JPH11349718A - Crystalline polypropylene-based resin foam and its production - Google Patents

Crystalline polypropylene-based resin foam and its production

Info

Publication number
JPH11349718A
JPH11349718A JP10157902A JP15790298A JPH11349718A JP H11349718 A JPH11349718 A JP H11349718A JP 10157902 A JP10157902 A JP 10157902A JP 15790298 A JP15790298 A JP 15790298A JP H11349718 A JPH11349718 A JP H11349718A
Authority
JP
Japan
Prior art keywords
crystalline polypropylene
foam
molecular orientation
based resin
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.)
Granted
Application number
JP10157902A
Other languages
Japanese (ja)
Other versions
JP3640531B2 (en
Inventor
裕之 ▲樽▼本
Hiroyuki Tarumoto
Tsuneo Doi
恒雄 土井
Ikuo Azuma
郁夫 東
Shuichi Shishida
修一 宍田
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 Kasei Co Ltd
Original Assignee
Sekisui Plastics 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 Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP15790298A priority Critical patent/JP3640531B2/en
Publication of JPH11349718A publication Critical patent/JPH11349718A/en
Application granted granted Critical
Publication of JP3640531B2 publication Critical patent/JP3640531B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce a crystalline polypropylene-based resin foam excellent in mechanical strength and impact resistance. SOLUTION: This crystalline polypropylene-based resin foam has a cross- shaped molecular orientation in the plane direction measured by a microwave molecular orientation analyzer. Furthermore, the method for producing the crystalline polypropylene-based resin foam comprises carrying out the extrusion expansion of a crystalline polypropylene-based resin containing a foaming agent, orienting the resultant extruded foam 4 in a state of the softened resin in the interior while cooling and thereby providing the cross-shaped molecular orientation in the plane direction measured with the microwave molecular orientation analyzer.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、結晶性ポリプロピ
レン系樹脂発泡体及びその製造方法に関する。さらに詳
しくは、低密度でありながら、機械的強度の高い結晶性
ポリプロピレン系樹脂発泡体及びその製造方法に関す
る。
TECHNICAL FIELD The present invention relates to a crystalline polypropylene resin foam and a method for producing the same. More specifically, the present invention relates to a crystalline polypropylene resin foam having low density and high mechanical strength, and a method for producing the same.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】従来、
二次成形可能な発泡体としてはポリスチレン系樹脂発泡
体及び結晶性ポリプロピレン系樹脂発泡体が多く使用さ
れている。しかし、ポリスチレン系樹脂発泡体は、耐熱
性、耐薬品性、耐油性等の特性において必ずしも満足で
きる物ではなかった。また、結晶性ポリプロピレン系樹
脂発泡体は、耐熱性、耐薬品性、耐油性等の諸物性に優
れた樹脂であり、工業用部材、食品容器等に広く使用さ
れているが、一般に結晶性ポリプロピレン系樹脂発泡体
は、溶融状態から冷却される過程で結晶が生成するもの
であり、その結晶状態は、大きな球晶が不均一に分布し
た状態である。従って、結晶化をコントロールしなけれ
ば安定した性質の結晶性ポリプロピレン系樹脂発泡体を
得ることができない。
2. Description of the Related Art
Polystyrene-based resin foams and crystalline polypropylene-based resin foams are often used as the foams that can be secondary-molded. However, polystyrene resin foams have not always been satisfactory in properties such as heat resistance, chemical resistance, and oil resistance. In addition, crystalline polypropylene resin foam is a resin excellent in various physical properties such as heat resistance, chemical resistance, and oil resistance, and is widely used for industrial members, food containers, and the like. In the system resin foam, crystals are generated in a process of cooling from a molten state, and the crystal state is a state in which large spherulites are unevenly distributed. Therefore, a crystalline polypropylene-based resin foam having stable properties cannot be obtained unless crystallization is controlled.

【0003】そこで、結晶性ポリプロピレン系樹脂の結
晶化をコントロールするために、結晶造核剤を添加剤と
して配合することが考えられ、実際に結晶性ポリプロピ
レン系樹脂の結晶を均一かつ微細にすると、得られる発
泡体の機械的性質を向上させる効果がある。しかしなが
ら、結晶性ポリプロピレン系樹脂中に結晶造核剤が存在
すると結晶化速度が著しく速くなってしまい、良好な発
泡体が得られない。具体的には、結晶性ポリプロピレン
系樹脂の押出発泡成形では、押し出された樹脂を、溶融
状態にある未結晶化から結晶化に至るまでの短時間の間
に発泡させ、成形を行う必要がある。従って、結晶化速
度が速くなると、発泡成形時間が非常に短くなり、結果
として成形条件を狭めてしまい、良好な発泡体を得るこ
とができない。一方、その他の公知の手段により、逆に
結晶化速度を遅くすると、得られる発泡体の結晶化度が
低くなり、そのため機械的強度が劣るという問題があっ
た。
Therefore, in order to control the crystallization of the crystalline polypropylene resin, it is conceivable to add a crystal nucleating agent as an additive. When the crystal of the crystalline polypropylene resin is actually made uniform and fine, This has the effect of improving the mechanical properties of the foam obtained. However, if a crystal nucleating agent is present in the crystalline polypropylene-based resin, the crystallization rate is significantly increased, and a good foam cannot be obtained. Specifically, in the extrusion foam molding of a crystalline polypropylene resin, it is necessary to foam the extruded resin in a short period of time from uncrystallization in a molten state to crystallization, and perform molding. . Therefore, when the crystallization speed is high, the foam molding time becomes very short, and as a result, the molding conditions are narrowed, and a good foam cannot be obtained. On the other hand, when the crystallization rate is reduced by other known means, the crystallinity of the obtained foam decreases, and thus the mechanical strength is deteriorated.

【0004】[0004]

【課題を解決するための手段】上記問題に鑑み、本発明
者等は、面方向の分子配向が十文字型である結晶性ポリ
プロピレン系樹脂発泡体が、意外にも耐熱性、耐薬品
性、耐油性等に優れ、さらには良好な機械的強度と耐衝
撃性を示すことを見いだし本発明を完成するに至った。
In view of the above problem, the present inventors have surprisingly found that a crystalline polypropylene resin foam having a cross-shaped molecular orientation is unexpectedly resistant to heat, chemical, and oil. The present invention has been found to be excellent in properties and the like, and furthermore to show good mechanical strength and impact resistance.

【0005】かくして、本発明によれば、マイクロ波分
子配向計で測定した面方向の分子配向が十文字型である
ことを特徴とする結晶性ポリプロピレン系樹脂発泡体が
提供される。さらに、本発明によれば、発泡剤を含む結
晶性ポリプロピレン系樹脂を押出発泡させ、押し出され
た発泡体をその内部の樹脂が軟化している状態で冷却し
つつ延伸することにより、マイクロ波分子配向計で測定
した面方向の分子配向が十文字である結晶性ポリプロピ
レン系樹脂発泡体を得ることを特徴とする結晶性ポリプ
ロピレン系樹脂発泡体の製造方法が提供される。
Thus, according to the present invention, there is provided a crystalline polypropylene-based resin foam characterized in that the molecular orientation in the plane direction measured by a microwave molecular orientation meter is cross-shaped. Furthermore, according to the present invention, a crystalline polypropylene-based resin containing a foaming agent is extruded and foamed, and the extruded foam is stretched while being cooled while the resin inside the foamed resin is softened, whereby the microwave molecule is expanded. A method for producing a crystalline polypropylene-based resin foam, characterized in that a crystalline polypropylene-based resin foam having a crosswise molecular orientation measured by an orientation meter is obtained.

【0006】[0006]

【発明の実施の態様】本発明に使用される結晶性ポリプ
ロピレン系樹脂は、特に限定されず、市販されている結
晶性ポリプロピレン系樹脂をいずれも使用することがで
きる。また、プロピレンからなるポリプロピレンホモポ
リマーやプロピレンを主体としたオレフィン(例えば、
エチレン,α−オレフィン等)との共重合体からなるオ
レフィン−プロピレンコポリマーであってもよい。な
お、このコポリマーはオレフィン成分を含むランダムま
たはブロック共重合体であり、ポリプロピレンの脆性を
改善する効果がある。特に、エチレン−プロピレンコポ
リマーが好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The crystalline polypropylene resin used in the present invention is not particularly limited, and any commercially available crystalline polypropylene resin can be used. In addition, a polypropylene homopolymer composed of propylene or an olefin mainly composed of propylene (for example,
Olefin-propylene copolymer comprising a copolymer with ethylene, α-olefin or the like. This copolymer is a random or block copolymer containing an olefin component, and has the effect of improving the brittleness of polypropylene. Particularly, an ethylene-propylene copolymer is preferred.

【0007】特に、本発明に使用される結晶性ポリプロ
ピレン系樹脂として、特公平7−45551号公報に記
載されている、低レベルの放射線を照射する方法や少量
の過酸化物を混合する方法により、ポリプロピレン系樹
脂に分岐構造を与え、超高分子量成分の割合を増加させ
たポリプロピレン系樹脂を用いるのが好ましい。本発明
においては上記結晶性ポリプロピレン系樹脂を単独で用
いるのみならず、目的に応じて非結晶性ポリプロピレン
系樹脂、他種類の樹脂又はエラストマー等を混合して使
用することもできる。
[0007] In particular, as the crystalline polypropylene resin used in the present invention, a method of irradiating a low-level radiation or a method of mixing a small amount of peroxide described in Japanese Patent Publication No. 7-45551. It is preferable to use a polypropylene-based resin having a branched structure imparted to the polypropylene-based resin to increase the proportion of the ultrahigh molecular weight component. In the present invention, not only the above-mentioned crystalline polypropylene-based resin can be used alone, but also a non-crystalline polypropylene-based resin, another kind of resin or an elastomer can be mixed and used according to the purpose.

【0008】例えば、結晶性ポリプロピレン系樹脂の脆
性をさらに改善する他種類の樹脂として、ポリエチレン
系樹脂を混合することが好ましい。ポリエチレン系樹脂
としては、エチレンの単独重合体、エチレン−αオレフ
ィンの共重合体又はエチレンと官能基に炭素、酸素、水
素原子をもつ非オレフィン単量体との共重合体等が挙げ
られる。
For example, it is preferable to mix a polyethylene resin as another type of resin for further improving the brittleness of the crystalline polypropylene resin. Examples of the polyethylene resin include a homopolymer of ethylene, a copolymer of ethylene-α-olefin, and a copolymer of ethylene with a non-olefin monomer having a carbon, oxygen, or hydrogen atom in a functional group.

【0009】エチレンの単独重合体としては、低密度ポ
リエチレン(LDPE)、高密度ポリエチレン(HDP
E)等が挙げられる。エチレン−αオレフィンの共重合
体としては、直鎖状低密度ポリエチレン(L−LDP
E)、直鎖状超低密度ポリエチレン(VLDPE)等
で、そのα−オレフィンとしては1−ブテン、1−ヘキ
セン、1−オクテン、4−メチル−1−ペンテン等が挙
げられる。エチレンと官能基に炭素、酸素、水素原子を
もつ非オレフィン単量体との共重合体としては、エチレ
ン系アイオノマー樹脂、エチレン−酢酸ビニル共重合体
樹脂、エチレン−ビニルアルコール共重合体樹脂、エチ
レン−アクリル酸共重合体樹脂、エチレン−メチルメタ
クリレート共重合体樹脂等が挙げられる。なお、これら
ポリエチレン系樹脂は1種又は複数種を混合したもので
あってもよい。
The homopolymers of ethylene include low-density polyethylene (LDPE) and high-density polyethylene (HDP).
E) and the like. As the ethylene-α-olefin copolymer, linear low-density polyethylene (L-LDP)
E), linear very low density polyethylene (VLDPE) and the like, and the α-olefin includes 1-butene, 1-hexene, 1-octene, 4-methyl-1-pentene and the like. Examples of the copolymer of ethylene and a non-olefin monomer having a carbon, oxygen, or hydrogen atom as a functional group include ethylene ionomer resin, ethylene-vinyl acetate copolymer resin, ethylene-vinyl alcohol copolymer resin, and ethylene. -Acrylic acid copolymer resin, ethylene-methyl methacrylate copolymer resin and the like. These polyethylene resins may be one kind or a mixture of a plurality of kinds.

【0010】上記の他種類の樹脂の混合割合は、結晶性
ポリプロピレン系樹脂100重量部に対して、5〜10
0重量部混合することが好ましく、10〜50重量部混
合することが特に好ましい。本発明に使用される結晶性
ポリプロピレン系樹脂には、気泡調整剤を適時添加して
もよい。気泡調整剤としては、例えば、微粉末タルク、
シリカ、炭酸水素ナトリウムとクエン酸との混合物のよ
うな気泡核剤を従来通り使用することができる。更に、
押出発泡性に影響のない範囲で、所望に応じて、安定
剤、着色剤、難燃剤、帯電防止剤、抗菌剤、充填剤等の
添加剤を加えてもよい。
The mixing ratio of the other resin is 5 to 10 parts by weight based on 100 parts by weight of the crystalline polypropylene resin.
It is preferable to mix 0 parts by weight, and it is particularly preferable to mix 10 to 50 parts by weight. A bubble regulator may be added to the crystalline polypropylene resin used in the present invention as appropriate. Examples of the foam adjuster include fine powder talc,
Bubble nucleating agents such as silica, a mixture of sodium bicarbonate and citric acid can be used conventionally. Furthermore,
Additives such as a stabilizer, a colorant, a flame retardant, an antistatic agent, an antibacterial agent, and a filler may be added as needed within a range that does not affect the extrusion foaming property.

【0011】本発明の方法では、任意に添加剤を含む原
料樹脂を公知の押出機にて溶融することにより溶融樹脂
を得る。次に、押出機内の溶融樹脂に発泡剤が添加され
る。発泡剤としては、公知の発泡剤をいずれも使用する
ことができる。発泡剤は、大きく分けると物理発泡剤と
化学発泡剤に分けられ、本発明ではどちらも使用できる
が、物理発泡剤が好ましい。物理発泡剤には、不活性ガ
ス、飽和脂肪族炭化水素、飽和脂環式炭化水素、芳香族
炭化水素、ハロゲン化炭化水素、エーテル、ケトン等に
分類されるが、本発明ではそのいずれも使用することが
できる。具体的には、炭酸ガス、窒素等の不活性ガス、
メタン、エタン、プロパン、ノルマルブタン、イソブタ
ン、ノルマルペンタン、イソペンタン、ネオペンタン、
ノルマルヘキサン、2−メチルペンタン、3−メチルペ
ンタン、2,2−ジメチルブタン等の飽和脂肪族炭化水
素、メチルシクロプロパン、シクロペンタン、1,1−
ジメチルシクロプロパン、シクロヘキサン、メチルシク
ロペンタン、エチルシクロブタン、1,1,2−トリメ
チルシクロプロパン等の飽和脂環式炭化水素、ベンゼン
等の芳香族炭化水素、塩化メチル、各種フロン(たとえ
ば、トリクロロモノフルオロメタン、ジクロロジフルオ
ロメタン、モノクロロジフルオロメタン、1,1,2−
トリクロロトリフルオロエタン、1,2−ジクロロテト
ラフルオロエタン、1,1−ジクロロ−2,2,2−ト
リフルオロエタン、モノクロロ−1,2,2,2−テト
ラフルオロエタン、1,1,1,2−テトラフルオロエ
タン、1,1−ジクロロ−1−フルオロエタン、1−ク
ロロ−1,1−ジフルオロエタン、1,1−ジフルオロ
エタン等)のハロゲン化炭化水素、ジメチルエーテル、
2−エトキシエタノール、メチルターシャルブチルエー
テル等のエーテル、アセトン、エチルメチルケトン、ア
セチルアセトン等のケトンが挙げられる。これら発泡剤
は、単独でも、混合して使用してもよい。
In the method of the present invention, a molten resin is obtained by melting a raw material resin optionally containing an additive with a known extruder. Next, a foaming agent is added to the molten resin in the extruder. As the foaming agent, any of known foaming agents can be used. The foaming agent is roughly classified into a physical foaming agent and a chemical foaming agent, and both can be used in the present invention, but the physical foaming agent is preferable. Physical blowing agents are classified into inert gases, saturated aliphatic hydrocarbons, saturated alicyclic hydrocarbons, aromatic hydrocarbons, halogenated hydrocarbons, ethers, ketones, etc., and any of them is used in the present invention. can do. Specifically, carbon dioxide gas, an inert gas such as nitrogen,
Methane, ethane, propane, normal butane, isobutane, normal pentane, isopentane, neopentane,
Saturated aliphatic hydrocarbons such as normal hexane, 2-methylpentane, 3-methylpentane and 2,2-dimethylbutane; methylcyclopropane; cyclopentane;
Saturated alicyclic hydrocarbons such as dimethylcyclopropane, cyclohexane, methylcyclopentane, ethylcyclobutane, 1,1,2-trimethylcyclopropane, aromatic hydrocarbons such as benzene, methyl chloride, various fluorocarbons (for example, trichloromonofluoro Methane, dichlorodifluoromethane, monochlorodifluoromethane, 1,1,2-
Trichlorotrifluoroethane, 1,2-dichlorotetrafluoroethane, 1,1-dichloro-2,2,2-trifluoroethane, monochloro-1,2,2,2-tetrafluoroethane, 1,1,1, Halogenated hydrocarbons of 2-tetrafluoroethane, 1,1-dichloro-1-fluoroethane, 1-chloro-1,1-difluoroethane, 1,1-difluoroethane, etc.), dimethyl ether,
Examples thereof include ethers such as 2-ethoxyethanol and methyl tert-butyl ether, and ketones such as acetone, ethyl methyl ketone and acetylacetone. These foaming agents may be used alone or as a mixture.

【0012】次いで、発泡剤が添加された溶融樹脂を押
出機から低圧帯域へ押し出すことにより、発泡させ発泡
体を得る。ここで、押出は押出機から金型を介して行わ
れるが、金型内で幅方向に溶融樹脂を急展開させること
が好ましい。急展開における展開角度は90°以上が好
ましく、120°以上が特に好ましい。得られた発泡体
を、表面温度を100℃以下に調節した冷却ロールで冷
却しつつ、シート状又は板状等の任意の形状に成形する
ことが好ましい。
Next, the molten resin to which the foaming agent has been added is extruded from an extruder into a low-pressure zone, whereby the foamed resin is obtained. Here, the extrusion is performed via a mold from an extruder, but it is preferable to rapidly expand the molten resin in the width direction in the mold. The deployment angle in rapid deployment is preferably 90 ° or more, and particularly preferably 120 ° or more. The obtained foam is preferably formed into an arbitrary shape such as a sheet or a plate while being cooled by a cooling roll whose surface temperature is adjusted to 100 ° C. or lower.

【0013】本発明では、押し出された発泡体をその内
部の樹脂が軟化している状態で冷却しつつ延伸すること
により、マイクロ波分子配向計で測定した面方向の分子
配向が十文字型である結晶性ポリプロピレン系樹脂発泡
体を得ることができる。マイクロ波分子配向計による面
方向の分子配向の測定は、例えば、特開平2−2657
25号公報に記載されたマイクロ波分子配向計(KSシ
ステム株式会社製MOA−2001A)を用いて、同公
報で記載された方法によって測定することができる。即
ち、3.5〜4.2GHzの範囲で、マイクロ波透過強
度が最大値の1/2程度となる周波数のマイクロ波を測
定波長とし、このマイクロ波をサンプルの表面に垂直に
照射することにより面方向(VD方向、つまりMD方向
及びTD方向に垂直な方向)の分子配向を測定すること
ができる。但し、この公報記載のマイクロ波分子配向計
では、サンプル厚みが3.0mmまでしか測定できない
ため、3.0mmを超えるサンプルについては、厚みが
約2.0mmになるまで(ハムスライサーではぎ取る方
法等により)スライスされた表面のサンプルを使用す
る。
In the present invention, the extruded foam is stretched while cooling while the resin inside is softened, so that the molecular orientation in the plane direction measured by a microwave molecular orientation meter is cross-shaped. A crystalline polypropylene-based resin foam can be obtained. Measurement of the molecular orientation in the plane direction using a microwave molecular orientation meter is described in, for example,
The measurement can be performed using a microwave molecular orientation meter (MOA-2001A manufactured by KS System Co., Ltd.) described in Japanese Patent Publication No. 25 by the method described in the same publication. That is, in the range of 3.5 to 4.2 GHz, a microwave having a frequency at which the microwave transmission intensity is about 1/2 of the maximum value is set as a measurement wavelength, and the microwave is irradiated perpendicularly to the surface of the sample. The molecular orientation in the plane direction (the VD direction, that is, the direction perpendicular to the MD direction and the TD direction) can be measured. However, since the microwave molecular orientation meter described in this publication can measure only a sample thickness of up to 3.0 mm, a sample exceeding 3.0 mm is reduced to a thickness of about 2.0 mm (for example, a method of removing with a ham slicer). Use a sample of the sliced surface.

【0014】測定結果はグラフで出力される。本発明に
おいて、結晶性ポリプロピレン系樹脂発泡体の十文字型
の分子配向のグラフの軸の傾きは、どのような角度であ
ってもかまわない。このような配向の発泡体は、延伸・
配向がかかっているため、高強度で、脆性も改善されて
いる。ここで、十文字型の形状は、厳密な意味を示すの
ではなく、縦軸と横軸とが任意の角度で交差する形状を
含む。なお、得られたグラフの形が、円形である場合、
分子が各方向に均一に配向しているか又は全く配向して
いないことを示している。また、市販されている一軸延
伸されたシート及びフィルムは瓢箪型のグラフになり、
二軸延伸されたものは、延伸のかかっている部分の軸が
45°傾いた瓢箪型のグラフになる。
The measurement results are output as a graph. In the present invention, the inclination of the axis of the cross-shaped molecular orientation graph of the crystalline polypropylene-based resin foam may be any angle. Foam with such orientation is stretched
Due to the orientation, it has high strength and improved brittleness. Here, the cross-shaped shape does not indicate a strict meaning, but includes a shape in which the vertical axis and the horizontal axis intersect at an arbitrary angle. In addition, when the shape of the obtained graph is circular,
It indicates that the molecules are oriented uniformly in each direction or not at all. In addition, commercially available uniaxially stretched sheets and films become gourd-shaped graphs,
The biaxially stretched one is a gourd-shaped graph in which the axis of the stretched portion is inclined by 45 °.

【0015】上記方法により得られた本発明の結晶性ポ
リプロピレン系樹脂発泡体は、1.0〜30mmの厚み
を有していることが好ましく、1.5〜20mmの厚み
が特に好ましい。密度は0.025〜0.7g/ccの
範囲が好ましく、0.05〜0.5g/ccの範囲が特
に好ましい。
The crystalline polypropylene resin foam of the present invention obtained by the above method preferably has a thickness of 1.0 to 30 mm, particularly preferably 1.5 to 20 mm. The density is preferably in the range of 0.025 to 0.7 g / cc, particularly preferably in the range of 0.05 to 0.5 g / cc.

【0016】[0016]

【実施例】以下、実施例及び比較例により、本発明を更
に詳細に説明する。
The present invention will be described below in more detail with reference to Examples and Comparative Examples.

【0017】実施例1 結晶性ポリプロピレン系樹脂:SD632(プロピレン
−エチレンブロック共重合体、モンテル社製)100重
量部に、気泡核剤としてクエン酸と炭酸水素ナトリウム
の混合物であるハイドロセロールHK(ベーリンガー・
インゲルハイム社製)0.2重量部をあらかじめブレン
ダーで混合し、その混合物を90mmの第1番目の押出
機と115mmの第2番目の押出機とを連結した発泡押
出機1(図1)に供給し、温度150〜230℃に調節
された第1番目の押出機で溶融混練した。次いで、第1
番目の押出機の先端部より、基材樹脂に対し2.0重量
部の割合で発泡剤としてのノルマルブタンを圧入した。
その後、温度145〜180℃に調節された第2番目の
押出機に混合物が供給され、混合物(樹脂)の温度を発
泡に適する温度(165℃)に調節した。発泡剤を含ん
だ溶融混合物を内径16mmφの円筒型2から金型3に
移動させ、金型3内で600mm幅に急展開(展開角度
170゜)させた。この後、幅600mm、スリット
0.5mmの金型3から大気中へ押し出すことにより、
溶融混合物を発泡させた。押し出された発泡体4を、3
0℃の冷却水を通した口径40mmの冷却ロール5(周
速度3.3m/分)で、表面を冷却しつつ板状に成形
し、引き取りロール6で引き取ることにより発泡体を得
た。
Example 1 Hydrocerol HK (a mixture of citric acid and sodium hydrogen carbonate as a cell nucleating agent) was added to 100 parts by weight of a crystalline polypropylene resin: SD632 (propylene-ethylene block copolymer, manufactured by Montell). Boehringer
(Ingelheim Co., Ltd.) 0.2 parts by weight were previously mixed with a blender, and the mixture was fed to a foam extruder 1 (FIG. 1) in which a 90 mm first extruder and a 115 mm second extruder were connected. The mixture was supplied and melt-kneaded in a first extruder adjusted to a temperature of 150 to 230 ° C. Then the first
Normal butane as a foaming agent was pressed into the base resin at a ratio of 2.0 parts by weight from the tip of the second extruder.
Thereafter, the mixture was supplied to a second extruder adjusted to a temperature of 145 to 180 ° C, and the temperature of the mixture (resin) was adjusted to a temperature (165 ° C) suitable for foaming. The molten mixture containing the foaming agent was moved from the cylindrical mold 2 having an inner diameter of 16 mmφ to the mold 3 and rapidly developed in the mold 3 to a width of 600 mm (development angle 170 °). Then, by extruding from the mold 3 having a width of 600 mm and a slit of 0.5 mm into the atmosphere,
The molten mixture was foamed. Extruded foam 4
The surface was cooled and formed into a plate shape with a cooling roll 5 having a diameter of 40 mm (peripheral speed of 3.3 m / min) through which cooling water at 0 ° C. was passed.

【0018】得られた発泡体は厚み2.5mm、密度
0.18g/cc、坪量450g/m 2 、結晶化度40
%、穿孔衝撃値64kgf・cm、曲げ強度4.4Mp
a、10%圧縮強度0.44Mpaであった。なお、結
晶化度、穿孔衝撃値、曲げ強度及び圧縮強度は、以下の
条件で測定された。
The obtained foam has a thickness of 2.5 mm and a density of 2.5 mm.
0.18 g / cc, basis weight 450 g / m Two, Crystallinity 40
%, Puncture impact value 64 kgf · cm, bending strength 4.4 Mp
a and the 10% compressive strength was 0.44 Mpa. Note that
The crystallinity, puncture impact value, flexural strength and compressive strength are as follows:
Measured under conditions.

【0019】〔結晶化度〕 JIS K7122に従っ
て、 示差走査熱量計(DSC)により求められた結晶化
熱測定結果から結晶化熱量を算出し、その結晶化熱量を
以下の式に代入することにより求めた。
[Crystallinity] According to JIS K7122, the heat of crystallization is calculated from the result of the heat of crystallization measured by a differential scanning calorimeter (DSC), and the heat of crystallization is calculated by substituting the heat of crystallization into the following equation. Was.

【0020】PP結晶化度(%)=(結晶化熱量(mJ/m
g )/209.5)×100 測定装置:示差走査熱量計装置 DSC200型(セイ
コー電子工業(株)製) 測定開始・終了温度:−40℃〜220℃・−40℃〜
220℃
PP crystallinity (%) = (heat of crystallization (mJ / m
g) /209.5) × 100 Measuring apparatus: Differential scanning calorimeter DSC200 type (manufactured by Seiko Instruments Inc.) Measurement start / end temperature: −40 ° C. to 220 ° C.−40 ° C.
220 ° C

【0021】〔穿孔衝撃値〕 JIS P8134に準
拠し、測定した。 装 置:衝撃穿孔強さ試験機(東洋テスター工業(株)
製) 試験片:(幅)150×(長さ)150W×原厚み(m
m)
[Punch Impact Value] Measured according to JIS P8134. Equipment: Impact piercing strength tester (Toyo Tester Co., Ltd.)
Test piece: (width) 150 x (length) 150 W x original thickness (m
m)

【0022】〔曲げ強度〕 JIS K7203に準拠
し、測定した。 装 置:テンシロン万能試験機 UCT−10T
((株)オリエンテック製) 試験片:(幅)25×(長さ)100×原厚み(mm) 試験速度:1.5mm/分 支点間距離:45mm
[Bending strength] Measured according to JIS K7203. Apparatus: Tensilon universal tester UCT-10T
(Orientec Co., Ltd.) Specimen: (width) 25 x (length) 100 x original thickness (mm) Test speed: 1.5 mm / min Distance between supports: 45 mm

【0023】〔圧縮強度〕 JIS K6767に準拠
し、測定した。 装 置:テンシロン万能試験機 UCT−10T
((株)オリエンテック製) 試験片:(幅)50×(長さ)50×(積重)25(m
m) 試験速度:10mm/分
[Compressive strength] Measured according to JIS K6767. Apparatus: Tensilon universal tester UCT-10T
(Made by Orientec Co., Ltd.) Test piece: (width) 50 x (length) 50 x (stack) 25 (m
m) Test speed: 10 mm / min

【0024】また、図2に示すように、得られた発泡体
の分子配向を、TD方向に4点サンプルを取り、特開平
2−265725号公報に記載された装置及び方法によ
り測定した。この測定結果を図3に示す。図3から明ら
かなように、面方向の分子配向は、いずれも十文字型で
あった。
Further, as shown in FIG. 2, the molecular orientation of the obtained foam was measured with a device and a method described in JP-A-2-265725 by taking four samples in the TD direction. FIG. 3 shows the measurement results. As is clear from FIG. 3, the molecular orientation in the plane direction was a cross shape.

【0025】実施例2 ノルマルブタンの注入量を3.0重量%とし、冷却ロー
ルの周速度を2.5m/分とした以外は実施例1と同じ
方法で発泡体を作成した。得られた発泡体は、厚み5.
0mm、密度0.12g/cc、坪量590g/m2
結晶化度41%、穿孔衝撃値122kgf・cm、曲げ
強度2.8Mpa、10%圧縮強度0.43Mpaであ
った。また、実施例1と同様にして測定した面方向の分
子配向を図4に示す。図4から明らかなように、面方向
の分子配向は、いずれも十文字型であった。
Example 2 A foam was produced in the same manner as in Example 1 except that the amount of normal butane injected was 3.0% by weight and the peripheral speed of the cooling roll was 2.5 m / min. The resulting foam has a thickness of 5.
0 mm, density 0.12 g / cc, basis weight 590 g / m 2 ,
The crystallinity was 41%, the puncture impact value was 122 kgf · cm, the bending strength was 2.8 Mpa, and the 10% compression strength was 0.43 Mpa. FIG. 4 shows the molecular orientation in the plane direction measured in the same manner as in Example 1. As is clear from FIG. 4, the molecular orientations in the plane direction were all cross-shaped.

【0026】比較例1 実施例1と同じ溶融混合物を、口径φ80mm、スリッ
ト0.5mmのサーキュラー金型から大気中へ押し出
し、管状発泡体となった物を外径φ380mmの円筒形
マンドレルに沿わせて引き取り、円周上の1点でカッタ
ーにより切開して板状とし、発泡体を得た。得られた製
品は、厚み2.5mm、密度0.18g/cc、坪量4
50g/m2 、結晶化度43%、穿孔衝撃値16kgf
・cm、曲げ強度4.3Mpa、10%圧縮強度0.3
0Mpaであった。また、実施例1と同様の方法により
測定した面方向の分子配向を図5に示す。図5から明ら
かなように、面方向の分子配向はいずれも楕円状であっ
た。
Comparative Example 1 The same molten mixture as in Example 1 was extruded into the atmosphere from a circular mold having a diameter of 80 mm and a slit of 0.5 mm, and the resulting tubular foam was placed along a cylindrical mandrel having an outer diameter of 380 mm. The plate was cut out at one point on the circumference with a cutter to obtain a foam. The obtained product has a thickness of 2.5 mm, a density of 0.18 g / cc and a basis weight of 4
50 g / m 2 , crystallinity 43%, puncture impact value 16 kgf
・ Cm, bending strength 4.3 Mpa, 10% compression strength 0.3
It was 0 Mpa. FIG. 5 shows the molecular orientation in the plane direction measured by the same method as in Example 1. As is clear from FIG. 5, the molecular orientations in the plane direction were all elliptical.

【0027】比較例2 ノルマルブタンの注入量を3.0重量%とした以外は比
較例1と同じ方法で発泡体を作成した。
Comparative Example 2 A foam was prepared in the same manner as in Comparative Example 1 except that the amount of normal butane was 3.0% by weight.

【0028】得られた発泡体は、厚み5.0mm、密度
0.11g/cc、坪量570g/m2 、結晶化度39
%、穿孔衝撃値90kgf・cm、曲げ強度1.6Mp
a、10%圧縮強度0.22Mpaであった。また、実
施例1と同様にして測定した面方向の分子配向を図6に
示す。図6から明らかなように、面方向の分子配向はい
ずれも楕円形であった。
The obtained foam had a thickness of 5.0 mm, a density of 0.11 g / cc, a basis weight of 570 g / m 2 , and a crystallinity of 39.
%, Puncture impact value 90 kgf · cm, bending strength 1.6 Mp
a, 10% compressive strength was 0.22 Mpa. FIG. 6 shows the molecular orientation in the plane direction measured in the same manner as in Example 1. As is clear from FIG. 6, the molecular orientations in the plane direction were all elliptical.

【0029】なお、表1に実施例1及び2並びに比較例
1及び2の製品の厚み、密度、坪量、結晶化度、穿孔衝
撃値、曲げ強度及び10%圧縮強度をまとめて示す。
Table 1 summarizes the thickness, density, basis weight, crystallinity, puncture impact value, bending strength and 10% compressive strength of the products of Examples 1 and 2 and Comparative Examples 1 and 2.

【0030】[0030]

【表1】 [Table 1]

【0031】実施例1及び2並びに比較例1及び2から
明らかなように、面方向の分子配向が十文字型であれ
ば、ポリプロピレン系樹脂発泡体は優れた機械的強度を
有する。
As is clear from Examples 1 and 2 and Comparative Examples 1 and 2, if the molecular orientation in the plane direction is a cross shape, the polypropylene-based resin foam has excellent mechanical strength.

【0032】[0032]

【発明の効果】本発明の面方向の分子配向が十文字型で
ある結晶性ポリプロピレン系樹脂発泡体は、耐熱性、耐
薬品性、耐油性等に優れ、さらには良好な機械的強度と
耐衝撃性を有する。
The crystalline polypropylene resin foam having a cross-shaped molecular orientation according to the present invention is excellent in heat resistance, chemical resistance, oil resistance, etc., and furthermore has good mechanical strength and impact resistance. Has the property.

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

【図1】実施例1の発泡体の製造装置の概略図である。FIG. 1 is a schematic view of an apparatus for producing a foam of Example 1.

【図2】面方向の分子配向の測定部位を示す概略図であ
る。
FIG. 2 is a schematic view showing a measurement site of a molecular orientation in a plane direction.

【図3】実施例1の面方向の分子配向を示すグラフであ
る。
FIG. 3 is a graph showing the molecular orientation in the plane direction of Example 1.

【図4】実施例2の面方向の分子配向を示すグラフであ
る。
FIG. 4 is a graph showing the molecular orientation in the plane direction of Example 2.

【図5】比較例1の面方向の分子配向を示すグラフであ
る。
5 is a graph showing the molecular orientation in the plane direction of Comparative Example 1. FIG.

【図6】比較例2の面方向の分子配向を示すグラフであ
る。
FIG. 6 is a graph showing the molecular orientation in the plane direction of Comparative Example 2.

【符号の説明】[Explanation of symbols]

1.押出機 2.円筒型 3.金型 4.発泡体 5.冷却ロール 6.引き取りロール 1. Extruder 2. Cylindrical type 3. Mold 4. Foam 5. Cooling roll 6. Pickup roll

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29K 105:04 B29L 7:00 C08L 23:10 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI B29K 105: 04 B29L 7:00 C08L 23:10

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 マイクロ波分子配向計で測定した面方向
の分子配向が十文字型であることを特徴とする結晶性ポ
リプロピレン系樹脂発泡体。
1. A crystalline polypropylene-based resin foam characterized in that the molecular orientation in the plane direction measured by a microwave molecular orientation meter is cross-shaped.
【請求項2】 発泡剤を含む結晶性ポリプロピレン系樹
脂を押出発泡させ、押し出された発泡体をその内部の樹
脂が軟化している状態で冷却しつつ延伸することによ
り、マイクロ波分子配向計で測定した面方向の分子配向
が十文字型である結晶性ポリプロピレン系樹脂発泡体を
得ることを特徴とする結晶性ポリプロピレン系樹脂発泡
体の製造方法。
2. Extrusion and foaming of a crystalline polypropylene resin containing a foaming agent, and stretching of the extruded foam while cooling it while the resin inside the foamed resin is softened. A method for producing a crystalline polypropylene-based resin foam, characterized in that a crystalline polypropylene-based resin foam having a cross-shaped measured molecular orientation is obtained.
JP15790298A 1998-06-05 1998-06-05 Crystalline polypropylene-based resin foam and method for producing the same Expired - Fee Related JP3640531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15790298A JP3640531B2 (en) 1998-06-05 1998-06-05 Crystalline polypropylene-based resin foam and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15790298A JP3640531B2 (en) 1998-06-05 1998-06-05 Crystalline polypropylene-based resin foam and method for producing the same

Publications (2)

Publication Number Publication Date
JPH11349718A true JPH11349718A (en) 1999-12-21
JP3640531B2 JP3640531B2 (en) 2005-04-20

Family

ID=15659939

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3640531B2 (en)

Also Published As

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