JPH05193018A - Manufacture of laminate - Google Patents

Manufacture of laminate

Info

Publication number
JPH05193018A
JPH05193018A JP4027486A JP2748692A JPH05193018A JP H05193018 A JPH05193018 A JP H05193018A JP 4027486 A JP4027486 A JP 4027486A JP 2748692 A JP2748692 A JP 2748692A JP H05193018 A JPH05193018 A JP H05193018A
Authority
JP
Japan
Prior art keywords
temperature
laminated
polyolefin resin
laminate
ozone
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
JP4027486A
Other languages
Japanese (ja)
Other versions
JP2905328B2 (en
Inventor
Misao Mukui
美佐夫 椋井
Nobuyuki Ito
信幸 伊藤
Mitsuhiko Kiso
光彦 木曽
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP4027486A priority Critical patent/JP2905328B2/en
Publication of JPH05193018A publication Critical patent/JPH05193018A/en
Application granted granted Critical
Publication of JP2905328B2 publication Critical patent/JP2905328B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To manufacture a laminate having excellent strength simply at a low cost by a method wherein a polyolefin resin is melted and extruded at a specific temperature, treated with ozone under a molten state while being laminated on a laminating base material and matured only for a specific time at a specific temperature. CONSTITUTION:A polyolefin resin is extruded and laminated on a laminating base material, thus manufacturing a laminate. First, the polyolefin resin is melted and extruded at a temperature of 170-290 deg.C and treated with ozone under a molten state at that time. The ozone-treated polyolefin resin is laminated on the laminating base material, and matured for five min or more at a temperature from 50 deg.C to a temperature lower than the melting point in an olefin resin. Ozone treatment is conducted under conditions of 0.2g/hr.cm or more (conversion into ozone spray nozzle width). An oxygen impermeable laminating base material is used, and the polyolefin resin may also be matured for two hr or more. A metallized film or a metal foil is employed as the oxygen impermeable laminating base material.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、積層体の製造方法に関
し、詳しくはラミネート基材にアンカーコーティングな
しで押出ラミネートすることができ、このため工程を簡
略化できるとともに、アンカーコート剤が溶出するおそ
れが全くなく、食品包装用や医薬包装用などとして好適
な積層体を製造しうる方法、及び酸素不透過性のラミネ
ート基材にアンカーコーティングなしで押出ラミネート
することができ、このため工程を簡略化できるととも
に、アンカーコート剤が溶出するおそれが全くなく、ボ
イル,レトルト用として好適な積層フィルムを製造しう
る方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a laminate, and more specifically, it can be extrusion-laminated on a laminate base material without anchor coating, which simplifies the process and elutes the anchor coating agent. There is no danger, and a method that can produce a laminate suitable for food packaging, pharmaceutical packaging, etc., and extrusion lamination without anchor coating to an oxygen impermeable laminated base material, thus simplifying the process The present invention relates to a method for producing a laminated film suitable for boiling and retorting, which has no risk of the anchor coating agent being eluted at all.

【0002】[0002]

【従来技術及び発明が解決しようとする課題】従来よ
り、各々の樹脂の特性を活かしたり、或いは欠点を減殺
するために、さらにはその相乗効果を期待して、種々の
積層体が製造されている。例えば、ガスバリヤー性等に
優れたラミネート用基材と、耐薬品性等に優れ、しかも
低価格でヒートシール性に優れたポリオレフィンとの両
方の特性を活かした積層体が知られている。また、積層
する際に、ポリオレフィンをオゾン処理して接着性を高
める方法も知られている。さらに、このような積層材を
用い、ボイル,レトルト処理(積層材を容器状にして内
容物を入れ、100℃以上で加熱処理をして、内容物の
加熱や殺菌を行なう)後も、接着性及びガスバリヤー性
等の積層材としての機能を保持するような材料も現れて
いる。
2. Description of the Related Art Conventionally, various laminates have been manufactured in order to utilize the characteristics of each resin or to reduce the defects, and further expect the synergistic effect thereof. There is. For example, a laminate is known which utilizes the properties of both a laminating substrate having an excellent gas barrier property and the like, and a polyolefin having an excellent chemical resistance and a low cost and excellent heat sealing property. Further, a method is also known in which a polyolefin is treated with ozone to enhance the adhesiveness when laminated. Furthermore, even after using such a laminated material, boil and retort treatment (bonding the contents of the laminated material into a container, heating the contents at 100 ° C. or more to heat and sterilize the contents), and then bond A material that retains the function as a laminated material such as the properties and gas barrier properties has also appeared.

【0003】具体的には例えば、ポリオレフィンが不活
性であり、接着力が不足するため、ラミネート用基材の
表面にポリウレタン,イソシアネート化合物等により、
アンカーコート処理を施した後、オゾン処理したポリオ
レフィンと積層する方法が提案されている(特開昭61
−283533号公報)。しかしながら、この方法では
アンカーコート処理設備が必要となり、また、アンカー
コート剤が溶出するおそれがあり、衛生上問題となるの
で、用途が限定されているとともに、接着強度が不充分
であるという問題があった。
Specifically, for example, since polyolefin is inactive and the adhesive strength is insufficient, the surface of the laminating substrate is treated with polyurethane, an isocyanate compound or the like.
A method has been proposed in which an anchor coat treatment is performed, and then the resultant is laminated with ozone-treated polyolefin (Japanese Patent Application Laid-Open No. 61-61160).
-283533). However, this method requires an anchor coat treatment facility, and there is a risk that the anchor coat agent may elute, which is a sanitary problem, so that the application is limited and the adhesive strength is insufficient. there were.

【0004】そこでアンカーコート剤を使用せずに、特
定の条件でオゾン処理してラミネート物を製造する方法
が提案されている(特開昭63−49423号公報) 。
しかしながら、この場合には溶融押出温度が高く、積層
体に臭気が出るという問題があり、しかもボイル,レト
ルトに使用できるものではなかった。
Therefore, there has been proposed a method for producing a laminate by subjecting it to ozone treatment under specific conditions without using an anchor coating agent (JP-A-63-49423).
However, in this case, there is a problem that the melt extrusion temperature is high and an odor is generated in the laminate, and it cannot be used for boiling and retorting.

【0005】[0005]

【課題を解決するための手段】本発明者らは、従来のこ
のような問題を解決すべく鋭意研究を進めた結果、比較
的低温で溶融押出したポリオレフィン系樹脂を溶融状態
でオゾン処理し、次いでアンカーコート処理していない
ラミネート用基材(酸素不透過性のラミネート用基材を
含む)にラミネートした後、得られるラミネートフィル
ム(積層体)を適当な温度と時間をかけて熟成(エージ
ング或いはアニーリング)することにより、アンカーコ
ート剤を使用することなく、接着強度やヒートシール強
度、或いはボイル,レトルト処理後の接着強度やヒート
シール強度、並びに酸素不透過性が大幅に改良されるこ
とを見出し、この知見に基づいて本発明を完成するに到
った。
Means for Solving the Problems As a result of intensive research aimed at solving such problems as described above, the present inventors have conducted ozone treatment in a molten state on a polyolefin resin melt-extruded at a relatively low temperature, Then, after laminating on a laminating substrate (including an oxygen-impermeable laminating substrate) that has not been subjected to anchor coating treatment, the resulting laminated film (laminate) is aged (aged or aged) at an appropriate temperature and time. It was found that the bonding strength and heat sealing strength, or the bonding strength and heat sealing strength after boil or retort treatment, and oxygen impermeability are significantly improved by using annealing) without using an anchor coating agent. The present invention has been completed based on this finding.

【0006】すなわち本発明は、ラミネート基材にポリ
オレフィン系樹脂を押出ラミネートして積層体を製造す
るにあたり、前記ポリオレフィン系樹脂を170〜29
0℃の温度で溶融押出した後、溶融状態でオゾン処理
し、次いでラミネート基材にラミネートした後、50℃
以上であり、かつ、前記オレフィン系樹脂の融点以下の
温度で、5分間以上熟成することを特徴とする積層体の
製造方法を提供するものである。
That is, according to the present invention, when the polyolefin resin is extrusion-laminated on the laminated base material to produce a laminate, the polyolefin resin is 170 to 29.
After melt extrusion at a temperature of 0 ° C, ozone treatment in the molten state, then laminating on a laminating substrate, then 50 ° C
It is the above, and provides the manufacturing method of the laminated body characterized by ageing for 5 minutes or more at the temperature below the melting point of the said olefin resin.

【0007】さらに本発明は、酸素不透過性のラミネー
ト基材にポリオレフィン系樹脂を押出ラミネートして積
層フィルムを製造するにあたり、前記ポリオレフィン系
樹脂を170〜260℃の温度で溶融押出した後、溶融
状態でオゾン処理し、次いでラミネート基材にラミネー
トした後、80℃以上であり、かつ、前記オレフィン系
樹脂の融点以下の温度で、2時間以上熟成することを特
徴とするボイル,レトルト用積層フィルムの製造方法を
も提供するものである。
Further, in the present invention, when a polyolefin resin is extrusion-laminated on an oxygen-impermeable laminated base material to produce a laminated film, the polyolefin resin is melt-extruded at a temperature of 170 to 260 ° C. and then melted. Laminated film for boil and retort, characterized by being subjected to ozone treatment in the state, then laminated on a laminating substrate, and then aged for 2 hours or more at a temperature of 80 ° C. or higher and below the melting point of the olefin resin. The present invention also provides a method of manufacturing the same.

【0008】本発明の方法で用いられるラミネート用基
材としては、様々なものがあり、例えば酸化珪素蒸着ポ
リエチレンテレフタレート(PET)フィルム(GTフ
ィルム)等の各種金属蒸着フィルム、アルミ箔等の各種
金属箔、二軸延伸ナイロンフィルム等の各種延伸プラス
チックフィルム或いは未延伸プラスチックフィルム、紙
類、不織布類等が挙げられる。本発明の方法で用いられ
るラミネート用基材としては、これらの中でも特に酸化
珪素蒸着PETフィルム等の各種金属蒸着フィルムやア
ルミ箔等の各種金属箔が好ましい。これらラミネート用
基材の厚みは特に制限はなく、目的等に応じて適宜選定
すればよいが、通常は5〜50μm程度である。これら
のラミネート用基材は、これとラミネートするポリオレ
フィン系樹脂との接着性を向上させるために、必要に応
じてコロナ放電処理や火炎処理等の表面処理を行なって
もよい。但し、本発明の方法においてはアンカーコート
処理は全く行なわない。
There are various types of laminating substrates used in the method of the present invention. For example, various metal vapor deposition films such as silicon oxide vapor deposited polyethylene terephthalate (PET) film (GT film) and various metals such as aluminum foil. Examples include various stretched plastic films such as foils and biaxially stretched nylon films, unstretched plastic films, papers and nonwoven fabrics. Among these, as the laminating substrate used in the method of the present invention, various metal vapor deposition films such as silicon oxide vapor deposition PET film and various metal foils such as aluminum foil are particularly preferable. The thickness of these laminating substrates is not particularly limited and may be appropriately selected depending on the purpose and the like, but is usually about 5 to 50 μm. These laminating substrates may be subjected to surface treatment such as corona discharge treatment or flame treatment, if necessary, in order to improve the adhesiveness with the polyolefin resin to be laminated. However, no anchor coat treatment is performed in the method of the present invention.

【0009】なお、ボイル,レトルト用積層フィルムを
製造する場合には、ラミネート用基材としては、上記ラ
ミネート用基材のなかでも、酸素不透過性のものが用い
られる。具体的には例えば、例えば酸化珪素蒸着PET
フィルム(GTフィルム)等の各種金属蒸着フィルム、
アルミ箔等の各種金属箔、エチレン・ビニルアルコール
樹脂フィルム、ポリ塩化ビニリデンフィルム等の各種延
伸フィルム或いは未延伸フィルムが挙げられる。これら
の中でも特に酸化珪素蒸着PETフィルム等の各種金属
蒸着フィルムやアルミ箔等の各種金属箔が好ましい。
In the case of producing a laminated film for boil and retort, an oxygen-impermeable one of the above-mentioned laminating substrates is used as the laminating substrate. Specifically, for example, silicon oxide vapor deposition PET
Various metal vapor deposition films such as films (GT films),
Examples include various metal foils such as aluminum foil, various stretched films such as ethylene / vinyl alcohol resin film and polyvinylidene chloride film, and unstretched films. Among these, various metal vapor deposition films such as silicon oxide vapor deposition PET film and various metal foils such as aluminum foil are particularly preferable.

【0010】また、本発明の方法で用いられるポリオレ
フィン系樹脂としては、特に制限はなく、例えばポリエ
チレン系樹脂,ポリプロピレン系樹脂等が挙げられ、単
独重合体であってもよいし、共重合体であってもよい。
さらに、これらのブレンド物であってもよい。本発明の
方法で用いられるポリオレフィン系樹脂としては、これ
らの中でも低密度ポリエチレンが好ましく、特にヒート
シール性,耐熱性等に優れることから線状低密度ポリエ
チレン(LLDPE)が好ましい。このポリオレフィン
系樹脂の厚みは特に制限はなく、目的等に応じて適宜選
定すればよいが、通常は10〜200μm程度である。
The polyolefin resin used in the method of the present invention is not particularly limited, and examples thereof include polyethylene resins and polypropylene resins, which may be homopolymers or copolymers. It may be.
Further, it may be a blend of these. Among these, low density polyethylene is preferable as the polyolefin resin used in the method of the present invention, and linear low density polyethylene (LLDPE) is particularly preferable because it has excellent heat-sealing properties and heat resistance. The thickness of the polyolefin resin is not particularly limited and may be appropriately selected depending on the purpose and the like, but is usually about 10 to 200 μm.

【0011】本発明の方法においては、上記の如きポリ
オレフィン系樹脂を170〜290℃の温度で溶融押出
した後、さらに溶融状態でオゾン処理し、次いで前記ラ
ミネート基材に圧着し、ラミネート(押出ラミネート)
する。このように本発明の方法では、押出ラミネーショ
ン法により積層体を製造するが、前記した如く、ラミネ
ート用基材にアンカーコート処理を施すことなく押出ラ
ミネートする。
In the method of the present invention, the above-mentioned polyolefin resin is melt-extruded at a temperature of 170 to 290 ° C., further subjected to ozone treatment in a molten state, then pressure-bonded to the above-mentioned laminated base material, and laminated (extrusion laminate). )
To do. As described above, according to the method of the present invention, a laminate is manufactured by the extrusion lamination method, but as described above, extrusion lamination is performed without subjecting the laminating substrate to the anchor coat treatment.

【0012】本発明の方法においては、ポリオレフィン
系樹脂を170〜290℃の温度、好ましくは230〜
290℃の温度で溶融押出する。ここで溶融押出したポ
リオレフィン系樹脂の温度が290℃を超えると、ポリ
オレフィン系樹脂の分解が生じ、積層体に臭気が出るの
で好ましくない。一方、溶融押出したポリオレフィン系
樹脂の温度が170℃未満であると、積層体の接着強度
が低下するため、好ましくない。
In the method of the present invention, the polyolefin resin is heated to a temperature of 170 to 290 ° C., preferably 230 to 290 ° C.
Melt extrude at a temperature of 290 ° C. If the temperature of the melt-extruded polyolefin-based resin exceeds 290 ° C, the polyolefin-based resin is decomposed and an odor is produced in the laminate, which is not preferable. On the other hand, if the temperature of the melt-extruded polyolefin-based resin is lower than 170 ° C., the adhesive strength of the laminate is lowered, which is not preferable.

【0013】なお、ボイル,レトルト用積層フィルムを
製造する場合には、上記の如きポリオレフィン系樹脂を
170〜260℃の温度で溶融押出した後、さらに溶融
状態でオゾン処理し、次いで前記ラミネート基材に圧着
し、ラミネート(押出ラミネート)する。このようにボ
イル,レトルト用積層フィルムを製造する場合には、ポ
リオレフィン系樹脂を170〜260℃の温度、好まし
くは230〜260℃の温度で溶融押出する。ここで溶
融押出したポリオレフィン系樹脂の温度が260℃を超
えると、積層フィルムに臭気が出たり、酸素バリヤー性
が低下するので好ましくない。一方、溶融押出したポリ
オレフィン系樹脂の温度が170℃未満であると、積層
フィルムの接着強度が低下するため、好ましくない。
In the case of producing a laminated film for boil and retort, the polyolefin resin as described above is melt extruded at a temperature of 170 to 260 ° C., further ozone-treated in a molten state, and then the above-mentioned laminated base material. It is pressure-bonded to and laminated (extrusion lamination). In the case of producing a laminated film for boil and retort, the polyolefin resin is melt extruded at a temperature of 170 to 260 ° C, preferably 230 to 260 ° C. If the temperature of the melt-extruded polyolefin-based resin exceeds 260 ° C., odor is generated in the laminated film and the oxygen barrier property is deteriorated, which is not preferable. On the other hand, when the temperature of the melt-extruded polyolefin resin is lower than 170 ° C., the adhesive strength of the laminated film is lowered, which is not preferable.

【0014】次に、押出されたポリオレフィン系樹脂は
溶融状態でオゾン処理される。すなわち、押出直後のま
だ溶融状態にあるポリオレフィン系樹脂の表面にオゾン
処理を施し、接着力を向上させる。ここでオゾン処理
は、オゾン吹き付けノズル巾換算で、0.2g/hr・
cm以上、好ましくは0.5〜3.0g/hr・cmの
条件で行なわれる。ここでオゾン処理量が0.2g/h
r・cm未満であると、充分な接着力が得られない。オ
ゾン処理量は0.2g/hr・cm以上あれば充分であ
って、例えば3g/hr・cm以上としても、より高い
接着性は得られない。
Next, the extruded polyolefin resin is subjected to ozone treatment in a molten state. That is, the surface of the polyolefin resin which is still in a molten state immediately after extrusion is subjected to ozone treatment to improve the adhesive strength. Here, the ozone treatment is 0.2 g / hr · in terms of ozone spray nozzle width conversion.
cm or more, preferably 0.5 to 3.0 g / hr · cm. Here, the ozone treatment amount is 0.2 g / h
If it is less than r · cm, sufficient adhesive force cannot be obtained. It is sufficient that the ozone treatment amount is 0.2 g / hr · cm or more, and even if it is 3 g / hr · cm or more, higher adhesiveness cannot be obtained.

【0015】本発明の方法においては、上記の如く溶融
押出されたポリオレフィン系樹脂を溶融状態でオゾン処
理した後、前記ラミネート基材に圧着し、ラミネート
(押出ラミネート)する。具体的には、例えば金属ロー
ルとゴムロール間で圧着ラミネートする。ここで金属ロ
ールは、冷却ロールとしての役目を持つものであり、通
常、5〜70℃、好ましくは15〜50℃の温度に保持
されたものを用いる。また、ゴムロールは、シリコンゴ
ムやクロロプレンゴムなどからなるものを用いればよ
い。なお、圧着線圧は、通常、5〜40kg/cmとす
ればよい。
In the method of the present invention, the polyolefin resin melt-extruded as described above is subjected to ozone treatment in a molten state, and then pressure-bonded to the above-mentioned laminated base material to laminate (extrusion lamination). Specifically, for example, pressure bonding lamination is performed between a metal roll and a rubber roll. Here, the metal roll has a role as a cooling roll, and is usually kept at a temperature of 5 to 70 ° C., preferably 15 to 50 ° C. The rubber roll may be made of silicone rubber or chloroprene rubber. The crimping linear pressure may be usually 5 to 40 kg / cm.

【0016】本発明の方法では、上記のように押出ラミ
ネートした後、熟成(エージング或いはアニーリング)
を行なうことが必要である。ここで熟成は、50℃以上
であり、かつ、前記オレフィン系樹脂の融点以下の温度
で、5分間以上、好ましくは60〜100℃の温度で、
30分間〜1日程度行なえばよい。ここで熟成の際の処
理温度が50℃より低いと充分な接着力が得られず、一
方、融点以上では積層体の変形が生ずるため、いずれも
好ましくない。また、処理時間が5分間未満では熟成効
果が充分でなく、接着力が不充分となる。
In the method of the present invention, extrusion lamination as described above is followed by aging (aging or annealing).
It is necessary to do. Here, the aging is performed at a temperature of 50 ° C. or higher and a temperature not higher than the melting point of the olefin resin for 5 minutes or longer, preferably at a temperature of 60 to 100 ° C.
It may be carried out for 30 minutes to 1 day. Here, if the treatment temperature during aging is lower than 50 ° C., sufficient adhesive force cannot be obtained, while if the treatment temperature is higher than the melting point, the laminate is deformed, which is not preferable. Further, if the treatment time is less than 5 minutes, the aging effect is insufficient and the adhesive strength is insufficient.

【0017】また、ボイル,レトルト用積層フィルムを
製造する場合には、熟成は、80℃以上であり、かつ、
前記オレフィン系樹脂の融点以下の温度で、2時間以
上、好ましくは90〜120℃の温度で、3時間〜1日
程度行なえばよい。ここで熟成の際の処理温度が80℃
より低いと、ボイル,レトルト処理後に充分な接着力が
得られず、一方、融点以上では積層フィルムの変形が生
ずるため、いずれも好ましくない。また、処理時間が2
時間未満では熟成効果が充分でなく、ボイル,レトルト
処理後の接着力が不充分となる。
When producing a laminated film for boil and retort, aging is performed at 80 ° C. or higher, and
It may be carried out at a temperature not higher than the melting point of the olefin resin for 2 hours or longer, preferably at 90 to 120 ° C. for 3 hours to 1 day. Here, the processing temperature during aging is 80 ° C.
If it is lower than this, sufficient adhesive force cannot be obtained after boil or retort treatment. On the other hand, if the melting point is higher than the melting point, the laminated film is deformed. Also, the processing time is 2
If it is less than the time, the aging effect is not sufficient, and the adhesive strength after boil or retort treatment is insufficient.

【0018】このようにして目的とする積層体(積層フ
ィルム)を得ることができる。この積層体の厚みは、通
常15〜250μm程度である。
In this way, the desired laminate (laminated film) can be obtained. The thickness of this laminate is usually about 15 to 250 μm.

【0019】[0019]

【実施例】次に本発明を、実施例により詳しく説明す
る。
EXAMPLES Next, the present invention will be described in detail with reference to Examples.

【0020】実施例1〜16および比較例1〜3 ラミネート用基材として、東洋インキ製造(株)製GT
フィルム〔酸化珪素蒸着PETフィルム(PETフィル
ムの片面に、Six y を真空蒸着したフィルム) ,グ
レード:1000R,厚み12μm〕を用いた。一方、ポリ
オレフィン系樹脂として、LLDPE(エチレン・オク
テン−1共重合体、MI=2g/10分、出光石油化学
(株)製、密度は第1表に示す。)を用いた。上記ラミ
ネート用基材と上記ポリオレフィン系樹脂とを、直径5
0mmの押出ラミネーターを用いて、ラミネート用基材
の真空蒸着面を挟むようにして積層して、積層体を得
た。なお、ラミネート速度(フィルム送り速度)は15
m/分であって、得られた積層体の膜厚(ラミネート膜
厚)は100μmであった。この際、押出直後の溶融状
態にあるポリオレフィン系樹脂について、上記ラミネー
ト前に、第1表に示す樹脂温度(但し、この温度は押出
時のポリオレフィン系樹脂の表面温度を示した。)に
て、オゾン処理量がオゾン吹き付けノズル巾換算で、2
g/hr・cmとなる条件でオゾン処理を行なっておい
た。
Examples 1 to 16 and Comparative Examples 1 to 3 As a substrate for laminating, GT manufactured by Toyo Ink Mfg. Co., Ltd.
A film [a silicon oxide-deposited PET film (a film in which Si x O y was vacuum-deposited on one side of the PET film), grade: 1000R, thickness 12 μm] was used. On the other hand, LLDPE (ethylene / octene-1 copolymer, MI = 2 g / 10 minutes, manufactured by Idemitsu Petrochemical Co., Ltd., density is shown in Table 1) was used as the polyolefin resin. A diameter of the laminating substrate and the polyolefin resin is 5
Using a 0 mm extrusion laminator, the base material for lamination was laminated so as to sandwich the vacuum vapor deposition surface to obtain a laminate. The laminating speed (film feed speed) is 15
It was m / min, and the film thickness of the obtained laminate (laminate film thickness) was 100 μm. At this time, regarding the polyolefin resin in a molten state immediately after extrusion, before the above-mentioned lamination, at the resin temperature shown in Table 1 (however, this temperature shows the surface temperature of the polyolefin resin at the time of extrusion). The ozone treatment amount is 2 in terms of the ozone spray nozzle width.
The ozone treatment was performed under the condition of g / hr · cm.

【0021】このようにして得られた積層体(フィル
ム)を、空気中において、第1表に示す条件で熟成し
た。熟成後の積層体の接着強度とヒートシール強度を第
1表に示す。なお、接着強度とヒートシール強度の試験
方法は次の通りである。 接着強度:巾15mm,長さ100mmの試験片を
作成し、この試験片を、長さ方向に50mmにわたって
手で剥離した後、引張試験機で180度方向に300m
m/分の引張速度で剥離したときの強度を測定した。な
お、手で剥離できないときは「剥離不可」とした。 ヒートシール強度: 巾40mm,長さ100mmの
試験片を2枚作成し、この試験片同士を、ポリオレフィ
ン系樹脂同士が接触するようにして、ヒートシールし
て、ヒートシール巾15mmの試験片を作成し、この試
験片を引張試験機で180度方向に300mm/分の引
張速度で剥離したときの強度を測定した。なお、ヒート
シール温度は実施例16が170℃で行なった他は、全
て200℃で行なった。
The laminate (film) thus obtained was aged in air under the conditions shown in Table 1. Table 1 shows the adhesive strength and heat seal strength of the laminate after aging. The test methods for the adhesive strength and heat seal strength are as follows. Adhesive strength: A test piece having a width of 15 mm and a length of 100 mm was prepared, and the test piece was peeled by hand for 50 mm in the length direction, and then 300 m in a 180 degree direction with a tensile tester.
The strength when peeled at a tensile speed of m / min was measured. In addition, when it cannot be peeled by hand, it is defined as “not peelable”. Heat-sealing strength: Two test pieces having a width of 40 mm and a length of 100 mm were prepared, and the test pieces were heat-sealed so that the polyolefin resins were in contact with each other to prepare a test piece having a heat-seal width of 15 mm. Then, the strength when the test piece was peeled in a 180 ° direction at a tensile speed of 300 mm / min was measured by a tensile tester. The heat-sealing temperature was 200 ° C. except for 170 ° C. in Example 16.

【0022】[0022]

【表1】 [Table 1]

【0023】実施例17〜24および比較例4,5 実施例1において、ラミネート用基材として、東洋イン
キ製造(株)製GTフィルムの代わりに、アルミ箔 (サ
ンアルミニウム(株) 製, グレード:1100,厚み20μ
m、ポリオレフィン系樹脂との積層面にコロナ放電処理
を30w/m2 /分(ワット密度)で行なったもの。)
を用いるとともに、樹脂温度を280℃とし、かつ、第
2表に示す条件で行なったこと以外は、実施例1と同様
にして積層体を製造し、熟成後の積層体の接着強度とヒ
ートシール強度を測定した。結果を第2表に示す。
Examples 17 to 24 and Comparative Examples 4 and 5 In Example 1, instead of the GT film manufactured by Toyo Ink Mfg. Co., Ltd. as the base material for laminating, an aluminum foil (manufactured by Sun Aluminum Co., Ltd., grade: 1100, thickness 20μ
m, a layer on which a polyolefin resin was laminated was subjected to corona discharge treatment at 30 w / m 2 / min (watt density). )
Was used, the resin temperature was 280 ° C., and the laminate was produced in the same manner as in Example 1 except that the conditions were as shown in Table 2, and the adhesive strength and heat seal of the laminate after aging were produced. The strength was measured. The results are shown in Table 2.

【0024】[0024]

【表2】 [Table 2]

【0025】実施例25〜34および比較例6〜9 実施例1において、ラミネート用基材として、東洋イン
キ製造(株)製GTフィルムの代わりに、二軸延伸ナイ
ロン(出光石油化学(株)製,グレード: ユニロンG10
0 ,厚み15μm)を用いるとともに、ポリオレフィン
系樹脂としてLLDPE(エチレン・オクテン−1共重
合体、MI=8g/10分、密度0.910g/c
3 、出光石油化学(株)製)を用い、かつ、ラミネー
ト速度(フィルム送り速度)を80m/分とするととも
に、さらに第3表に示す条件で行なったこと以外は、実
施例1と同様にして膜厚30μmの積層体を製造し、熟
成後の積層体の接着強度とヒートシール強度を測定し
た。結果を第3表に示す。
Examples 25 to 34 and Comparative Examples 6 to 9 In Example 1, the biaxially stretched nylon (manufactured by Idemitsu Petrochemical Co., Ltd.) was used as the laminating substrate instead of the GT film manufactured by Toyo Ink Mfg. Co., Ltd. , Grade: Unilon G10
0, thickness 15 μm) and used as a polyolefin resin LLDPE (ethylene / octene-1 copolymer, MI = 8 g / 10 min, density 0.910 g / c)
m 3 manufactured by Idemitsu Petrochemical Co., Ltd., the same as in Example 1 except that the laminating speed (film feed speed) was 80 m / min and the conditions shown in Table 3 were used. Then, a laminate having a film thickness of 30 μm was produced, and the adhesive strength and heat seal strength of the aged laminate were measured. The results are shown in Table 3.

【0026】[0026]

【表3】 [Table 3]

【0027】実施例35〜40および比較例10〜12 ラミネート用基材として、東洋インキ製造(株)製GT
フィルム〔酸化珪素蒸着PETフィルム(PETフィル
ムの片面に、Six y を真空蒸着したフィルム) ,グ
レード:1000R,厚み12μm〕を用いた。一方、ポリ
オレフィン系樹脂としてLLDPE(エチレン・オクテ
ン−1共重合体、MI=2g/10分、出光石油化学
(株)製、密度0.928g/cm3 )を用いた。上記
ラミネート用基材と上記ポリオレフィン系樹脂とを、直
径50mmの押出ラミネーターを用いて、ラミネート用
基材の真空蒸着面を挟むようにして積層して、積層フィ
ルムを得た。なお、ラミネート速度(フィルム送り速
度)は、15m/分であって、得られた積層フィルムの
膜厚(ラミネート膜厚)は100μmであった。この
際、押出直後の溶融状態にあるポリオレフィン系樹脂に
ついて、上記ラミネート前に、第4表に示す樹脂温度
(但し、この温度は押出時のポリオレフィン系樹脂の表
面温度を示した。)にて、オゾン処理量がオゾン吹き付
けノズル巾換算で、2g/hr・cmとなる条件でオゾ
ン処理を行なっておいた。
Examples 35 to 40 and Comparative Examples 10 to 12 As a laminating substrate, GT manufactured by Toyo Ink Mfg. Co., Ltd.
A film [a silicon oxide-deposited PET film (a film in which Si x O y was vacuum-deposited on one side of the PET film), grade: 1000R, thickness 12 μm] was used. On the other hand, LLDPE (ethylene / octene-1 copolymer, MI = 2 g / 10 min, manufactured by Idemitsu Petrochemical Co., Ltd., density 0.928 g / cm 3 ) was used as the polyolefin resin. The laminating substrate and the polyolefin resin were laminated using an extrusion laminator having a diameter of 50 mm so as to sandwich the vacuum vapor deposition surface of the laminating substrate to obtain a laminated film. The laminating speed (film feeding speed) was 15 m / min, and the film thickness (laminating film thickness) of the obtained laminated film was 100 μm. At this time, regarding the polyolefin resin in the molten state immediately after extrusion, before the above-mentioned lamination, at the resin temperature shown in Table 4 (however, this temperature shows the surface temperature of the polyolefin resin at the time of extrusion). The ozone treatment was performed under the condition that the ozone treatment amount was 2 g / hr · cm in terms of ozone spray nozzle width conversion.

【0028】このようにして得られた積層フィルムを、
空気中において、第4表に示す条件で熟成し、さらに下
記のようにしてボイル処理した。なお、ボイル処理は次
のようにして行なった。まず、上記のようにして得られ
た積層フィルム(巾160mm×長さ300mm)の三
方を、LLDPEが内側となるように、各フィルム端か
ら10mmのところから内側に巾10mmにわたってヒ
ートシールした。次いで、この内部に純水を1リットル
充填した後、トップシールを行ない、評価用サンプル
(水充填袋)を作製した。なお、ヒートシールは、1k
g/cm2 (面圧)で1秒間行なった。また、ヒートシ
ール温度は、シール温度とシール強度のデータより、シ
ール強度が強く、かつ、バラツキの小さいシール温度を
選定した(実際には200℃でヒートシールを実施し
た。) この評価用サンプル(水充填袋)を95℃に加熱した熱
水槽中に入れ、115℃の温度まで12分間で昇温し、
当該温度で30分間保持した後、さらに95℃の温度ま
で30分間かけて降温した。このようにして滅菌処理
(ボイル処理)された評価用サンプル(水充填袋)を熱
水槽から取り出し、約20℃の純水中で10分間冷却し
た。
The laminated film thus obtained is
It was aged in the air under the conditions shown in Table 4, and further boiled as described below. The boil treatment was performed as follows. First, three sides of the laminated film (width 160 mm × length 300 mm) obtained as described above were heat-sealed over a width of 10 mm from 10 mm from each film end so that LLDPE was on the inside. Then, 1 liter of pure water was filled in the inside, and then top sealing was performed to prepare an evaluation sample (water-filled bag). The heat seal is 1k
It was performed at g / cm 2 (contact pressure) for 1 second. As the heat seal temperature, a seal temperature having a high seal strength and a small variation was selected from the data of the seal temperature and the seal strength (actually, the heat seal was carried out at 200 ° C.). Water-filled bag) is placed in a hot water bath heated to 95 ° C, and the temperature is raised to 115 ° C in 12 minutes.
After the temperature was maintained for 30 minutes, the temperature was further lowered to 95 ° C over 30 minutes. The evaluation sample (water-filled bag) thus sterilized (boiled) was taken out from the hot water tank and cooled in pure water at about 20 ° C. for 10 minutes.

【0029】上記ボイル処理前及び後の評価用サンプル
(水充填袋)についての接着強度,酸素透過量,ヘイ
ズ,耐融着性,落下破袋強度を第4表に示す。また、第
4表にはボイル処理前(滅菌前)の性能も併せて示し
た。なお、接着強度,ヒートシール強度,酸素透過量,
耐融着性,落下破袋強度の試験方法は次の通りである。 接着強度:上記ボイル処理前及び後の評価用サンプ
ル(水充填袋)から、巾15mm,長さ100mmの試
験片を作成し、この試験片を、長さ方向に50mmにわ
たって手で剥離した後、引張試験機で180度方向に、
300mm/分の引張速度で剥離したときの強度を測定
した。なお、手で剥離できないときは「剥離不可」とし
た。 酸素透過量:ASTM D 1434に従って評価
した。 ヘイズ:上記ボイル処理前及び後の評価用サンプル
(水充填袋)から試験片を作製し、ASTM D 10
03に従って評価した。 耐融着性:評価用サンプル(水充填袋)の耳部(四
方)の融着状態を目視により観察し、次の三段階で評価
した。○:融着なし、△:やや融着(軽く剥離可能)、
×:完全融着(または袋内部融着) 落下破袋強度:上記ボイル処理後の評価用サンプル
(水充填袋)を、23℃で1日保管し、さらに23℃の
室内で2日保管後、落下破袋強度を測定した。落下破袋
強度の測定は、上記ボイル処理後の評価用サンプル(水
充填袋)を水平状態で(袋の胴部が床面と平行状態
で)、2.5mの高さから、コンクリート床面に繰り返
し落下させ、破袋に至るまでの落下回数を確認した。な
お、繰り返し落下回数は、1サンプル20回までとし
た。
Table 4 shows the adhesive strength, oxygen permeation amount, haze, fusion resistance, and drop bag breaking strength of the evaluation sample (water-filled bag) before and after boil treatment. Table 4 also shows the performance before boil treatment (before sterilization). In addition, adhesive strength, heat seal strength, oxygen transmission rate,
The test methods for fusion resistance and drop-breaking bag strength are as follows. Adhesive strength: A test piece having a width of 15 mm and a length of 100 mm was prepared from the evaluation sample (water-filled bag) before and after the boil treatment, and after peeling the test piece by 50 mm in the length direction by hand, 180 degree direction with a tensile tester,
The strength when peeled at a tensile speed of 300 mm / min was measured. In addition, when it cannot be peeled by hand, it is defined as “not peelable”. Oxygen transmission rate: evaluated according to ASTM D 1434. Haze: A test piece was prepared from the evaluation sample (water-filled bag) before and after the boil treatment, and ASTM D 10
It was evaluated according to 03. Fusion resistance: The fusion state of the ears (four sides) of the evaluation sample (water-filled bag) was visually observed and evaluated in the following three stages. ○: No fusion, △: Some fusion (lightly peelable),
×: Complete fusion (or fusion inside the bag) Drop rupture strength: The evaluation sample (water-filled bag) after the boil treatment was stored at 23 ° C for 1 day, and further stored at 23 ° C in the room for 2 days. The strength of the dropped bag was measured. The drop-breaking bag strength was measured by measuring the sample for boil treatment (water-filled bag) in a horizontal state (the body of the bag was parallel to the floor surface), from a height of 2.5 m, to the concrete floor surface. Repeatedly dropped to confirm the number of drops until the bag was broken. Note that the number of repeated drops was 20 times per sample.

【0030】[0030]

【表4】 [Table 4]

【0031】[0031]

【発明の効果】本発明の方法によれば、接着強度,ヒー
トシール強度に優れた積層体を製造することができる。
しかも本発明の方法によれば、ラミネート用基材にアン
カーコーティング処理を施すことが不要であるため、工
程を簡略化することができ、コストダウンを図ることが
できると共に、アンカーコーティング処理剤が溶出する
おそれが全くない。また、酸素不透過性フィルムを用い
る場合には、ボイル,レトルト処理後でも接着強度,ヒ
ートシール強度に優れ、かつ、酸素不透過性にも優れた
積層フィルムを製造することができる。したがって、安
全衛生面での心配がなく、積層体の用途が限定されず、
食品包装用フィルム,医薬品包装用フィルムなどをはじ
めとして、各種用途に有効に用いることができ、特にボ
イル,レトルト用フィルムとして極めて有効に用いるこ
とができる。
According to the method of the present invention, a laminate having excellent adhesive strength and heat seal strength can be manufactured.
Moreover, according to the method of the present invention, since it is not necessary to perform the anchor coating treatment on the laminating substrate, the process can be simplified, the cost can be reduced, and the anchor coating treatment agent can be eluted. There is no danger of When an oxygen impermeable film is used, it is possible to produce a laminated film having excellent adhesive strength and heat seal strength even after boil or retort treatment, and excellent oxygen impermeability. Therefore, there is no concern about safety and health, the use of the laminate is not limited,
It can be effectively used for various purposes including a film for food packaging, a film for pharmaceutical packaging, and the like, and can be particularly effectively used as a film for boiling and retorting.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 // B29K 23:00 B29L 9:00 4F ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location // B29K 23:00 B29L 9:00 4F

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 ラミネート基材にポリオレフィン系樹脂
を押出ラミネートして積層体を製造するにあたり、前記
ポリオレフィン系樹脂を170〜290℃の温度で溶融
押出した後、溶融状態でオゾン処理し、次いでラミネー
ト基材にラミネートした後、50℃以上であり、かつ、
前記オレフィン系樹脂の融点以下の温度で、5分間以上
熟成することを特徴とする積層体の製造方法。
1. When a polyolefin resin is extrusion-laminated on a laminated base material to produce a laminate, the polyolefin resin is melt extruded at a temperature of 170 to 290 ° C., ozone-treated in a molten state, and then laminated. After laminating on a substrate, the temperature is 50 ° C or higher, and
A method for producing a laminate, which comprises aging at a temperature not higher than the melting point of the olefin resin for 5 minutes or more.
【請求項2】 オゾン処理を0.2g/hr・cm以上
(オゾン吹き付けノズル巾換算)の条件で行なう請求項
1記載の方法。
2. The method according to claim 1, wherein the ozone treatment is carried out under the condition of 0.2 g / hr · cm or more (converted into ozone blowing nozzle width).
【請求項3】 酸素不透過性のラミネート基材にポリオ
レフィン系樹脂を押出ラミネートして積層フィルムを製
造するにあたり、前記ポリオレフィン系樹脂を170〜
260℃の温度で溶融押出した後、溶融状態でオゾン処
理し、次いでラミネート基材にラミネートした後、80
℃以上であり、かつ、前記オレフィン系樹脂の融点以下
の温度で、2時間以上熟成することを特徴とするボイ
ル,レトルト用積層フィルムの製造方法。
3. When the polyolefin resin is extrusion-laminated on an oxygen-impermeable laminate base material to produce a laminated film, the polyolefin resin is added in an amount of 170 to
After melt extrusion at a temperature of 260 ° C., ozone treatment in a molten state and then laminating on a laminating substrate,
A method for producing a laminated film for boil / retort, which comprises aging for 2 hours or more at a temperature not lower than 0 ° C. and not higher than the melting point of the olefin resin.
【請求項4】 オゾン処理を0.2g/hr・cm以上
(オゾン吹き付けノズル巾換算)の条件で行なう請求項
3記載の製造方法。
4. The method according to claim 3, wherein the ozone treatment is carried out under the condition of 0.2 g / hr · cm or more (converted into ozone blowing nozzle width).
【請求項5】 酸素不透過性のラミネート基材が、金属
蒸着フィルム又は金属箔である請求項3又は4記載の製
造方法。
5. The production method according to claim 3, wherein the oxygen-impermeable laminate base material is a metal vapor deposition film or a metal foil.
JP4027486A 1992-01-20 1992-01-20 Manufacturing method of laminate Expired - Fee Related JP2905328B2 (en)

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JPH05193018A true JPH05193018A (en) 1993-08-03
JP2905328B2 JP2905328B2 (en) 1999-06-14

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0644032A2 (en) * 1993-09-21 1995-03-22 Sumitomo Chemical Company, Limited Process for producing laminated film and laminated sheet
WO1999062708A1 (en) * 1998-05-29 1999-12-09 Tetra Laval Holdings & Finance S.A. A method of producing a well-integrated packaging laminate, as well as packaging containers produced from the packaging laminate
JP2011020375A (en) * 2009-07-16 2011-02-03 C I Kasei Co Ltd Method of manufacturing low-shrinkable resin film
KR101399387B1 (en) * 2012-08-24 2014-06-27 (주)태방파텍 Medicine packing film manufacture method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0644032A2 (en) * 1993-09-21 1995-03-22 Sumitomo Chemical Company, Limited Process for producing laminated film and laminated sheet
EP0644032A3 (en) * 1993-09-21 1995-04-26 Sumitomo Chemical Co
WO1999062708A1 (en) * 1998-05-29 1999-12-09 Tetra Laval Holdings & Finance S.A. A method of producing a well-integrated packaging laminate, as well as packaging containers produced from the packaging laminate
JP2011020375A (en) * 2009-07-16 2011-02-03 C I Kasei Co Ltd Method of manufacturing low-shrinkable resin film
KR101399387B1 (en) * 2012-08-24 2014-06-27 (주)태방파텍 Medicine packing film manufacture method

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