JP4948224B2 - Polypropylene foam sheet and method for producing the same - Google Patents

Polypropylene foam sheet and method for producing the same Download PDF

Info

Publication number
JP4948224B2
JP4948224B2 JP2007084721A JP2007084721A JP4948224B2 JP 4948224 B2 JP4948224 B2 JP 4948224B2 JP 2007084721 A JP2007084721 A JP 2007084721A JP 2007084721 A JP2007084721 A JP 2007084721A JP 4948224 B2 JP4948224 B2 JP 4948224B2
Authority
JP
Japan
Prior art keywords
foam sheet
weight
polypropylene foam
ethylene
flow rate
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.)
Active
Application number
JP2007084721A
Other languages
Japanese (ja)
Other versions
JP2008239879A (en
Inventor
政一 品田
康宏 榎本
弘和 小松
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.)
THE FURUKAW ELECTRIC CO., LTD.
Original Assignee
THE FURUKAW ELECTRIC 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 THE FURUKAW ELECTRIC CO., LTD. filed Critical THE FURUKAW ELECTRIC CO., LTD.
Priority to JP2007084721A priority Critical patent/JP4948224B2/en
Publication of JP2008239879A publication Critical patent/JP2008239879A/en
Application granted granted Critical
Publication of JP4948224B2 publication Critical patent/JP4948224B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Description

本発明は、高級感が要求される化粧品、文房具品等の容器、包装材、ラベル材、ディスプレイの壁紙等に好適なパール調光沢を有するポリプロピレン発泡シートおよび其の製造方法に関する。   The present invention relates to a polypropylene foam sheet having a pearly luster suitable for containers such as cosmetics and stationery products, packaging materials, label materials, display wallpaper, and the like, which require a high-class feeling, and a method for producing the same.

従来、きめ細かで均一な異方的光沢(以下、パール調光沢という)を有するプラスチック成形体は、雲母等を含むパール顔料を熱可塑性樹脂に添加した樹脂組成物を溶融成形することによって得られている。しかしながら、パール顔料は、高価なためコストがかさむという欠点を有する。   Conventionally, a plastic molding having a fine and uniform anisotropic gloss (hereinafter referred to as pearly gloss) is obtained by melt molding a resin composition in which a pearl pigment containing mica or the like is added to a thermoplastic resin. Yes. However, pearl pigments have the disadvantage that they are expensive and expensive.

そこで、高価なパール顔料を用いない方法として、例えば、熱可塑性ポリエステル樹脂(A)とそれとは相溶しない樹脂(B)との樹脂組成物を押出、射出成形し、特定の内部構造を有するプラスチック成形体とすることによってさらに高級感を高めたパール調光沢を得る方法が提案されている(特許文献1)。   Therefore, as a method not using an expensive pearl pigment, for example, a resin composition of a thermoplastic polyester resin (A) and an incompatible resin (B) is extruded and injection molded, and a plastic having a specific internal structure There has been proposed a method for obtaining a pearly luster that further enhances the sense of quality by forming a molded body (Patent Document 1).

特開平06−080789号公報Japanese Patent Laid-Open No. 06-080789

しかしながら、その特定の内部構造を押出、射出等の単一工程で安定して得るのは難しく、後工程で延伸工程等を行う必要があった。   However, it is difficult to stably obtain the specific internal structure in a single process such as extrusion or injection, and it is necessary to perform a stretching process or the like in a subsequent process.

本発明は前述した事情に鑑みてなされたもので、高級感のある、良好なパール調の光沢が得られるポリプロピレン発泡シート、および、押出等の単一工程にて低コストで安定して良好なパール調の光沢が得られるポリプロピレン発泡シートを製造する方法を提供することを目的とする。   The present invention has been made in view of the above-described circumstances, and is a high-quality polypropylene foam sheet that provides a good pearly luster, and is stable and good at a low cost in a single step such as extrusion. It is an object of the present invention to provide a method for producing a polypropylene foam sheet capable of obtaining a pearly luster.

本発明者らは、前記目的を達成するために種々検討を行った結果、以下の特徴を具備するポリプロピレン発泡シートが、高級感のある、良好なパール調の光沢が得られるここと、および、以下の特徴を具備するポリプロピレン発泡シートの製造方法が、前記良好なパール調の光沢が得られるポリプロピレン発泡シートを低コストで、安定的に供給できることを見出した。   As a result of various studies to achieve the above object, the present inventors have obtained a high-quality, high-quality, pearly glossy polypropylene foam sheet having the following characteristics, and It has been found that a method for producing a polypropylene foam sheet having the following characteristics can stably supply the polypropylene foam sheet capable of obtaining the good pearly luster at low cost.

すなわち、請求項1に係るポリプロピレン発泡シートは、エチレン含有量5〜20重量%、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのエチレン−プロピレンブロック共重合体20〜80重量%と、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%との混和物100重量部に対して、発泡核剤を2〜5重量部を配合した樹脂組成物に無機系ガスを圧入したのち、押出機のダイスより押出成形し発泡させたパール調光沢を有するポリプロピレン発泡シートであって、前記ポリプロピレン発泡シート表面のJIS B0601に基づく中心線平均粗さが0.5〜2.0μm、JIS B0601に基づく最大高さが5〜25μmであることを特徴とする。   That is, the polypropylene foam sheet according to claim 1 is an ethylene-propylene block copolymer having an ethylene content of 5 to 20% by weight, a melt flow rate of 0.1 to 10 g / 10 minutes, and a melt tension at 190 ° C. of 15 to 25 g. Mixing of 20 to 80% by weight with 20 to 80% by weight of ethylene-propylene block copolymer or / and ethylene-propylene random copolymer having an ethylene content of 5 to 20% by weight and a melt flow rate of 5 to 20 g / 10 min Polypropylene foam having a pearly luster that is foamed by extrusion molding from a die of an extruder after injecting an inorganic gas into a resin composition containing 2 to 5 parts by weight of a foam nucleating agent for 100 parts by weight of the product A center line average roughness based on JIS B0601 on the surface of the polypropylene foam sheet is 0.5 to .0Myuemu, the maximum height based on JIS B0601 is characterized in that it is a 5 to 25 [mu] m.

前記組成とされ、ポリプロピレン発泡シートの表面粗さ等を上記規定値内におさめた本発明のポリプロピレン発泡シートによれば、高級感のある、良好なパール調光沢を得ることができる。   According to the polypropylene foam sheet of the present invention, which has the above composition and the surface roughness of the polypropylene foam sheet falls within the above specified values, a high-quality and good pearly gloss can be obtained.

また、請求項2に係るポリプロピレン発泡シートは、請求項1に記載のポリプロピレン発泡シートにおいて、前記ポリプロピレン発泡シート表面の長手方向および幅方向での前記中心線平均粗さが0.5〜2.0μm、かつ前記ポリプロピレン発泡シート表面の長手方向および幅方向での前記最大高さが5〜25μmであることを特徴とする。   The polypropylene foam sheet according to claim 2 is the polypropylene foam sheet according to claim 1, wherein the center line average roughness in the longitudinal direction and the width direction of the polypropylene foam sheet surface is 0.5 to 2.0 μm. And the said maximum height in the longitudinal direction and the width direction of the said polypropylene foam sheet surface is 5-25 micrometers, It is characterized by the above-mentioned.

またさらに、請求項3に係るポリプロピレン発泡シートは、請求項1または請求項2に記載のポリプロピレン発泡シートであって、前記ポリプロピレン発泡シートの平均気泡径が20〜80μmであることを特徴とする。   Furthermore, the polypropylene foam sheet according to claim 3 is the polypropylene foam sheet according to claim 1 or 2, wherein the polypropylene foam sheet has an average cell diameter of 20 to 80 μm.

ポリプロピレン発泡シートの表面粗さや平均気泡径等を上記規定値内におさめた本発明のポリプロピレン発泡シートによれば、高級感のある、良好なパール調光沢を確実に得ることができる。   According to the polypropylene foam sheet of the present invention in which the surface roughness, average cell diameter and the like of the polypropylene foam sheet are within the above specified values, a high-quality and good pearly gloss can be obtained with certainty.

そして、請求項4に係るポリプロピレン発泡シートの製造方法は、エチレン含有量5〜20重量%、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのエチレン−プロピレンブロック共重合体20〜80重量%と、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%との混和物100重量部に対して、発泡核剤を2〜5重量部を配合した樹脂組成物に無機系ガスを圧入したのち、押出機先端に設けたダイスより押出成形し発泡させることを特徴とする。   And the manufacturing method of the polypropylene foam sheet which concerns on Claim 4 is an ethylene-propylene block whose ethylene content is 5-20 weight%, melt flow rate is 0.1-10 g / 10min, and melt tension in 190 degreeC is 15-25 g Copolymer 20 to 80 wt%, ethylene content 5 to 20 wt%, melt flow rate 5 to 20 g / 10 min ethylene-propylene block copolymer and / or ethylene-propylene random copolymer 20 to 80 wt% After injecting an inorganic gas into a resin composition containing 2 to 5 parts by weight of a foam nucleating agent with respect to 100 parts by weight of the admixture, and then extruding and foaming from a die provided at the tip of the extruder Features.

本発明のポリプロピレン発泡シートの製造方法によれば、押出等の工程後に延伸等の処理を行なうことなく、安定して良好なパール調の光沢が得られるポリプロピレン発泡シートを製造することができる。   According to the method for producing a polypropylene foam sheet of the present invention, it is possible to produce a polypropylene foam sheet capable of stably obtaining a good pearly luster without performing a treatment such as stretching after a process such as extrusion.

このように構成された本発明に係るポリプロピレン発泡シートは、高級感のある、良好なパール調光沢を得ることができ、しかも、その製造方法は、押出等の単一工程にて低コストであり、安定して良好なパール調光沢が得られるポリプロピレン発泡シートを供給することができるといった優れた効果を有する。   The polypropylene foam sheet according to the present invention configured as described above can obtain a high-quality and good pearly gloss, and its manufacturing method is low cost in a single process such as extrusion. It has an excellent effect of being able to supply a polypropylene foam sheet capable of stably obtaining a good pearly luster.

以下、本発明のポリプロピレン発泡シートについてさらに詳しく説明する。   Hereinafter, the polypropylene foam sheet of the present invention will be described in more detail.

本実施形態のポリプロピレン発泡シートは、エチレン含有量5〜20重量%、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのエチレン−プロピレンブロック共重合体20〜80重量%と、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%との混和物100重量部に対して、発泡核剤を2〜5重量部を配合した樹脂組成物に無機系ガスを圧入したのち、押出機のダイスより押出成形し発泡させて製造されており、前記ポリプロピレン発泡シート表面のJIS B0601に基づく中心線平均粗さが0.5〜2.0μm、JIS B0601に基づく最大高さが5〜25μmとされている。   The polypropylene foam sheet of this embodiment has an ethylene content of 5 to 20% by weight, a melt flow rate of 0.1 to 10 g / 10 min, and an ethylene-propylene block copolymer 20 to 80 having a melt tension at 190 ° C. of 15 to 25 g. 100 wt.% Of a blend of 20 wt.% And 20 to 80 wt.% Ethylene-propylene block copolymer or / and ethylene-propylene random copolymer having an ethylene content of 5 to 20 wt.% And a melt flow rate of 5 to 20 g / 10 min. The surface of the polypropylene foam sheet is manufactured by pressing an inorganic gas into a resin composition containing 2 to 5 parts by weight of a foam nucleating agent and then extruding and foaming from a die of an extruder. The center line average roughness based on JIS B0601 is 0.5 to 2.0 μm, and the maximum height based on JIS B0601 is 5 There is a 5μm.

本発明において用いられるエチレン−プロピレンブロック共重合体は、エチレン含有量5〜20重量%、好ましくは7〜15重量%であって、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのものである(溶融張力は、直径2.1mm、長さ8mmのオリフィスを装着したキャピラリーメーターを用い、試験温度190℃、押出速度10mm/minで押し出した溶融樹脂を4m/minの速度で引き取ったときの張力を測定する)。このようなブロック共重合体を少なくとも20重量%用いることにより発泡性に優れる発泡シートが得られる。また、このようなエチレン含量、およびメルトフローレートを有するエチレン−プロピレンブロック共重合体は、押出時に樹脂組成物の発泡に適した粘弾性を示すため、良好な発泡組織を容易に形成させることができるからである。上記の範囲外では、高倍率発泡シートが得られず、物性面においても優れたものが得られない。   The ethylene-propylene block copolymer used in the present invention has an ethylene content of 5 to 20% by weight, preferably 7 to 15% by weight, a melt flow rate of 0.1 to 10 g / 10 minutes, and a melting at 190 ° C. Tensile strength is 15 to 25 g (melting tension is 4 m / min of molten resin extruded at a test temperature of 190 ° C. and an extrusion speed of 10 mm / min using a capillary meter equipped with an orifice having a diameter of 2.1 mm and a length of 8 mm. Measure the tension when pulled at a speed of min). By using at least 20% by weight of such a block copolymer, a foam sheet having excellent foamability can be obtained. In addition, an ethylene-propylene block copolymer having such an ethylene content and melt flow rate exhibits viscoelasticity suitable for foaming of the resin composition at the time of extrusion, so that a good foamed structure can be easily formed. Because it can. Outside the above range, a high-magnification foamed sheet cannot be obtained, and excellent physical properties cannot be obtained.

また、本実施形態において、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%をブレンドした理由は、押出機内の樹脂温度の上昇を抑制し、シートの長手方向の発泡倍率のバラツキを少なくするという効果もあり、長時間安定した発泡シートが得られるからである。   In this embodiment, an ethylene-propylene block copolymer or / and an ethylene-propylene random copolymer 20 to 80% by weight with an ethylene content of 5 to 20% by weight and a melt flow rate of 5 to 20 g / 10 minutes were blended. The reason is that an increase in the resin temperature in the extruder is suppressed, and the variation of the expansion ratio in the longitudinal direction of the sheet is also reduced, and a foam sheet that is stable for a long time can be obtained.

また、発泡核剤としては例えば、重炭酸ソーダ系、重炭酸アンモニウム系、重曹クエン酸系、アゾジカーボンアミド系などの発泡助剤などが挙げられる。市販品としては永和化成工業株式会社製のポリスレンシリーズが好適に用いられる。さらに、発泡剤としては、窒素ガス、炭酸ガス等の無機系ガスがあげられる。これらを圧入して発泡させるガス発泡法は、発泡剤の分解による発熱がないので、樹脂温度のコントロールを容易に行うことができ、好適な樹脂粘度を保持しやすい。また、得られた発泡シートに有害な残渣がなく、衛生上も好ましい。   Examples of the foam nucleating agent include foaming aids such as sodium bicarbonate, ammonium bicarbonate, sodium bicarbonate citrate, and azodicarbonamide. As a commercially available product, Polyslen series manufactured by Eiwa Chemical Industry Co., Ltd. is preferably used. Further, examples of the foaming agent include inorganic gases such as nitrogen gas and carbon dioxide gas. In the gas foaming method in which these are injected and foamed, there is no heat generation due to the decomposition of the foaming agent, so that the resin temperature can be easily controlled and a suitable resin viscosity is easily maintained. Moreover, there is no harmful residue in the obtained foamed sheet, which is preferable in terms of hygiene.

なお、造核剤、改質用のほかのポリマーや無機フィラー、難燃剤、カーボンブラックのような導電性付与剤、帯電防止剤、着色剤、紫外線吸収剤など、公知の添加物を適量配合しても良い。   Add appropriate amounts of known additives such as nucleating agents, other modifying polymers and inorganic fillers, flame retardants, conductivity-imparting agents such as carbon black, antistatic agents, colorants, and UV absorbers. May be.

そして、押出機内で溶融混練させた樹脂組成物を押出機途中から無機系ガスを圧入したのち、押出機先端に設けたダイスを通して押出成形し発泡させて目的とするポリプロピレン発泡シートを製造する。   The resin composition melt-kneaded in the extruder is injected with an inorganic gas from the middle of the extruder, then extruded through a die provided at the tip of the extruder and foamed to produce the desired polypropylene foam sheet.

この際、発泡用ダイスの先端より水平方向に少なくとも一組以上の成形ロールを設置し、該ロール間を通過させる押出発泡シート表面及び内部の温度を70〜130℃に保持させながら圧壊することなく、シート状に成形し、ついで冷却すると、気泡径が均一で、独立気泡率が高く、表面平滑性、耐衝撃性に優れたポリプロピレン発泡シートが得られる。   At this time, at least one set of forming rolls is installed in the horizontal direction from the tip of the foaming die, and the extruded foam sheet surface that passes between the rolls and the internal temperature are maintained at 70 to 130 ° C. without being crushed. When formed into a sheet and then cooled, a polypropylene foam sheet having a uniform cell diameter, a high closed cell ratio, and excellent surface smoothness and impact resistance can be obtained.

シート表面及び内部の温度は70〜130℃に保つことが重要であり、70℃未満では、樹脂の発泡が抑制されて、目的とする肉厚や発泡倍率のものが得られにくく、また130℃以上では表面からガスが抜け易くなるといった問題が生じる。   It is important to maintain the sheet surface and internal temperature at 70 to 130 ° C. When the temperature is less than 70 ° C., foaming of the resin is suppressed, and it is difficult to obtain the desired wall thickness and expansion ratio. The above causes a problem that gas easily escapes from the surface.

次に、本発明のポリプロピレン発泡シートの実施例を示すが、本発明は下記例に限定されるものではない。   Next, although the Example of the polypropylene foam sheet of this invention is shown, this invention is not limited to the following example.

[実施例]
シリンダー径65mmの押出機に、エチレン含量10重量%、メルトフローレート0.5g/10分、190℃における溶融張力が23gのエチレン−プロピレンブロック共重合体40重量部、エチレン含量7重量%、メルトフローレート9g/10分のエチレン−プロピレンランダム共重合体60重量部、発泡核剤としてのポリスレンEE207E(永和化成工業株式会社製)を、下記表1に示すように2〜5重量部(詳しくは、実施例1においては2重量部、実施例2においては3重量部、実施例3においては5重量部)投入し、押出機途中のシリンダ部より、無機系ガスとしての炭酸ガスを7kg/cm2 の圧力で圧入した後、幅400mmのT型発泡ダイスの先端の中心から水平方向に二組の成形ロールダイを設置し、該ロールダイの間を通過させる時に、シート表面の温度を110℃に保持して押出発泡させて表に示す厚みが0.75〜1mm(詳しくは、実施例1においては0.75mm、実施例2乃至実施例4においては1.0mm)のポリプロピレン発泡シートを作製した。
[Example]
In an extruder with a cylinder diameter of 65 mm, an ethylene content of 10% by weight, a melt flow rate of 0.5 g / 10 minutes, an ethylene-propylene block copolymer of 40 g by weight with a melt tension at 190 ° C. of 23 g, an ethylene content of 7% by weight, a melt 60-5 parts by weight of an ethylene-propylene random copolymer having a flow rate of 9 g / 10 min and 2-5 parts by weight of Polyslene EE207E (manufactured by Eiwa Kasei Kogyo Co., Ltd.) as a foam nucleating agent as shown in Table 1 below 2 parts by weight in Example 1, 3 parts by weight in Example 2, and 5 parts by weight in Example 3), and carbon dioxide as an inorganic gas is 7 kg / cm from the cylinder part in the middle of the extruder. after press-fitted in the second pressure, set up two sets of molding Rorudai horizontally from the center of the tip of the T-type foaming die width 400 mm, the Rorudai When passing through, the sheet surface temperature is maintained at 110 ° C. and extrusion foamed, and the thickness shown in the table is 0.75 to 1 mm (specifically, 0.75 mm in Example 1, Examples 2 to Example) A polypropylene foam sheet of 4 mm was prepared.

[比較例]
実施例における組成比のうち、発泡核剤としてのポリスレンEE207E(永和化成工業株式会社製)を比較例1および比較例2においては1重量部とし、比較例3においては10重量部とし、押出発泡させるポリプロピレン発泡シートの厚みを、比較例1においては0.80mm、比較例2および比較例3においては1.0mmとした点のみを異ならせ、ポリプロピレン発泡シートを作製した。
[Comparative example]
Of the composition ratios in the examples, Polyslen EE207E (manufactured by Eiwa Kasei Kogyo Co., Ltd.) as a foam nucleating agent is 1 part by weight in Comparative Examples 1 and 2, 10 parts by weight in Comparative Example 3, and extrusion foaming. The polypropylene foam sheet was produced by changing the thickness of the polypropylene foam sheet to be used in Comparative Example 1 only to 0.80 mm and in Comparative Example 2 and Comparative Example 3 to 1.0 mm.

[評 価]
1) 表面粗度
得られた実施例1乃至実施例3、比較例1乃至比較例3の6つの試料につき、ポリプロピレン発泡シートの表面のJIS B0601に基づく中心線平均粗さ(Ra)、最大高さ(Rmax)を測定した。なお測定は発泡シートの長手方向(機械方向)および幅方向について、東京精密ハンディサーフE−30Aを用いて測定した。
2) 平均気泡径
前記6つの試料につき、ASTM D3576−77に準じ、シートの断面のSEM写真を撮影し、SEM写真上に水平方向と垂直方向に直線を引き、直線が横切る気泡の弦の長さtを平均した。写真の倍率をMとして、下記式に代入して平均気泡径dを求めた。
d=t/(0.616×M)
3) 記録媒体の外観評価
前記6つの試料の記録品位につき、目視にて外観を評価した。なお、表1中にはパール調の光沢を良好に得られたものは○、パール調の光沢が観察されなかったものを×として示した。
[Evaluation]
1) Surface Roughness Centerline average roughness (Ra) based on JIS B0601 of the surface of the polypropylene foam sheet and the maximum height for the obtained six samples of Examples 1 to 3 and Comparative Examples 1 to 3 The thickness (Rmax) was measured. In addition, the measurement was measured about the longitudinal direction (machine direction) and width direction of the foam sheet using Tokyo Seimitsu Handy Surf E-30A.
2) Average bubble diameter According to ASTM D3576-77, SEM photographs of the cross section of the sheet were taken for the above six samples, straight lines were drawn in the horizontal and vertical directions on the SEM photograph, and the length of the bubble chord that the straight lines crossed The average t was averaged. Assuming that the magnification of the photograph is M, the average bubble diameter d was determined by substituting it into the following equation.
d = t / (0.616 × M)
3) Appearance evaluation of recording medium The appearance was evaluated visually for the recording quality of the six samples. In Table 1, those having a good pearly luster were shown as ◯, and those having no pearly luster were shown as x.

Figure 0004948224
Figure 0004948224

[考 察]
実施例1乃至実施例3の試料はいずれも良好なパール調の光沢を得ることができ、高級感が感じられた。一方、比較例1および比較例2においては、パール調の光沢は観察されず、単なる白色系のプラスチックシートの外観を呈した。また、比較例3においては、パール調の光沢は観察されないが、白色が非常に強いものとなった。
[Discussion]
All of the samples of Examples 1 to 3 were able to obtain a good pearly luster, and a high-class feeling was felt. On the other hand, in Comparative Example 1 and Comparative Example 2, no pearly luster was observed, and the appearance of a simple white plastic sheet was exhibited. In Comparative Example 3, pearly luster was not observed, but white was very strong.

この結果、良好なパール調の光沢は、ポリプロピレン発泡シートの組成比、前記ポリプロピレン発泡シートの厚さ、表面のJIS B0601に基づく中心線平均粗さ(Ra)、同じくJIS B0601に基づく最大高さ(Rmax)および平均気泡径を本実施形態のように規定値内とすることで、確実に得ることができ、しかも、本実施形態の製造方法によれば、押出成形の単一工程で安定して製造することができることが確認された。   As a result, the gloss of good pearl tone is the composition ratio of the polypropylene foam sheet, the thickness of the polypropylene foam sheet, the center line average roughness (Ra) based on JIS B0601, and the maximum height based on JIS B0601 ( Rmax) and the average bubble diameter can be reliably obtained by making them within the specified values as in the present embodiment. Moreover, according to the manufacturing method of the present embodiment, the process can be stably performed in a single process of extrusion molding. It was confirmed that it could be manufactured.

Claims (4)

エチレン含有量5〜20重量%、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのエチレン−プロピレンブロック共重合体20〜80重量%と、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%との混和物100重量部に対して、発泡核剤を2〜5重量部を配合した樹脂組成物に無機系ガスを圧入したのち、押出機のダイスより押出成形し発泡させたパール調光沢を有するポリプロピレン発泡シートであって、前記ポリプロピレン発泡シート表面のJIS B0601に基づく中心線平均粗さが0.5〜2.0μm、JIS B0601に基づく最大高さが5〜25μmであることを特徴とするポリプロピレン発泡シート。 An ethylene-propylene block copolymer of 20 to 80% by weight having an ethylene content of 5 to 20% by weight, a melt flow rate of 0.1 to 10 g / 10 min, and a melt tension at 190 ° C. of 15 to 25 g; The foam nucleating agent is added to 100 parts by weight of a blend of 20% by weight of an ethylene-propylene block copolymer or / and an ethylene-propylene random copolymer having a melt flow rate of 5-20 g / 10 min. A polypropylene foam sheet having a pearly luster that is extruded and foamed from a die of an extruder after injecting an inorganic gas into a resin composition containing 2 to 5 parts by weight. Centerline average roughness based on B0601 is 0.5 to 2.0 μm, maximum height based on JIS B0601 is 5-2 Polypropylene foam sheet which is a [mu] m. 前記ポリプロピレン発泡シート表面の長手方向および幅方向での前記中心線平均粗さが0.5〜2.0μm、かつ前記ポリプロピレン発泡シート表面の長手方向および幅方向での前記最大高さが5〜25μmであることを特徴とする請求項1記載のポリプロピレン発泡シート。 The center line average roughness in the longitudinal direction and the width direction of the polypropylene foam sheet surface is 0.5 to 2.0 μm, and the maximum height in the longitudinal direction and the width direction of the polypropylene foam sheet surface is 5 to 25 μm. The polypropylene foam sheet according to claim 1, wherein: 前記ポリプロピレン発泡シートの平均気泡径が20〜80μmであることを特徴とする請求項1または請求項2に記載のポリプロピレン発泡シート。 The polypropylene foam sheet according to claim 1 or 2, wherein the polypropylene foam sheet has an average cell diameter of 20 to 80 µm. エチレン含有量5〜20重量%、メルトフローレート0.1〜10g/10分、190℃における溶融張力が15〜25gのエチレン−プロピレンブロック共重合体20〜80重量%と、エチレン含量5〜20重量%、メルトフローレート5〜20g/10分のエチレン−プロピレンブロック共重合体または/およびエチレン−プロピレンランダム共重合体20〜80重量%との混和物100重量部に対して、発泡核剤を2〜5重量部を配合した樹脂組成物に無機系ガスを圧入したのち、押出機先端に設けたダイスより押出成形し発泡させることを特徴とするポリプロピレン発泡シートの製造方法。 An ethylene-propylene block copolymer of 20 to 80% by weight having an ethylene content of 5 to 20% by weight, a melt flow rate of 0.1 to 10 g / 10 min, and a melt tension at 190 ° C. of 15 to 25 g; The foam nucleating agent is added to 100 parts by weight of a blend of 20% by weight of an ethylene-propylene block copolymer or / and an ethylene-propylene random copolymer having a melt flow rate of 5-20 g / 10 min. A method for producing a polypropylene foam sheet, comprising: injecting an inorganic gas into a resin composition containing 2 to 5 parts by weight, and then extruding and foaming from a die provided at the tip of an extruder.
JP2007084721A 2007-03-28 2007-03-28 Polypropylene foam sheet and method for producing the same Active JP4948224B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007084721A JP4948224B2 (en) 2007-03-28 2007-03-28 Polypropylene foam sheet and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007084721A JP4948224B2 (en) 2007-03-28 2007-03-28 Polypropylene foam sheet and method for producing the same

Publications (2)

Publication Number Publication Date
JP2008239879A JP2008239879A (en) 2008-10-09
JP4948224B2 true JP4948224B2 (en) 2012-06-06

Family

ID=39911601

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007084721A Active JP4948224B2 (en) 2007-03-28 2007-03-28 Polypropylene foam sheet and method for producing the same

Country Status (1)

Country Link
JP (1) JP4948224B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5892283B1 (en) * 2014-11-28 2016-03-23 住友化学株式会社 Molded body made of thermoplastic resin composition

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61168634A (en) * 1985-01-21 1986-07-30 Furukawa Electric Co Ltd:The Production of propylene/ethylene copolymer foam
JP3505230B2 (en) * 1994-09-29 2004-03-08 古河電気工業株式会社 Method for producing polypropylene foam sheet
JP2003147110A (en) * 2001-11-09 2003-05-21 Mitsui Chemicals Inc Foam of polyolefin composition and its manufacturing method

Also Published As

Publication number Publication date
JP2008239879A (en) 2008-10-09

Similar Documents

Publication Publication Date Title
KR101455435B1 (en) Polypropylene resin foam particle and molding thereof
JP5512672B2 (en) Polypropylene resin expanded particles and expanded molded articles
JP5360975B2 (en) Method for producing polyethylene resin foam blow molded article and polyethylene resin foam blow molded article
JP5123021B2 (en) Method for producing polypropylene resin foam and polypropylene resin foam
JP2010270228A (en) Method for producing polypropylene-based resin foam and polypropylene-based resin foam
WO1991007461A1 (en) Resin composition for film and process for producing film using the same
JP2011132420A (en) Method for producing polypropylene-based resin foam and polypropylene-based resin foam
JP2011074127A (en) Polypropylene resin foam
JP4948224B2 (en) Polypropylene foam sheet and method for producing the same
JP2008272972A (en) Recording medium for inkjet printer
JP4612266B2 (en) Thermoplastic resin molded article excellent in wood texture and method for producing the same
US6462101B1 (en) Foam comprising a blend of low density polyethylene and high melt tension polypropylene
JP3634469B2 (en) Method for producing polypropylene resin foam
JP2000103960A (en) Polyamide-based resin foam and its production
JP5958636B1 (en) Molded body made of thermoplastic resin composition
JP5456421B2 (en) Extrusion foam board
JP5992193B2 (en) Resin composition for extrusion foaming, method for producing resin foam, and resin foam
JP2013209545A (en) Resin composition for extrusion foaming, method for producing resin foam and resin foam
JP2004122717A (en) Extruded foam sheet of polypropylene resin, its manufacturing method, and molded product of the same
JP2020093562A (en) Air-conditioning duct for vehicle
JP2006248187A (en) Polypropylene resin-laminated foamed sheet, its manufacturing method and its molding
JP3505230B2 (en) Method for producing polypropylene foam sheet
JP2004269611A (en) Production method for styrenic resin foam sheet
JP4134323B2 (en) Foamable resin composition and propylene-based resin foam
JPH03231936A (en) Foamed film

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20100326

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20120221

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20120222

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20120306

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150316

Year of fee payment: 3

R151 Written notification of patent or utility model registration

Ref document number: 4948224

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150316

Year of fee payment: 3

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350