[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JP3483369B2 - Coextrusion multilayer film for deep drawing - Google Patents

Coextrusion multilayer film for deep drawing

Info

Publication number
JP3483369B2
JP3483369B2 JP28381395A JP28381395A JP3483369B2 JP 3483369 B2 JP3483369 B2 JP 3483369B2 JP 28381395 A JP28381395 A JP 28381395A JP 28381395 A JP28381395 A JP 28381395A JP 3483369 B2 JP3483369 B2 JP 3483369B2
Authority
JP
Japan
Prior art keywords
layer
resin
multilayer film
film
deep drawing
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 - Fee Related
Application number
JP28381395A
Other languages
Japanese (ja)
Other versions
JPH09123376A (en
Inventor
喜明 樋口
孝夫 山田
圭三 谷垣
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.)
Mitsubishi Plastics Inc
Original Assignee
Mitsubishi Plastics Inc
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 Mitsubishi Plastics Inc filed Critical Mitsubishi Plastics Inc
Priority to JP28381395A priority Critical patent/JP3483369B2/en
Publication of JPH09123376A publication Critical patent/JPH09123376A/en
Application granted granted Critical
Publication of JP3483369B2 publication Critical patent/JP3483369B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

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、高度のガスバリア
性や強度を要求される包装用トレー等に好適に使用でき
る深絞り成形用共押出多層フイルムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coextrusion multilayer film for deep drawing, which can be suitably used for packaging trays and the like which are required to have high gas barrier properties and strength.

【0002】[0002]

【従来技術とその課題】従来、深絞り成形法により各種
包装用トレーが成形されており、使用されるフイルム
(以下、比較的肉厚の厚いシートも含む)として各種層
構成の多層フイルムがある。このような多層フイルムに
要求される機能としては加工性、強度、透明性、ガスバ
リア性、保香性、耐熱性、シール性等があり必要に応じ
た層構成からなる多層フイルムが選択される。
2. Description of the Related Art Conventionally, various packaging trays have been formed by a deep-drawing method, and as a film to be used (hereinafter, also including a relatively thick sheet), there is a multi-layered film having various layers. . The functions required for such a multilayer film are processability, strength, transparency, gas barrier properties, aroma retention, heat resistance, sealing properties, etc., and a multilayer film having a layer structure as necessary is selected.

【0003】一般的に多層フイルムを得る方法として
は、各層を各々製膜した後に、接着剤により積層するド
ライラミネート法、又はいずれかの材料を基材にして押
出ラミネート、またはコートする方法、さらに共押出法
がある。
Generally, as a method for obtaining a multilayer film, a dry laminating method in which each layer is formed into a film and then laminated with an adhesive, or a method in which any material is used as a substrate for extrusion laminating or coating, There is a coextrusion method.

【0004】これらの多層フイルムを得る方法におい
て、ドライラミネート法、押出ラミネート法、コート法
においては積層工程の複雑化によって生産性が悪化し、
製造コストがかかるという問題がある。
In the methods for obtaining these multilayer films, in the dry laminating method, extrusion laminating method and coating method, the productivity is deteriorated due to the complicated laminating process,
There is a problem that the manufacturing cost is high.

【0005】共押出法においても、外観が良好でかつ、
各層の厚さが均一であって、さらに深絞り成形性に優れ
た多層フイルムを得るには、共押出法に特有の製造条
件、例えば、共押出温度、口金温度、口金構造、キャス
ト温度、引取速度等の成形条件の最適な組合せに合った
層構成や原料樹脂が限定されるという問題がある。
Also in the coextrusion method, the appearance is good and
In order to obtain a multilayer film in which each layer has a uniform thickness and is excellent in deep drawability, manufacturing conditions specific to the coextrusion method, such as coextrusion temperature, spinneret temperature, spinneret structure, casting temperature, and take-off There is a problem in that the layer structure and the raw material resin that match the optimum combination of molding conditions such as speed are limited.

【0006】その最大の不良要因は、共押出成形法にお
ける樹脂の口金内多層流動の安定性に起因する樹脂界面
における欠陥である。これは共押出成形法の特有の問題
で、特に流動特性が片寄った樹脂構成の多層フイルムで
顕著に現れる。現象的には多層樹脂流動の樹脂間の界面
に不安定現象が発生し、フイルム内面に微細な波状の模
様が発生、程度の激しい場合はフイルム全面に凹凸が発
生して、孔あきとなることもある。このようなフイルム
を深絞り成形等の後加工をすると不良程度がさらに助長
される傾向がある。
[0006] The largest cause of the defects is a defect at the resin interface due to the stability of the multilayer flow of the resin in the die in the coextrusion molding method. This is a problem peculiar to the co-extrusion molding method, and is particularly remarkable in a multi-layer film having a resin composition with uneven flow characteristics. Phenomenon instability occurs at the interface between the resins in the flow of multi-layered resin, and a fine wavy pattern occurs on the inner surface of the film.In severe cases, unevenness occurs on the entire surface of the film, resulting in holes. There is also. When such a film is post-processed such as deep drawing, the degree of defects tends to be further promoted.

【0007】[0007]

【課題を解決するための手段】本発明は、上記問題点を
解消したポリエステル系樹脂層を最外層に設けた深絞り
成形用共押出多層フイルムを見出したものであり、その
要旨とするところは、第1層がポリエステル系樹脂層、
第2層が接着性樹脂層、第3層がエチレン酢酸ビニル共
重合体ケン化物層、第4層が接着性樹脂層、第5層がシ
ール性樹脂層からなる多層フイルムであって、第1層の
ポリエステル系樹脂の極限粘度(IV)が0.65〜
0.85で、かつ第1層の全厚みに対する厚み比率が
0.75〜0.92の範囲であるとともに、第1層以外
の樹脂のメルトインデックス(MI)が5.0〜35.
0であることを特徴とする深絞り成形用共押出多層フイ
ルムにある。
DISCLOSURE OF THE INVENTION The present invention has found a coextrusion multilayer film for deep drawing, in which a polyester resin layer having the above-mentioned problems is provided as the outermost layer, and the gist thereof is , The first layer is a polyester resin layer,
The second layer is an adhesive resin layer, the third layer is a saponified ethylene vinyl acetate copolymer layer, the fourth layer is an adhesive resin layer, and the fifth layer is a sealing resin layer. The intrinsic viscosity (IV) of the polyester resin of the layer is 0.65
0.85, the thickness ratio to the total thickness of the first layer is in the range of 0.75 to 0.92, and the melt index (MI) of the resin other than the first layer is 5.0 to 35.
It is a coextrusion multilayer film for deep drawing, which is characterized by 0.

【0008】本発明多層フイルムの第1層に用いるポリ
エステル系樹脂は剛性、強度、二次加工性を付与するた
めに設けるものであり、具体的な樹脂としては、ポリエ
チレンテレフタレート樹脂(PET)やポリブチレンテ
レフタレート樹脂(PBT)が好適に使用できる。
The polyester resin used in the first layer of the multilayer film of the present invention is provided to impart rigidity, strength and secondary processability. Specific resins include polyethylene terephthalate resin (PET) and poly Butylene terephthalate resin (PBT) can be preferably used.

【0009】上記第1層のポリエステル系樹脂の極限粘
度(IV)は0.65〜0.85、好ましくは0.7〜
0.8の範囲のものを使用する。ここで、極限粘度(I
V)の測定方法は、試料の樹脂300mgを溶媒30m
l(フェノール、1,1,2,2−テトラクロルエタン
重量比1:1)に溶解させウベローゼ型粘度計を用い
て、試料落下時間を測定し、IV値を計算したものであ
る。
The polyester resin of the first layer has an intrinsic viscosity (IV) of 0.65 to 0.85, preferably 0.7 to
Use the one in the range of 0.8. Here, the intrinsic viscosity (I
V) is measured by using 300 mg of resin as a sample and 30 m of solvent as the solvent.
It was dissolved in 1 (phenol, 1,1,2,2-tetrachloroethane weight ratio of 1: 1) and the sample drop time was measured using an Uberose viscometer to calculate the IV value.

【0010】IVが0.65未満では、剛性や強度に対
する改良効果がなく、0.85を越えるものでは、生産
性に劣るという問題がある。また、第1層の全厚みに対
する厚み比率を0.75〜0.92の範囲とする必要が
あり、0.75未満では剛性や強度に対する改良効果が
なく、0.92を越えるものでは、成形性に劣るという
問題がある。
When IV is less than 0.65, there is no effect of improving rigidity and strength, and when IV exceeds 0.85, there is a problem that productivity is poor. Further, the thickness ratio to the total thickness of the first layer needs to be in the range of 0.75 to 0.92. If it is less than 0.75, there is no improvement effect on rigidity and strength, and if it exceeds 0.92, it is molded. There is a problem of poor sex.

【0011】第2層と第4層に用いる接着性樹脂は各層
間の接着力を向上するためであり、使用する接着性樹脂
としては、不飽和カルボン酸またはその誘導体から選ば
れた少なくとも一種のモノマーをグラフトした変性ポリ
オレフィン樹脂が好適に使用でき、各接着性樹脂層の厚
みは5〜20μmの範囲とすればよい。
The adhesive resin used for the second layer and the fourth layer is for improving the adhesive force between the layers, and the adhesive resin used is at least one kind selected from unsaturated carboxylic acids or their derivatives. A modified polyolefin resin grafted with a monomer can be preferably used, and the thickness of each adhesive resin layer may be in the range of 5 to 20 μm.

【0012】第3層に用いるエチレン酢酸ビニル共重合
体ケン化物(以下「EVOH」という)としては、エチ
レン含有率が30〜60モル%で、けん化度が95%以
上のものが、成形性やガスバリアー性の点から好まし
く、層の厚みは5〜50μmの範囲とすればよい。
As the saponified ethylene vinyl acetate copolymer used for the third layer (hereinafter referred to as "EVOH"), those having an ethylene content of 30 to 60 mol% and a saponification degree of 95% or more may be used as moldability and It is preferable in terms of gas barrier properties, and the layer thickness may be in the range of 5 to 50 μm.

【0013】さらに第5層に用いるシール性樹脂として
はアイオノマー樹脂、ポリエチレン、またはエチレンと
他の成分との共重合体、例えばエチレン−酢酸ビニル共
重合体等が使用でき、厚みは20〜150μmの範囲で
好適に使用できる。
Further, as the sealing resin used for the fifth layer, an ionomer resin, polyethylene, or a copolymer of ethylene and other components such as ethylene-vinyl acetate copolymer can be used, and the thickness is 20 to 150 μm. It can be suitably used in the range.

【0014】本発明の多層フイルムでは上記の層構成及
び、各層の厚み構成以外として第1層以外に使用する樹
脂のメルトインデックス(MI)が5.0〜35.0、
好ましくは10.0〜20.0のものを使用する必要が
ある。メルトインデックス(MI)はJISK6760
に準拠して測定した数値であり、MIが5.0未満では
共押出成形後のフイルム内面に微細な波状の模様が発生
し良好な製品とならないという問題があり、35.0を
越えるものでは製膜性に劣るという問題がある。
In the multilayer film of the present invention, the melt index (MI) of the resin used in the layers other than the first layer other than the above layer structure and the thickness structure of each layer is 5.0 to 35.0,
It is necessary to use the thing of 10.0-20.0 preferably. Melt index (MI) is JISK6760
When the MI is less than 5.0, there is a problem that fine wavy patterns are generated on the inner surface of the film after coextrusion and the product is not good, and when it exceeds 35.0. There is a problem of poor film forming property.

【0015】ここで、上記構成の多層フイルムにおいて
は、共押出成形時に製造条件によっては第1層のポリエ
ステル系樹脂層と、第2層の接着性樹脂層の間で流れム
ラや接着不良が発生することがあり、外観不良や層間剥
離の原因となることがあった。そこで、第1層と第2層
の間に非晶質ポリエチレンテレフタレート樹脂層を介在
させることにより、上記問題を解決できる。
Here, in the multi-layer film having the above-mentioned structure, uneven flow or defective adhesion occurs between the first polyester resin layer and the second adhesive resin layer depending on the manufacturing conditions during coextrusion molding. In some cases, this may cause poor appearance and delamination. Therefore, the above problem can be solved by interposing an amorphous polyethylene terephthalate resin layer between the first layer and the second layer.

【0016】具体的な層構成としては、第1層がポリエ
チレンテレフタレート樹脂層、第2層が非晶質ポリエチ
レンテレフタレート樹脂層、第3層が接着性樹脂層、第
4層がエチレン酢酸ビニル共重合体ケン化物層、第5層
が接着性樹脂層、第6層がシール性樹脂層からなる多層
フイルムであり、第2層以外は前述した多層フイルムの
内容と同一である。
As a concrete layer structure, the first layer is a polyethylene terephthalate resin layer, the second layer is an amorphous polyethylene terephthalate resin layer, the third layer is an adhesive resin layer, and the fourth layer is ethylene vinyl acetate copolymer. The multi-layer film is composed of a combined saponified layer, the fifth layer is an adhesive resin layer, and the sixth layer is a sealing resin layer. The contents other than the second layer are the same as those of the above-mentioned multi-layer film.

【0017】第2層に使用する非晶質ポリエチレンテレ
フタレート樹脂としては、アルコール成分が1,4シク
ロヘキサンジメチルアルコール、エチレングリコールか
らなり、酸成分がテレフタル酸からなるポリエチレンテ
レフタレート樹脂が好適に使用できる。厚み範囲は10
μm〜100μmが好適で10μm未満では流れムラ改
良効果がなく、100μm越えるとフイルムの剛性が強
すぎる傾向があり好ましくない。
As the amorphous polyethylene terephthalate resin used for the second layer, a polyethylene terephthalate resin having an alcohol component of 1,4 cyclohexanedimethyl alcohol and ethylene glycol and an acid component of terephthalic acid can be preferably used. Thickness range is 10
If the thickness is less than 10 μm, there is no flow unevenness improving effect, and if it exceeds 100 μm, the rigidity of the film tends to be too strong, which is not preferable.

【0018】また、上記の非晶質ポリエチレンテレフタ
レート樹脂層を有する多層フイルムでは第1層と第2層
のポリエステル系樹脂のIVが0.65〜0.85,好
ましくは0.7〜0.8の範囲のものを使用する。IV
が0.65未満では、剛性や強度に対する改良効果がな
く、0.85を越えるものでは、生産性に劣るという問
題がある。また、第1層と第2層の合計厚みに対する厚
み比率を0.75〜0.92の範囲とする必要があり、
0.75未満では剛性や強度に対する改良効果がなく、
0.92を越えるものでは、成形性に劣るという問題が
ある。
In the multilayer film having the above-mentioned amorphous polyethylene terephthalate resin layer, IV of the polyester resin of the first layer and the second layer is 0.65 to 0.85, preferably 0.7 to 0.8. Use the one in the range. IV
If less than 0.65, there is no improvement effect on rigidity and strength, and if more than 0.85, there is a problem that productivity is poor. Further, the thickness ratio with respect to the total thickness of the first layer and the second layer needs to be in the range of 0.75 to 0.92,
If it is less than 0.75, there is no improvement effect on rigidity and strength,
If it exceeds 0.92, there is a problem that the moldability is poor.

【0019】さらに第1層と第2層以外の樹脂のMIが
5.0〜35.0、好ましくは10.0〜20.0のも
のを使用する必要がある。MIが5.0未満では共押出
成形後のフイルム内面に微細な波状の模様が発生し良好
な製品とならないという問題がある。MIが35.0を
越えるものでは、製膜性に劣るという問題がある。
Further, it is necessary to use a resin other than the first layer and the second layer having MI of 5.0 to 35.0, preferably 10.0 to 20.0. If the MI is less than 5.0, there is a problem in that a fine wavy pattern is generated on the inner surface of the film after coextrusion and a good product cannot be obtained. If the MI exceeds 35.0, there is a problem that the film forming property is poor.

【0020】[0020]

【発明の実施の形態】以下、本発明を実施例にて説明す
る。 実施例1 層構成: 最外層(第1層):ポリエチレンテレフタレート樹脂
(PET)、第2層:カルボン酸変性直鎖低密度ポリエ
チレン(AD)、第3層:エチレン酢酸ビニル共重合体
ケン化物(EVOH)、第4層:カルボン酸変性エチレ
ン−酢酸ビニル共重合体(AD)、第5層:直鎖低密度
ポリエチレン(LLDPE)を配した構成 。 PET/ AD / EVOH / AD /LLDPE IV=0.8/ MI=15 / MI=6.4 / MI=15 / MI=12 295 μm/10μm/ 12μm / 5μm/ 33μm PET樹脂層の全体厚みに対する比率=0.83 上記構成の多層フイルムを共押出し成形法により製膜し
た。ついでこの多層フイルムを用いて、ムルチバック
(株)製の深絞り成形機(Rー7000)により深絞り
成形を実施したところ、成形性が良好で、得られた成形
品の強度や外観等問題なかった。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described below with reference to Examples. Example 1 Layer structure: Outermost layer (first layer): polyethylene terephthalate resin (PET), second layer: carboxylic acid-modified linear low-density polyethylene (AD), third layer: saponified ethylene vinyl acetate copolymer ( EVOH), the fourth layer: a carboxylic acid-modified ethylene-vinyl acetate copolymer (AD), and the fifth layer: a linear low-density polyethylene (LLDPE). PET / AD / EVOH / AD / LLDPE IV = 0.8 / MI = 15 / MI = 6.4 / MI = 15 / MI = 12 295 μm / 10 μm / 12 μm / 5 μm / 33 μm Ratio of the PET resin layer to the total thickness = 0.83 The multilayer film having the above structure was formed into a film by a coextrusion molding method. Then, using this multi-layer film, deep drawing was carried out with a deep drawing machine (R-7000) manufactured by Multibag Co., Ltd., and it was found that the moldability was good, and the strength and appearance of the resulting molded product were not a problem. There wasn't.

【0021】実施例2 層構成: 最外層(第1層):ポリエチレンテレフタレート樹脂
(PET)、第2層:非晶質ポリエチレンテレフタレー
ト樹脂(PETG)、第3層:カルボン酸変性垂直鎖低
密度ポリエチレン(AD)、第4層:エチレン酢酸ビニ
ル共重合体ケン化物(EVOH)、第5層:カルボン酸
変性エチレン−酢酸ビニル共重合体(AD)、第6層:
直鎖低密度ポリエチレン(LDPE)を配した構成。
Example 2 Layer Structure: Outermost layer (first layer): polyethylene terephthalate resin (PET), second layer: amorphous polyethylene terephthalate resin (PETG), third layer: carboxylic acid modified vertical chain low density polyethylene (AD), 4th layer: saponified ethylene vinyl acetate copolymer (EVOH), 5th layer: carboxylic acid-modified ethylene-vinyl acetate copolymer (AD), 6th layer:
A structure in which linear low density polyethylene (LDPE) is arranged.

【0022】 PET / PETG/ AD / EVOH / AD /LLDPE IV=0.755/ IV=0.75 / MI=15 / MI=5.5 / MI=15 / MI=23 255 μm/ 43μm/ 15μm / 14μm/ 5μm / 32μm PET+PETG層の全体厚みに対する比率=0.82 上記構成の多層フイルムを共押出し成形法により製膜し
た。ついでこの多層フイルムを用いて、ムルチバック
(株)製の深絞り成形機(Rー7000)により深絞り
成形を実施したところ、成形性が良好で、得られた成形
品の強度や表面のムラ等外観上問題なかった。
PET / PETG / AD / EVOH / AD / LLDPE IV = 0.755 / IV = 0.75 / MI = 15 / MI = 5.5 / MI = 15 / MI = 23 255 μm / 43 μm / 15 μm / 14 μm / 5 μm / 32 μm PET + PETG Ratio of layer to total thickness = 0.82 The multilayer film having the above structure was formed into a film by a coextrusion molding method. Then, using this multi-layer film, deep drawing was carried out by a deep drawing machine (R-7000) manufactured by Multibag Co., Ltd., and the moldability was good, and the strength and surface unevenness of the obtained molded product were excellent. There was no problem in appearance.

【0023】比較例1 構成が下記内容の多層フイルムを得、実施例1と同様に
評価した。
Comparative Example 1 A multilayer film having the following constitution was obtained and evaluated in the same manner as in Example 1.

【0024】 PET / AD /EVOH / AD /LLDPE IV=0.63 / MI=3.4 / MI=2.5/ MI=3.4 / MI=3.5 281 μm/ 13μm / 19μm / 13μm/ 65μm PET層の全体厚みに対する比率=0.72 上記構成の多層フイルムを共押出し成形法により製膜し
た。得られたフイルムに流れムラが見られた。ついでこ
の多層フイルムを用いて、実施例1と同様に深絞り成形
を実施したところ、得られた成形品の透明度、および強
度が悪く実用上問題があった。
PET / AD / EVOH / AD / LLDPE IV = 0.63 / MI = 3.4 / MI = 2.5 / MI = 3.4 / MI = 3.5 281 μm / 13 μm / 19 μm / 13 μm / 65 μm Ratio of PET layer to total thickness = 0 .72 The multilayer film having the above structure was formed into a film by a coextrusion molding method. Flow unevenness was found in the obtained film. Then, using this multilayer film, deep drawing was carried out in the same manner as in Example 1, and the transparency and strength of the obtained molded product were poor and there was a practical problem.

【0025】比較例2 構成が下記内容の多層フイルムを得、実施例1と同様に
評価した。
Comparative Example 2 A multilayer film having the following constitution was obtained and evaluated in the same manner as in Example 1.

【0026】 PET / AD / EVOH / AD /LLDPE IV=0.8 / MI=3.4 / MI=2.5 / MI=1.5 / MI=7.0 280 μm/ 5μm / 15μm / 10μm/ 60μm PET層の全体厚みに対する比率=0.76 上記構成の多層フイルムを共押出し成形法により製膜し
た。得られたフイルムの外観は良好であった。ついでこ
の多層フイルムを用いて、実施例1と同様に深絞り成形
を実施したところ、得られた成形品に微細な波状の模様
が見られ実用上問題があった。
PET / AD / EVOH / AD / LLDPE IV = 0.8 / MI = 3.4 / MI = 2.5 / MI = 1.5 / MI = 7.0 280 μm / 5 μm / 15 μm / 10 μm / 60 μm Ratio of PET layer to total thickness = 0 .76 The multilayer film having the above structure was formed into a film by a coextrusion molding method. The appearance of the obtained film was good. Then, using this multilayer film, deep drawing was carried out in the same manner as in Example 1. As a result, a fine wavy pattern was found on the obtained molded product, which was a problem in practical use.

【0027】[0027]

【発明の効果】上述したように本発明の共押出多層フイ
ルムは、高度のガスバリア性や強度を有しており、深絞
り成形による各種包装用トレー等に好適に使用できる。
As described above, the coextruded multilayer film of the present invention has a high gas barrier property and strength, and can be suitably used for various packaging trays by deep drawing.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平7−96582(JP,A) 特開 昭63−270140(JP,A) 特開 平7−108655(JP,A) 特開 平6−226930(JP,A) 実開 昭56−163533(JP,U) (58)調査した分野(Int.Cl.7,DB名) B32B 1/00 - 35/00 ─────────────────────────────────────────────────── --- Continuation of the front page (56) Reference JP-A-7-96582 (JP, A) JP-A-63-270140 (JP, A) JP-A-7-108655 (JP, A) JP-A-6- 226930 (JP, A) Actual development Sho 56-163533 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) B32B 1/00-35/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 第1層がポリエステル系樹脂層、第2層
が接着性樹脂層、第3層がエチレン酢酸ビニル共重合体
ケン化物層、第4層が接着性樹脂層、第5層がシール性
樹脂層からなる多層フイルムであって、第1層のポリエ
ステル系樹脂の極限粘度(IV)が0.65〜0.85
で、かつ第1層の全厚みに対する厚み比率が0.75〜
0.92の範囲であるとともに、第1層以外の樹脂のメ
ルトインデックス(MI)が5.0〜35.0であるこ
とを特徴とする深絞り成形用共押出多層フイルム。
1. A first layer is a polyester resin layer, a second layer is an adhesive resin layer, a third layer is a saponified ethylene vinyl acetate copolymer layer, a fourth layer is an adhesive resin layer, and a fifth layer is A multilayer film having a sealing resin layer, wherein the polyester resin of the first layer has an intrinsic viscosity (IV) of 0.65 to 0.85.
And the thickness ratio to the total thickness of the first layer is 0.75
A coextrusion multilayer film for deep drawing, wherein the melt index (MI) of the resin other than the first layer is in the range of 0.92 and is 5.0 to 35.0.
【請求項2】 第1層がポリエチレンテレフタレート樹
脂層、第2層が非晶質ポリエチレンテレフタレート樹脂
層、第3層が接着性樹脂層、第4層がエチレン酢酸ビニ
ル共重合体ケン化物層、第5層が接着性樹脂層、第6層
がシール性樹脂層からなる多層フイルムであって、第1
層と第2層のポリエステル系樹脂の極限粘度(IV)が
0.65〜0.85で、かつ第1層と第2層の合計厚み
の全厚みに対する比率が0.75〜0.92の範囲であ
るとともに、第1層と第2層以外の樹脂のメルトインデ
ックス(MI)が5.0〜35.0であることを特徴と
する深絞り成形用共押出多層フイルム。
2. A first layer is a polyethylene terephthalate resin layer, a second layer is an amorphous polyethylene terephthalate resin layer, a third layer is an adhesive resin layer, a fourth layer is a saponified ethylene vinyl acetate copolymer layer, and A multi-layer film comprising five layers of an adhesive resin layer and a sixth layer of a sealing resin layer,
The intrinsic viscosity (IV) of the polyester resin of the first layer and the second layer is 0.65 to 0.85, and the ratio of the total thickness of the first layer and the second layer to the total thickness is 0.75 to 0.92. A coextrusion multilayer film for deep drawing, characterized in that the melt index (MI) of the resin other than the first layer and the second layer is in the range of 5.0 to 35.0.
JP28381395A 1995-10-31 1995-10-31 Coextrusion multilayer film for deep drawing Expired - Fee Related JP3483369B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28381395A JP3483369B2 (en) 1995-10-31 1995-10-31 Coextrusion multilayer film for deep drawing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28381395A JP3483369B2 (en) 1995-10-31 1995-10-31 Coextrusion multilayer film for deep drawing

Publications (2)

Publication Number Publication Date
JPH09123376A JPH09123376A (en) 1997-05-13
JP3483369B2 true JP3483369B2 (en) 2004-01-06

Family

ID=17670487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28381395A Expired - Fee Related JP3483369B2 (en) 1995-10-31 1995-10-31 Coextrusion multilayer film for deep drawing

Country Status (1)

Country Link
JP (1) JP3483369B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4495912B2 (en) * 2003-01-14 2010-07-07 三菱樹脂株式会社 Multilayer film and container

Also Published As

Publication number Publication date
JPH09123376A (en) 1997-05-13

Similar Documents

Publication Publication Date Title
CA2439578C (en) Packaging films containing coextruded polyester and nylon layers
JP2915324B2 (en) Saponified ethylene-vinyl acetate copolymer resin composition and multilayer structure using the same
US6322899B1 (en) Plastic laminate
WO2008050486A1 (en) Laminated paper packaging material and method of producing the same
JPH03138145A (en) Elongated laminated film
EP0393991A2 (en) Laminated film or sheet and box-shaped vessel prepared therefrom
KR20060048529A (en) Extrusion-coatable polyester film comprising poly(m-xyleneadipamide)
JP3782164B2 (en) Coextruded composite film for deep drawing
JP3483369B2 (en) Coextrusion multilayer film for deep drawing
DE69030179T2 (en) METHOD FOR PRODUCING A LAMINATE
AU2059599A (en) Film for wrapping objects
JP2011152733A (en) Laminate film and molding sheet using the same
JP4059966B2 (en) White film for metal lamination
EP0838331A2 (en) White film to be laminated to metal surface and method of producing same
JP3555911B2 (en) Multi-layer structure
JP3583833B2 (en) Co-extrusion multilayer film for deep drawing
JP3846974B2 (en) Multilayer structure
JPH06328541A (en) Manufacture of multilayer structure
EP0390113B1 (en) Multilayered structure
JPS62113526A (en) Manufacture of multi-layer molded product and multi-layer orientated film
JP3222431B2 (en) Multilayer polyester sheet
JPH11348200A (en) Production of multilayered container
JP3010757B2 (en) Laminate
JPH0813505B2 (en) Method for producing laminated stretched film
JPH0573572B2 (en)

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081017

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20091017

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20091017

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20101017

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20101017

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20111017

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20121017

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20131017

Year of fee payment: 10

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

LAPS Cancellation because of no payment of annual fees