using the organic peroxide. Therefore, it is necessary to perform a complicated step of b) kneading and molding the obtained graft resin with a foaming agent, and c) giving an appropriate degree of crosslinking necessary for foaming, and then heat-foaming, thereby improving productivity. Is extremely low, and a solution to this point has been desired.

したがって、本発明の目的は、熱寸法安定性に優れたオ
レフィン系樹脂発泡体を簡略化された工程及び高められ
た生産性で製造する方法を提供することにある。
Therefore, it is an object of the present invention to provide a method for producing an olefin resin foam excellent in thermal dimensional stability with a simplified process and increased productivity.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明者らは、前記課題を解決するため鋭意検討した結
果、本発明を完成した。
The present inventors have completed the present invention as a result of extensive studies to solve the above problems.

本発明は、オレフィン系樹脂、分子中にアクリロイル基
及び又はメタクリロイル基を有するアルコキシシラン化
合物及び化学分解型発泡剤を含有する混合原料を、前記
化学分解型発泡剤の分解温度未満の温度で成形し、得ら
れた成形物に電離放射線を照射したのち、前記化学分解
型発泡剤の分解温度以上に加熱す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である。
The present invention molds a mixed raw material containing an olefin resin, an alkoxysilane compound having an acryloyl group and / or a methacryloyl group in the molecule and a chemical decomposition type foaming agent at a temperature lower than the decomposition temperature of the chemical decomposition type foaming agent. After irradiating the obtained molded product with ionizing radiation, it is heated to a temperature not lower than the decomposition temperature of the chemical decomposition type foaming agent,
It is a method for producing an olefin resin foam.

以下に本発明をさらに詳しく説明する。The present invention will be described in more detail below.

本発明に使用されるオレフィン系樹脂としては、例えば
低密度ないし高密度ポリエチレン、直鎖状ポリエチレ
ン、ポリプロピレン、エチレン−プロピレン共重合体、
エチレンと他のモノマー例えば酢酸ビニル、アクリル
酸、メタクリル酸との共重合体があげられる。これらは
単独で又は2種以上の混合物として使用される。
Examples of the olefin resin used in the present invention include low-density to high-density polyethylene, linear polyethylene, polypropylene, ethylene-propylene copolymer,
Examples thereof include copolymers of ethylene and other monomers such as vinyl acetate, acrylic acid, and methacrylic acid. These are used alone or as a mixture of two or more kinds.

本発明に使用されるアクリロイル基及び/又はメタクリ
ロイル基を有するアルコキシラン化合物としては、例え
ば(メタ)アクリロイルオキシアルキル−トリメトキシ
シランなどがあげられる。アクリロイル基及び/又はメ
タクリロイル基は分子中に1個以上含有されることが好
ましい。アルコキシシラン化合物の添加量は、オレフィ
ン系樹脂100重量部に対し一般に0.1〜15重量部、好まし
くは、1〜3重量部である。
Examples of the alkoxylane compound having an acryloyl group and / or a methacryloyl group used in the present invention include (meth) acryloyloxyalkyl-trimethoxysilane. One or more acryloyl groups and / or methacryloyl groups are preferably contained in the molecule. The amount of the alkoxysilane compound added is generally 0.1 to 15 parts by weight, preferably 1 to 3 parts by weight, based on 100 parts by weight of the olefin resin.

本発明において使用される化学分解型発泡剤としては、
例えばアゾジカルボンアミド、オキシベンゼンスルホニ
ルヒドラジド、アゾビスイソブチロニトリル、N,N′−
ジニトロソペンタメチレンテトラミンなどがあげられ
る。発泡剤の添加量は、オレフィン系樹脂100重量部に
対し0.5〜40重量部、好ましくは10〜30重量部である。
The chemical decomposition type foaming agent used in the present invention,
For example, azodicarbonamide, oxybenzenesulfonyl hydrazide, azobisisobutyronitrile, N, N'-
Examples thereof include dinitrosopentamethylenetetramine. The amount of the foaming agent added is 0.5 to 40 parts by weight, preferably 10 to 30 parts by weight, based on 100 parts by weight of the olefin resin.

オレフィン系樹脂、前記のアルコキシシラン化合物及び
発泡剤からなる混合原料中には、必要に応じ普通の添加
物例えば滑剤、難燃剤、帯電防止剤、抗酸化剤、老化防
止剤、紫外線吸収剤、無機及び有機充填剤、着色剤など
を添加することができる。アルコキシシラン化合物間の
重合を抑制するため、メルカプタン等の反応禁止剤を添
加してもよい。
In the mixed raw material consisting of an olefin resin, the above-mentioned alkoxysilane compound and a foaming agent, if necessary, common additives such as lubricants, flame retardants, antistatic agents, antioxidants, anti-aging agents, ultraviolet absorbers and inorganic materials are added. In addition, organic fillers, colorants and the like can be added. A reaction inhibitor such as mercaptan may be added to suppress the polymerization between the alkoxysilane compounds.

前記混合原料を、前記発泡剤の分解温度未満の温度で溶
融、混練したのち成形する。このためには例えばバンバ
リミキサー、ニーダーミキサー等のほか、単軸又は多軸
押出機を使用できる。成形物は任意の形を有していてよ
いが、シート状に押出成形することが好ましい。
The mixed raw material is melted and kneaded at a temperature lower than the decomposition temperature of the foaming agent, and then molded. For this purpose, for example, a Banbury mixer, a kneader mixer, etc., as well as a single-screw or multi-screw extruder can be used. The molded product may have any shape, but is preferably extruded into a sheet.

次いで得られた形成物に電離放射線を照射することによ
り、形成物中のオレフィン系樹脂をラジカル反応架橋さ
せて、発泡に必要な架橋を得る。この反応と同時に、オ
レフィン系樹脂からのラジカル発生により前記アルコキ
シシラン化合物をオレフィン系樹脂に対しグラフト結合
させる。電離放射線とはα線、β線、γ線、及び電子線
をいう。そのうち電子線が特に好ましい。
Then, by irradiating the obtained formed product with ionizing radiation, the olefinic resin in the formed product is radically reactively crosslinked to obtain the necessary crosslinking for foaming. Simultaneously with this reaction, radicals are generated from the olefin resin to graft bond the alkoxysilane compound to the olefin resin. Ionizing radiation refers to α rays, β rays, γ rays, and electron rays. Of these, electron beams are particularly preferable.

こうして得られた架橋・グラフトした成形物を、化学分
解型発泡剤の分解温度以上の温度に加熱して発泡させ
る。この発泡工程において、発泡と同時又は発泡後にア
ルコキシシラン化合物による縮合架橋反応が進行する。
この反応は、発泡剤の分割に必要な熱と、樹脂混合物中
又は加熱処理時の雰囲気中例えば空気中の微量水分によ
り充分に行われる。
The crosslinked / grafted molded product thus obtained is heated to a temperature equal to or higher than the decomposition temperature of the chemical decomposition type foaming agent to foam. In this foaming step, the condensation-crosslinking reaction with the alkoxysilane compound proceeds simultaneously with or after foaming.
This reaction is sufficiently carried out by the heat required for dividing the foaming agent and a trace amount of water in the resin mixture or in the atmosphere during the heat treatment, for example, in the air.

〔作 用〕[Work]

本発明の方法によれば、前記成形物に電離放射線を照射
することにより、オレフィン系樹脂中でラジカル架橋反
応が生じ、発泡に必要な架橋が得られると同時に、成形
したラジカルにより前記アルコキシシラン化合物がオレ
フィン系樹脂に対しグラフト結合する。前記アルコキシ
ラン化合物は成形時には単に混合されている状態である
ため、部分的架橋を生じて成形性を阻害することがな
い。また、電離放射線により一定した架橋が得られるた
め、その後の発泡工程において均一な気泡が容易に得ら
れ、品質の安定と生産効率の向上とが達成される。さら
に、発泡時又はその後に前記アルコキシシラン化合物の
縮合架橋反応を進行することにより、気泡の残留歪が緩
和されるとともに架橋度が高められ、熱寸法安定性に優
れた発泡体が得られる。
According to the method of the present invention, by irradiating the molded product with ionizing radiation, a radical cross-linking reaction occurs in the olefin resin, and the cross-linking necessary for foaming is obtained, and at the same time, the molded radical causes the alkoxy silane compound Graft-bonds to the olefin resin. Since the above-mentioned alkoxy lan compound is in a state of being simply mixed at the time of molding, it does not cause partial cross-linking and hinder the moldability. Further, since uniform crosslinking is obtained by ionizing radiation, uniform bubbles can be easily obtained in the subsequent foaming step, and stable quality and improved production efficiency can be achieved. Furthermore, by advancing the condensation-crosslinking reaction of the alkoxysilane compound at the time of foaming or thereafter, the residual strain of bubbles is alleviated and the degree of crosslinking is increased, and a foam having excellent thermal dimensional stability is obtained.

〔実施例〕〔Example〕

以下に本発明を実施例により説明する。 The present invention will be described below with reference to examples.

低密度ポリエチレン(MI:4.5、密度:0.924g/cm3、M.P:1
12℃)100重量部に3−メタクリルオキシプロピルトリ
メトキシシラン1.5重量部を加え、さらにアゾジカルボ
ンアミド13重量部及びフェノール系抗酸化剤1重量部を
加え、この混合物を単軸押出機(150φ)により樹脂温
度140℃で押出し、シート状に成形した(厚さ1.6mm)。
Low density polyethylene (MI: 4.5, density: 0.924g / cm 3 , MP: 1
12 ° C) 1.5 parts by weight of 3-methacryloxypropyltrimethoxysilane was added to 100 parts by weight, 13 parts by weight of azodicarbonamide and 1 part by weight of a phenolic antioxidant were further added, and this mixture was uniaxial extruder (150φ). Was extruded at a resin temperature of 140 ° C to form a sheet (thickness: 1.6 mm).

次いで、このシートに電子線照射機により電子線を2.2M
radの線量で照射し、グラフト結合及び架橋を行わせ
た。このシートの架橋指数は31%であった。さらにこの
シートを発泡オーブン(250℃)中で発泡させると、厚
さ4.3mm、密度0.0323g/cm3の発泡体が得られた。この発
泡シートの架橋指数は67%であった。
Next, an electron beam of 2.2M is applied to this sheet by an electron beam irradiation machine.
Irradiation was performed at a dose of rad to cause grafting and crosslinking. The crosslinking index of this sheet was 31%. Further, when this sheet was foamed in a foaming oven (250 ° C.), a foam having a thickness of 4.3 mm and a density of 0.0323 g / cm 3 was obtained. The crosslinking index of this foamed sheet was 67%.

架橋指数とは、発泡体小片を120℃のキシレン中に24時
間放置したのち、残分を80℃で8時間真空乾燥した重量
を、処理前の発泡体重量で除した値の100倍をいう。
The cross-linking index is 100 times the value obtained by dividing the weight of a foam piece left in xylene at 120 ° C for 24 hours and then vacuum drying the residue at 80 ° C for 8 hours by the weight of the foam before treatment. .

比較例1 低密度ポリエチレン(MI=4.5、密度:0.924g/cm3、M.P1
12℃)100重量部、ビニルメトキシシラン1.5重量部と有
機過酸化物0.1重量部(ジクミルパーオキシド:1分半減
期が71℃)を65φ2軸押出機により樹脂温180℃で押出
し、これをシート状に成形したのち粉砕した。この粉砕
した樹脂にアゾジカルボンアミド13重量部、フェノール
系抗酸化剤1重量部を加え、発泡剤の分解する温度以下
で厚さ1.6mmに押出し、シート状に成形した。この成形
物を110℃に温調されたオイルバス(長さ2m)を2m/hrの
速度で通過させた。この時点でのシートの架橋指数は21
%であった。
Comparative Example 1 Low density polyethylene (MI = 4.5, density: 0.924 g / cm 3 , M.P1
12 ° C) 100 parts by weight, vinylmethoxysilane 1.5 parts by weight and organic peroxide 0.1 parts by weight (dicumyl peroxide: 1 minute half-life 71 ° C) are extruded at a resin temperature of 180 ° C by a 65φ twin-screw extruder, It was formed into a sheet and then crushed. Azodicarbonamide (13 parts by weight) and a phenolic antioxidant (1 part by weight) were added to the crushed resin, and the mixture was extruded to a thickness of 1.6 mm at a temperature not higher than the decomposition temperature of the foaming agent to form a sheet. This molded product was passed through an oil bath (length: 2 m), the temperature of which was adjusted to 110 ° C., at a speed of 2 m / hr. The crosslinking index of the sheet at this point is 21
%Met.

このシートを250℃の熱風オーブン中で加熱発泡させた
ところ、厚さ3.9mm、密度0.0323g/cm3の発泡体が得られ
た。この発泡シートの架橋指数は59%であった。
When this sheet was heated and foamed in a hot air oven at 250 ° C., a foam having a thickness of 3.9 mm and a density of 0.0323 g / cm 3 was obtained. The crosslinking index of this foamed sheet was 59%.

比較例2 低密度ポリエチレン(MI=4.5、密度:0.924g/cm3、M.P1
12℃)100重量部にアゾジカルボンアミド13重量部及び
フェノール系抗酸化剤1重量部を加え、単軸押出機(15
0φ)により樹脂温140℃で押出し、シート状に成形した
(厚さ1.6mm)。このシートに電子線を2.5Mradの線量で
照射した。このシートの架橋指数は38%であった。さら
にこのシートを250℃の発泡オーブン中で発泡させる
と、厚さ4.0mm、密度0.0319g/cm3の発泡体が得られた。
この発泡シートの架橋指数も38%であった。
Comparative Example 2 Low density polyethylene (MI = 4.5, density: 0.924 g / cm 3 , M.P1
12 ° C.) 13 parts by weight of azodicarbonamide and 1 part by weight of phenolic antioxidant were added to 100 parts by weight of a single screw extruder (15
0φ) was extruded at a resin temperature of 140 ° C. to form a sheet (thickness: 1.6 mm). This sheet was irradiated with an electron beam at a dose of 2.5 Mrad. The crosslinking index of this sheet was 38%. Further, when this sheet was foamed in a foaming oven at 250 ° C., a foam having a thickness of 4.0 mm and a density of 0.0319 g / cm 3 was obtained.
The cross-linking index of this foam sheet was also 38%.

比較例3 比較例2の条件で照射線量を4.0Mradに変更したとこ
ろ、素シートの架橋指数は58%であった。ついで、これ
を250℃の発泡オーブン中で発泡させたところ、安定し
た発泡体を得ることができなかった。
Comparative Example 3 When the irradiation dose was changed to 4.0 Mrad under the conditions of Comparative Example 2, the crosslinking index of the raw sheet was 58%. Then, when this was foamed in a foaming oven at 250 ° C., a stable foam could not be obtained.

実施例及び比較例1及び2の結果を次表にまとめて示
す。
The results of Examples and Comparative Examples 1 and 2 are summarized in the following table.

この結果から明らかなように、比較例2は電離放射線に
よる架橋法では最終架橋度を高めることができないこと
を示している。また、比較例1に示すように、従来のシ
ラン化合物を用いる方法では、本発明(実施例)と同等
の結果を得るために極めて煩雑な工程が必要である。
As is clear from this result, Comparative Example 2 shows that the final crosslinking degree cannot be increased by the crosslinking method using ionizing radiation. Further, as shown in Comparative Example 1, the method using a conventional silane compound requires extremely complicated steps in order to obtain the same result as that of the present invention (Example).

〔発明の効果〕 本発明の方法によれば、有機過酸化物を使用しないため
に、従来の方法に比べて工程が簡略化され、著しく生産
効率が向上する。また、成形工程が安定し、かつ架橋度
も均一安定化するため、均一な気泡が得られ、発泡体品
質が大きく向上する。さらに、得られた発泡体は熱寸法
安定性にも優れている。
[Effect of the Invention] According to the method of the present invention, since no organic peroxide is used, the process is simplified as compared with the conventional method, and the production efficiency is remarkably improved. In addition, the molding process is stable and the degree of crosslinking is uniformly stabilized, so that uniform cells are obtained and the quality of the foam is greatly improved. Furthermore, the obtained foam is also excellent in thermal dimensional stability.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】オレフィン系樹脂、分子中にアクリロイル
基及び/又はメタクリロイル基を有するアルコキシシラ
ン化合物及び化学分解型発泡剤を含有する混合原料を、
前記化学分解型発泡剤の分解温度未満の温度で成形し、
得られた成形物に電離放射線を照射したのち、前記化学
分解型発泡剤の分解温度以上に加熱することを特徴とす
る、オレフィン系樹脂発泡体の製造方法。
1. A mixed raw material containing an olefin resin, an alkoxysilane compound having an acryloyl group and / or a methacryloyl group in the molecule, and a chemical decomposition type foaming agent,
Molding at a temperature below the decomposition temperature of the chemical decomposition type foaming agent,
A method for producing an olefin-based resin foam, which comprises irradiating the obtained molded product with ionizing radiation and then heating it to a temperature not lower than the decomposition temperature of the chemical decomposition type foaming agent.
JP2019891A 1990-01-29 1990-01-29 Method for producing olefin resin foam Expired - Fee Related JPH0776284B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2019891A JPH0776284B2 (en) 1990-01-29 1990-01-29 Method for producing olefin resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2019891A JPH0776284B2 (en) 1990-01-29 1990-01-29 Method for producing olefin resin foam

Publications (2)

Publication Number Publication Date
JPH03221542A JPH03221542A (en) 1991-09-30
JPH0776284B2 true JPH0776284B2 (en) 1995-08-16

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JP2019891A Expired - Fee Related JPH0776284B2 (en) 1990-01-29 1990-01-29 Method for producing olefin resin foam

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JP (1) JPH0776284B2 (en)

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Publication number Publication date
JPH03221542A (en) 1991-09-30

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