JPH0486259A - Film for packaging - Google Patents
Film for packagingInfo
- Publication number
- JPH0486259A JPH0486259A JP2202824A JP20282490A JPH0486259A JP H0486259 A JPH0486259 A JP H0486259A JP 2202824 A JP2202824 A JP 2202824A JP 20282490 A JP20282490 A JP 20282490A JP H0486259 A JPH0486259 A JP H0486259A
- Authority
- JP
- Japan
- Prior art keywords
- film
- thickness
- resin
- layer
- packaging
- 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
Links
- 238000004806 packaging method and process Methods 0.000 title abstract description 8
- 239000010410 layer Substances 0.000 claims abstract description 46
- 229920005989 resin Polymers 0.000 claims abstract description 33
- 239000011347 resin Substances 0.000 claims abstract description 33
- -1 polypropylene Polymers 0.000 claims abstract description 26
- 229920001155 polypropylene Polymers 0.000 claims abstract description 26
- 239000004743 Polypropylene Substances 0.000 claims abstract description 25
- 239000004953 Aliphatic polyamide Substances 0.000 claims abstract description 12
- 229920003231 aliphatic polyamide Polymers 0.000 claims abstract description 12
- 239000002344 surface layer Substances 0.000 claims abstract description 6
- 238000000465 moulding Methods 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 15
- 229920006280 packaging film Polymers 0.000 claims description 13
- 239000012785 packaging film Substances 0.000 claims description 13
- 229920002292 Nylon 6 Polymers 0.000 abstract description 10
- 230000004888 barrier function Effects 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 229920001577 copolymer Polymers 0.000 abstract description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 abstract description 3
- 238000001125 extrusion Methods 0.000 abstract 2
- 239000004952 Polyamide Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 229920002647 polyamide Polymers 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 abstract 1
- 235000013305 food Nutrition 0.000 description 8
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000009998 heat setting Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 239000005033 polyvinylidene chloride Substances 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229920000305 Nylon 6,10 Polymers 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 229920006122 polyamide resin Polymers 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 229920001384 propylene homopolymer Polymers 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 229920005604 random copolymer Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 229920006015 heat resistant resin Polymers 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Laminated Bodies (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は食品包装用等に用いられる包装用フィルムに関
する。詳しくは、本発明はカット性、透明性、耐熱性、
水藤気バリア性、非熱収縮性及び食品安全性に優れた包
装用フィルムに好適な延伸積層フィルムに関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a packaging film used for food packaging and the like. Specifically, the present invention has excellent cutability, transparency, heat resistance,
The present invention relates to a stretched laminated film suitable for use as a packaging film having excellent water-to-air barrier properties, non-heat shrinkability, and food safety.
従来、食品包装用に用いられるラップ用フィルムとして
は、ポリ塩化ビニリデン、ポリエチレン、或いはポリ塩
化ビニルを主原料とするものが知られている。BACKGROUND ART Conventionally, wrap films used for food packaging are known that are mainly made of polyvinylidene chloride, polyethylene, or polyvinyl chloride.
しかしながら、ポリ塩化ビニリデン系のフィルムは、加
熱時の収縮が大きいという不都合があり、ポリエチレン
系のフィルムは油動(例えば、食肉やてんぷら等)に接
触しかつ高熱となった場合は、フィルムが溶融してしま
うという欠点があり、さらにポリ塩化ビニル系のフィル
ムは、沸騰熱湯に接触すると白化現象を起すという問題
がある。However, polyvinylidene chloride-based films have the disadvantage of large shrinkage when heated, and polyethylene-based films may melt if they come into contact with oily objects (e.g., meat, tempura, etc.) and are exposed to high heat. Furthermore, polyvinyl chloride films have the problem of whitening when they come into contact with boiling water.
他方、包装用フィルムとして耐熱性を有する樹脂として
は脂肪族ポリアミド樹脂が知られている。On the other hand, aliphatic polyamide resins are known as heat-resistant resins that can be used as packaging films.
脂肪族ポリアミド樹脂は、優れた耐熱性及び機械的強度
を具備しているが、吸湿性が高いため、本来の物性を保
つことが難しい。特にナイロン−〇およびナイロン−6
/6,6、ナイロン−6/6゜10等の共重合ナイロン
は、そのモノマー成分であるε−カプロラクタムがフィ
ルム表面ヘブリードするため、食品安全性の面より食品
包装用の用途への使用が制限されている。Although aliphatic polyamide resin has excellent heat resistance and mechanical strength, it is difficult to maintain its original physical properties because of its high hygroscopicity. Especially nylon-〇 and nylon-6
Copolymerized nylons such as /6,6 and nylon-6/6゜10 are restricted from being used in food packaging applications due to food safety concerns, as their monomer component ε-caprolactam bleeds onto the film surface. has been done.
また、かかるラップ用フィルムは、カット性(切断のし
易さ)において次のような問題点がある。即ち、ラップ
用フィルムは通常、紙管などのケースに収納してあり、
このケースに取付けられた「のこ刃」と呼ばれる切断刃
に当ててフィルムを引き取って適宜の長さに切断するも
のである。Furthermore, such wrapping films have the following problems in terms of cuttability (ease of cutting). In other words, wrapping film is usually stored in a case such as a paper tube.
The film is pulled out by applying it to a cutting blade called a ``saw blade'' attached to this case and cut into an appropriate length.
フィルムの切断に利用される「のこ刃」としては、一般
に0.2 mm厚程度の鉄板をのこぎり型に打ち抜いた
だけの簡単な刃が使用されており、また、この「のこ刃
」を支えるケースについても、350〜700 g/ポ
程度のコートボール紙製の紙箱が使われており、剛性は
極く低い。The ``saw blade'' used to cut the film is generally a simple blade made by punching a saw-shaped iron plate approximately 0.2 mm thick. As for the supporting case, a paper box made of coated cardboard with a weight of about 350 to 700 g/po is used, and its rigidity is extremely low.
この種のフィルムは、このような簡単な切断機構によっ
ても、使用者の意志に従って容易に切断されることが要
請されるのであるが、実際は、ケースや「のこ刃」が変
形したりするばかりでなく、フィルムが変形したり、「
のこ刃」から外れた位置で切断が起こったりする場合が
ある。具体的に述べると、従来のポリ塩化ビニリデン系
のフィルムは、切断の際、フィルムの一部に裂は目がで
きると、この避は目が広がって、「のこ刃」に沿って切
断されることなく斜めに切れてしまう傾向がある。また
従来のポリエチレン系のフィルムは、切断時にかなりの
引張力を要し、ケースが曲折したりするばかりでなく、
フィルムが変形したりすることがある。This type of film is required to be easily cut according to the user's will even with such a simple cutting mechanism, but in reality, the case and the "saw blade" are often deformed. Otherwise, the film may be deformed or
Cutting may occur at a position that is outside the saw blade. Specifically, when conventional polyvinylidene chloride film is cut, if a tear forms in a part of the film, the tear spreads and the film is cut along the "saw blade". There is a tendency to cut diagonally without cutting. In addition, conventional polyethylene films require considerable tensile force when cut, which not only causes the case to bend, but also
The film may become deformed.
本発明者は従来のラップ用フィルムの上記問題点の解決
された包装用フィルムを製造すべく鋭意検討を重ねた結
果、脂肪族ポリアミド樹脂の両側にポリプロピレン系樹
脂を特定の共押出法で積層したものを、フィルムの引取
方向に延伸することにより、上記問題点が解消され、か
つポリアミド樹脂本来の特性(耐熱性及び機械的強度)
を損うことなく、カッl−性、透明性、耐熱性、水蒸気
遮断性、非熱収縮性および食品安全性に優れた包装用フ
ィルムが得られることを見出して本発明に到達した。As a result of extensive research in order to produce a packaging film that solves the above-mentioned problems of conventional wrapping films, the inventors of the present invention have laminated polypropylene resin on both sides of an aliphatic polyamide resin using a specific coextrusion method. By stretching the material in the direction in which the film is taken, the above problems are resolved and the inherent properties of polyamide resin (heat resistance and mechanical strength) are improved.
The present invention was achieved by discovering that it is possible to obtain a packaging film that has excellent heat resistance, water vapor barrier properties, non-heat shrinkability, and food safety without impairing the properties of the packaging material.
即ち本発明の要旨は、それぞれポリプロピレン系樹脂か
らなる外層及び内層が両表面層を構成し、該両表面層の
間に脂肪族ポリアミド樹脂からなる中間層を有する多層
フィルムであって、上記各樹脂をTダイ成形法又は水冷
式インフレーション成形法により共押出成形した後、フ
ィルムの引取方向に延伸倍率2ないし4.5倍で延伸し
て得られたものであり、フィルム全体の厚みが40μm
以下であり、かつ、上記中間層の厚みがフィルム全体の
厚みの10〜90%の範囲であることを特徴とする包装
用フィルム、に存する。That is, the gist of the present invention is a multilayer film having an outer layer and an inner layer each made of a polypropylene resin, each of which constitutes both surface layers, and an intermediate layer made of an aliphatic polyamide resin between the two surface layers. It is obtained by coextrusion molding by T-die molding method or water-cooled inflation molding method, and then stretching at a stretching ratio of 2 to 4.5 times in the drawing direction of the film, and the total thickness of the film is 40 μm.
or less, and the thickness of the intermediate layer is in the range of 10 to 90% of the thickness of the entire film.
以下、本発明につき詳細に説明する。Hereinafter, the present invention will be explained in detail.
本発明の包装用フィルムは両表面層の外層及び内層並び
にその間の中間層を含む少なくとも3層以上の層構成を
有し、例えば外層/中間層/内層の3′層からなってい
る。The packaging film of the present invention has a layer structure of at least three layers including both outer and inner layers and an intermediate layer therebetween, for example, a 3' layer consisting of outer layer/intermediate layer/inner layer.
該包装用フィルムの外層及び内層を構成するポリプロピ
レン系樹脂の種類は特に制限はなく、プロピレン単独重
合体はもちろんエチレン等とプロピレンとの共重合体で
あってもよい。プロピレン単独重合体としては、アイソ
タクチックポリプロピレン、シンジオククチックポリプ
ロピレン、アククチツクポリプロピレンをあげることが
できるが、アイソタクチックポリプロピレンが特に好ま
しい。さらにプロピレンとエチレン等他成分との共重合
体はランダム共重合体、ブロック共重合体のいずれであ
ってもよい。なお、このポリプロピレン系樹脂の物性は
、各種用途、条件等に応じて選定すればよいが、通常、
メルトフローレート(MFR)0.5〜10 g/l
0分、密度0.89〜0、91 g /crR1のもの
が好適である。メルトフローレートはJIS K67
58に準拠し、230°C12、16kg荷重で測定し
たものである。The type of polypropylene resin constituting the outer layer and inner layer of the packaging film is not particularly limited, and may be a propylene homopolymer or a copolymer of ethylene or the like and propylene. Examples of the propylene homopolymer include isotactic polypropylene, syndioctic polypropylene, and acidic polypropylene, and isotactic polypropylene is particularly preferred. Furthermore, the copolymer of propylene and other components such as ethylene may be either a random copolymer or a block copolymer. Note that the physical properties of this polypropylene resin may be selected depending on various uses, conditions, etc., but usually,
Melt flow rate (MFR) 0.5-10 g/l
0 minutes and a density of 0.89 to 0.91 g/crR1 are preferred. Melt flow rate is JIS K67
58, measured at 230°C and 16kg load.
一方、本発明の包装用フィルムの中間層を構成する脂肪
族ポリアミドとしては、ナイロン−6、ナイロン−6,
6、ナイロン−6,10およびナイロン−6/6.6共
重合体、ナイロン−6/610共重合体等を例示するこ
とができる。On the other hand, examples of the aliphatic polyamide constituting the intermediate layer of the packaging film of the present invention include nylon-6, nylon-6,
6, nylon-6,10, nylon-6/6.6 copolymer, nylon-6/610 copolymer, and the like.
本発明の包装用フィルムは一上記ポリプロピレン系樹脂
と脂肪族ポリアミド樹脂とを特定の共押出成形によって
2種3層の層構成、例えば〔ポリプロピレン系樹脂/脂
肪族ポリアミド樹脂/ポリプロピレン系樹脂〕の多層フ
ィルムを成形し、次いで該フィルムをその引取方向(縦
方向)に−軸延伸することにより、成形される。The packaging film of the present invention has a two-layer, three-layer structure, for example, a multilayer structure of [polypropylene resin/aliphatic polyamide resin/polypropylene resin] by coextrusion molding of the above-mentioned polypropylene resin and aliphatic polyamide resin in a specific manner. The film is formed by forming the film and then axially stretching the film in the drawing direction (longitudinal direction).
該共押出成形としてば、Tダイ成形法又は、水冷式イン
フレーション成形法が採用される。すなわち、熔融押出
しされた樹脂を」二記成形法により急冷することにより
、通常よく用いられる空冷式インフレーション成形法と
比較してより透明性に優れたフィルムが得られる。As the coextrusion molding, a T-die molding method or a water-cooled inflation molding method is adopted. That is, by rapidly cooling the melt-extruded resin using the second molding method, a film with better transparency can be obtained compared to the commonly used air-cooled inflation molding method.
上記共押出成形により得られた未延伸多層フィルムは、
次いでフィルムの引取方向(縦方向)に延伸倍率2〜4
.5倍、好ましくは2.5〜4侑に−・軸延伸する。該
延伸倍率が2倍未満ではフィルムのカッl−性が不十分
であり、また4、5倍より大きいと延伸性が低下し、破
断もしくはフィルムに延伸むらができるので望ましくな
い。該延伸処理は上記未延伸フィルムをそのまま或は所
定の幅にスリットしたものを加熱し、例えば延伸ロール
の周速度を変化させることによりフィルムの引取方向部
ぢ縦方向に延伸させる方法等により行なわれる。The unstretched multilayer film obtained by the above coextrusion molding is
Then, the film is stretched at a stretching ratio of 2 to 4 in the direction of take-up (vertical direction).
.. Axial stretching is carried out 5 times, preferably 2.5 to 4 times. If the stretching ratio is less than 2 times, the film will have insufficient curling properties, and if it is more than 4 or 5 times, the stretching property will decrease, resulting in breakage or uneven stretching of the film, which is not desirable. The stretching treatment is carried out by heating the above-mentioned unstretched film as it is or after slitting it to a predetermined width, and stretching the film in the longitudinal direction by changing the circumferential speed of a stretching roll, for example. .
該延伸処理における予熱温度としては、通常〔ポリプロ
ピレン系樹脂の融点−20°C〕以下、望ましくは40
〜120°Cの範囲で行なうのが好適である。The preheating temperature in the stretching process is usually below [the melting point of the polypropylene resin -20°C], preferably 40°C.
It is preferable to carry out the reaction at a temperature in the range of 120°C to 120°C.
また延伸後の熱固定温度は該予熱温度より高い温度とし
、さらにフィルムのシワ防止、横強度向上のためには、
出来るだけ高い温度とすることが好ましく、通常は〔ポ
リプロピレン系樹脂の融点20°C〕以下、望ましくは
80〜150°Cの範囲で行なうのが好適である。In addition, the heat setting temperature after stretching should be higher than the preheating temperature, and in order to prevent wrinkles and improve the transverse strength of the film,
The temperature is preferably as high as possible, usually below [the melting point of the polypropylene resin, 20°C], preferably in the range of 80 to 150°C.
該予熱及び熱固定温度が〔ポリプロピレン系樹脂の融点
−20°C〕より高い場合は、延伸ロールにフィルムが
溶融付着し、また、予熱温度が40°C未満では、脂肪
族ポリアミド樹脂が予熱不十分のために延伸困難となり
、フィルム破断が起こるので望ましくない。If the preheating and heat setting temperature is higher than [the melting point of polypropylene resin -20°C], the film will melt and adhere to the stretching roll, and if the preheating temperature is less than 40°C, the aliphatic polyamide resin will not be preheated. This is not desirable because the film becomes difficult to stretch and the film breaks.
本発明の包装用フィルムの厚みとしては40μm以下、
好ましくは2〜30μm、さらに好ましくは5〜20μ
mの範囲であり、また中間層の厚みはフィルム全体の厚
みに対し10〜90%の範囲である。該フィルムの厚み
が40μmより大きいとフィルム切断時の引裂強度が大
きくなりすぎ、ラップフィルムの用途には不適である。The thickness of the packaging film of the present invention is 40 μm or less,
Preferably 2 to 30 μm, more preferably 5 to 20 μm
The thickness of the intermediate layer is in the range of 10 to 90% of the total thickness of the film. If the thickness of the film is greater than 40 μm, the tear strength upon cutting the film will be too high, making it unsuitable for use as a wrap film.
中間層の厚みが全体厚みの10%より小さいとポリアミ
ド樹脂本来の耐熱性、機械的強度等を維持することはで
きず、また−軸延伸ポリプロピレンフィルムとしての物
性が支配的になるので、延伸方向に裂は易(なる。中間
層の厚みは全体厚みの15%以上であるのが好ましい。If the thickness of the intermediate layer is less than 10% of the total thickness, it will not be possible to maintain the heat resistance, mechanical strength, etc. inherent to the polyamide resin, and the physical properties of an axially stretched polypropylene film will become dominant. It is easy to tear. The thickness of the intermediate layer is preferably 15% or more of the total thickness.
逆に90%より大きいと、ポリプロピレン層の厚みが薄
(なり、共押出成形により均一に中間層を覆うことが困
難となる。中間層の厚みは全体厚みの80%以下である
のが好ましい。On the other hand, if it is larger than 90%, the thickness of the polypropylene layer becomes thin, making it difficult to uniformly cover the intermediate layer by coextrusion molding. The thickness of the intermediate layer is preferably 80% or less of the total thickness.
本発明の包装用フィルムは食品包装用等の種々の包装用
途に用いられる。さらに両表面層を構成する外層及び内
層に適当な方法で自己粘着性を付与することによりラッ
プフィルムとして好適に使用される。The packaging film of the present invention is used for various packaging applications such as food packaging. Further, by imparting self-adhesive properties to the outer layer and inner layer constituting both surface layers by an appropriate method, it can be suitably used as a wrap film.
以下、本発明の具体的態様について実施例により更に詳
しく説明するが、本発明はその要旨を越えない限りこれ
ら実施例によって限定されるものではない。Hereinafter, specific embodiments of the present invention will be explained in more detail with reference to Examples, but the present invention is not limited by these Examples unless the gist thereof is exceeded.
実施例中の測定は下記の方法で行なった。Measurements in the examples were performed using the following method.
(1)透湿性
JIS 20208に準じ、40°C190%RHの
条件で測定した。(1) Moisture permeability Measured according to JIS 20208 at 40°C and 190%RH.
(2)透明性(ヘーズ値)
JIS K−6714に準拠し、ヘーズメーターによ
り測定した。(2) Transparency (haze value) Measured using a haze meter in accordance with JIS K-6714.
(3)耐熱温度
幅30mm、長さ14cmの短冊状フィルム、試料片の
上下25mmに紙をあてLogの重りを下げる。1時間
で切れない最高雰囲気温度を10°C刻みで測定した。(3) A strip of film with a heat resistance temperature width of 30 mm and a length of 14 cm. Place paper 25 mm above and below the sample piece to lower the Log weight. The maximum atmospheric temperature that did not break in one hour was measured in 10°C increments.
(4)熱収縮率
打抜き治具によりフィルJ、を直径10mmの試料にし
、これをシリコンオイルを入れたアルミパン中に浸し、
このアルミパンを140°Cのホットプレート上に置く
。アルミパンに熱を奪われるため一旦ポットプレー1・
の温度は下がるが、これが、140°Cになってから4
5秒後にサンプルを取り出し、そのサイズ変化を測定す
る。(4) Heat shrinkage rate Make a sample of Fill J with a diameter of 10 mm using a punching jig, immerse it in an aluminum pan containing silicone oil,
Place this aluminum pan on a hot plate at 140°C. Because the heat is taken away by the aluminum pan, pot play 1.
temperature decreases, but after reaching 140°C
After 5 seconds, the sample is removed and its size change is measured.
(5)カット性
フィルムを芯管に巻き、ラップフィルム用ケースに収納
し、のこ刃による切断テストを行ない、4段階レベル(
良好、普通、やや不良、不良)によって評価した。なお
、評価の基準として市販のラップフィルムのカットレベ
ルを普通として評価した。(5) Wrap the cuttable film around the core tube, store it in a wrap film case, and perform a cutting test with a saw blade.
Good, fair, slightly poor, poor) were evaluated. As an evaluation standard, the cut level of a commercially available wrap film was evaluated as normal.
実施例1
450mm幅3種3層共押出Tダイ成形機を用いて表1
に示す樹脂を3台の押出機よりダイス温度280°Cで
同時に押出し、チルロール温度30°C1引取速度20
m/分の条件で製膜し、外層(ポリプロピレン)/中間
層(ナイロン−6/6.6)/内層(ポリプロピレン)
からなる2種3層フィルム(厚み30μm、層比1:2
:1)を成形した。次いで該フィルムをロール延伸によ
り、予熱温度60°C1熱固定温度110’Cで縦方向
に3.6倍延伸した。得られたフィルムの透湿度、透明
性、耐熱温度、熱収縮率及びカット性を上記方法で評価
した。その結果を表2に示す。Example 1 Using a 450 mm width 3 types 3 layer coextrusion T-die molding machine Table 1
The resin shown in is simultaneously extruded from three extruders at a die temperature of 280°C, a chill roll temperature of 30°C, a take-up speed of 20
The film was formed under conditions of m/min, outer layer (polypropylene)/intermediate layer (nylon-6/6.6)/inner layer (polypropylene).
Two types of three-layer film (thickness: 30 μm, layer ratio: 1:2)
:1) was molded. The film was then stretched 3.6 times in the machine direction by roll stretching at a preheating temperature of 60°C and a heat setting temperature of 110'C. The obtained film was evaluated for moisture permeability, transparency, heat resistance, heat shrinkage rate, and cuttability using the above methods. The results are shown in Table 2.
実施例2
実施例1において多層フィルムの各層比を2:1:2に
すること以外は同様にして行った。その結果を表2に示
す。Example 2 The same procedure as in Example 1 was carried out except that the ratio of each layer of the multilayer film was 2:1:2. The results are shown in Table 2.
実施例3
実施例1において、原反成形を水冷式インフレーション
成形としたこと以外は同様にして行なった。その結果を
表2に示す。なお、原反成形条件は、ダイス径75mm
φ、ダイス温度250°C、ブローアツプ比1.8.引
き取り速度17 m /min とし、折幅210mm
、厚さ30μmのフィルムを成形した。Example 3 Example 1 was carried out in the same manner as in Example 1 except that water-cooled inflation molding was used for forming the original fabric. The results are shown in Table 2. The original fabric forming conditions are a die diameter of 75 mm.
φ, die temperature 250°C, blowup ratio 1.8. The take-up speed is 17 m/min, and the folding width is 210 mm.
, a film with a thickness of 30 μm was molded.
比較例1〜5
実施例1において、表2に示す様なフィルム厚さ、フィ
ルム層比、延伸倍率にしたこと以外は同様にして行なっ
た。その結果を表2に示す。Comparative Examples 1 to 5 Comparative Examples 1 to 5 were carried out in the same manner as in Example 1 except that the film thickness, film layer ratio, and stretching ratio were as shown in Table 2. The results are shown in Table 2.
比較例6
実施例1において、原反成形を空冷式インフレーション
成形とした以外は同様にして行なった。Comparative Example 6 The same procedure as in Example 1 was carried out except that the original fabric was formed by air-cooled inflation molding.
その結果を表2に示す。なお、原反成形条件は、ダイス
径100mtnφ、ダイス温度250°C,フローアッ
プ比1.8.引き取り速度23m/min とし、折幅
280mm、厚さ30μmのフィルムを成形した。The results are shown in Table 2. The original fabric forming conditions were a die diameter of 100 mtnφ, a die temperature of 250°C, and a flow-up ratio of 1.8. A film having a fold width of 280 mm and a thickness of 30 μm was formed at a take-up speed of 23 m/min.
表 1
注)ポリプロピレン(プロピレン−エチレンランダム共
重合体)
三菱化成■製
三菱ポリプロ 6500J
ナイロン−6/6.6
三菱化成■製
ツバミツド■2030
〔発明の効果〕
本発明の包装用フィルムは、カット性、透明性、耐熱性
、水蒸気バリア性及び非熱収縮性に優れ、また、ナイロ
ン−6及びその共重合ナイロンの原料モノマーであるε
−カプロラクタムのフィルム表面へのブリードをポリプ
ロピレン系樹脂を積層することにより抑制するために、
食品安全性にも優れている。Table 1 Note) Polypropylene (propylene-ethylene random copolymer) Mitsubishi Polypro 6500J manufactured by Mitsubishi Chemical Corporation Nylon-6/6.6 Tsubamitsudo ■2030 manufactured by Mitsubishi Chemical Corporation [Effects of the invention] The packaging film of the present invention has excellent cutability. , has excellent transparency, heat resistance, water vapor barrier properties, and non-heat shrinkability, and is a raw material monomer for nylon-6 and its copolymerized nylon.
- In order to suppress the bleeding of caprolactam onto the film surface by laminating polypropylene resin,
It also has excellent food safety.
Claims (1)
内層が両表面層を構成し、該両表面層の間に脂肪族ポリ
アミド樹脂からなる中間層を有する多層フィルムであっ
て、上記各樹脂をTダイ成形法又は水冷式インフレーシ
ョン成形法により共押出成形した後、フィルムの引取方
向に延伸倍率2ないし4.5倍で延伸して得られたもの
であり、フィルム全体の厚みが40μm以下であり、か
つ、上記中間層の厚みがフィルム全体の厚みの10〜9
0%の範囲であることを特徴とする包装用フィルム。(1) A multilayer film in which an outer layer and an inner layer each made of a polypropylene resin constitute both surface layers, and an intermediate layer made of an aliphatic polyamide resin is formed between the two surface layers, and each of the above resins is formed by T-die molding. The film is obtained by coextrusion molding by a method or water-cooled inflation molding method, and then stretching at a stretching ratio of 2 to 4.5 times in the drawing direction of the film, and the total thickness of the film is 40 μm or less, and The thickness of the above-mentioned intermediate layer is 10 to 9 times the thickness of the entire film.
A packaging film characterized in that the content is in the range of 0%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2202824A JP2929679B2 (en) | 1990-07-31 | 1990-07-31 | Packaging film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2202824A JP2929679B2 (en) | 1990-07-31 | 1990-07-31 | Packaging film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0486259A true JPH0486259A (en) | 1992-03-18 |
JP2929679B2 JP2929679B2 (en) | 1999-08-03 |
Family
ID=16463801
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2202824A Expired - Fee Related JP2929679B2 (en) | 1990-07-31 | 1990-07-31 | Packaging film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2929679B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5686173A (en) * | 1994-09-13 | 1997-11-11 | Mitsubishi Chemical Corporation | Biaxially stretched film for packaging |
JP2006272965A (en) * | 2005-03-27 | 2006-10-12 | Huhtamaki Forchheim Zweigniederlassung Der Huhtamaki Deutschland Gmbh & Co Kg | Method for manufacturing oriented plastic film |
-
1990
- 1990-07-31 JP JP2202824A patent/JP2929679B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5686173A (en) * | 1994-09-13 | 1997-11-11 | Mitsubishi Chemical Corporation | Biaxially stretched film for packaging |
JP2006272965A (en) * | 2005-03-27 | 2006-10-12 | Huhtamaki Forchheim Zweigniederlassung Der Huhtamaki Deutschland Gmbh & Co Kg | Method for manufacturing oriented plastic film |
Also Published As
Publication number | Publication date |
---|---|
JP2929679B2 (en) | 1999-08-03 |
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