JPH0710933B2 - Method for producing crosslinked olefin resin foam - Google Patents
Method for producing crosslinked olefin resin foamInfo
- Publication number
- JPH0710933B2 JPH0710933B2 JP23319688A JP23319688A JPH0710933B2 JP H0710933 B2 JPH0710933 B2 JP H0710933B2 JP 23319688 A JP23319688 A JP 23319688A JP 23319688 A JP23319688 A JP 23319688A JP H0710933 B2 JPH0710933 B2 JP H0710933B2
- Authority
- JP
- Japan
- Prior art keywords
- foaming
- olefin resin
- temperature
- vinylalkoxysilane
- foam
- 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
Links
Landscapes
- 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、ポリオレフィン系樹脂架橋発泡体の製造方法
に関する。TECHNICAL FIELD The present invention relates to a method for producing a polyolefin resin crosslinked foam.
[従来の技術] オレフィン系樹脂発泡体は、独立気泡を有し柔軟で断熱
性および機械的強度が大きいという特性を有しているた
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。[Prior Art] Olefin resin foams are widely used in various fields as heat insulating materials and cushioning materials because they have the characteristics of having closed cells, flexibility, heat insulating properties and high mechanical strength. There is.
このようなオレフィン系樹脂発泡体の製造方法として
は、たとえばビニルアルコキシシランの縮合反応を利用
した方法が知られている。このビニルアルコキシシラン
を用いたオレフィン系樹脂の発泡方法は、予めビニルア
ルコキシシランをグラフト反応もしくは共重合させたオ
レフィン系樹脂に化学分解型発泡剤を混合し、たとえば
押出成形法によって発泡性樹脂組成物素シートを作製す
る。次いで、この発泡性樹脂組成物素シートを樹脂の融
点未満および発泡剤の分解温度未満の温度の熱水槽また
は水蒸気槽中に長時間浸漬し、発泡に必要な縮合反応架
橋を得た後、発泡剤の分解温度以上の温度に加熱して発
泡させると同時にまたはその後に、さらに架橋させる方
法である。As a method for producing such an olefin resin foam, for example, a method utilizing a condensation reaction of vinylalkoxysilane is known. The method for foaming an olefin resin using this vinylalkoxysilane is a foamable resin composition obtained by mixing a chemically decomposable foaming agent with an olefin resin obtained by graft-reacting or copolymerizing vinylalkoxysilane in advance, for example, by an extrusion molding method. A blank sheet is prepared. Then, this foamable resin composition elemental sheet is immersed for a long time in a hot water tank or a steam tank at a temperature lower than the melting point of the resin and lower than the decomposition temperature of the foaming agent to obtain condensation reaction crosslinks necessary for foaming, and then foaming. At the same time as or after foaming by heating to a temperature equal to or higher than the decomposition temperature of the agent, further crosslinking is performed.
[発明が解決しようとする課題] 上述したビニルアルコキシシランを用いたオレフィン系
樹脂の発泡方法は、発泡と同時にまたはその後にさらに
架橋が進行するため、高架橋になり熱寸法安定性の高い
発泡体が得られるという利点を有している半面、以下に
示すような欠点があった。[Problems to be Solved by the Invention] In the method for foaming an olefin resin using vinylalkoxysilane described above, since cross-linking proceeds further simultaneously with or after foaming, a highly cross-linked foam having high thermal dimensional stability is obtained. On the other hand, it has the advantage that it can be obtained, but has the following drawbacks.
すなわち、発泡工程の前工程として、発泡に必要な架橋
を得るために熱水槽や水蒸気槽によって長時間の処理が
必要であり、このため生産性が極めて低いという問題が
あった。また、熱水槽や水蒸気槽での架橋工程における
架橋度が一定せず、これにより気泡径や外観などの品質
にバラツキが生じやすいという問題もあった。さらに、
この品質のバラツキが発生しやすいという問題は、熱水
槽や水蒸気槽による反応をはやめるために、たとえばジ
ブチルスズジラウレートのような縮合反応触媒を使用す
ると、押出機などの成形機内で部分的に架橋が発生しや
すくなり、これによってさらに顕著となる。That is, as a pre-step of the foaming step, a hot water tank or a steam tank requires a long-time treatment in order to obtain the cross-linking necessary for foaming, which causes a problem of extremely low productivity. There is also a problem that the degree of cross-linking in the cross-linking process in the hot water tank or the steam tank is not constant, which tends to cause variations in quality such as bubble diameter and appearance. further,
The problem that this quality variation easily occurs is that when a condensation reaction catalyst such as dibutyltin dilaurate is used to stop the reaction in the hot water tank or the steam tank, partial crosslinking occurs in a molding machine such as an extruder. It is more likely to occur, which makes it more prominent.
本発明は、このような従来技術の課題に対処するために
なされたもので、生産性を向上させるとともに品質を安
定させ、かつ従来法と同様に熱寸法安定性の高いオレフ
ィン系樹脂架橋発泡体を製造する方法を提供することを
目的としている。The present invention has been made to address such a problem of the conventional art, and improves the productivity, stabilizes the quality, and has the same high dimensional stability as that of the conventional method. It is intended to provide a method of manufacturing.
[課題を解決するための手段] すなわち本発明は、ビニルアルコキシシランをグラフト
反応もしくは共重合させたオレフィン系樹脂と化学分解
型発泡剤とを少なくとも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所望の形状に成形す
る工程と、この成形物に放射線もしくは電子線を照射し
前記オレフィン系樹脂をラジカル反応架橋させる工程
と、このラジカル反応架橋させた成形物を前記化学分解
型発泡剤の分解温度以上に加熱し発泡させるとともに前
記ビニルアルコキシシランによる縮合反応架橋を生じさ
せる工程とを有することを特徴としている。[Means for Solving the Problem] That is, the present invention is to decompose a chemical decomposition type foaming agent by mixing a mixed raw material containing at least an olefin resin graft-polymerized or copolymerized with vinylalkoxysilane and a chemical decomposition type foaming agent. A step of molding into a desired shape at a temperature lower than a temperature, a step of irradiating the molded article with radiation or an electron beam to radically react and crosslink the olefin resin, and the radically crosslinked molded article to the chemically decomposing type. And a step of heating the foaming agent at a temperature equal to or higher than the decomposition temperature for foaming and causing condensation reaction crosslinking by the vinylalkoxysilane.
本発明において使用するオレフィン系樹脂としては、低
密度ポリエチレン(直鎖状を含む)、高密度ポリエチレ
ン、ポリプロピレン、エチレン−プロピレン共重合体、
エチレンと酢酸ビニル、アクリル酸、メタクリル酸など
との共重合体などが例示され、これらを単独であるいは
2種以上の混合物として用いる。As the olefin resin used in the present invention, low density polyethylene (including linear), high density polyethylene, polypropylene, ethylene-propylene copolymer,
Examples thereof include copolymers of ethylene and vinyl acetate, acrylic acid, methacrylic acid and the like, and these are used alone or as a mixture of two or more kinds.
また、本発明におけるビニルアルコキシシランとして
は、ビニルトリメトキシシラン、ビニルトリエトキシシ
ランなどが例示される。そして、これらビニルアルコキ
シシランを予めオレフィン系樹脂に対してグラフト反応
または共重合させたものを出発原料として用いる。これ
らビニルアルコキシシランのグラフト反応量または共重
合量は、モノマー比として0.2〜2.5重量%が好ましく、
より好ましくは0.7〜1.5重量%の範囲である。In addition, examples of the vinylalkoxysilane in the present invention include vinyltrimethoxysilane and vinyltriethoxysilane. Then, those obtained by graft-reacting or copolymerizing these vinylalkoxysilanes with an olefin resin in advance are used as starting materials. The graft reaction amount or copolymerization amount of these vinylalkoxysilanes is preferably 0.2 to 2.5% by weight as a monomer ratio,
The range is more preferably 0.7 to 1.5% by weight.
化学分解型発泡剤としては、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などが例示され、こ
れらを上記樹脂材料に対して適量添加混合し、この混合
原料を用いて押出成形などによって発泡性樹脂組成物素
シートを作製する。この混合原料中には、必要に応じて
滑剤、難燃剤、帯電防止剤、着色剤などを添加すること
が可能である。Examples of the chemically decomposable foaming agent include azodicarbonamide, oxybenzenesulfonyl hydrazide, and the like. An appropriate amount of these is added to the above resin material and mixed, and a foamable resin composition element is formed by extrusion molding using this mixed raw material. Make a sheet. If necessary, a lubricant, a flame retardant, an antistatic agent, a coloring agent, etc. can be added to this mixed raw material.
次に、発泡性樹脂組成物素シートに対して放射線あるい
は電子線を照射し、発泡性樹脂組成物素シート中のオレ
フィン系樹脂をラジカル反応架橋させ、発泡に必要な樹
脂粘度を得るための架橋を得る。Next, the foamable resin composition elemental sheet is irradiated with radiation or an electron beam to radically crosslink the olefinic resin in the foamable resin composition elemental sheet and crosslink to obtain the resin viscosity necessary for foaming. To get
この後、化学分解型発泡剤の分解温度以上の温度に加熱
することによって発泡させる。この発泡工程の際に、発
泡と同時にもしくは発泡の後にビニルアルコキシシラン
による縮合反応架橋が進行する。このビニルアルコキシ
シランによる縮合反応架橋は、発泡に要する加熱と樹脂
中または加熱処理時の雰囲気、たとえば空気中の微量水
分によって充分に達成される。After that, the foaming is performed by heating to a temperature equal to or higher than the decomposition temperature of the chemical decomposition type foaming agent. During this foaming step, condensation reaction crosslinking with vinylalkoxysilane proceeds simultaneously with or after foaming. The condensation reaction crosslinking with the vinylalkoxysilane is sufficiently achieved by the heating required for foaming and the trace amount of water in the resin or the atmosphere during the heat treatment, for example, air.
[作 用] ビニルアルコキシンランをグラフト反応もしくは共重合
させたオレフィン系樹脂に対して、予め放射線または電
子線を照射することによって、オレフィン系樹脂はラジ
カル反応架橋を起こし、発泡に必要な架橋が得られる。
この放射線や電子線による架橋は、生産効率が高いとと
もに架橋度も一定している。したがって、この後に行う
発泡工程において、気泡径の均一な気泡が得られやす
く、また外観品質も安定する。そして、化学分解型発泡
剤の分解温度以上の温度で発泡処理することによって、
発泡処理時の熱と樹脂中や処理雰囲気中の微量の水分と
でビニルアルコキシシランの縮合反応架橋が発泡時にあ
るいはその後に進行し、発泡気泡の残留歪が緩和される
とともに高架橋となり、熱寸法安定性に優れた発泡体が
得られる。[Operation] By irradiating the olefin resin graft-reacted or copolymerized with vinylalkoxylane with radiation or electron beam in advance, the olefin resin undergoes radical reaction cross-linking to obtain the cross-linking necessary for foaming. To be
Crosslinking by radiation or electron beams has high production efficiency and a constant degree of crosslinking. Therefore, in the subsequent foaming step, it is easy to obtain bubbles having a uniform bubble diameter and the appearance quality is stable. Then, by performing the foaming treatment at a temperature equal to or higher than the decomposition temperature of the chemical decomposition type foaming agent,
The condensation reaction crosslinking of vinylalkoxysilane progresses during or after foaming due to the heat during foaming treatment and a small amount of water in the resin or processing atmosphere, and the residual strain of the foam bubbles is alleviated and highly crosslinked, resulting in thermal dimensional stability. A foam having excellent properties is obtained.
[実施例] 次に、本発明の実施例について説明する。[Examples] Next, examples of the present invention will be described.
実施例 M1(メルトインデックス)4.5g/10分、密度0.924、融点
ピーク112℃の低密度ポリエチレン100重量部に対し、ビ
ニルトリメトキシシラン1.2重量部、ジクミルペルオキ
サイド0.2重量部を加えて充分に混合した後、直径65mm
の2軸押出機で樹脂温度200℃の条件によって押出し、
ビニルメトキシシランをグラフト反応させたポリエチレ
ン(以下、GPEと略す)を作製した。Example M1 (melt index) 4.5 g / 10 minutes, density 0.924, melting point peak 112 ℃ to 100 parts by weight of low-density polyethylene, 1.2 parts by weight of vinyltrimethoxysilane, 0.2 parts by weight of dicumyl peroxide was added sufficiently. 65mm diameter after mixing
Extruded with a twin screw extruder at a resin temperature of 200 ° C,
A polyethylene (hereinafter abbreviated as GPE) was prepared by graft reaction with vinylmethoxysilane.
次に、上記GPE100重量部に対して化学分解型発泡剤とし
てアゾジカルボンアミド15重量部を添加混合し、直径65
mmの2軸押出機で樹脂温度150℃以下の条件によって押
出し、厚さ1.5mmの発泡性樹脂組成物素シートを作製し
た。Next, 15 parts by weight of azodicarbonamide as a chemically decomposing foaming agent was added to 100 parts by weight of the above GPE and mixed to give a diameter of 65.
Extrusion was carried out under a condition of a resin temperature of 150 ° C. or less by a twin-screw extruder of mm to prepare a foamable resin composition material sheet having a thickness of 1.5 mm.
次いで、この発泡性樹脂組成物素シートに電子線照射機
で3.4Mradの電子線を照射してポリエチレンをラジカル
反応架橋させた。Next, this foamable resin composition element sheet was irradiated with an electron beam of 3.4 Mrad by an electron beam irradiator to radically crosslink polyethylene.
この後、このラジカル反応架橋させた発泡性樹脂組成物
素シートを約250℃に設定した加熱炉中に配置し、発泡
処理を行って厚さ4mm(発泡倍率:約31倍)の発泡体を
得た。Then, the radical reaction cross-linkable foamable resin composition elemental sheet is placed in a heating furnace set at about 250 ° C., and foaming treatment is performed to form a foam having a thickness of 4 mm (foaming ratio: about 31 times). Obtained.
このようにして得た発泡体の架橋度をゲル分率評価法
(測定方法:試験片を130℃のキシレンに24時間浸漬
し、非溶解分を乾燥した後に重量測定し、初期の重量に
対する比率として評価)によって測定した。まず、電子
線を照射した後の発泡性樹脂組成物素シートは35%であ
り、発泡後は72%であった。また、発泡体は気泡が細か
く均一で、外観も表面平滑性に優れたものであった。The degree of cross-linking of the foam thus obtained was evaluated by the gel fraction evaluation method (measurement method: the test piece was immersed in xylene at 130 ° C. for 24 hours, the insoluble matter was dried and then weighed, and the ratio to the initial weight was measured. Was evaluated). First, the expandable resin composition raw sheet after irradiation with an electron beam was 35%, and after foaming was 72%. Further, the foam had fine and uniform cells, and the appearance was also excellent in surface smoothness.
また、本発明との比較として、電子線を照射して架橋さ
せる代りに、95℃の熱水槽に65分間浸漬して架橋させる
以外は、上記実施例と同一条件で厚さ4mm(発泡倍率:
約30倍)の発泡体を作製した。Further, as a comparison with the present invention, instead of irradiating with an electron beam to crosslink, except for dipping in a hot water bath at 95 ° C for 65 minutes to crosslink, a thickness of 4 mm (foaming ratio:
About 30 times) foam was prepared.
この発泡体についても上記実施例と同様にして架橋度を
測定したところ、熱水槽処理後の素シートは38%で、発
泡後は67%であった。The degree of cross-linking of this foam was measured in the same manner as in the above-mentioned example, and it was 38% in the raw sheet after the hot water bath treatment and 67% after the foaming.
これら実施例および比較例で作製した発泡体をそれぞれ
150mm×150mmに切断し、120℃の加熱炉中に24時間放置
して寸法の変化率を測定した。その結果を次表に示す。The foams produced in these examples and comparative examples are respectively
It was cut into 150 mm x 150 mm and left in a heating furnace at 120 ° C for 24 hours to measure the dimensional change rate. The results are shown in the table below.
この表の結果からも明らかなように、この実施例による
発泡体は、熱水槽処理を行った従来法による発泡体と熱
寸法安定性はほとんど遜色なく、品質的には気泡径がむ
しろ細かく、表面の平滑性も優れたものであった。 As is clear from the results in this table, the foam according to this example has almost the same thermal dimensional stability as the foam according to the conventional method subjected to the hot water bath treatment, and the bubble diameter is rather fine in terms of quality. The surface smoothness was also excellent.
[発明の効果] 以上の実施例からも明らかなように、本発明のオレフィ
ン系樹脂架橋発泡体の製造方法によれば、発泡に必要な
架橋を電子線や放射線の照射によって得ているので、従
来の熱水槽等による処理に比べて大幅に生産効率が向上
するとともに、架橋度も一定することによって気泡や外
観の品質も向上する。さらに、従来法と同様に発泡時ま
たはその後に架橋が進行するので、熱寸法安定性に優れ
た発泡体が得られる。[Effects of the Invention] As is clear from the above examples, according to the method for producing an olefin resin crosslinked foam of the present invention, since the crosslinking necessary for foaming is obtained by irradiation with an electron beam or radiation, Compared with the conventional treatment using a hot water tank or the like, the production efficiency is significantly improved, and the constant degree of crosslinking also improves the quality of bubbles and appearance. Further, since the crosslinking proceeds during or after foaming as in the conventional method, a foam having excellent thermal dimensional stability can be obtained.
Claims (1)
しくは共重合させたオレフィン系樹脂と化学分解型発泡
剤とを少なくとも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所望の形状に成形する工程
と、この成形物に放射線もしくは電子線を照射し前記オ
レフィン系樹脂をラジカル反応架橋させる工程と、この
ラジカル反応架橋させた成形物を前記化学分解型発泡剤
の分解温度以上に加熱し発泡させるとともに前記ビニル
アルコキシシランによる縮合反応架橋を生じさせる工程
とを有することを特徴とするオレフィン系樹脂架橋発泡
体の製造方法。1. A mixed raw material containing at least an olefin resin graft-polymerized or copolymerized with vinylalkoxysilane and a chemical decomposition type blowing agent is formed into a desired shape at a temperature lower than the decomposition temperature of the chemical decomposition type blowing agent. A step of molding, a step of irradiating the molded article with radiation or an electron beam to radically crosslink the olefin resin, and heating the molded article subjected to radical reaction crosslinking to a temperature not lower than the decomposition temperature of the chemical decomposition type foaming agent. And a step of causing the condensation reaction crosslinking with the vinylalkoxysilane to occur, and a method for producing an olefin-based resin crosslinked foam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23319688A JPH0710933B2 (en) | 1988-09-16 | 1988-09-16 | Method for producing crosslinked olefin resin foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23319688A JPH0710933B2 (en) | 1988-09-16 | 1988-09-16 | Method for producing crosslinked olefin resin foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0280436A JPH0280436A (en) | 1990-03-20 |
| JPH0710933B2 true JPH0710933B2 (en) | 1995-02-08 |
Family
ID=16951254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23319688A Expired - Fee Related JPH0710933B2 (en) | 1988-09-16 | 1988-09-16 | Method for producing crosslinked olefin resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0710933B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3782458B2 (en) * | 1995-09-29 | 2006-06-07 | ザ ダウ ケミカル カンパニー | Cross-linked polyolefin foam and method for producing the same |
| US6124370A (en) * | 1999-06-14 | 2000-09-26 | The Dow Chemical Company | Crosslinked polyolefinic foams with enhanced physical properties and a dual cure process of producing such foams |
-
1988
- 1988-09-16 JP JP23319688A patent/JPH0710933B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0280436A (en) | 1990-03-20 |
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