JP3163588B2 - Method for producing open-cell foam - Google Patents

Method for producing open-cell foam

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Publication number
JP3163588B2
JP3163588B2 JP20008892A JP20008892A JP3163588B2 JP 3163588 B2 JP3163588 B2 JP 3163588B2 JP 20008892 A JP20008892 A JP 20008892A JP 20008892 A JP20008892 A JP 20008892A JP 3163588 B2 JP3163588 B2 JP 3163588B2
Authority
JP
Japan
Prior art keywords
weight
open
parts
styrene
thermoplastic elastomer
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
JP20008892A
Other languages
Japanese (ja)
Other versions
JPH061872A (en
Inventor
壮 滝本
正明 佐原
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.)
Sanwa Kako Co Ltd
Original Assignee
Sanwa Kako 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 Sanwa Kako Co Ltd filed Critical Sanwa Kako Co Ltd
Priority to JP20008892A priority Critical patent/JP3163588B2/en
Publication of JPH061872A publication Critical patent/JPH061872A/en
Application granted granted Critical
Publication of JP3163588B2 publication Critical patent/JP3163588B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、連続気泡体の製造方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an open cell.

【0002】[0002]

【従来の技術】従来、架橋ポリオレフィン連続気泡体の
製造方法としては、密閉金型中で発泡性架橋性組成物中
の発泡剤と架橋剤を部分的に分解させ、常圧下で残存す
る発泡剤と架橋剤を分解させて独立気泡体を得、次いで
得られた独立気泡体を圧縮して独立気泡を破壊する方法
が提案されていた(特公昭59−23545号及び特開
昭56−146732号参照)。しかし、このような方
法では、加圧された密閉金型中において加熱により発泡
剤及び架橋剤の分解が行われ、架橋反応は生じているが
気泡の形成は行われておらず、除圧時に初めて発泡する
ことになる。すなわち、まず架橋反応を生ぜしめ、しか
る後に発泡を行わせる方法を採用しており、独立気泡体
の製造段階においていわゆる先架橋が行われているた
め、気泡膜が強靭なものとなる。従って、独立気泡の連
通化が困難であり、連続気泡率100%又は100%に
近い気泡体を得ることができなかった。
2. Description of the Related Art Conventionally, as a method for producing a cross-linked polyolefin open cell, a foaming agent and a cross-linking agent in a foamable cross-linkable composition are partially decomposed in a closed mold, and a foaming agent remaining under normal pressure is obtained. And a crosslinking agent are decomposed to obtain closed cells, and then the obtained closed cells are compressed to break closed cells (Japanese Patent Publication No. 59-23545 and Japanese Patent Application Laid-Open No. 56-146732). reference). However, in such a method, the foaming agent and the cross-linking agent are decomposed by heating in a pressurized closed mold, and a cross-linking reaction has occurred, but no bubbles have been formed. It will be foaming for the first time. That is, a method of first causing a cross-linking reaction and then performing foaming is adopted. Since so-called pre-crosslinking is performed in the production stage of the closed cell, the foam film becomes tough. Therefore, it was difficult to make closed cells open, and it was not possible to obtain a foam having an open cell ratio of 100% or close to 100%.

【0003】上記問題を解決するため、本出願人は、発
泡性架橋性組成物を所望の形状に加熱整形した後、常圧
下にて加熱して架橋剤及び発泡剤を同時進行的に分解さ
せて気泡体を生成させ、次いで機械的変形を加えて気泡
を連通化させる方法を開発した(特公昭62−1929
4号、特公平1−44499号参照)。
In order to solve the above problem, the present applicant heat-shapes a foamable crosslinkable composition into a desired shape and then heats it under normal pressure to simultaneously decompose the crosslinker and the foaming agent. A method was developed to generate bubbles and then to apply mechanical deformation to make the bubbles open (Japanese Patent Publication No. 62-1929).
No. 4, JP-B 1-44499).

【0004】[0004]

【発明が解決しようとする課題】前記した本出願人の方
法によれば、100%又は100%に近い連続気泡率を
有する連続気泡体を得ることができる。しかしながら、
この方法は、低密度ポリエチレン又はエチレン−酢酸ビ
ニル共重合体を基材とした連続気泡体の製造方法を開示
したものであり、ポリエチレン又はエチレン−酢酸ビニ
ル共重合体を基材とした連続気泡体は、耐熱温度が低い
ため、用途が制限されていた。一方、この方法をポリプ
ロピレンに適用すると、耐熱性は向上するが、ゴム弾性
に劣り、パッキン材、シール材等の用途には使用できな
い。
According to the above-described method of the present applicant, it is possible to obtain an open-cell body having an open-cell ratio of 100% or close to 100%. However,
This method discloses a method for producing an open-cell foam based on low-density polyethylene or ethylene-vinyl acetate copolymer, and discloses an open-cell foam based on polyethylene or ethylene-vinyl acetate copolymer. Has a limited use because of its low heat resistance temperature. On the other hand, when this method is applied to polypropylene, the heat resistance is improved, but the rubber elasticity is inferior and cannot be used for applications such as packing materials and sealing materials.

【0005】従って、本発明の目的は、前記したような
従来の欠点を解消し、エチレン−酢酸ビニル共重合体又
は低密度ポリエチレンを基材とした連続気泡体よりも耐
熱性が高く、且つ、ゴム弾性に優れた連続気泡体の製造
方法を提供することにある。
[0005] Accordingly, an object of the present invention is to solve the above-mentioned conventional disadvantages, to have higher heat resistance than an open-cell body based on an ethylene-vinyl acetate copolymer or low-density polyethylene, and An object of the present invention is to provide a method for producing an open cell having excellent rubber elasticity.

【0006】[0006]

【課題を解決するための手段】本発明によれば、前記目
的を達成するため、スチレン系熱可塑性エラストマーに
発泡剤及び架橋剤を添加混練し、得られた発泡性架橋性
組成物を気密でない金型中で加熱発泡させて気泡体を生
成させ、次いで機械的変形を加えて気泡を連通化させる
ことを特徴とする連続気泡体の製造方法が提供される。
本発明の方法において、成形性を良くするために、スチ
レン系熱可塑性エラストマー99〜20重量部にポリエ
チレン系樹脂1〜80重量部を添加することが好まし
い。又、スチレン系熱可塑性エラストマー70〜30重
量部にポリエチレン系樹脂30〜70重量部を添加する
と、成形性が更に改善される。
According to the present invention, a foaming agent and a crosslinking agent are added and kneaded to a styrene-based thermoplastic elastomer to achieve the above object, and the resulting foamable crosslinkable composition is not airtight. There is provided a method for producing an open-cell body, characterized in that the cell is heated and foamed in a mold to form a cell, and then the cell is subjected to mechanical deformation to make the cell open.
In the method of the present invention, it is preferable to add 1 to 80 parts by weight of a polyethylene resin to 99 to 20 parts by weight of a styrene-based thermoplastic elastomer in order to improve moldability. Further, when 30 to 70 parts by weight of the polyethylene resin is added to 70 to 30 parts by weight of the styrene-based thermoplastic elastomer, the moldability is further improved.

【0007】[0007]

【発明の作用及び態様】本発明の方法によれば、上記の
ように、スチレン系熱可塑性エラストマーを基材の樹脂
として使用する。スチレン系熱可塑性エラストマーは、
SBS(スチレン−ブタジエン−スチレンブロックコポ
リマー)系とSEBS(スチレン−エチレン−ブチレン
−スチレンブロックコポリマー)系に大別される。スチ
レン系熱可塑性エラストマーの構造は、ポリスチレン部
分とポリブタジエン(又はエチレン/ブチレン)部分は
互いに非相溶であり、ポリブタジエン(又はエチレン/
ブチレン)の海の中にポリスチレンが島となって分散さ
れている。常温では、このポリスチレン部分がブタジエ
ン(又はエチレン/ブチレン)部分を拘束するが、高温
下(成形加工)において、ポリスチレンが溶融し、熱可
塑性を示すため、熱可塑性樹脂と同様に容易に成形でき
る。又、スチレン系熱可塑性エラストマーはゴムのよう
な弾性と粘性を有しているため、得られた発泡体が特殊
な気泡構造を有し、容易に水を通さず、止水性に優れ
る。
According to the method of the present invention, a styrenic thermoplastic elastomer is used as a base resin as described above. Styrene-based thermoplastic elastomers are
It is roughly classified into SBS (styrene-butadiene-styrene block copolymer) type and SEBS (styrene-ethylene-butylene-styrene block copolymer) type. The structure of the styrene-based thermoplastic elastomer is such that the polystyrene portion and the polybutadiene (or ethylene / butylene) portion are incompatible with each other, and the polybutadiene (or ethylene / butylene)
Polystyrene is dispersed as islands in the sea of (butylene). At room temperature, the polystyrene portion constrains the butadiene (or ethylene / butylene) portion. However, at high temperatures (molding), the polystyrene melts and exhibits thermoplasticity, so that it can be easily molded in the same manner as a thermoplastic resin. Further, since the styrene-based thermoplastic elastomer has elasticity and viscosity like rubber, the obtained foam has a special cell structure, does not easily pass water, and is excellent in water stoppage.

【0008】本発明の連続気泡体を得る方法としては、
基材樹脂に発泡剤及び架橋剤を添加混練し、得られた発
泡性架橋性組成物を加熱発泡させて気泡体を形成させ、
次いで機械的変形を加えて気泡を連通化させる方法であ
れば、従来公知の方法が適用でき、特に限定されない。
このような方法のうち、特に特公昭62−19294号
公報及び特公平1−44499号公報に記載されている
ように、発泡性架橋性組成物を所望の形状に加熱整形し
た後、気密でない金型中で常圧下にて加熱して架橋剤及
び発泡剤を同時進行的に分解させて気泡体を形成させ、
次いで機械的変形を加えて気泡を連通化させる方法にお
いて、本発明の効果は特に顕著である。
The method for obtaining the open-cell body of the present invention includes:
A foaming agent and a crosslinking agent are added and kneaded to the base resin, and the resulting foamable crosslinkable composition is foamed by heating to form a foam,
Next, a conventionally known method can be applied as long as it is a method of making the bubbles open by applying mechanical deformation, and is not particularly limited.
Among such methods, as described in JP-B-62-19294 and JP-B-1-44499, after heat-shaping a foamable crosslinkable composition into a desired shape, non-airtight gold is used. Heating under normal pressure in the mold to simultaneously decompose the crosslinking agent and the foaming agent to form a foam,
The effect of the present invention is particularly remarkable in a method in which bubbles are communicated by applying mechanical deformation.

【0009】以下、本発明に係る連続気泡体の製造方法
についてその好適な態様を具体的に説明する。まず、基
材樹脂として、スチレン系熱可塑性エラストマーを使用
する。スチレン系熱可塑性エラストマーは、スチレン系
熱可塑性樹脂としては、一般式、A−(B−A)
(ここで、Aはスチレン、Bはブタジエンであり、nは
1〜5の整数。)で表わされるブロック共重合体の水素
添加誘導体を主成分とするものが好ましく、ポリプロピ
レン等のポリオレフィン樹脂、各種軟化剤、充填剤等が
適宜添加される(例えば、三菱油化株式会社製、商品名
「ラバロン」)。該水素添加誘導体は、スチレン−ブタ
ジエン−スチレンブロックコポリマーのブタジエン部分
を高度に水添することにより、主鎖及び側鎖の二重結合
部分を飽和させたものであるため、耐候性、耐熱性に特
に優れている。成形性を改善するために、該組成物99
〜20重量部にポリエチレン系樹脂1〜80重量部を添
加することが好ましい。特に好ましくは、該組成物70
重量部〜30重量部にポリエチレン系樹脂30〜70重
量部を添加する。上記の様な基材樹脂又は基材樹脂とポ
リエチレン系樹脂との混合物に発泡剤、架橋剤、及び必
要に応じて発泡助剤、充填剤、顔料等を添加し、これを
加熱したミキシングロール、加圧形ニーダー、バンバリ
ーミキサー、押出機等によって練和する。上記のように
練和して得られた発泡性架橋性組成物を金型に仕込み、
プレスにて加圧下で樹脂及び架橋剤の種類に応じて11
5℃〜165℃、好ましくは、120℃〜150℃にお
いて加熱整形する。この加熱整形工程において、発泡性
架橋性組成物を、好ましくはゲル分率ゼロの状態に維持
して整形することが、連続気泡率100%又は100%
に近い連続気泡体を得る条件である。ここで、ゲル分率
とは200メッシュの金網の中にサンプルを入れ、ソッ
クスレー抽出器により溶媒トリクロルエチレン還流下で
24時間抽出を行って測定した抽出前サンプルと抽出後
サンプルの重量比である。なお、この加熱整形工程にお
いて、非常に微量の発泡剤が初期分解を生じ、整形した
組成物を金型から取り出した場合に2倍程度まで膨張し
得るが、これは発泡という概念からは程遠く、本発明に
とって何ら差し支えない。
Hereinafter, a preferred embodiment of the method for producing an open-cell body according to the present invention will be specifically described. First, a styrene-based thermoplastic elastomer is used as a base resin. The styrene-based thermoplastic elastomer is a styrene-based thermoplastic resin represented by the general formula: A- (BA) n ,
(Here, A is styrene, B is butadiene, and n is an integer of 1 to 5.) It is preferable to use as a main component a hydrogenated derivative of a block copolymer represented by the following formula: A softening agent, a filler, and the like are appropriately added (for example, trade name “Lavalon” manufactured by Mitsubishi Yuka Co., Ltd.). The hydrogenated derivative is a product obtained by highly hydrogenating the butadiene portion of a styrene-butadiene-styrene block copolymer, thereby saturating a double bond portion of a main chain and a side chain. Especially excellent. In order to improve moldability, the composition 99
It is preferable to add 1 to 80 parts by weight of the polyethylene resin to about 20 parts by weight. Particularly preferably, the composition 70
To 30 to 70 parts by weight of the polyethylene resin is added 30 to 70 parts by weight of the polyethylene resin. A foaming agent, a crosslinking agent, and, if necessary, a foaming aid, a filler, a pigment, etc. are added to the above-described base resin or a mixture of the base resin and the polyethylene-based resin, and a mixing roll heated by heating is added. The mixture is kneaded with a pressure kneader, a Banbury mixer, an extruder or the like. Charge the foamable crosslinkable composition obtained by kneading as described above in a mold,
Depending on the type of resin and crosslinking agent under pressure with a press, 11
Heat shaping is performed at 5 ° C to 165 ° C, preferably at 120 ° C to 150 ° C. In this heating shaping step, shaping while maintaining the foamable crosslinkable composition preferably in a state where the gel fraction is zero can be performed by an open cell ratio of 100% or 100%.
This is the condition for obtaining an open cell close to Here, the gel fraction is a weight ratio of a sample before extraction and a sample after extraction measured by placing a sample in a 200-mesh wire net and performing extraction with a Soxhlet extractor under reflux of a solvent of trichloroethylene for 24 hours. In this heating shaping step, a very small amount of the foaming agent undergoes initial decomposition, and when the shaped composition is taken out of the mold, it can expand to about twice, but this is far from the concept of foaming, There is no problem for the present invention.

【0010】上記のようにして得られた整形した組成物
は、次いで、常圧下にて加熱することによって、架橋剤
及び発泡剤の分解を同時進行的に行わしめられる。この
発泡・架橋工程は、例えば、整形した組成物を所望の断
面形状、寸法を有する気密でない、すなわち密閉されて
いない金型中に入れ、該金型の金属板を外部から加熱す
ることによって上記組成物を間接的に加熱せしめる。間
接的に加熱せしめる方法としては、例えば金属板外表面
にヒーターを密着させて加熱するか、あるいは金属板に
熱媒の流路を設け、ジャケット方式で蒸気、加熱オイル
等によって加熱する方法がある。あるいは、中間発泡体
を気密でない開閉式の金型に入れ、ローゼ合金、ウッド
合金などを用いるメタルバスやオイルバス中、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、もしくは窒素気流
中で、あるいは伸張(ないし拡張)可能な鉄板等により
覆われた状態で直接加熱せしめる。又は、高周波を用い
て加熱しても良い。上記の方法によって、所定時間加熱
した後、冷却して気泡体を得る。加熱温度は、使用する
ポリオレフィンの種類に応じて140℃〜210℃、好
ましくは150℃〜180℃の範囲に設定する。加熱時
間は、好ましくは30〜300分、さらに好ましくは1
00〜200分である。このようにして、機械的変形を
与えることによって容易に破壊しうる気泡膜を有し、か
つ従来の気泡体と同程度の架橋度(ゲル分率90%程度
まで)を有する気泡体が得られる。
The shaped composition obtained as described above is then heated under normal pressure to simultaneously decompose the crosslinking agent and the foaming agent. The foaming / crosslinking step is performed, for example, by placing the shaped composition in a non-hermetic, i.e., unsealed mold having a desired cross-sectional shape and dimensions, and heating the metal plate of the mold from the outside. The composition is heated indirectly. As a method of indirectly heating, for example, there is a method in which a heater is closely attached to an outer surface of a metal plate, or a method in which a heating medium flow path is provided in a metal plate, and heating is performed by steam, heating oil, or the like in a jacket system. . Alternatively, the intermediate foam is placed in a mold that is not airtight and can be opened and closed, and one or more kinds of salts such as sodium nitrate, potassium nitrate, and potassium nitrite are melted in a metal bath or an oil bath using a rose alloy, a wood alloy, or the like. It is heated directly in a salt bath using salt, in a nitrogen stream, or in a state covered with an extensible (or expandable) iron plate or the like. Alternatively, heating may be performed using high frequency. According to the above-mentioned method, after heating for a predetermined time, it is cooled to obtain a foam. The heating temperature is set in the range of 140 ° C to 210 ° C, preferably 150 ° C to 180 ° C, depending on the type of polyolefin used. The heating time is preferably 30 to 300 minutes, more preferably 1 minute.
00 to 200 minutes. In this way, a foam having a foam film that can be easily broken by applying mechanical deformation and having a degree of crosslinking (up to a gel fraction of about 90%) similar to that of a conventional foam can be obtained. .

【0011】以上のようにして得られた気泡体(いわゆ
る独立気泡体)は、次いで例えば等速二本ロール等によ
り圧縮変形を加えることによって気泡膜は破壊され、気
泡が連通化されて連続気泡体が得られる。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/又は後に無数の針を設けたロールを配置
して、該気泡体の表面に無数の小孔を開けることによっ
て、気泡の連通化を促進させることができる。この方法
によって、Remington Pariser法に基
づいて測定した連続気泡率で100%又は100%に近
い連続気泡体が得られる。
The foam obtained as described above (a so-called closed cell) is then subjected to compressive deformation by, for example, a constant-speed double roll or the like, whereby the bubble film is broken, and the bubbles are made open to open cells. The body is obtained. A countless small needles are provided on the surface of the constant velocity double roll, or a roll provided with countless needles before and / or after the constant velocity double roll is arranged, and countless small holes are formed on the surface of the foam. By opening the opening, communication of air bubbles can be promoted. According to this method, an open-cell body having an open-cell ratio of 100% or close to 100% is obtained based on the Remington Parser method.

【0012】本発明で用いられるポリエチレン系樹脂と
しては、例えば通常市販の高、中、低圧法により製造さ
れたポリエチレン、又は酢酸ビニル等との共重合体であ
る。本発明で用いられる発泡剤としては各種の化学発泡
剤、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、トリニトロソトリ
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ジッド、トルエンスルホ
ニルセミカルバジッド等が好適に使用できるが、これら
に限定されるものではない。
The polyethylene resin used in the present invention is, for example, a commercially available polyethylene resin produced by a high, medium or low pressure method, or a copolymer with vinyl acetate or the like. Examples of the blowing agent used in the present invention include various chemical blowing agents such as azo compounds such as azodicarbonamide and barium azodicarboxylate: nitroso compounds such as dinitrosopentamethylenetetramine and trinitrosotrimethyltriamine; and hydrazide compounds. P, p '
-Oxybisbenzenesulfonylhydrazide and the like; sulfonylsemicarbazide-based compounds such as p, p'-oxybisbenzenesulfonylsemicardide and toluenesulfonylsemicarbazide can be suitably used, but not limited thereto. .

【0013】本発明で用いらる架橋剤としては、使用す
る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ぜしめるラジカ
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−ジーt−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−ジーt−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
キシジ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
ート等があるが、その時に使用される樹脂の種類によっ
て最適な有機過酸化物を選ばなければならない。
The cross-linking agent used in the present invention has a decomposition temperature higher than the flow start temperature of the resin to be used, and is decomposed by heating to generate free radicals to form intermolecular or intramolecular molecules. Organic peroxides which are radical generators that cause cross-linking, such as dicumyl peroxide, 1,1-di-tert-butylperoxy-3,3,5-trimethylcyclohexane, 2,5-dimethyl-2,5 -T-butyl peroxyhexane,
2,5-Dimethyl-2,5-di-tert-butylperoxyhexine, α, α-di-tert-butylperoxydiisopropylbenzene, tert-butyl peroxyketone, tert-butylperoxybenzoate, etc., used at that time The optimum organic peroxide must be selected according to the type of resin to be used.

【0014】本発明に於ては、使用する組成物の物性の
改良或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、或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、その他の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 lowering the price, a compounding agent (filler) which does not significantly affect cross-linking, for example, zinc oxide, titanium oxide, oxide, etc. Requires metal oxides such as calcium, magnesium oxide and silicon oxide, carbonates such as magnesium carbonate and calcium carbonate, or fibrous materials such as pulp, or various dyes, pigments, fluorescent materials, and other common rubber compounding agents. It can be added according to.

【0015】[0015]

【実施例】以下に実施例を挙げて本発明についてさらに
具体的に説明するが、本発明は下記実施例により何ら限
定されるものではない。 実施例1 スチレン系熱可塑性エラストマー(商品名:ラバロンS
J4400N、三菱油化(株)製)100重量部、アゾ
ジカルボンアミド17重量部、亜鉛華0.03重量部、
ステアリン酸亜鉛0.01重量部、尿素0.01重量
部、ジクミルパーオキサイド0.8重量部からなる組成
物を110℃のミキシングロールにて練和し、135℃
に加熱されたプレス内の金型(160x160x37m
m)に上記練和物を充填し、上記温度で50分間加圧下
で加熱し、前記組成物を整形した。次いで、該組成物
を、既に170℃に加熱されている気密でない開閉式の
金型(500x500x100mm)に入れ、ジャケッ
ト式により170℃の蒸気で140分間加熱し、冷却後
取り出し、発泡体を得た。得られた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4回通過させ
て気泡を破壊させ、気泡の連通化を行った。得られた連
通後の表皮付発泡体のサイズは500x500x100
mmであり、みかけ密度0.027g/cm、連続気
泡率100%であり、内部の気泡が均一であった。JI
S K 6767に準拠して、得られた連続気泡体の圧
縮永久歪を測定(50%、70℃で22時間圧縮し、2
0℃で(a)1時間放置、(b)24時間放置)した結
果、(a)34%、(b)35%であり、耐熱性の高い
ことがわかった。
EXAMPLES The present invention will be described more specifically with reference to the following examples, but the present invention is not limited to the following examples. Example 1 Styrene-based thermoplastic elastomer (trade name: Lavalon S)
J4400N, manufactured by Mitsubishi Yuka Co., Ltd.) 100 parts by weight, azodicarbonamide 17 parts by weight, zinc white 0.03 parts by weight,
A composition comprising 0.01 part by weight of zinc stearate, 0.01 part by weight of urea, and 0.8 part by weight of dicumyl peroxide was kneaded with a mixing roll at 110 ° C., and 135 ° C.
(160x160x37m)
m) was filled with the above kneaded material, and heated under pressure at the above temperature for 50 minutes to shape the composition. Next, the composition was placed in a non-hermetic open / close mold (500 × 500 × 100 mm) already heated to 170 ° C., heated with steam at 170 ° C. for 140 minutes by a jacket method, taken out after cooling, and a foam was obtained. . The obtained foam was passed four times between two constant-velocity rolls set at a roll interval of 20 mm to break bubbles, thereby making the bubbles open. The size of the obtained foam with skin after communication is 500 × 500 × 100.
mm, the apparent density was 0.027 g / cm 3 , the open cell ratio was 100%, and the internal air bubbles were uniform. JI
The compression set of the obtained open-cell foam was measured in accordance with S K 6767 (50%, compression at 70 ° C. for 22 hours, 2
(A) left at 0 ° C. for 1 hour and (b) left for 24 hours). As a result, it was found that (a) was 34% and (b) was 35%, indicating high heat resistance.

【0016】実施例2 スチレン系熱可塑性エラストマー(前出)70重量部と
低密度ポリエチレン(商品名:ユカロンYF−30、M
FR1.0、密度0.920g/cm三菱油化株式会
社製)30重量部を混合し、混合した樹脂100重量部
にジクミルパーオキサイドを0.7重量部添加した以外
は、実施例1と同じ配合及び同じ発泡条件、連通化条件
で、連続気泡体を得た。得られた連続気泡体のサイズ、
見掛け密度及び連続気泡率は、実施例1と同じであり、
実施例1と同じ方法で圧縮永久歪を測定した結果、
(a)35%、(b)36%であり、耐熱性の高いこと
がわかった。
Example 2 70 parts by weight of a styrene-based thermoplastic elastomer (described above) and low-density polyethylene (trade name: Yucalon YF-30, M
Example 1 except that 30 parts by weight of FR 1.0 and a density of 0.920 g / cm 3 manufactured by Mitsubishi Yuka Co., Ltd.) were mixed, and 0.7 part by weight of dicumyl peroxide was added to 100 parts by weight of the mixed resin. Under the same blending conditions and the same foaming conditions and communication conditions, open-celled bodies were obtained. The size of the resulting open cell,
Apparent density and open cell rate are the same as in Example 1,
As a result of measuring the compression set by the same method as in Example 1,
(A) 35% and (b) 36%, indicating high heat resistance.

【0017】実施例3 スチレン系熱可塑性エラストマー(前出)50重量部と
低密度ポリエチレン(前出)50重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
6重量部添加した以外は、実施例1と同じ配合及び同じ
発泡条件、連通化条件で、連続気泡体を得た。得られた
連続気泡体のサイズ、見掛け密度及び連続気泡率は、実
施例1と同じであり、実施例1と同じ方法で圧縮永久歪
を測定した結果、(a)36%、(b)37%であり、
耐熱性の高いことがわかった。 実施例4 スチレン系熱可塑性エラストマー(前出)30重量部と
低密度ポリエチレン(前出)70重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
5重量部添加した以外は、実施例1と同じ配合及び同じ
発泡条件、連通化条件で、連続気泡体を得た。得られた
連続気泡体のサイズ、見掛け密度及び連続気泡率は、実
施例1と同じであり、実施例1と同じ方法で圧縮永久歪
を測定した結果、(a)37%、(b)38%であり、
耐熱性の高いことがわかった。
Example 3 50 parts by weight of a styrene-based thermoplastic elastomer (supra) and 50 parts by weight of a low-density polyethylene (supra) were mixed, and 100 parts by weight of the mixed resin was mixed with 0.1 part of dicumyl peroxide.
Except for the addition of 6 parts by weight, an open-cell body was obtained under the same composition as in Example 1, under the same foaming conditions and communication conditions. The size, apparent density, and open cell ratio of the obtained open-cell foam were the same as those in Example 1. As a result of measuring the compression set by the same method as in Example 1, (a) 36%, (b) 37 %
It turned out that heat resistance was high. Example 4 30 parts by weight of a styrene-based thermoplastic elastomer (described above) and 70 parts by weight of a low-density polyethylene (described above) were mixed, and 100 parts by weight of the mixed resin was added with 0.1 part of dicumyl peroxide.
Except for adding 5 parts by weight, an open-celled body was obtained under the same composition as in Example 1, and under the same foaming conditions and communication conditions. The size, apparent density, and open cell rate of the obtained open-cell foam were the same as those in Example 1. As a result of measuring the compression set by the same method as in Example 1, (a) 37% and (b) 38 %
It turned out that heat resistance was high.

【0018】比較例1 スチレン系熱可塑性エラストマー(前出)10重量部と
低密度ポリエチレン(前出)90重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
45重量部添加した以外は、実施例1と同じ配合及び同
じ発泡条件、連通化条件で、連続気泡体を得た。得られ
た連続気泡体のサイズ、見掛け密度及び連続気泡率は、
実施例1と同じであり、実施例1と同じ方法で圧縮永久
歪を測定した結果、(a)43%、(b)43%であ
り、耐熱性が低く、熱圧成形されて厚みが回復しなかっ
た。 比較例2 エチレン−酢酸ビニル共重合体(商品名エバフレックス
P1403、酢酸ビニル含有率14重量%、デュポン−
三井ポリケミカル株式会社製)100重量部にジクミル
パーオキサイド0.6重量部を添加した以外は、実施例
1と同じ配合を用意し、ミキシングロールの温度を90
℃にした以外は、実施例1と同じ発泡及び連通化条件で
連続気泡体を得た。得られた連続気泡体のサイズ、見掛
け密度及び連続気泡率は、実施例1と同じであり、実施
例1と同じ方法で圧縮永久歪を測定した結果、(a)4
3%、(b)43%であり、耐熱性が低く、熱圧成形さ
れて厚みが回復しなかった。
COMPARATIVE EXAMPLE 1 10 parts by weight of a styrene-based thermoplastic elastomer (described above) and 90 parts by weight of a low-density polyethylene (described above) were mixed, and 100 parts by weight of the mixed resin was mixed with 0.1 part of dicumyl peroxide.
Except for the addition of 45 parts by weight, an open-cell body was obtained under the same composition as in Example 1, under the same foaming conditions and communication conditions. The size, apparent density and open cell rate of the obtained open cell,
It was the same as in Example 1, and the compression set was measured by the same method as in Example 1. As a result, (a) 43% and (b) 43%, the heat resistance was low, and the thickness was recovered by hot pressing. Did not. Comparative Example 2 Ethylene-vinyl acetate copolymer (trade name Evaflex P1403, vinyl acetate content 14% by weight, DuPont
Except that 0.6 parts by weight of dicumyl peroxide was added to 100 parts by weight of Mitsui Polychemicals Co., Ltd., the same formulation as in Example 1 was prepared.
An open cell was obtained under the same foaming and communicating conditions as in Example 1 except that the temperature was changed to ° C. The size, apparent density, and open cell rate of the obtained open-cell foam were the same as those in Example 1. As a result of measuring the compression set by the same method as in Example 1, (a) 4
3%, (b) 43%, heat resistance was low, and the thickness did not recover due to hot pressing.

【0019】[0019]

【発明の効果】以上のように、本発明の方法によれば、
スチレン系熱可塑性エラストマーを基材樹脂として使用
するため、得られる連続気泡体は、エチレン−酢酸ビニ
ル共重合体又は低密度ポリエチレンを基材とする連続気
泡体よりも、耐熱性に優れ、且つ、エチレン−酢酸ビニ
ル共重合体の連続気泡体と同等の弾性を有し、エアコ
ン、自動車等のパッキン材、シール材、断熱材として好
適である。又、スチレン系熱可塑性エラストマーにポリ
エチレン系樹脂を添加することにより、発泡工程におけ
る成形性及び加工性が良くなり、簡単な作業で物性が均
一で優れた連続気泡体を得ることができる。更に、スチ
レン系熱可塑性エラストマーとして、一般式、A−(B
−A)、(ここで、Aはスチレン、Bはブタジエンで
あり、nは1〜5の整数。)で表わされるブロック共重
合体の水素添加誘導体を使用することによって、二重結
合がないため、耐熱性、耐候性に特に優れた連続気泡体
を得ることができる。
As described above, according to the method of the present invention,
Since the styrene-based thermoplastic elastomer is used as the base resin, the obtained open-cell body has higher heat resistance than the open-cell body based on the ethylene-vinyl acetate copolymer or the low-density polyethylene, and It has the same elasticity as an open cell of ethylene-vinyl acetate copolymer, and is suitable as a packing material, a sealing material, and a heat insulating material for air conditioners and automobiles. Further, by adding a polyethylene resin to the styrene-based thermoplastic elastomer, the moldability and workability in the foaming step are improved, and an open cell having uniform properties and excellent physical properties can be obtained by a simple operation. Further, as a styrene-based thermoplastic elastomer, a compound represented by the general formula: A- (B
-A) n , wherein A is styrene, B is butadiene, and n is an integer of 1 to 5. By using a hydrogenated derivative of a block copolymer represented by the formula: Therefore, it is possible to obtain an open cell having particularly excellent heat resistance and weather resistance.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C08L 25:00 53:02 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI C08L 25:00 53:02

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 スチレン系熱可塑性エラストマーに発泡
剤及び架橋剤を添加混練し、得られた発泡性架橋性組成
物を気密でない金型中で加熱発泡させて気泡体を生成さ
せ、次いで機械的変形を加えて気泡を連通化させること
を特徴とする連続気泡体の製造方法
1. A foaming agent and a crosslinking agent are added and kneaded to a styrene-based thermoplastic elastomer, and the resulting foamable crosslinkable composition is heated and foamed in a non-hermetic mold to form a foam. A method for producing an open-cell body, characterized in that cells are made open by deformation.
【請求項2】 スチレン系熱可塑性エラストマー99〜
20重量部にポリエチレン系樹脂1〜80重量部を添加
したことを特徴とする請求項1記載の製造方法。
2. A styrenic thermoplastic elastomer 99 or more.
2. The method according to claim 1, wherein 1 to 80 parts by weight of the polyethylene resin is added to 20 parts by weight.
【請求項3】 スチレン系熱可塑性エラストマー70〜
30重量部とポリエチレン系樹脂30〜70重量部を添
加したことを特徴とする請求項1記載の製造方法。
3. A styrenic thermoplastic elastomer 70 to
The method according to claim 1, wherein 30 parts by weight and 30 to 70 parts by weight of a polyethylene resin are added.
【請求項4】 スチレン系熱可塑性エラストマーが、一
般式、A−(B−A)、(ここで、Aはスチレン、B
はブタジエンであり、nは1〜5の整数。)で表わされ
るブロック共重合体の水素添加誘導体から成る請求項
1,2又は3記載の製造方法。
4. A styrene-based thermoplastic elastomer represented by the general formula: A- (BA) n , wherein A is styrene and B is
Is butadiene, and n is an integer of 1 to 5. 4. The method according to claim 1, 2, or 3, which comprises a hydrogenated derivative of a block copolymer represented by the formula:
JP20008892A 1992-06-16 1992-06-16 Method for producing open-cell foam Expired - Fee Related JP3163588B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20008892A JP3163588B2 (en) 1992-06-16 1992-06-16 Method for producing open-cell foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20008892A JP3163588B2 (en) 1992-06-16 1992-06-16 Method for producing open-cell foam

Publications (2)

Publication Number Publication Date
JPH061872A JPH061872A (en) 1994-01-11
JP3163588B2 true JP3163588B2 (en) 2001-05-08

Family

ID=16418659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20008892A Expired - Fee Related JP3163588B2 (en) 1992-06-16 1992-06-16 Method for producing open-cell foam

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Country Link
JP (1) JP3163588B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5091388B2 (en) * 2002-08-15 2012-12-05 アドバンスド エラストマー システムズ,エル.ピー. Thermoplastic elastomer with enhanced foaming and physical properties
DE102017126429B4 (en) 2017-11-10 2021-03-18 Grammer Aktiengesellschaft Vehicle seat with an operating device and an adjusting device

Also Published As

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