JPH05214144A - Polypropylene-based resin crosslinked foam - Google Patents

Polypropylene-based resin crosslinked foam

Info

Publication number
JPH05214144A
JPH05214144A JP1892992A JP1892992A JPH05214144A JP H05214144 A JPH05214144 A JP H05214144A JP 1892992 A JP1892992 A JP 1892992A JP 1892992 A JP1892992 A JP 1892992A JP H05214144 A JPH05214144 A JP H05214144A
Authority
JP
Japan
Prior art keywords
resin
weight
parts
polypropylene
based resin
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
JP1892992A
Other languages
Japanese (ja)
Inventor
Eiichi Takahashi
栄一 高橋
Toshihiro Arai
俊弘 新井
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 JP1892992A priority Critical patent/JPH05214144A/en
Publication of JPH05214144A publication Critical patent/JPH05214144A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the subject foam having improved elongation and tensile force in a high temperature range, excellent moldability and processability by crosslinking and foaming an expandable resin composition comprising a specific polyolefin-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) 10-60 pts.wt. polypropylene-based resin (e.g. ethylene-propylene block copolymer having two or more total peaks of one peak in 100-135 deg.C and one peak in 135-175 deg.C prepared by polymerization using a stereoregular catalyst, (ii) 10-80 pts.wt. ethylene- propylenebutene random copolymer having 1-10wt.% ethylene content and 125-160 deg.C melting point prepared by polymerization using a stereoregular catalyst and (iii) 10-80 pts.wt. polyethylene-based resin (preferably linear low-density polyethylene), (B) a thermal decomposition type blowing agent and (C) a crosslinking agent 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、ポリオレフィン系樹脂
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
性に優れたポリオレフィ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 polyolefin resin cross-linked foam, and more specifically, it has improved elongation and tensile strength in the high temperature range 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 Patent Publication No. 46-38716, Japanese Patent Publication No. 59-191107, Japanese Patent Publication No. 60-28552, Japanese 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
での伸び性、特に140〜160℃での伸び性を改善
し、温度依存性が少なく、深絞り成形性に優れたポリオ
レフィ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 extensibility at high temperature, particularly the extensibility at 140 to 160 ° C., the temperature dependency is small, and the polyolefin resin is excellent in deep drawability. To provide a crosslinked foam.

【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、ポリオ
レフィン系樹脂、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・発泡して成るポリオレフィン系
樹脂架橋発泡体において、該ポリオレフィン系樹脂が、
(1)立体規則性触媒を用いて重合され、少なくとも1
00℃以上135℃未満の間に1つと、135℃以上1
75℃以下の間に1つの合計2つ以上の融点ピークを有
するポリプロピレン系樹脂10〜60重量部、(2)立
体規則性触媒を用いて重合され、エチレン含有量が1〜
10重量%で、融点が125〜160℃のエチレン−プ
ロピレンランダム共重合体10〜80重量部、及び
(3)ポリエチレン系樹脂10〜80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
オレフィン系樹脂架橋発泡体が提供される。
According to the present invention, a polyolefin resin crosslinked foam obtained by crosslinking and foaming a foamable resin composition containing a polyolefin resin, a thermal decomposition type foaming agent and a crosslinking aid, The polyolefin resin is
(1) Polymerized with a stereoregular catalyst to obtain at least 1
One between 00 ℃ and less than 135 ℃, and 135 ℃ or more 1
10 to 60 parts by weight of a polypropylene resin having a total of two or more melting point peaks at 75 ° C. or lower, (2) polymerized using a stereoregular catalyst, and having an ethylene content of 1 to 1
10% by weight and 10 to 80 parts by weight of ethylene-propylene random copolymer having a melting point of 125 to 160 ° C., and (3) 10 to 80 parts by weight of polyethylene resin (total 100 parts by weight). A cross-linked foamed polyolefin resin is provided.

【0008】以下、本発明について詳述する。本発明で
用いられるポリプロピレン系樹脂(1)は、立体規則性
触媒を用い、気相法、バルク重合法などにより重合さ
れ、少なくとも100℃以上135℃未満の間に1つ
と、135℃以上175℃以下の間に1つの合計2つ以
上の融点ピークを有するポリプロピレン系樹脂である。
この融点ピークは、差動走査熱量計(DSC)により1
0℃/分の速度で昇温した際に得られる吸熱ピークであ
る。
The present invention will be described in detail below. The polypropylene resin (1) used in the present invention is polymerized by a gas phase method, a bulk polymerization method or the like using a stereoregular catalyst, and at least one resin is present between 100 ° C. and 135 ° C. and 135 ° C. or higher and 175 ° C. It is a polypropylene resin having a total of two or more melting point peaks between the following:
This melting point peak is 1 by a differential scanning calorimeter (DSC).
It is an endothermic peak obtained when the temperature is raised at a rate of 0 ° C./min.

【0009】ポリプロピレン系樹脂(1)は、エチレン
−プロピレンブロック共重合体に代表される樹脂であ
り、エチレンのブロック部分と、プロピレンのブロック
部分の2種類の融点ピークが存在する。また、プロピレ
ンに共重合されるものは、エチレンに限らず、ブテン、
オクテン、4−メチルペンテン等でもよい。
The polypropylene resin (1) is a resin represented by an ethylene-propylene block copolymer, and has two kinds of melting point peaks of an ethylene block portion and a propylene block portion. Further, what is copolymerized with propylene is not limited to ethylene, butene,
Octene, 4-methylpentene, etc. may be used.

【0010】ポリプロピレン系樹脂(1)のコモノマー
成分は、通常3〜30重量%、望ましくは7〜15重量
%である。融点ピークの低い方は、望ましくは120〜
130℃であり、高い方の融点は、望ましくは150〜
165℃である。低い方の融点が100℃未満であると
発泡体の耐熱性が不十分となり、高い方の融点が175
℃を越えると、押出成形性が損なわれ、しかも発泡体の
高温での抗張力が高くなり成形加工性が悪くなる。 ポ
リプロピレン系樹脂(1)のメルトインデックス(M
I;ASTM D1238)は、通常0.5〜15程度
である。
The comonomer component of the polypropylene resin (1) is usually 3 to 30% by weight, preferably 7 to 15% by weight. The lower melting point peak is preferably 120-
130 ° C., the higher melting point is preferably 150-
165 ° C. When the lower melting point is less than 100 ° C, the heat resistance of the foam becomes insufficient, and the higher melting point is 175
If the temperature exceeds ℃, extrusion moldability will be impaired, and the tensile strength of the foam at high temperature will be high, resulting in poor moldability. Polypropylene resin (1) melt index (M
I; ASTM D1238) is usually about 0.5 to 15.

【0011】ポリプロピレン系樹脂(2)は、立体規則
性触媒を用いて重合され、エチレン含有量が1〜10重
量%で、融点が125〜160℃のエチレン−プロピレ
ンランダム共重合体である。エチレン含有量は、望まし
くは2〜6重量%であり、また、融点は、望ましくは1
30〜150である。ポリプロピレン系樹脂(2)のM
Iは、通常0.5〜15程度である。
The polypropylene resin (2) is an ethylene-propylene random copolymer which is polymerized by using a stereoregular catalyst and has an ethylene content of 1 to 10% by weight and a melting point of 125 to 160 ° C. The ethylene content is preferably 2 to 6% by weight, and the melting point is preferably 1
30 to 150. Polypropylene resin (2) M
I is usually about 0.5 to 15.

【0012】ポリエチレン系樹脂(3)は、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、エチレン−酢酸ビニル共重合
体、エチレン−ブテン共重合体などのポリエチレンまた
はエチレン系共重合体であればよく、特に制限されな
い。ポリエチレン系樹脂(3)は、通常、融点が105
〜135℃で、MIが0.5〜15程度である。これら
の中でも密度0.910〜0.925、融点118〜1
23℃の線状低密度ポリエチレンが望ましい。
The polyethylene resin (3) is a low density polyethylene, a medium density polyethylene, a high density polyethylene,
There is no particular limitation as long as it is a polyethylene or ethylene-based copolymer such as linear low-density polyethylene, ethylene-vinyl acetate copolymer, ethylene-butene copolymer and the like. Polyethylene resin (3) usually has a melting point of 105.
MI is about 0.5 to 15 at ˜135 ° C. Among these, density 0.910 to 0.925, melting point 118 to 1
23 ° C. linear low density polyethylene is preferred.

【0013】各樹脂成分の配合割合は、樹脂(1)が1
0〜60重量部、好ましくは20〜50重量部、樹脂
(2)が10〜80重量部、好ましくは20〜50重量
部、樹脂(3)が10〜80重量部、好ましくは30〜
40重量部である(合計100重量部)。これら樹脂成
分の1つでも欠けると、高温での伸度が低下したり、高
温での抗張力が大きくなり、深絞り性が悪くなる。特に
耐熱性が要求される場合には、樹脂(1)と樹脂(2)
との合計量が60〜70重量%であることが好ましい。
The resin (1) has a mixing ratio of 1 for each resin component.
0-60 parts by weight, preferably 20-50 parts by weight, resin (2) 10-80 parts by weight, preferably 20-50 parts by weight, resin (3) 10-80 parts by weight, preferably 30-
40 parts by weight (total 100 parts by weight). If even one of these resin components is lacking, the elongation at high temperature decreases, the tensile strength at high temperature increases, and the deep drawability deteriorates. Especially when heat resistance is required, resin (1) and resin (2)
It is preferable that the total amount thereof is 60 to 70% by weight.

【0014】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。
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砲させる方法、
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 heating above the decomposition temperature to fire,
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, heating of azodicarbonamide (ADCA), oxybenzenesulfonyl hydrazide, azobisisobutyronitrile, barium azodicarboxylic acid, dinitrosopantamethylenetetramine, hydrazodicarbonamide, etc. 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(TMPT)、1,9−ノナンジオールジメ
タクリレート(1,9ND)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。
As the crosslinking aid, for example, divinylbenzene (DVB), diallyl phthalate, ethylene glycol dimethacrylate, trimethylolpropane triacrylate (TMPT), 1,9-nonanediol dimethacrylate (1,9ND) and the like are used. Mention may be made of functional monomers. 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.

【0018】さらに必要に応じて各種添加剤、例えば、
抗酸化剤、老化防止剤、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。
If necessary, various additives such as, for example,
Antioxidants, anti-aging agents, pigments, UV absorbers, anti-aging agents and the like can be added.

【0019】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.

【0020】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.

【0021】[0021]

【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。
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.

【0022】なお、発泡体の物性の測定方法は以下のと
おりである。 〈架橋度〉発泡体約50mgを秤量し、120℃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。
The method for measuring the physical properties of the foam is as follows. <Crosslinking degree> About 50 mg of foam is weighed, immersed in xylene at 120 ° C for 24 hours, taken out, dried for 8 hours, weighed, and divided by the weight of the first foam. Multiply by 100 and calculate.

【0023】〈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.

【0024】〈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、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 drawability> The far infrared heater was used to set the surface temperature of the foam to 150 to 160 ° C., vacuum molding was performed using a cylindrical female die, and the depth (H ) And the diameter (D) (H / D). The larger this value is, the better the moldability is.

【0025】〈PVC剥離強度〉発泡体をコロナ処理し
た後、PVCと接着剤でラミネートをし、24時間後放
置後に、25mmの短冊に切断して試片とし、剥離強度
を測定した。
<PVC Peel Strength> The foam was corona-treated, laminated with PVC and an adhesive, and allowed to stand for 24 hours, then cut into 25 mm strips to prepare test pieces, and the peel strength was measured.

【0026】[実施例1〜3、比較例1〜3]表1及び
表2に示すような物性を持つポリプロピレン系樹脂(P
P1)、ポリプロピレン系樹脂(PP2)、及びポリエ
チレン系樹脂(PE)をそれぞれ表1及び表2に示した
ように配合し、樹脂成分100重量部に対して、フェノ
ール系抗酸化剤0.5重量部、イオウ系抗酸化剤1.0
重量部、発泡剤としてアゾジカルボンアミド(ADC
A)10重量部、架橋剤としてジビニルベンゼン(DV
B)6重量部を加え、65mmφ単軸押出機で樹脂温度
を180℃以下にして厚み1.0mmの発泡性シートを
押出した。
[Examples 1 to 3, Comparative Examples 1 to 3] Polypropylene resin (P
P1), polypropylene-based resin (PP2), and polyethylene-based resin (PE) were blended as shown in Table 1 and Table 2, respectively, and 0.5 parts by weight of a phenol-based antioxidant was added to 100 parts by weight of the resin component. Parts, sulfur antioxidant 1.0
Parts by weight, azodicarbonamide (ADC) as a foaming agent
A) 10 parts by weight, divinylbenzene (DV as a cross-linking agent
B) 6 parts by weight was added, and a resin sheet having a thickness of 1.0 mm was extruded at a resin temperature of 180 ° C. or lower with a 65 mmφ single screw extruder.

【0027】得られた発泡性シートに、電子線照射機で
3.0Mradの照射をして架橋ささせた後、縦型発泡
炉で300℃の熱風をふきかけ発泡させたところ、密度
0.04g/cm3、厚み2.5mmの発泡体を得た。
得られた発泡体の物性を測定し、結果を表1及び表2に
示した。実施例1〜3のの伸度(140℃、160℃)
は、比較例1〜3に比べ良好であり、また、比較例3の
発泡体の表面はザラザラしていた。
The obtained foamable sheet was irradiated with an electron beam irradiator at 3.0 Mrad to be crosslinked, and then was blown with hot air at 300 ° C. in a vertical foaming furnace to be foamed. A foam having a thickness of 04 g / cm 3 and a thickness of 2.5 mm was obtained.
The physical properties of the obtained foam were measured, and the results are shown in Tables 1 and 2. Elongation of Examples 1 to 3 (140 ° C, 160 ° C)
Was better than Comparative Examples 1 to 3, and the surface of the foam of Comparative Example 3 was rough.

【0028】[実施例4、5、比較例4、5]表1及び
表2に示すような物性を持つポリプロピレン系樹脂(P
P1)、ポリプロピレン系樹脂(PP2)、及びポリエ
チレン系樹脂(PE)をそれぞれ表1及び表2に示した
ように配合し、フェノール系抗酸化剤0.5重量部、イ
オウ系抗酸化剤1.0重量部、ADCA10重量部、架
橋剤としてトリメチロールプロパントリアクリレート
(TMPT)2.0重量部を加え、120mmφ同方向
2軸押出機で樹脂温度を180℃以下にして厚み1.0
mmの発泡性シートを押出した。
[Examples 4 and 5, Comparative Examples 4 and 5] A polypropylene resin (P
P1), polypropylene resin (PP2), and polyethylene resin (PE) were blended as shown in Table 1 and Table 2, respectively, and 0.5 parts by weight of phenol antioxidant, sulfur antioxidant 1. 0 parts by weight, 10 parts by weight of ADCA, and 2.0 parts by weight of trimethylolpropane triacrylate (TMPT) as a cross-linking agent were added, and the resin temperature was set to 180 ° C. or less with a 120 mmφ co-rotating twin-screw extruder to a thickness of 1.0.
A mm foamable sheet was extruded.

【0029】得られた発泡性シートに、電子線照射機で
2.0Mradの照射をして架橋させた後、縦型発泡炉
で300℃の熱風をふきかけ発泡させたところ、密度
0.04g/cm3、厚み2.5mmの発泡体を得た。
得られた発泡体の物性を測定し、結果を表1及び表2に
示した。
The obtained foamable sheet was irradiated with 2.0 Mrad with an electron beam irradiator to be crosslinked, and then was blown with hot air at 300 ° C. in a vertical foaming furnace to be foamed. The density was 0.04 g. A foam having a thickness of / cm 3 and a thickness of 2.5 mm was obtained.
The physical properties of the obtained foam were measured, and the results are shown in Tables 1 and 2.

【0030】[実施例6〜8、比較例6〜8]表1及び
表2に示すような物性を持つポリプロピレン系樹脂(P
P1)、ポリプロピレン系樹脂(PP2)、及びポリエ
チレン系樹脂(PE)をそれぞれ表1及び表2に示した
ように配合した(ただし、PP1として比較例6〜8で
は、融点が163℃のホモポリプロピレンを使用した。
PEとして、実施例6および比較例6では低密度ポリエ
チレン、実施例7及び比較例7では高密度ポリエチレ
ン、実施例8および比較例8では線状低密度ポリエチレ
ンを使用した。)。
[Examples 6 to 8 and Comparative Examples 6 to 8] A polypropylene-based resin having the physical properties shown in Tables 1 and 2 (P
P1), polypropylene-based resin (PP2), and polyethylene-based resin (PE) were blended as shown in Table 1 and Table 2, respectively (however, in Comparative Examples 6 to 8 as PP1, homopolypropylene having a melting point of 163 ° C.). It was used.
As PE, low-density polyethylene was used in Example 6 and Comparative Example 6, high-density polyethylene in Example 7 and Comparative Example 7, and linear low-density polyethylene was used in Example 8 and Comparative Example 8. ).

【0031】上記配合物にフェノール系抗酸化剤0.5
重量部、イオウ系抗酸化剤1.0重量部、ADCA10
重量部、架橋剤として1,9−ノナンジオールジメタク
リレート(1,9ND)3重量部を加え、65mmφ単
軸押出機で樹脂温度を180℃以下にして厚み1.0m
mの発泡性シートを押出した。
0.5% phenolic antioxidant in the above formulation
Parts by weight, sulfur-based antioxidant 1.0 parts by weight, ADCA10
Parts by weight, 3 parts by weight of 1,9-nonanediol dimethacrylate (1,9ND) as a cross-linking agent, and a resin temperature of 180 ° C. or less with a 65 mmφ single-screw extruder to a thickness of 1.0 m.
m foamable sheet was extruded.

【0032】得られた発泡性シートに、電子線照射機で
2.7Mradの照射をして架橋させた後、縦型発泡炉
で発泡させたところ、密度0.04g/cm3、厚み
2.5mmの発泡体を得た。得られた発泡体の物性を測
定し、結果を表1及び表2に示した。実施例6〜8の発
泡体については、コロナ処理した後、PVCと接着剤で
ラミネートをし、24時間後放置後に、25mmの短冊
に切断して試片とし、剥離強度を測定した。発泡体は、
いずれも材料破壊していたが、その剥離強度は表1に示
す通りであった。
The obtained foamable sheet was irradiated with an electron beam irradiator at 2.7 Mrad to be crosslinked, and then foamed in a vertical foaming furnace to have a density of 0.04 g / cm 3 and a thickness of 2. A 5 mm foam was obtained. The physical properties of the obtained foam were measured, and the results are shown in Tables 1 and 2. The foams of Examples 6 to 8 were subjected to corona treatment, then laminated with PVC and an adhesive, left for 24 hours, and then cut into 25 mm strips to obtain test pieces, and the peel strength was measured. The foam is
The material was destroyed in all cases, but the peel strength was as shown in Table 1.

【0033】[0033]

【表1】 [Table 1]

【0034】[0034]

【表2】 [Table 2]

【0035】[0035]

【発明の効果】本発明によれば、高温時(特に140〜
160℃)における伸度、温度依存性を改善して、深絞
り成形性の良いポリオレフィン系発泡体を提供すること
ができる。本発明の発泡体は、特に車両用内装材として
好適である。
According to the present invention, at high temperature (especially 140-
It is possible to provide a polyolefin-based foam having good deep drawability by improving the elongation at 160 ° C.) and temperature dependence. The foam of the present invention is particularly suitable as an interior material for vehicles.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリオレフィン系樹脂、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
成るポリオレフィン系樹脂架橋発泡体において、該ポリ
オレフィン系樹脂が、(1)立体規則性触媒を用いて重
合され、少なくとも100℃以上135℃未満の間に1
つと、135℃以上175℃以下の間に1つの合計2つ
以上の融点ピークを有するポリプロピレン系樹脂10〜
60重量部、(2)立体規則性触媒を用いて重合され、
エチレン含有量が1〜10重量%で、融点が125〜1
60℃のエチレン−プロピレンランダム共重合体10〜
80重量部、及び(3)ポリエチレン系樹脂10〜80
重量部を含有するものである(合計100重量部)こと
を特徴とするポリオレフィン系樹脂架橋発泡体。
1. A polyolefin resin crosslinked foam obtained by crosslinking and foaming a foamable resin composition containing a polyolefin resin, a thermal decomposition type foaming agent and a crosslinking aid, wherein the polyolefin resin is (1) three-dimensional. Polymerized using a regular catalyst and at least 100 ° C. and less than 135 ° C.
And a polypropylene resin having a total of two or more melting point peaks between 135 ° C and 175 ° C.
60 parts by weight, (2) polymerized using a stereoregular catalyst,
Ethylene content is 1-10% by weight, melting point 125-1
60 ° C ethylene-propylene random copolymer 10
80 parts by weight, and (3) polyethylene resin 10-80
A polyolefin resin crosslinked foam comprising 100 parts by weight (total 100 parts by weight).
JP1892992A 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam Pending JPH05214144A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1892992A JPH05214144A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1892992A JPH05214144A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Publications (1)

Publication Number Publication Date
JPH05214144A true JPH05214144A (en) 1993-08-24

Family

ID=11985329

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1892992A Pending JPH05214144A (en) 1992-02-04 1992-02-04 Polypropylene-based resin crosslinked foam

Country Status (1)

Country Link
JP (1) JPH05214144A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100409070B1 (en) * 1999-12-23 2003-12-11 주식회사 엘지화학 Polyolefin complex resin composition having non-glossing properties for hollow-molding and method for preparing the same
JP2005200475A (en) * 2004-01-13 2005-07-28 Sekisui Chem Co Ltd Crosslinked polyolefin resin foam
JP2006052262A (en) * 2004-08-10 2006-02-23 Sekisui Chem Co Ltd Polyolefin-based resin foam sheet
WO2006123569A1 (en) * 2005-05-18 2006-11-23 Toray Industries, Inc. Crosslinked polyolefin resin foam
JP2007284486A (en) * 2006-04-13 2007-11-01 Toray Ind Inc Cross-linked polyolefinic resin foam
KR101014002B1 (en) * 2008-10-24 2011-02-14 충남대학교산학협력단 Producing method of polyolefin bead foam with two melting temperatures by using continuous extruding process and its fabrication
JP2012072258A (en) * 2010-09-28 2012-04-12 Sekisui Chem Co Ltd Method for producing crosslinked polyolefin-based resin foam and laminate using the resin foam
WO2018025343A1 (en) * 2016-08-03 2018-02-08 東レ株式会社 Laminate body

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100409070B1 (en) * 1999-12-23 2003-12-11 주식회사 엘지화학 Polyolefin complex resin composition having non-glossing properties for hollow-molding and method for preparing the same
JP2005200475A (en) * 2004-01-13 2005-07-28 Sekisui Chem Co Ltd Crosslinked polyolefin resin foam
JP2006052262A (en) * 2004-08-10 2006-02-23 Sekisui Chem Co Ltd Polyolefin-based resin foam sheet
WO2006123569A1 (en) * 2005-05-18 2006-11-23 Toray Industries, Inc. Crosslinked polyolefin resin foam
AU2006248556B2 (en) * 2005-05-18 2011-04-07 Toray Industries, Inc. Crosslinked polyolefin resin foam
JP5217164B2 (en) * 2005-05-18 2013-06-19 東レ株式会社 Cross-linked polyolefin resin foam
KR101361340B1 (en) * 2005-05-18 2014-02-10 도레이 카부시키가이샤 Crosslinked Polyolefin Resin Foam
JP2007284486A (en) * 2006-04-13 2007-11-01 Toray Ind Inc Cross-linked polyolefinic resin foam
KR101014002B1 (en) * 2008-10-24 2011-02-14 충남대학교산학협력단 Producing method of polyolefin bead foam with two melting temperatures by using continuous extruding process and its fabrication
JP2012072258A (en) * 2010-09-28 2012-04-12 Sekisui Chem Co Ltd Method for producing crosslinked polyolefin-based resin foam and laminate using the resin foam
WO2018025343A1 (en) * 2016-08-03 2018-02-08 東レ株式会社 Laminate body
KR20190034495A (en) * 2016-08-03 2019-04-02 도레이 카부시키가이샤 The laminate

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