JPS6140184B2 - - Google Patents
Info
- Publication number
- JPS6140184B2 JPS6140184B2 JP55066369A JP6636980A JPS6140184B2 JP S6140184 B2 JPS6140184 B2 JP S6140184B2 JP 55066369 A JP55066369 A JP 55066369A JP 6636980 A JP6636980 A JP 6636980A JP S6140184 B2 JPS6140184 B2 JP S6140184B2
- Authority
- JP
- Japan
- Prior art keywords
- foamed resin
- resin layer
- tube
- weight
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229920005989 resin Polymers 0.000 claims description 78
- 239000011347 resin Substances 0.000 claims description 78
- -1 polyethylene Polymers 0.000 claims description 26
- 229920001684 low density polyethylene Polymers 0.000 claims description 19
- 239000004702 low-density polyethylene Substances 0.000 claims description 19
- 239000004743 Polypropylene Substances 0.000 claims description 18
- 229920001155 polypropylene Polymers 0.000 claims description 18
- 239000011342 resin composition Substances 0.000 claims description 16
- 239000002985 plastic film Substances 0.000 claims description 15
- 229920006255 plastic film Polymers 0.000 claims description 15
- 239000000835 fiber Substances 0.000 claims description 13
- 239000004604 Blowing Agent Substances 0.000 claims description 12
- 229920005992 thermoplastic resin Polymers 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000004698 Polyethylene Substances 0.000 claims description 7
- 229920000573 polyethylene Polymers 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 5
- 230000008018 melting Effects 0.000 claims description 5
- 239000012809 cooling fluid Substances 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 claims description 3
- 239000004088 foaming agent Substances 0.000 claims description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 3
- 229920005604 random copolymer Polymers 0.000 claims description 3
- 239000010408 film Substances 0.000 description 46
- 238000004806 packaging method and process Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 4
- 230000035699 permeability Effects 0.000 description 4
- 229920000554 ionomer Polymers 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 239000004156 Azodicarbonamide Substances 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 229920006257 Heat-shrinkable film Polymers 0.000 description 2
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 2
- 235000019399 azodicarbonamide Nutrition 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229920001903 high density polyethylene Polymers 0.000 description 2
- 239000004700 high-density polyethylene Substances 0.000 description 2
- 239000012785 packaging film Substances 0.000 description 2
- 229920006280 packaging film Polymers 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 229920013716 polyethylene resin Polymers 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- CZGWDPMDAIPURF-UHFFFAOYSA-N (4,6-dihydrazinyl-1,3,5-triazin-2-yl)hydrazine Chemical compound NNC1=NC(NN)=NC(NN)=N1 CZGWDPMDAIPURF-UHFFFAOYSA-N 0.000 description 1
- 235000008766 Murraya exotica Nutrition 0.000 description 1
- 240000001899 Murraya exotica Species 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- VRFNYSYURHAPFL-UHFFFAOYSA-N [(4-methylphenyl)sulfonylamino]urea Chemical compound CC1=CC=C(S(=O)(=O)NNC(N)=O)C=C1 VRFNYSYURHAPFL-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002666 chemical blowing agent Substances 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 239000002654 heat shrinkable material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 229920001384 propylene homopolymer Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
Landscapes
- Molding Of Porous Articles (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Laminated Bodies (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Description
【発明の詳細な説明】
本発明は和紙状の風合を有する多層プラスチツ
クフイルム及びその製造方法に関する。更に詳し
くは内面に微細な繊維構造に起因する和紙状の風
合を有する熱収縮性の高いチユーブ状の薄い多層
プラスチツクフイルムを共押出インフレーシヨン
法で製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a multilayer plastic film having a Japanese paper-like texture and a method for producing the same. More specifically, the present invention relates to a method for producing a highly heat-shrinkable, tubular thin multilayer plastic film having a Japanese paper-like texture due to a fine fiber structure on the inner surface by a coextrusion inflation method.
近年、プラスチツク二軸延伸フイルムの製造技
術の発展に伴つて、熱収縮性フイルムが集積シユ
リンク包装及び個別シユリンク包装用として広く
普及してきた。シユリンク包装では、ポリエチレ
ン、ポリプロピレン等のチユーブ状のインフレー
シヨンフイルムが広く使われており、これらのチ
ユーブ状のフイルムの中へ被包装物を入れ、赤外
加熱トンネルを通して被包装物をぴつたりと収縮
包装することが出来る。従来のシユリンク包装用
フイルムは強靭で透明性が良いという長所を有す
るが、緩衝性及び落着いた風合に欠けるという短
所があつた。 In recent years, with the development of manufacturing technology for plastic biaxially stretched films, heat-shrinkable films have become widely used for integrated shrink packaging and individual shrink packaging. In Shrink packaging, tube-shaped inflation films made of polyethylene, polypropylene, etc. are widely used, and the packaged items are placed inside these tube-shaped films and passed through an infrared heating tunnel to tightly fit the packaged items. Can be shrink wrapped. Conventional Shrink packaging films have the advantages of being strong and transparent, but have the disadvantages of lacking cushioning properties and a calm texture.
緩衝性包装材料として発泡スチロールシート、
発泡ポリエチレンシート等が開発されており、適
度のクツシヨン性を発泡体に保持させることによ
つて耐衝撃性の必要な商品の包装に広く採用され
ている。然し乍ら、これらの発泡シートは厚くて
不透明である為、包装体が嵩張る、被包装物品が
殆んど見えない、非収縮性である為に収縮包装用
として使用することが出来ない等の短所がある。 Styrofoam sheets as cushioning packaging materials,
Foamed polyethylene sheets and the like have been developed, and are widely used for packaging products that require impact resistance by allowing the foam to maintain appropriate cushioning properties. However, since these foam sheets are thick and opaque, they have disadvantages such as bulky packaging, almost invisible packaging, and non-shrinkable properties that prevent them from being used for shrink wrapping. be.
その他、最近和紙に近い風合を有する包装材料
として不織布が開発され広く使用されているが、
密閉性が不充分、熱収縮性がない等の欠点があ
る。 In addition, non-woven fabrics have recently been developed and widely used as packaging materials with a texture similar to Japanese paper.
It has drawbacks such as insufficient sealing properties and lack of heat shrinkability.
本発明者らはこのような現状に鑑み、和紙のよ
うな風合を有し、熱収縮性があつて、しかも適度
の気密性あるは通気性を有し、かつ透視性のある
熱収縮性フイルムを得んとして種々研究の結果、
低密度ポリエチレン樹脂とポリプロピレン樹脂と
発泡剤とを混合した樹脂組成物を発泡性樹脂層の
主成分とし、低密度ポリエチレンを主成分とする
樹脂組成物を非発泡性樹脂層とし、これらの二層
の共押出インフレーシヨンによつて極めて和紙に
近い風合を有する熱収縮性フイルムを製造出来る
ことを見出し、更に詳細な研究を進めて本発明を
完成させるに至つたものである。 In view of the current situation, the present inventors developed a heat-shrinkable material that has a Japanese paper-like texture, is heat-shrinkable, has appropriate airtightness or air permeability, and is transparent. As a result of various studies to obtain film,
A resin composition containing a mixture of low-density polyethylene resin, polypropylene resin, and a foaming agent is used as the main component of the foamable resin layer, and a resin composition containing low-density polyethylene as the main component is used as the non-foamable resin layer. The inventors discovered that a heat-shrinkable film having a texture very similar to that of Japanese paper could be produced by coextrusion inflation, and conducted further detailed research to complete the present invention.
本発明の第一の目的は、加熱収縮包装に適した
和紙状の風合を有する透視性の優れた熱収縮性プ
ラスチツクフイルムを提供することにある。 A first object of the present invention is to provide a heat-shrinkable plastic film with a Japanese paper-like feel suitable for heat-shrink packaging and excellent transparency.
本発明の第二の目的は、軽くて、丈夫で、しか
も引き裂き性の良好な和紙状の風合を有する多層
プラスチツクフイルムを提供することにある。 A second object of the present invention is to provide a multilayer plastic film that is light, strong, and has a Japanese paper-like texture with good tearability.
本発明の第三の目的は、紙と従来のプラスチツ
クフイルムとの中間程度の通気性を有する微孔性
フイルムを提供することにある。 A third object of the present invention is to provide a microporous film having air permeability intermediate between that of paper and conventional plastic film.
本発明の多層プラスチツクフイルムは、発泡樹
脂層と非発泡樹脂層との少くとも二層から成る厚
さ20μ乃至200μの多層プラスチツクフイルムで
あり、発泡樹脂層はポリエチレン100重量部に対
して、ポリプロピレン樹脂30乃至300重量部と発
泡剤0.3乃至10重量部とを添加した樹脂組成物か
ら成り、非発泡樹脂層は熱可塑性樹脂を主成分と
する樹脂組成物から成り、発泡樹脂層は最外層に
あつて微細な繊維構造に起因する和紙状の風合を
形成していることを特徴としている。 The multilayer plastic film of the present invention is a multilayer plastic film having a thickness of 20μ to 200μ and consisting of at least two layers, a foamed resin layer and a non-foamed resin layer, and the foamed resin layer is made of polypropylene resin based on 100 parts by weight of polyethylene. It consists of a resin composition containing 30 to 300 parts by weight and 0.3 to 10 parts by weight of a blowing agent, the non-foamed resin layer consists of a resin composition whose main component is a thermoplastic resin, and the foamed resin layer is the outermost layer. It is characterized by a Japanese paper-like texture due to its fine fiber structure.
本発明の多層プラスチツクフイルムの製造方法
は、発泡剤を添加した熱可塑性樹脂を主成分とす
る発泡樹脂層と発泡剤を添加しない熱可塑性樹脂
を主成分とする非発泡樹脂層とから成る多層プラ
スチツクフイルムの製造方法において、ポリエチ
レン樹脂100重量部に対して、ポリプロピレン樹
脂30乃至300重量部及び発泡剤0.3乃至10重量部を
添加した発泡樹脂組成物と熱可塑性樹脂を主成分
とする非発泡樹脂組成物とを別々の押出機でそれ
ぞれ混練溶融した後、円筒状共押出ダイの内部で
発泡樹脂層と非発泡樹脂層とを溶融接着し、次い
で押出ダイの出口から少くとも内面が発泡樹脂層
となるように積層チユーブ状に押出し、次いで該
チユーブ内外の気圧の差により該チユーブを幅方
向へ膨張させると共に引取方向へ延伸し、更に該
チユーブの表面に冷却流体を吹き付けて該チユー
ブを外面から冷却しながら最終的にブロー比率が
3以上に達するまで該チユーブを膨張させ、同時
に引取比率が2以上に達するまで引取方向へ該チ
ユーブを延伸して後少くとも一組の引取ロールの
間隙で該チユーブを圧締して発泡樹脂層の微細な
繊維構造に起因する和紙状の風合を形成させるこ
とを特徴としている。 The method for producing a multilayer plastic film of the present invention comprises a foamed resin layer mainly composed of a thermoplastic resin to which a blowing agent is added and a non-foamed resin layer mainly composed of a thermoplastic resin to which no blowing agent is added. In the film manufacturing method, a foamed resin composition in which 30 to 300 parts by weight of a polypropylene resin and 0.3 to 10 parts by weight of a blowing agent are added to 100 parts by weight of a polyethylene resin, and a non-foamed resin composition whose main components are a thermoplastic resin. After kneading and melting the materials in separate extruders, the foamed resin layer and non-foamed resin layer are melted and bonded inside a cylindrical coextrusion die, and then from the exit of the extrusion die, at least the inner surface is the foamed resin layer. The tube is then extruded into a laminated tube shape so that the tube is expanded in the width direction due to the difference in air pressure between the inside and outside of the tube, and is stretched in the take-up direction. Cooling fluid is then sprayed onto the surface of the tube to cool the tube from the outside. At the same time, the tube is expanded until the blow ratio finally reaches 3 or more, and at the same time, the tube is stretched in the drawing direction until the take-up ratio reaches 2 or more. The foamed resin layer is compressed to form a Japanese paper-like texture due to the fine fiber structure of the foamed resin layer.
本発明において、発泡樹脂層は、ポリエチレン
樹脂100重量部に対して、ポリプロピレン樹脂30
乃至300重量部及び発泡剤0.3乃至10重量部を添加
した樹脂組成物を主成分としている。発泡樹脂層
が低密度ポリエチレン単独の場合あるいはポリプ
ロピレン単独の場合にはフイルムの風合に特長が
ないが、発泡樹脂層の樹脂が低密度ポリエチレン
とポリプロピレンとの混合物の場合に特有の和紙
に近い風合が生じることが分つた。発泡樹脂組成
物中の低密度ポリエチレンとポリプロピレンとの
混合比を変えてフイルムを製造した結果、低密度
ポリエチレン100重量部に対してポリプロピレン
80乃至150重量部を添加した配合のフイルムが最
も和紙に近い風合を示し、ポリプロピレン30乃至
300重量部を添加した配合が好ましい範囲である
ことが分つた。 In the present invention, the foamed resin layer contains 30 parts by weight of polypropylene resin per 100 parts by weight of polyethylene resin.
The main component is a resin composition to which 300 parts by weight and 0.3 to 10 parts by weight of a blowing agent are added. When the foamed resin layer is made of low-density polyethylene or polypropylene alone, the film has no special texture, but when the foamed resin layer is made of a mixture of low-density polyethylene and polypropylene, it has a characteristic texture similar to Japanese paper. It was found that there is a possibility that the As a result of manufacturing films by changing the mixing ratio of low density polyethylene and polypropylene in the foamed resin composition, it was found that polypropylene was mixed with 100 parts by weight of low density polyethylene.
Films containing 80 to 150 parts by weight of polypropylene have a texture most similar to that of Japanese paper;
It was found that a formulation in which 300 parts by weight was added was within a preferable range.
発泡樹脂層に添加するポリプロピレン樹脂とし
ては、プロピレン系ランダム共重合体樹脂が最も
好ましく、プロピレンホモポリマーと低密度ポリ
エチレンとの混合物ではややフイルムに軟かい風
合が欠ける。低密度ポリエチレンの代りに高密度
ポリエチレンを使用しても良いが、若干フイルム
の風合が変化する。従つて、低密度ポリエチレン
とポリプロピレンとの混合物が最も好ましい。 As the polypropylene resin added to the foamed resin layer, a propylene-based random copolymer resin is most preferable, and a mixture of a propylene homopolymer and a low-density polyethylene results in a film that somewhat lacks a soft feel. High-density polyethylene may be used instead of low-density polyethylene, but the texture of the film will change slightly. Therefore, a mixture of low density polyethylene and polypropylene is most preferred.
低密度ポリエチレンとポリプロピレンとの混合
物が和紙状の風合を造り出す為に好ましい理由は
明確ではないが、おそらく低密度ポリエチレンと
ポリプロピレンとの相溶性の良くないことがフイ
ルムの風合の向上に寄与しているものと考えられ
る。相溶性の悪い低密度ポリエチレンとポリプロ
ピレンとの混合物は発泡剤を添加することによつ
て、フイルムの発泡延伸過程で微細な繊維構造が
生じ、その為に和紙状の独特の風合が現われてく
るものと推定される。 The reason why a mixture of low-density polyethylene and polypropylene is preferable for creating a Japanese paper-like texture is not clear, but perhaps the poor compatibility between low-density polyethylene and polypropylene contributes to improving the texture of the film. It is thought that the When a foaming agent is added to a mixture of low-density polyethylene and polypropylene, which have poor compatibility, a fine fiber structure is created during the foaming and stretching process of the film, resulting in a unique Japanese paper-like texture. It is estimated that
発泡剤はポリエチレン100重量部に対して0.3乃
至10重量部添加する。発泡剤の添加量は発泡剤の
種類にも依存するが、通常の添加量の範囲を越え
るものではない。発泡剤の種類は特に限定しない
が、重炭酸ソーダ、アゾジカルボンアミド、p−
トルエンスルホニルセミカルバジド、トリヒドラ
ジノトリアジン等が好ましい。 The blowing agent is added in an amount of 0.3 to 10 parts by weight per 100 parts by weight of polyethylene. The amount of the blowing agent added depends on the type of blowing agent, but does not exceed the range of usual amounts. The type of blowing agent is not particularly limited, but includes sodium bicarbonate, azodicarbonamide, p-
Toluenesulfonyl semicarbazide, trihydrazinotriazine and the like are preferred.
非発泡樹脂層は熱可塑性樹脂であり、発泡樹脂
層に隣接する層の樹脂はポリオレフイン樹脂、特
に低密度ポリエチレン、高密度ポリエチレン、ポ
リプロピレン、エチレン−醋酸ビニル共重合体樹
脂、1・2ポリブタジエン樹脂、アイオノマー樹
脂等が好ましい。高い熱収縮率を要求される用途
には非発泡樹脂層として低密度ポリエチレンある
いはアイオノマー樹脂が好ましい。非発泡樹脂層
の樹脂の種類が変化してもフイルムの和紙状の風
合への影響は小さいが、発泡樹脂層との接着性の
良好な樹脂としてポリオレフイン樹脂が適当であ
る。 The non-foamed resin layer is a thermoplastic resin, and the resin in the layer adjacent to the foamed resin layer is a polyolefin resin, particularly low-density polyethylene, high-density polyethylene, polypropylene, ethylene-vinyl acetate copolymer resin, 1.2 polybutadiene resin, Ionomer resins and the like are preferred. For applications requiring a high thermal shrinkage rate, low density polyethylene or ionomer resin is preferred as the non-foamed resin layer. Even if the type of resin in the non-foamed resin layer changes, the effect on the Japanese paper-like texture of the film is small, but polyolefin resin is suitable as a resin that has good adhesiveness with the foamed resin layer.
発泡樹脂組成物と非発泡樹脂組成物とをそれぞ
れ別々の押出機で加熱、混練、溶融した後、円筒
状共押出ダイの内部で発泡樹脂層と非発泡樹脂層
とを溶融接着し、押出ダイの出口から積層チユー
ブに押出す。発泡樹脂層と非発泡樹脂層とのダイ
内接着はフイルムに和紙状の風合を生ぜしめる為
に重要である。発泡樹脂層と非発泡樹脂層とがダ
イ内で十分強固に溶融接着することにより、積層
チユーブのブロー延伸の際、発泡樹脂層が非発泡
樹脂層と一体となつて延伸され、微細な繊維構造
が形成されるものと考えられる。 After heating, kneading, and melting the foamed resin composition and the non-foamed resin composition in separate extruders, the foamed resin layer and the non-foamed resin layer are melted and bonded inside a cylindrical coextrusion die, and the extrusion die extrude from the outlet into the laminated tube. In-die adhesion between the foamed resin layer and the non-foamed resin layer is important for producing a Japanese paper-like texture in the film. By melting and adhering the foamed resin layer and the non-foamed resin layer sufficiently firmly in the die, the foamed resin layer and the non-foamed resin layer are stretched together with the non-foamed resin layer during blow stretching of the laminated tube, creating a fine fiber structure. is thought to be formed.
積層チユーブの内面は発泡樹脂層にすることが
必要である。発泡樹脂層がチユーブの内面にある
場合と外面にある場合とでフイルムの微細構造を
比較すると、発泡樹脂層が外面にある場合はフイ
ルム面に網目状の凹凸が形成されやすく、和紙状
の風合に欠けるが、発泡樹脂層が内面にある場合
はフイルム面に微細な繊維構造が形成され、和紙
状の風合のフイルムが出来る。 It is necessary that the inner surface of the laminated tube be made of a foamed resin layer. Comparing the microstructure of the film when the foamed resin layer is on the inner surface of the tube and when it is on the outer surface, it is found that when the foamed resin layer is on the outer surface, network-like unevenness is more likely to be formed on the film surface, and the film has a Japanese paper-like appearance. However, if the foamed resin layer is on the inner surface, a fine fiber structure is formed on the film surface, resulting in a film with a Japanese paper-like texture.
積層チユーブは内外の気圧の差により、幅方向
へ膨張させると共に引取方向へ延伸し、更にチユ
ーブの表面に冷却流体を吹き付けてチユーブを外
面から冷却しながら、最終的にブロー比率が3以
上に達するまで該チユーブを膨張させ、同時に引
取比率が2以上に達するまで引取方向へ延伸す
る。ブロー比率とは膨張したチユーブ状フイルム
の直径と円筒状ダイスの出口、即ちリツプの直径
との比であり、引取比率は引取ロールの間隙を通
過する製造されたフイルムの通過速度と円筒状ダ
イスの出口を通過するチユーブ状溶融樹脂の通過
速度との比で定義される。フイルムに和紙状の風
合を形成させ、しかも高い熱収縮性を付与させる
為には、最終的にブロー比率を4以上、引取比率
を3以上にすることが好ましい。このようにブロ
ー比率と引取比率とを著しく高くすることによつ
て、非発泡樹脂層の薄いフイルムの表面に微細な
繊維が積み重なつて薄く散らばつて付着している
ような構造になり、微細な繊維が密に付着した透
視性の悪い部分と微細な繊維が疎に付着した透視
性の良い部分とが適度に分布して和紙のような風
合が形成される。 Due to the difference in air pressure between the inside and outside, the laminated tube expands in the width direction and stretches in the take-up direction, and cools the tube from the outside by spraying cooling fluid onto the surface of the tube, eventually reaching a blow ratio of 3 or more. The tube is inflated until the tube is expanded and simultaneously stretched in the take-off direction until the take-off ratio reaches 2 or more. The blowing ratio is the ratio between the diameter of the expanded tubular film and the diameter of the exit, or lip, of the cylindrical die, and the takeoff ratio is the ratio between the passing speed of the produced film through the gap between the takeoff rolls and the diameter of the cylindrical die. It is defined as the ratio to the passage speed of the tube-shaped molten resin passing through the outlet. In order to form a Japanese paper-like texture on the film and impart high heat shrinkability to the film, it is preferable that the final blow ratio be 4 or more and the take-up ratio be 3 or more. By significantly increasing the blow ratio and take-up ratio in this way, a structure is created in which fine fibers are piled up and thinly scattered and attached to the surface of the thin film of the non-foamed resin layer. A texture similar to that of Japanese paper is formed by appropriately distributing areas with poor transparency to which fine fibers are densely adhered and areas with good transparency to which fine fibers are sparsely adhered.
本発明のフイルムの厚みは20μ乃至200μであ
る。フイルムの厚みは、アンビル及びスピンドル
の測定面がいずれも円形で、その直径が6mmのマ
イクロメーターによつて測つたものである。フイ
ルムの厚みは発泡樹脂層の疎密の分布により局部
的に変動しているが、この方法で測つたフイルム
の厚みの振れは小さい。フイルムの厚みが20μ以
下では強度が著しく低下する為、実用性に乏し
く、フイルムの厚みが200μ以上では和紙状の風
合が低下する。 The thickness of the film of the present invention is 20μ to 200μ. The thickness of the film was measured using a micrometer with a diameter of 6 mm, and the measurement surfaces of the anvil and spindle were both circular. Although the thickness of the film varies locally depending on the density distribution of the foamed resin layer, the variation in the thickness of the film measured by this method is small. If the thickness of the film is less than 20 μm, the strength will be significantly reduced, making it impractical, and if the thickness of the film is more than 200 μm, the Japanese paper-like texture will deteriorate.
厚さ50μ程度の本発明の薄手のフイルムは軽く
て、丈夫であり、しかも引き裂き性が著しく良好
であり、フイルムの長手方向及び幅方向へ真つ直
ぐに引き裂くことが容易に出来る。これは発泡樹
脂層の微細な繊維構造と薄い非発泡樹脂層との層
状の組合せによるものであり、このフイルムの引
き裂き性は紙のそれに近い感じを持つている。 The thin film of the present invention having a thickness of about 50 μm is light and strong, and has extremely good tearability, and can be easily torn straight in the longitudinal and width directions of the film. This is due to the layered combination of the fine fiber structure of the foamed resin layer and the thin non-foamed resin layer, and the tearability of this film is similar to that of paper.
フイルムに和紙状の風合を形成させる為には発
泡樹脂層を最外層にすることが必要である。但し
本発明のフイルムは発泡樹脂層と非発泡樹脂層と
の二層に限定するものではなく、表裏とも発泡樹
脂層とし、中間に非発泡樹脂層を持つてくること
によつて、フイルムの風合を更に和紙の風合に近
づけることが出来る。フイルムにガスバリア性を
付与させる為、発泡樹脂層/低密度ポリエチレン
層/接着性ポリオレフイン層/エチレン−醋酸ビ
ニル共重合体けん化物樹脂層がこの順で配された
構成の多層フイルムも好ましい。このフイルムは
和紙のような風合を有し、しかもガスバリア性及
び熱収縮性に優れており、包装用フイルムとして
適している。 In order to form a Japanese paper-like texture on the film, it is necessary to make the foamed resin layer the outermost layer. However, the film of the present invention is not limited to two layers, a foamed resin layer and a non-foamed resin layer, but by having foamed resin layers on both the front and back sides and a non-foamed resin layer in the middle, it is possible to improve the wind resistance of the film. The texture can be made even closer to that of Japanese paper. In order to impart gas barrier properties to the film, a multilayer film having a structure in which a foamed resin layer/low density polyethylene layer/adhesive polyolefin layer/saponified ethylene-vinyl acetate copolymer resin layer is arranged in this order is also preferred. This film has a texture similar to Japanese paper, and has excellent gas barrier properties and heat shrinkability, making it suitable as a packaging film.
本発明のフイルムは紙よりも通気性が小さい
が、一般に広く使用されている低密度ポリエチレ
ンのフイルムよりも通気性が大きく、マイクロポ
ーラスフイルムとしての特長をも兼備している。 Although the film of the present invention has lower air permeability than paper, it has higher air permeability than the generally widely used low density polyethylene film, and also has the features of a microporous film.
以下に実施例を示す。 Examples are shown below.
実施例
低密度ポリエチレン(住友化学株式会社製スミ
カセン)100重量部に対して、プロピレン系ラン
ダムコポリマー(住友化学株式会社製住友ノーブ
レン、MI=7)100重量部と化学発泡剤アゾジカ
ルボンアミド2重量部とを混合した発泡樹脂組成
物とアイオノマー樹脂(三井ポリケミカル株式会
社製ハイミラン)から成る非発泡樹脂組成物とを
それぞれ2台の40mmφ押出機で混練溶融した後、
ダイリツプの直径50mmの円筒状二層共押出ダイか
ら内層が発泡樹脂層、外層が非発泡樹脂層の積層
チユーブを10Kg/hrの吐出速度で押出し、空冷イ
ンフレーシヨン法により約20m/minの引取速度
で折径380mm、厚さ60μのフイルムを製造した。
本フイルムのブロー比率は4.8、引取比率は3.1に
設定した。製造したフイルムは、微細な繊維構造
に起因する和紙状の風合を有しており、軽くて丈
夫であり、しかもフイルムの幅方向及び引取方向
への引き裂き性に優れている。Example: 100 parts by weight of low-density polyethylene (Sumikasen, manufactured by Sumitomo Chemical Co., Ltd.), 100 parts by weight of propylene random copolymer (Sumitomo Noblen, MI = 7, manufactured by Sumitomo Chemical Co., Ltd.) and 2 parts by weight of chemical blowing agent azodicarbonamide. After kneading and melting a foamed resin composition mixed with a non-foamed resin composition made of an ionomer resin (Himilan manufactured by Mitsui Polychemical Co., Ltd.) using two 40 mmφ extruders,
A laminated tube with a foamed resin inner layer and a non-foamed resin outer layer is extruded from the die lip's cylindrical two-layer coextrusion die with a diameter of 50 mm at a discharge rate of 10 kg/hr, and the air-cooled inflation method is used to extrude the laminated tube at a rate of approximately 20 m/min. A film with a fold diameter of 380 mm and a thickness of 60 μm was produced at this speed.
The blow ratio of this film was set at 4.8, and the take-off ratio was set at 3.1. The produced film has a Japanese paper-like feel due to its fine fiber structure, is light and strong, and has excellent tearability in the width direction and the pulling direction.
本フイルムの120℃のグリセリン浴に入れて2
秒後の熱収縮性は縦方向へ45%、横方向(幅方
向)へ55%であつた。 Put this film in a glycerin bath at 120℃ 2
The heat shrinkability after seconds was 45% in the vertical direction and 55% in the horizontal direction (width direction).
本フイルムはヒートシール性に優れており、化
粧箱等のシユリンク包装に適している。 This film has excellent heat sealability and is suitable for shrink packaging such as cosmetic boxes.
Claims (1)
から成る厚さ20μ乃至200μの多層プラスチツク
フイルムであり、発泡樹脂層が100重量部のポリ
エチレンに対して、30乃至300重量部のポリプロ
ピレンと0.3乃至10重量部の発泡剤を含有した樹
脂組成物を主成分とし、非発泡樹脂層が熱可塑性
樹脂を主成分とする樹脂組成物から成り、発泡樹
脂層は最外層にあつて、微細な繊維構造に起因す
る和紙状の風合を形成していることを特徴とする
多層プラスチツクフイルム。 2 発泡樹脂層のポリエチレンが低密度ポリエチ
レンである特許請求の範囲第1項記載の多層プラ
スチツクフイルム。 3 非発泡樹脂層の熱可塑性樹脂が低密度ポリエ
チレンである特許請求の範囲第1項又は第2項記
載の多層プラスチツクフイルム。 4 発泡剤を添加した熱可塑性樹脂を主成分とす
る発泡樹脂層と発泡剤を添加しない熱可塑性樹脂
を主成分とする非発泡樹脂層とから成る多層プラ
スチツクフイルムの製造方法において、100重量
部のポリエチレンに対して30乃至300重量部のポ
リプロピレン及び0.3乃至10重量部の発泡剤を添
加した発泡樹脂組成物と熱可塑性樹脂を主成分と
する非発泡樹脂組成物とを別々の押出機でそれぞ
れ混練溶融した後、円筒状共押出ダイの内部で発
泡樹脂層と非発泡樹脂層とを溶融接着し、次いで
押出ダイの出口から少くとも内面が発泡樹脂層に
なるように積層チユーブ状に押出し、次いで該チ
ユーブ内外の気圧の差により該チユーブを幅方向
へ膨張させると共に引取方向へ延伸し、更に該チ
ユーブの表面に冷却流体を吹き付けて該チユーブ
を外面から冷却しながら、最終的にブロー比率が
3以上に達するまで該チユーブを膨張させ、同時
に引取比率が2以上に達するまで引取方向へ該チ
ユーブを延伸して後、少くとも一組の引取ロール
の間隙で該チユーブを圧締して発泡樹脂層の微細
な繊維構造に起因する和紙状の風合を形成させる
ことを特徴とする多層プラスチツクフイルムの製
造方法。 5 ポリプロピレンがプロピレン系ランダム共重
合体樹脂である特許請求の範囲第4項記載の多層
プラスチツクフイルムの製造方法。[Scope of Claims] 1. A multilayer plastic film with a thickness of 20 to 200 μ, consisting of at least two layers, a foamed resin layer and a non-foamed resin layer, in which the foamed resin layer has a thickness of 30 to 200 μm to 100 parts by weight of polyethylene. The main component is a resin composition containing 300 parts by weight of polypropylene and 0.3 to 10 parts by weight of a foaming agent, the non-foamed resin layer is made of a resin composition containing a thermoplastic resin as the main component, and the foamed resin layer is the outermost layer. A multilayer plastic film characterized by forming a Japanese paper-like texture due to its fine fiber structure. 2. The multilayer plastic film according to claim 1, wherein the polyethylene of the foamed resin layer is low density polyethylene. 3. The multilayer plastic film according to claim 1 or 2, wherein the thermoplastic resin of the non-foamed resin layer is low density polyethylene. 4. In a method for producing a multilayer plastic film consisting of a foamed resin layer mainly composed of a thermoplastic resin to which a blowing agent has been added and a non-foamed resin layer mainly composed of a thermoplastic resin to which no blowing agent is added, 100 parts by weight of A foamed resin composition prepared by adding 30 to 300 parts by weight of polypropylene and 0.3 to 10 parts by weight of a blowing agent to polyethylene and a non-foamed resin composition whose main component is a thermoplastic resin are kneaded in separate extruders. After melting, the foamed resin layer and the non-foamed resin layer are melted and bonded inside a cylindrical coextrusion die, and then extruded from the exit of the extrusion die into a laminated tube shape so that at least the inner surface becomes the foamed resin layer. The tube is expanded in the width direction and stretched in the take-up direction due to the difference in air pressure inside and outside the tube, and cooling fluid is sprayed onto the surface of the tube to cool the tube from the outside until the blow ratio reaches 3. At the same time, the tube is expanded in the drawing direction until the drawing ratio reaches 2 or more, and then the tube is compressed in the gap between at least one set of drawing rolls to form a foamed resin layer. A method for producing a multilayer plastic film characterized by forming a Japanese paper-like texture due to its fine fiber structure. 5. The method for producing a multilayer plastic film according to claim 4, wherein the polypropylene is a propylene random copolymer resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6636980A JPS56162639A (en) | 1980-05-21 | 1980-05-21 | Multilayer plastic film and its manufacture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6636980A JPS56162639A (en) | 1980-05-21 | 1980-05-21 | Multilayer plastic film and its manufacture |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56162639A JPS56162639A (en) | 1981-12-14 |
JPS6140184B2 true JPS6140184B2 (en) | 1986-09-08 |
Family
ID=13313849
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6636980A Granted JPS56162639A (en) | 1980-05-21 | 1980-05-21 | Multilayer plastic film and its manufacture |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56162639A (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS597839U (en) * | 1982-07-08 | 1984-01-19 | 住友ベークライト株式会社 | packaging |
JPS599960U (en) * | 1982-07-12 | 1984-01-21 | トヨタ自動車株式会社 | Hydraulic pressure control device for vehicle braking system |
JPS6036132A (en) * | 1983-08-09 | 1985-02-25 | Sekisui Plastics Co Ltd | Sheet for formation of shrinkable sleeve |
JPS60132750A (en) * | 1983-12-21 | 1985-07-15 | 積水化成品工業株式会社 | Sheet for forming shrinkable sleeve |
JP4895985B2 (en) * | 2007-12-03 | 2012-03-14 | 新電元工業株式会社 | Variable capacitor |
WO2016084888A1 (en) * | 2014-11-28 | 2016-06-02 | 住友化学株式会社 | Molded article comprising thermoplastic resin composition |
JP5892283B1 (en) * | 2014-11-28 | 2016-03-23 | 住友化学株式会社 | Molded body made of thermoplastic resin composition |
JP7255664B2 (en) * | 2017-12-20 | 2023-04-11 | 日本ポリエチレン株式会社 | Foam appearance performance evaluation method and manufacturing control method for foam laminate |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4724701U (en) * | 1971-04-07 | 1972-11-20 | ||
JPS5145172A (en) * | 1974-09-30 | 1976-04-17 | Bakelite Xylonite Ltd | |
JPS5161389A (en) * | 1974-09-09 | 1976-05-27 | Owens Illinois Inc | |
JPS5236159A (en) * | 1975-09-18 | 1977-03-19 | Sekisui Plastics | Process for producing polyolefin foam |
-
1980
- 1980-05-21 JP JP6636980A patent/JPS56162639A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4724701U (en) * | 1971-04-07 | 1972-11-20 | ||
JPS5161389A (en) * | 1974-09-09 | 1976-05-27 | Owens Illinois Inc | |
JPS5145172A (en) * | 1974-09-30 | 1976-04-17 | Bakelite Xylonite Ltd | |
JPS5236159A (en) * | 1975-09-18 | 1977-03-19 | Sekisui Plastics | Process for producing polyolefin foam |
Also Published As
Publication number | Publication date |
---|---|
JPS56162639A (en) | 1981-12-14 |
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