JPH05214143A - Polypropylene-based resin crosslinked foam - Google Patents

Polypropylene-based resin crosslinked foam

Info

Publication number
JPH05214143A
JPH05214143A JP1892892A JP1892892A JPH05214143A JP H05214143 A JPH05214143 A JP H05214143A JP 1892892 A JP1892892 A JP 1892892A JP 1892892 A JP1892892 A JP 1892892A JP H05214143 A JPH05214143 A JP H05214143A
Authority
JP
Japan
Prior art keywords
weight
resin
ethylene
foam
melting point
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.)
Pending
Application number
JP1892892A
Other languages
Japanese (ja)
Inventor
Eiichi Takahashi
栄一 高橋
Toshihiro Arai
俊弘 新井
Hirobumi Inoue
博文 井上
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 JP1892892A priority Critical patent/JPH05214143A/en
Publication of JPH05214143A publication Critical patent/JPH05214143A/en
Pending legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain the subject foam having improved elongation at a high temperature, temperature dependence and bride during molding by crosslinking and expanding a fomable resin composition comprising a specific polypropylene- based resin, a thermal decomposition type blowing agent and a crosslinking auxiliary. CONSTITUTION:A fomable resin composition comprising (A) 100 pts.wt. total amount of a polypropylene-based resin composed of (i) 40-75 pts.wt. ethylene- propylene random copolymer having 3-7wt.% ethylene content and 130-145 deg.C melting point prepared by polymerization using a stereoregular catalyst, (ii) 5-40 pts.wt. ethylene-propylene-butene random copolymer having 1-7wt.% ethylene content, 1-7% butene content and 4-14wt.% total contents of ethylene and butene and 120-140 deg.C melting point prepared by polymerization using a stereoregular catalyst and (iii) 5-40 pts.wt. polyethylene-based resin having 105-135 deg.C melting point, (B) a thermal decomposition type blowing agent (e.g. azodicarbonamide) and (C) a crosslinking agent (e.g. divinylbenzene) is crosslinked and expanded to give the objective foam.

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、ポリプロピレン系樹脂
架橋発泡体に関し、更に詳しくは、高温領域での伸びや
抗張力が改善され、複雑で深い形状に対しても成形加工
性に優れたポリプロピレン系樹脂架橋発泡体に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polypropylene-based resin crosslinked foam, and more specifically, it has improved elongation and tensile strength in the high temperature region and is excellent in moldability even for complex and deep shapes. It relates to a resin crosslinked foam.

【0002】[0002]

【従来の技術】ポリプロピレン系樹脂に、熱分解型発泡
剤、及びジビニルベンゼンやエチレングリコールジメタ
クリレートなどの架橋助剤を添加し、有機過酸化物また
は電離性放射線を照射することにより架橋し、加熱発砲
して架橋発泡体を得ることは公知の技術である(特公昭
46−38716号、特開昭59−191107号、特
公昭60−28852号、特公平1−272641号な
ど)。
2. Description of the Related Art A polypropylene-based resin is added with a thermal decomposition type foaming agent and a crosslinking aid such as divinylbenzene or ethylene glycol dimethacrylate, which is crosslinked by being irradiated with an organic peroxide or ionizing radiation, and heated. It is a known technique to obtain a crosslinked foam by firing (Japanese Examined Patent Publication No. 46-38716, Japanese Unexamined Patent Publication No. 59-191107, Japanese Examined Patent Publication No. 60-28552, Japanese Examined Patent Publication No. 1-272641, etc.).

【0003】ポリプロピレン系樹脂架橋発泡体は、ポリ
オレフィン系樹脂架橋発泡体の中でも高い融点を持ち、
110〜120℃での伸びに優れているため、車両関係
をはじめとして、各種分野において汎用されている。し
かし、従来のポリプロピレン系樹脂架橋発泡体は、14
0〜160℃の高温領域では伸びが急速に低下し、高温
で成形すると形状保持性に劣るという問題がある。さら
に、ポリプロピレン系樹脂架橋発泡体は、高温での抗張
力が高く、複雑な形状に成形加工した場合、ブリッジ
(隙間)が生じるなどの問題があった。
Polypropylene resin crosslinked foam has a high melting point among polyolefin resin crosslinked foams,
Since it has excellent elongation at 110 to 120 ° C, it is widely used in various fields including vehicle-related products. However, the conventional polypropylene-based resin crosslinked foam has
There is a problem that elongation rapidly decreases in a high temperature range of 0 to 160 ° C, and shape retention is poor when molding at a high temperature. Further, the polypropylene-based resin crosslinked foam has a high tensile strength at high temperature, and has a problem that a bridge (gap) occurs when it is molded into a complicated shape.

【0004】最近の発泡体の成形分野において、例え
ば、車両内装材などでは、ドア、インスツルメントパネ
ル、コンソールボックス等の複雑な形状に加工された
り、深絞り成形が要求されている。また、生産性の向上
のための急加熱、それに伴う加工温度の上昇のため、特
に140〜160℃での伸び性(伸度)が要求される。
しかしながら、従来のポリプロピレン系樹脂架橋発泡体
は、温度依存性が大きく、これらの要求特性については
不十分であった。
In the recent field of foam molding, for example, vehicle interior materials are required to be processed into complicated shapes such as doors, instrument panels and console boxes, and deep drawing is required. Further, due to rapid heating for improving productivity and accompanying increase in processing temperature, extensibility (elongation) particularly at 140 to 160 ° C. is required.
However, the conventional polypropylene-based resin cross-linked foam has a large temperature dependency and is insufficient in these required properties.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、高温
での伸度、温度依存性、成形時のブリッジを改善し、高
温領域での深絞り成形性に優れたポリプロピレン系樹脂
架橋発泡体を提供することにある。
The object of the present invention is to improve the elongation at high temperature, the temperature dependence, the bridge at the time of molding, and the polypropylene resin crosslinked foam which is excellent in the deep drawing moldability in the high temperature region. To provide.

【0006】本発明者らは、鋭意研究した結果、樹脂成
分として、立体規則性触媒を用いて重合した2種類のポ
リプロピレン系樹脂と、ポリエチレン系樹脂とのブレン
ド物を使用し、常法により架橋・発砲させることによ
り、前記目的を達成できることを見いだし、その知見に
基づいて本発明を完成するに至った。
As a result of intensive studies, the inventors of the present invention used a blend of two kinds of polypropylene-based resin polymerized using a stereoregular catalyst and a polyethylene-based resin as a resin component, and cross-linked them by a conventional method. It was found that the above-mentioned object can be achieved by firing, and the present invention has been completed based on the findings.

【0007】[0007]

【課題を解決するための手段】本発明によれば、ポリプ
ロピレン系樹脂、熱分解型発泡剤及び架橋助剤を含む発
泡性樹脂組成物を架橋・発泡して成るポリプロピレン系
樹脂架橋発泡体において、該ポリプロピレン系樹脂が、
(a)立体規則性触媒を用いて重合され、エチレンの含
有量が3〜7重量%で、融点が130〜145℃のエチ
レン−プロピレンランダム共重合体40〜75重量部、
(b)立体規則性触媒を用いて重合され、エチレンの含
有量が1〜7重量%で、ブテンの含有量が1〜7重量%
であり、かつ、エチレンとブテンの含有量の合計が4〜
14重量%で、融点が120〜140℃のエチレン−プ
ロピレン−ブテンランダム共重合体5〜40重量部、及
び(c)融点が105〜135℃のポリエチレン系樹脂
5〜40重量部を含有するものである(合計100重量
部)ことを特徴とするポリプロピレン系樹脂架橋発泡体
が提供される。
According to the present invention, a polypropylene-based resin crosslinked foam obtained by crosslinking / foaming a foamable resin composition containing a polypropylene-based resin, a thermal decomposition type foaming agent and a crosslinking aid, The polypropylene resin is
(A) 40-75 parts by weight of an ethylene-propylene random copolymer polymerized using a stereoregular catalyst, having an ethylene content of 3-7% by weight and a melting point of 130-145 ° C.
(B) Polymerized using a stereoregular catalyst, the ethylene content is 1 to 7% by weight, and the butene content is 1 to 7% by weight.
And the total content of ethylene and butene is 4 to
14% by weight, 5 to 40 parts by weight of ethylene-propylene-butene random copolymer having a melting point of 120 to 140 ° C., and (c) 5 to 40 parts by weight of a polyethylene resin having a melting point of 105 to 135 ° C. (100 parts by weight in total) is provided, and a polypropylene resin crosslinked foam is provided.

【0008】以下、本発明について詳述する本発明で使
用するポリプロピレン系樹脂の1つは、立体規則性触媒
を用いて重合され、エチレンの含有量が3〜7重量%
で、融点が130〜145℃のエチレン−プロピレンラ
ンダム共重合体(樹脂a)である。エチレンの好ましい
含有量は3.5〜6重量%である。エチレン含有量が低
く、融点が高くなり過ぎると、高温での伸度が低下し
て、深絞り性が悪くなり、また、高温での抗張力が大き
くなるため、成形時にブリッジが生じやすい。
One of the polypropylene resins used in the present invention, which will be described in detail below, is polymerized using a stereoregular catalyst and has an ethylene content of 3 to 7% by weight.
And is an ethylene-propylene random copolymer (resin a) having a melting point of 130 to 145 ° C. The preferable content of ethylene is 3.5 to 6% by weight. When the ethylene content is low and the melting point is too high, the elongation at high temperature is lowered, the deep drawability is deteriorated, and the tensile strength at high temperature is increased, so that a bridge is likely to be formed at the time of molding.

【0009】本発明で使用するもう1つのポリプロピレ
ン系樹脂は、立体規則性触媒を用いて重合され、エチレ
ンの含有量が1〜7重量%で、ブテンの含有量が1〜7
重量%であり、かつ、エチレンとブテンの含有量の合計
が4〜14重量%で、融点が120〜140℃のエチレ
ン−プロピレン−ブテンランダム共重合体(樹脂b)で
ある。エチレンの含有量が2〜5重量%で、ブテンの含
有量が3〜5重量%であり、かつ、エチレンとブテンの
含有量の合計が6〜10重量%であることが好ましい。
エチレン及びブテンの含有量が低く、融点が高くなり過
ぎると、高温での伸度が低下して、深絞り性が悪くな
り、また、高温での抗張力が大きくなるため、成形時に
ブリッジが生じやすい。
Another polypropylene resin used in the present invention is polymerized by using a stereoregular catalyst and has an ethylene content of 1 to 7% by weight and a butene content of 1 to 7%.
It is an ethylene-propylene-butene random copolymer (resin b) having a total content of ethylene and butene of 4 to 14% by weight and a melting point of 120 to 140 ° C. It is preferable that the content of ethylene is 2 to 5% by weight, the content of butene is 3 to 5% by weight, and the total content of ethylene and butene is 6 to 10% by weight.
If the content of ethylene and butene is low and the melting point is too high, the elongation at high temperature will decrease, the deep drawability will deteriorate, and the tensile strength at high temperature will increase, so bridges are likely to occur during molding. ..

【0010】ポリプロピレン系樹脂(a)及び樹脂
(b)のメルトインデックス(MI)、分子量、分子量
分布などについては、特に限定されないが、MI(AS
TM D1238)が通常0.5〜15、重量平均分子
量(Mw)が18万〜29万、分子量分布(Mw/M
n)が3.3〜5.5のものが好ましい。
The melt index (MI), molecular weight, molecular weight distribution and the like of the polypropylene resin (a) and the resin (b) are not particularly limited, but MI (AS
TM D1238) is usually 0.5 to 15, weight average molecular weight (Mw) is 180,000 to 290,000, and molecular weight distribution (Mw / M).
It is preferable that n) is 3.3 to 5.5.

【0011】また、樹脂(a)及び樹脂(b)における
エチレンまたはブテンのポリプロピレン連鎖への入り方
は、どの部分にも均一に分布していること、すなわちラ
ンダム共重合体であることが望ましい。例えば、ポリプ
ロピレン連鎖中にエチレンのブロック部分が多いと、融
点のピークが2か所に発現したり、また、その結果、ポ
リプロピレンの分子鎖が長くなり、部分的に融点の高い
ホモポリプロピレンができてしまうため好ましくない。
In addition, in the resin (a) and the resin (b), the way ethylene or butene enters the polypropylene chain is preferably uniformly distributed in every portion, that is, a random copolymer. For example, if there are many ethylene blocks in the polypropylene chain, the melting point peaks will appear in two places, and as a result, the polypropylene molecular chain will become longer, and homopolypropylene with a partially higher melting point will be formed. It is not preferable because it will happen.

【0012】本発明で使用するポリエチレン系樹脂は、
融点が105〜135℃のポリエチレン系樹脂(樹脂
c)であり、例えば、低密度ポリエチレン、中密度ポリ
エチレン、高密度ポリエチレン、線状低密度ポリエチレ
ンなどが挙げられ、特に制限はないが、これらの中でも
線状低密度ポリエチレンが望ましい。
The polyethylene resin used in the present invention is
It is a polyethylene resin (resin c) having a melting point of 105 to 135 ° C., and examples thereof include low density polyethylene, medium density polyethylene, high density polyethylene, and linear low density polyethylene, but there is no particular limitation, but among these, Linear low density polyethylene is desirable.

【0013】各樹脂成分の配合割合は、樹脂(a)が4
0〜75重量部、好ましくは50〜70重量部、樹脂
(b)が5〜40重量部、好ましくは10〜30重量
部、樹脂(c)が5〜40重量部、好ましくは10〜3
0重量部である(合計100重量部)。
The resin (a) has a mixing ratio of 4 for each resin component.
0-75 parts by weight, preferably 50-70 parts by weight, resin (b) 5-40 parts by weight, preferably 10-30 parts by weight, resin (c) 5-40 parts by weight, preferably 10-3.
0 parts by weight (total 100 parts by weight).

【0014】これら樹脂成分の1つでも欠けると、深絞
り性が悪くなり、ブリッジを生じやすくなる。樹脂
(a)が多すぎると耐衝撃性が悪くなり、樹脂(b)が
多すぎると耐熱性が悪くなり、樹脂(c)が多すぎると
高温時の伸度が悪くなる。以上の樹脂成分に、熱分解型
発泡剤、架橋助剤、及び必要に応じて各種添加剤を加
え、公知のポリオレフィン系樹脂架橋発泡体の製造方法
により架橋発泡体を製造する。
If even one of these resin components is lacking, the deep drawability deteriorates, and a bridge is likely to occur. If the amount of the resin (a) is too large, the impact resistance will be poor, if the amount of the resin (b) is too large, the heat resistance will be poor, and if the amount of the resin (c) is too large, the elongation at high temperature will be poor. A thermal decomposition type foaming agent, a crosslinking aid, and various additives as required are added to the above resin components to produce a crosslinked foam by a known method for producing a polyolefin resin crosslinked foam.

【0015】具体的には、ポリプロピレン系樹脂、熱分
解型発泡剤、架橋助剤等を含む混合物をシート状などの
所定形状に成形し、電離性放射線を照射して架橋した
後、発泡剤の分解温度以上に加熱して発泡させる方法、
あるいは、ポリプロピレン系樹脂、熱分解型発泡剤、有
機過酸化物、架橋助剤等を含む混合物をシート状などの
所定形状に成形し、有機過酸化物及び発泡剤の分解温度
以上に加熱して架橋と発泡を行わせる方法などが挙げら
れる。成形加工性の観点からは、電離性放射線による照
射架橋法が好ましい。
Specifically, a mixture containing a polypropylene resin, a thermal decomposition type foaming agent, a cross-linking aid and the like is molded into a predetermined shape such as a sheet and irradiated with ionizing radiation to cross-link, and then the foaming agent Method of foaming by heating above the decomposition temperature,
Alternatively, a polypropylene resin, a pyrolytic foaming agent, an organic peroxide, a mixture containing a cross-linking aid, etc. is molded into a predetermined shape such as a sheet and heated to a temperature above the decomposition temperature of the organic peroxide and the foaming agent. Examples include a method of crosslinking and foaming. From the viewpoint of moldability, the irradiation crosslinking method using ionizing radiation is preferable.

【0016】熱分解型発泡剤としては、例えば、アゾジ
カルボンアミド(ADCA)、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、アゾジカ
ルボン酸バリウム、ジニトロソパンタメチレンテトラミ
ン、ヒドラゾジカルボンアミド等の加熱された時に分解
して気体を発生する化合物が用いられる。熱分解型発泡
剤の添加割合は、所望の発泡倍率に応じて適宜定めるこ
とができるが、通常、樹脂成分100重量部に対して、
2〜50重量部、好ましくは5〜30重量部である。
As the thermal decomposition type foaming agent, for example, azodicarbonamide (ADCA), oxybenzenesulfonyl hydrazide, azobisisobutyronitrile, barium azodicarboxylic acid, dinitrosopantamethylenetetramine, hydrazodicarbonamide, etc. can be heated. A compound is used that decomposes to generate a gas when exposed. The addition ratio of the thermal decomposition type foaming agent can be appropriately determined according to the desired expansion ratio, but usually 100 parts by weight of the resin component,
It is 2 to 50 parts by weight, preferably 5 to 30 parts by weight.

【0017】架橋助剤としては、例えば、ジビニルベン
ゼン(DVB)、ジアリルフタレート、エチレングリコ
ールジメタクリレート、トリメチロールプロパントリア
クリレート等の多官能モノマーを挙げることができる。
これらの架橋助剤の添加割合は、樹脂成分100重量部
に対して、通常1〜10重量部である。さらに必要に応
じて各種添加剤、例えば、抗酸化剤、顔料、紫外線吸収
剤、老化防止剤などを加えることができる。
Examples of the crosslinking aid include polyfunctional monomers such as divinylbenzene (DVB), diallyl phthalate, ethylene glycol dimethacrylate, and trimethylolpropane triacrylate.
The addition ratio of these crosslinking aids is usually 1 to 10 parts by weight with respect to 100 parts by weight of the resin component. Further, various additives such as antioxidants, pigments, ultraviolet absorbers, and antioxidants can be added if necessary.

【0018】これらの混合物を押出機(単軸、2軸)や
バンバリーミキサー、ニーダーなどで、発泡剤の分解温
度以下で溶融・混練し、押出して発泡性シートにする。
得られた発泡性シートに、電子線、α線、β線、γ線等
の電離性放射線を照射して架橋させ、さらに、これを熱
風循環オーブン、ソルトバスまたはメタルバス中で、発
泡剤の分解温度以上の温度で発泡させて、ポリプロピレ
ン系樹脂架橋発泡体とする。
The mixture is melted and kneaded at a temperature not higher than the decomposition temperature of the foaming agent with an extruder (single-screw, twin-screw), Banbury mixer, kneader, etc., and extruded into a foamable sheet.
The obtained foamable sheet is irradiated with ionizing radiation such as electron rays, α rays, β rays, and γ rays to be crosslinked, and further, this is treated with a foaming agent in a hot air circulation oven, a salt bath or a metal bath. A polypropylene resin crosslinked foam is obtained by foaming at a temperature equal to or higher than the decomposition temperature.

【0019】電離性放射線としては、電子線が好まし
く、照射線量は通常0.1〜50Mrad、好ましくは
0.5〜20Mradである。得られた架橋発泡体の架
橋度(ゲル分率)が20〜70%の範囲となるように照
射線量や架橋助剤の添加量等を調節することが好まし
い。架橋度が小さすぎると耐熱性が低下し、大きすぎる
と伸びなどの可撓性が低下する。
The ionizing radiation is preferably an electron beam, and the irradiation dose is usually 0.1 to 50 Mrad, preferably 0.5 to 20 Mrad. It is preferable to adjust the irradiation dose, the addition amount of the crosslinking aid, and the like such that the degree of crosslinking (gel fraction) of the obtained crosslinked foam is in the range of 20 to 70%. If the degree of crosslinking is too small, the heat resistance will decrease, and if it is too large, the flexibility such as elongation will decrease.

【0020】[0020]

【実施例】以下、本発明について、実施例および比較例
を挙げて具体的に説明するが、本発明は、これらの実施
例のみに限定されるものではない。なお、発泡体の物性
の測定方法は以下のとおりである。
EXAMPLES The present invention will be specifically described below with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples. The methods for measuring the physical properties of the foam are as follows.

【0021】〈架橋度〉発泡体約50mgを秤量し、1
20℃のキシレン中に24時間浸した後、それを取り出
し、8時間乾燥後に重さを測り、その重さを最初の発泡
体の重さで割ったものに100をかけて算出する。
<Crosslinking degree> About 50 mg of foam is weighed and
After soaking in xylene at 20 ° C. for 24 hours, it is taken out, dried for 8 hours, weighed, and then the weight is divided by the weight of the original foam, multiplied by 100.

【0022】〈伸度と抗張力〉温度条件を140℃また
は160℃に設定した保温箱に5分間放置した後、引張
試験機にて測定した。JIS K−6767に準拠。M
D:縦方向、TD:横方向。
<Elongation and Tensile Strength> After being left for 5 minutes in a heat-retaining box whose temperature condition was set at 140 ° C. or 160 ° C., it was measured by a tensile tester. Based on JIS K-6767. M
D: vertical direction, TD: horizontal direction.

【0023】〈深絞り性〉遠赤外線ヒーターにて発泡体
の表面温度が150〜160℃になるように設定し、図
1に示すような円柱状メス型を用いて真空成形を行い、
その成形時の深さ(H)と直径(D)との比(H/D)
で表示した。この値が大きいほど成形性が良好であるこ
とを示す。
<Deep drawing property> The far infrared heater was used to set the surface temperature of the foam to 150 to 160 ° C., and vacuum molding was performed using a cylindrical female die as shown in FIG.
Ratio (H / D) of depth (H) and diameter (D) at the time of molding
Displayed in. The larger this value is, the better the moldability is.

【0024】〈耐ブリッジ性〉図2に示すようなピラミ
ッド型(1)を作成して、発泡シートで覆い、型の中か
ら減圧して発泡シートを型に密着させた。まず、図3に
示すようにクランプで保持した発泡シート(2)を上下
からヒーター(3)で加熱し、次いで図4に示すように
型を発泡シートで覆い、減圧して型に密着させた。図5
に示すように、コーナー部に空隙(4)が発生した場合
には、耐ブリッジ性が不良であると評価し、図6に示す
ように発泡シートが型に密着して空隙を生じなかった場
合に耐ブリッジ性が良好であると評価した。評価は、目
視により次の3段階で行った。 ◎:発泡シートが型に完全に密着していた。 ○:発泡シートが型にほぼ密着していた。 ×:コーナーに空隙が生じていた。
<Bridge Resistance> A pyramid mold (1) as shown in FIG. 2 was prepared and covered with a foam sheet, and the foam sheet was depressurized to bring the foam sheet into close contact with the mold. First, as shown in FIG. 3, a foam sheet (2) held by a clamp was heated from above and below by a heater (3), and then the mold was covered with the foam sheet as shown in FIG. .. Figure 5
As shown in Fig. 6, when voids (4) were generated in the corners, it was evaluated that the bridge resistance was poor, and when the foam sheet was in close contact with the mold as shown in Fig. 6, no voids were formed. It was evaluated that the bridge resistance was good. The evaluation was visually conducted in the following three stages. A: The foamed sheet was completely adhered to the mold. ◯: The foamed sheet was in close contact with the mold. X: Voids were generated in the corners.

【0025】[実施例1]立体規則性触媒で重合され、
エチレン含有量3.6%、融点140℃のエチレン−プ
ロピレンランダム共重合体(樹脂a)70重量部、立体
規則性触媒で重合され、エチレン含有量3.0%、ブテ
ン含有量4.0%、融点126℃のエチレン−プロピレ
ン−ブテンランダム共重合体(樹脂b)10重量部、及
び融点120℃の線状低密度ポリエチレン(LLDP
E:樹脂c)20重量部に、アゾジカルボンアミド(A
DCA)10重量部、抗酸化剤1重量部、架橋剤として
ジビニルベンゼン(DVB)3重量部を加え、65mm
φ2軸押出機にて溶融混練し、厚さ1.0mmの発泡性
シートを得た。得られた発泡性シートに2.0Mrad
の電子線を照射した後、熱風循環式発泡炉で温度250
℃で発泡させ、厚み2.5mm、密度0.04g/cm
3の発泡体を得た。
Example 1 Polymerization with a stereoregular catalyst,
70% by weight of ethylene-propylene random copolymer (resin a) having an ethylene content of 3.6% and a melting point of 140 ° C., polymerized with a stereoregular catalyst, ethylene content of 3.0%, butene content of 4.0% , 10 parts by weight of ethylene-propylene-butene random copolymer (resin b) having a melting point of 126 ° C., and linear low-density polyethylene (LLDP) having a melting point of 120 ° C.
E: To 20 parts by weight of resin c), azodicarbonamide (A
65 mm by adding 10 parts by weight of DCA), 1 part by weight of antioxidant, and 3 parts by weight of divinylbenzene (DVB) as a cross-linking agent.
Melt-kneading was performed with a φ2 screw extruder to obtain a foamable sheet having a thickness of 1.0 mm. 2.0 Mrad on the resulting foamable sheet
After irradiating the electron beam of
Foamed at ℃, thickness 2.5mm, density 0.04g / cm
A foam of 3 was obtained.

【0026】[比較例1]樹脂成分として実施例1の樹
脂(a)70重量部と樹脂(c)30重量部を用いたこ
と以外は実施例1と全く同様にして、厚み2.5mm、
密度0.04g/cm3の発泡体を得た。この発泡体
は、高温時の伸度があまり良好ではなかった。また、耐
ブリッジ性も良くなかった。
Comparative Example 1 The same procedure as in Example 1 except that 70 parts by weight of the resin (a) and 30 parts by weight of the resin (c) of Example 1 were used as the resin components, and the thickness was 2.5 mm.
A foam having a density of 0.04 g / cm 3 was obtained. This foam did not have very good elongation at high temperature. Also, the bridge resistance was not good.

【0027】[実施例2]エチレン含有量4.5%、融
点138℃の樹脂(a)50重量部、エチレン含有量
3.0%、ブテン含有量4.0%、融点129℃の樹脂
(b)30重量部、融点122℃のLLDPE(樹脂
c)20重量部に、ADCA10重量部、抗酸化剤1重
量部、DVB3重量部を加えた以外は、実施例1と全く
同様にして、厚み2.5mm、密度0.04g/cm3
の発泡体を得た。この発泡体は、実施例1の発泡体より
も深絞り性及び耐ブリッジ性に優れていた。
Example 2 50 parts by weight of a resin (a) having an ethylene content of 4.5% and a melting point of 138 ° C., an ethylene content of 3.0%, a butene content of 4.0% and a melting point of 129 ° C. ( b) The same procedure as in Example 1 except that 10 parts by weight of ADCA, 1 part by weight of antioxidant, and 3 parts by weight of DVB were added to 20 parts by weight of LLDPE (resin c) having a melting point of 122 ° C. and 30 parts by weight. 2.5 mm, density 0.04 g / cm 3
To obtain a foam. This foam was more excellent in deep drawability and bridge resistance than the foam of Example 1.

【0028】[実施例3]樹脂成分として、エチレン含
有量5.5%、融点143℃の樹脂(a)60重量部、
エチレン含有量3.7%、ブテン含有量4.4%、融点
134℃の樹脂(b)20重量部、融点122℃のLL
DPE(樹脂c)20重量部を用いたこと遺骸は、実施
例1と全く同様にして、厚み2.5mm、密度0.04
g/cm3の発泡体を得た。
Example 3 As a resin component, 60 parts by weight of resin (a) having an ethylene content of 5.5% and a melting point of 143 ° C.,
Ethylene content 3.7%, butene content 4.4%, melting point 134 ° C. resin (b) 20 parts by weight, melting point 122 ° C. LL
The remains of using 20 parts by weight of DPE (resin c) were the same as in Example 1, and had a thickness of 2.5 mm and a density of 0.04.
A foam of g / cm 3 was obtained.

【0029】[実施例4]樹脂成分の配合割合を表1の
ように変えたこと以外は、実施例1と全く同様にして、
厚み2.5mm、密度0.04g/cm3の発泡体を得
た。この発泡体は、実施例1の発泡体より耐ブリッジ性
に優れていた。
Example 4 Except for changing the compounding ratio of the resin components as shown in Table 1, the same procedure as in Example 1 was carried out.
A foam having a thickness of 2.5 mm and a density of 0.04 g / cm 3 was obtained. This foam was superior to the foam of Example 1 in bridge resistance.

【0030】[比較例2]実施例3と全く同じ樹脂を用
い、樹脂(b)を40重量部にして、樹脂(c)を使用
しなかった以外は、実施例1と全く同様にして、厚み
2.5mm、密度0.04g/cm3の発泡体を得た。
この発泡体は触った感触がもろく、柔軟性に欠けてい
た。
[Comparative Example 2] The same procedure as in Example 1 was repeated except that the same resin as in Example 3 was used, the resin (b) was 40 parts by weight, and the resin (c) was not used. A foam having a thickness of 2.5 mm and a density of 0.04 g / cm 3 was obtained.
The foam had a soft feel to the touch and lacked flexibility.

【0031】[実施例5]実施例3と全く同じ樹脂で、
配合比だけを表1のように変えた以外は、実施例3と同
様にして、厚み2.5mm、密度0.04g/cm3
発泡体を得た。この発泡体は、実施例3の発泡体より耐
ブリッジ性にやや劣り、また、伸度もやや劣っていた。
[Example 5] The same resin as in Example 3 was used.
A foam having a thickness of 2.5 mm and a density of 0.04 g / cm 3 was obtained in the same manner as in Example 3 except that only the compounding ratio was changed as shown in Table 1. This foam was slightly inferior to the foam of Example 3 in bridging resistance and slightly inferior in elongation.

【0032】[実施例6]架橋剤をトリメチロールプロ
パントリアクリレート1重量部にした以外は、実施例1
と同様にして、厚み1.0mmのシートを得た。得られ
た発泡性シートに電子線を1.5Mrad照射した後、
熱風循環式オーブンで温度250℃で発泡させ、厚み
2.5mm、密度0.04g/cm3の発泡体を得た。
Example 6 Example 1 was repeated except that the cross-linking agent was 1 part by weight of trimethylolpropane triacrylate.
A sheet having a thickness of 1.0 mm was obtained in the same manner as in. After irradiating the obtained foamable sheet with an electron beam of 1.5 Mrad,
Foaming was performed at a temperature of 250 ° C. in a hot air circulation oven to obtain a foamed product having a thickness of 2.5 mm and a density of 0.04 g / cm 3 .

【0033】[比較例3]樹脂成分として、エチレン含
有量1.5%、融点149℃の樹脂(a)50重量部、
エチレン含有量1.5%、ブテン含有量1.0%、融点
148℃の樹脂(b)25重量部、及び融点120℃の
LLDPE(樹脂c)25重量部を用いたこと以外は、
実施例1と同様にして、厚み2.5mm、密度0.04
g/cm3の発泡体を得た。この発泡体は、140℃の
伸度と160℃の伸度の差が大きく、また、耐ブリッジ
性も良くなかった。
[Comparative Example 3] As a resin component, 50 parts by weight of a resin (a) having an ethylene content of 1.5% and a melting point of 149 ° C,
Except that 25 parts by weight of resin (b) having an ethylene content of 1.5%, butene content of 1.0%, a melting point of 148 ° C., and LLDPE (resin c) having a melting point of 120 ° C. were used,
Similar to Example 1, thickness 2.5 mm, density 0.04
A foam of g / cm 3 was obtained. This foam had a large difference between the elongation at 140 ° C. and the elongation at 160 ° C., and was also poor in bridge resistance.

【0034】[比較例4]実施例3と全く同じ種類の樹
脂で、樹脂(a)を使用せず、樹脂(b)70重量部と
樹脂(c)30重量部を用いたこと以外は、実施例1と
同様にして、厚み2.5mm、密度0.04g/cm3
の発泡体を得た。この発泡体は、140〜160℃の温
度依存性は小さかったが、絶対値が小さく、また、耐ブ
リッジ性も悪かった。これらの結果を一括して表1に示
す。
COMPARATIVE EXAMPLE 4 Except that the same kind of resin as in Example 3 was used, except that the resin (a) was not used and 70 parts by weight of the resin (b) and 30 parts by weight of the resin (c) were used. In the same manner as in Example 1, the thickness was 2.5 mm and the density was 0.04 g / cm 3.
To obtain a foam. This foam had a small temperature dependence at 140 to 160 ° C., but had a small absolute value and poor bridging resistance. The results are collectively shown in Table 1.

【0035】[0035]

【表1】 [Table 1]

【0036】[0036]

【発明の効果】本発明によれば、高温での伸度、温度依
存性、成形時のブリッジが改善され、高温領域での深絞
り成形性に優れたポリプロピレン系樹脂架橋発泡体が提
供される。本発明のポリプロピレン系樹脂架橋発泡体
は、特に車両用部材として好適である。
EFFECTS OF THE INVENTION According to the present invention, there is provided a polypropylene resin crosslinked foam which is improved in elongation at high temperature, temperature dependency and bridge at the time of molding and is excellent in deep drawability in a high temperature region. .. The polypropylene resin crosslinked foam of the present invention is particularly suitable as a vehicle member.

【図面の簡単な説明】[Brief description of drawings]

【図1】発泡体の深絞り性の測定に用いる型を説明した
図である。
FIG. 1 is a diagram illustrating a mold used for measuring the deep drawability of a foam.

【図2】発泡体の耐ブリッジ性の測定に用いる型を説明
した図である。
FIG. 2 is a diagram illustrating a mold used for measuring the bridging resistance of a foam.

【図3】発泡シートの加熱方法を説明した図である。FIG. 3 is a diagram illustrating a method for heating a foamed sheet.

【図4】加熱した発泡シートで型を覆う方法を説明した
図である。
FIG. 4 is a diagram illustrating a method of covering a mold with a heated foam sheet.

【図5】ブリッジの発生状態を説明した図である。FIG. 5 is a diagram illustrating a bridge generation state.

【図6】発泡シートが型に密着し、ブリッジのないこと
を説明した図である。
FIG. 6 is a diagram illustrating that the foam sheet is in close contact with the mold and has no bridge.

【符号の説明】[Explanation of symbols]

1 ピラミッド形状の型 2 発泡シート 3 ヒーター 4 隙間(ブリッジ) 1 Pyramid-shaped mold 2 Foamed sheet 3 Heater 4 Gap (bridge)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリプロピレン系樹脂、熱分解型発泡剤
及び架橋助剤を含む発泡性樹脂組成物を架橋・発泡して
成るポリプロピレン系樹脂架橋発泡体において、該ポリ
プロピレン系樹脂が、(a)立体規則性触媒を用いて重
合され、エチレンの含有量が3〜7重量%で、融点が1
30〜145℃のエチレン−プロピレンランダム共重合
体40〜75重量部、(b)立体規則性触媒を用いて重
合され、エチレンの含有量が1〜7重量%で、ブテンの
含有量が1〜7重量%であり、かつ、エチレンとブテン
の含有量の合計が4〜14重量%で、融点が120〜1
40℃のエチレン−プロピレン−ブテンランダム共重合
体5〜40重量部、及び(c)融点が105〜135℃
のポリエチレン系樹脂5〜40重量部を含有するもので
ある(合計100重量部)ことを特徴とするポリプロピ
レン系樹脂架橋発泡体。
1. A polypropylene resin crosslinked foam obtained by crosslinking and foaming a foamable resin composition containing a polypropylene resin, a thermal decomposition type foaming agent, and a crosslinking aid, wherein the polypropylene resin is a solid (a) solid. Polymerized using an ordered catalyst, ethylene content is 3 to 7% by weight, and melting point is 1.
40-75 parts by weight of an ethylene-propylene random copolymer having a temperature of 30 to 145 ° C., (b) is polymerized using a stereoregular catalyst, the content of ethylene is 1 to 7% by weight, and the content of butene is 1 to 1. 7% by weight, the total content of ethylene and butene is 4 to 14% by weight, and the melting point is 120 to 1
5 to 40 parts by weight of an ethylene-propylene-butene random copolymer at 40 ° C, and (c) a melting point of 105 to 135 ° C.
The polypropylene-based resin crosslinked foam containing 5 to 40 parts by weight of the polyethylene resin (total 100 parts by weight).
JP1892892A 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam Pending JPH05214143A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1892892A JPH05214143A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1892892A JPH05214143A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Publications (1)

Publication Number Publication Date
JPH05214143A true JPH05214143A (en) 1993-08-24

Family

ID=11985298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1892892A Pending JPH05214143A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Country Status (1)

Country Link
JP (1) JPH05214143A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005112884A (en) * 2003-10-02 2005-04-28 Mitsui Chemicals Inc Foamable polypropylene sheet and its production method
JP2006169404A (en) * 2004-12-16 2006-06-29 Sekisui Chem Co Ltd Foamed sheet of crosslinked polyolefinic resin
WO2006123569A1 (en) * 2005-05-18 2006-11-23 Toray Industries, Inc. Crosslinked polyolefin resin foam
WO2019189836A1 (en) * 2018-03-30 2019-10-03 積水化学工業株式会社 Polyolefin resin foam, method for producing polyolefin resin foam, and molded body

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005112884A (en) * 2003-10-02 2005-04-28 Mitsui Chemicals Inc Foamable polypropylene sheet and its production method
JP2006169404A (en) * 2004-12-16 2006-06-29 Sekisui Chem Co Ltd Foamed sheet of crosslinked polyolefinic resin
WO2006123569A1 (en) * 2005-05-18 2006-11-23 Toray Industries, Inc. Crosslinked polyolefin resin foam
WO2019189836A1 (en) * 2018-03-30 2019-10-03 積水化学工業株式会社 Polyolefin resin foam, method for producing polyolefin resin foam, and molded body
JP6591725B1 (en) * 2018-03-30 2019-10-16 積水化学工業株式会社 Polyolefin resin foam, method for producing polyolefin resin foam, and molded article

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