JP2011079998A - Surface-treated polyamide film and method for producing the same - Google Patents

Surface-treated polyamide film and method for producing the same Download PDF

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JP2011079998A
JP2011079998A JP2009234661A JP2009234661A JP2011079998A JP 2011079998 A JP2011079998 A JP 2011079998A JP 2009234661 A JP2009234661 A JP 2009234661A JP 2009234661 A JP2009234661 A JP 2009234661A JP 2011079998 A JP2011079998 A JP 2011079998A
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JP5645387B2 (en
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Akihiro Ohashi
暁弘 大橋
Kazuhide Ishii
和秀 石井
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Mitsubishi Plastics Inc
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a surface-treated polyamide film which has an excellent wet laminate strength, has excellent properties in low hot-water shrinkage and thickness accuracy, and can be suitably used as a base film of packaging bags, for example, for foodstuffs, chemicals, industrial products, and the like, and to provide a method for producing the same. <P>SOLUTION: The polyamide film includes an aliphatic polyamide resin as a main component. At least one of the film surfaces is subjected to surface treatment by electrodischarge treatment in an atmosphere having an inert gas concentration of 99% or more and an active gas concentration of 1% or less. The surface-treated surface has a wet laminate strength of 3.9 N/15 mm or more. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、優れた湿潤時のラミネート強度を有すると共に、低熱水収縮性や厚み精度にも優れた特性を有し、例えば食品、薬品、工業製品等の包装袋の基材フィルムとして好適に使用できる、表面処理ポリアミド系フィルム及び、表面処理ポリアミド系ラミネートフィルム、またその製造方法に関する。   The present invention has excellent laminate strength when wet, and also has excellent properties such as low hot water shrinkage and thickness accuracy, and is suitable as a base film for packaging bags of food, medicine, industrial products, etc. The present invention relates to a surface-treated polyamide-based film, a surface-treated polyamide-based laminate film, and a method for producing the same.

ナイロン6等のポリアミド樹脂を主体とするフィルムや、ポリアミド樹脂を層構成とする積層フィルムは引張強度、衝撃強度に優れていることから、これらのポリアミド系フィルムを食品、薬品等を包装するための包装袋に二次加工して、様々な形態で製造・販売されている。   Films mainly composed of polyamide resins such as nylon 6 and laminated films composed of polyamide resins as layers are excellent in tensile strength and impact strength, so that these polyamide-based films can be used for packaging foods, medicines, etc. It is secondarily processed into packaging bags and manufactured and sold in various forms.

近年、消費者の利便性、賞味期限の延長、保存性の向上の観点から、レトルト殺菌への適応が重要になっている。通常、このような用途にポリアミド系フィルムを使用する場合、(多くの場合は印刷をしたのち、)シーラントフィルムやその他のフィルムとラミネートしてラミネートフィルムを作製し、そのラミネートフィルムのシーラント層同士をヒートシールして袋状にし、さらに内容物を充填した後に開口部をヒートシールすることにより密閉し、容器として使用される。また、内容物を充填後高温でレトルト滅菌処理をすることで、内容物の賞味期限を延長したり、風味を保つ方法が行われる。   In recent years, adaptation to retort sterilization has become important from the viewpoint of consumer convenience, extension of the expiration date, and improvement of storage stability. Usually, when using a polyamide-based film for such an application (after printing in many cases), a laminate film is prepared by laminating with a sealant film or other films, and the sealant layers of the laminate film are bonded together. After heat-sealing to form a bag and filling the contents, the opening is sealed by heat-sealing and used as a container. Moreover, the method of extending the shelf life of a content or maintaining a flavor is performed by performing the retort sterilization process at high temperature after filling with the content.

しかし、レトルト処理中には内圧が高くなるため、ラミネート強度が劣るフィルムを用いた包装袋をレトルト処理する場合、破袋やデラミ等のトラブルがしばしば発生する。 However, since the internal pressure increases during the retort process, troubles such as broken bags and delamination often occur when a retort process is performed on a packaging bag using a film having poor laminate strength.

そこでナイロン等の機能性樹脂フィルムとシーラント等からなる複合フィルムを袋状にした容器で、内容物を充填後高温でレトルト滅菌処理する際に、破袋やデラミ等の不良が発生しない包装材が求められている。このような包装材に用いられる機能性樹脂フィルムに要求される特性としては、強度やガスバリア性等の基本特性に加え、デラミ発生を防ぐ為に高いラミネート強度が挙げられる。   Therefore, a packaging material that does not cause defects such as broken bags or delamination when retort sterilizing at high temperature after filling the contents with a bag made of a composite film made of a functional resin film such as nylon and a sealant. It has been demanded. Properties required for the functional resin film used for such a packaging material include basic properties such as strength and gas barrier properties, and high laminate strength to prevent delamination.

ここで、例えば特許文献1では、ポリアミドフィルムの、ナイロン等の機能性樹脂フィルム自体に高いラミネート強度を付与する手段として、フィルム表層の樹脂の配向を制御する方法がある。しかし、この場合、フィルム表面の凝集剥離によるデラミを防ぐことが目的であり、接着剤とフィルムの密着力を向上させる訳ではないため、実質的なラミネート強度が向上している訳ではない。   Here, for example, in Patent Document 1, there is a method of controlling the orientation of the resin on the film surface layer as means for imparting high laminate strength to the functional resin film itself such as nylon of the polyamide film. However, in this case, the purpose is to prevent delamination due to cohesive peeling of the film surface, and it does not improve the adhesive force between the adhesive and the film, so the substantial laminate strength is not improved.

また、その他の方法として、例えば特許文献2では、ポリアミドフィルムの、表面処理を二回以上行うことにより処理を均一に行うことで、処理ムラにより印刷抜け等のトラブルを防ぐ方法が提案されている。しかし、均一に処理されたことで処置ムラによる印刷抜け、ラミネート強度の低下を防ぐことは出来るが、ラミネート強度自体を向上させる訳ではないため根本的な解決に至っていない。   In addition, as another method, for example, Patent Document 2 proposes a method for preventing troubles such as printing omission due to processing unevenness by uniformly processing a polyamide film by performing surface treatment twice or more. . However, the uniform treatment can prevent printing omission due to treatment unevenness and decrease in the laminate strength, but it does not improve the laminate strength itself, so it has not led to a fundamental solution.

また、特許文献3では、窒素原子によりフィルム表面の処理を行うことにより、接着剤層を介すことなくフィルム同士を接着する方法が記載されている。しかし、この方法では湿潤時のラミネート強度は2.0N/15mm以上と低く、レトルト処理等の高い湿潤時のラミネート強度が必要な用途には使用出来ない。 Patent Document 3 describes a method of bonding films without using an adhesive layer by treating the film surface with nitrogen atoms. However, in this method, the laminate strength when wet is as low as 2.0 N / 15 mm or more, and it cannot be used for applications requiring high wet laminate strength such as retort treatment.

特開平9−239930JP-A-9-239930 特開2008−297416JP2008-297416 特開2007−307771JP2007-307771

そこで、本発明は、引張強度、衝撃強度等の機械的強度に優れると共に、高い湿潤時のラミネート強度を有する表面処理ポリアミド系フィルム及びその製造方法を提供することを目的とする。   Therefore, an object of the present invention is to provide a surface-treated polyamide film having excellent mechanical strength such as tensile strength and impact strength, and having high laminate strength when wet, and a method for producing the same.

本発明者らは、このような現状に鑑み、鋭意検討を重ねた結果、従来の問題点を解消できるポリアミド系フィルムを見出した。   In view of the current situation, the present inventors have made extensive studies and have found a polyamide-based film that can solve the conventional problems.

即ち、本発明は、以下の表面処理ポリアミド系フィルム及びその製造方法を提供するものである。 That is, the present invention provides the following surface-treated polyamide film and a method for producing the same.

1.脂肪族ポリアミド樹脂を主成分とするポリアミド系フィルムであって、少なくとも一方のフィルム表面に、不活性ガス濃度99%以上、活性ガス濃度1%以下の雰囲気下での放電処理による表面処理がなされた表面処理面の湿潤時のラミネート強度が3.9N/15mm以上であることを特徴とする表面処理ポリアミド系フィルム。
2.95℃×5分におけるフィルムの流れ方向(MD)の熱水収縮率が3.0%以下であり、且つ、フィルムの幅方向(TD)の厚み変動率が平均厚みの10%以下である上記1に記載の表面処理ポリアミド系フィルム。
3.前記表面処理時の雰囲気が、不活性ガス濃度99%以上、活性ガス濃度1%以下、反応性ガス濃度1%以下ある上記1又は2に記載の表面処理ポリアミド系フィルム。
4.前記不活性ガスが窒素、ヘリウム、ネオン、アルゴン、クリプトンから選ばれる少なくとも一種の気体である上記1から3のいずれか1つに記載の表面処理ポリアミド系フィルム。
5.上記1から4のいずれか1つに記載の表面処理ポリアミド系フィルムにおける前記表面処理面が、樹脂積層体の少なくともいずれか一方の表面を構成するよう配置された多層構造からなる表面処理ポリアミド系フィルム
6.上記1から5のいずれか1つに記載の表面処理ポリアミド系フィルムの前記表面処理面に、シーラントフィルムをラミネートしてなることを特徴とする表面処理ポリアミド系ラミネートフィルム。
7.上記6記載の表面処理ポリアミド系ラミネートフィルムからなる袋体。
8.フラットダイから押出された脂肪族ポリアミド系樹脂を主成分とする未延伸フィルムをMD、TDともに2.4倍以上の延伸倍率でテンター式逐次二軸延伸法により延伸する工程の後、200℃以上、且つ前記脂肪族ポリアミド系樹脂の補外融解開始温度(JIS K 7121に準拠して測定)より10℃高い温度以下で熱固定を行う工程を経て、フィルムの少なくとも一方の表面に、不活性ガス濃度99%以上、活性ガス濃度1%以下の雰囲気下でのコロナ処理又はプラズマ処理のいずれか一種の放電処理による表面処理を行う工程を有することを特徴とする表面処理ポリアミド系フィルムの製造方法。
1. A polyamide-based film containing an aliphatic polyamide resin as a main component, and at least one film surface is subjected to surface treatment by discharge treatment in an atmosphere having an inert gas concentration of 99% or more and an active gas concentration of 1% or less. A surface-treated polyamide film having a laminate strength when the surface-treated surface is wet is 3.9 N / 15 mm or more.
The hot water shrinkage rate in the film flow direction (MD) at 2.95 ° C. × 5 minutes is 3.0% or less, and the thickness variation rate in the width direction (TD) of the film is 10% or less of the average thickness. 2. The surface-treated polyamide film according to 1 above.
3. 3. The surface-treated polyamide film according to 1 or 2 above, wherein the atmosphere during the surface treatment is an inert gas concentration of 99% or more, an active gas concentration of 1% or less, and a reactive gas concentration of 1% or less.
4). 4. The surface-treated polyamide film according to any one of 1 to 3, wherein the inert gas is at least one gas selected from nitrogen, helium, neon, argon, and krypton.
5). 5. The surface-treated polyamide film having a multilayer structure in which the surface-treated surface in the surface-treated polyamide film according to any one of 1 to 4 is disposed so as to constitute at least one surface of a resin laminate. 6). 6. A surface-treated polyamide-based laminate film obtained by laminating a sealant film on the surface-treated surface of the surface-treated polyamide-based film according to any one of 1 to 5 above.
7). A bag comprising the surface-treated polyamide-based laminate film described in 6 above.
8). After a step of stretching an unstretched film mainly composed of an aliphatic polyamide-based resin extruded from a flat die by a tenter-type sequential biaxial stretching method at a stretching ratio of 2.4 times or more for both MD and TD, 200 ° C or more In addition, an inert gas is formed on at least one surface of the film through a step of heat setting at a temperature not higher than 10 ° C. higher than the extrapolated melting start temperature (measured in accordance with JIS K 7121) of the aliphatic polyamide resin. A method for producing a surface-treated polyamide film, comprising a step of performing a surface treatment by a discharge treatment of any one of corona treatment and plasma treatment in an atmosphere having a concentration of 99% or more and an active gas concentration of 1% or less.

本発明によれば、引張強度、衝撃強度等の機械的強度に優れると共に、高い湿潤時のラミネート強度を有する表面処理ポリアミド系フィルム及びその製造方法が提供できる。   ADVANTAGE OF THE INVENTION According to this invention, while being excellent in mechanical strength, such as tensile strength and impact strength, the surface treatment polyamide-type film which has the lamination strength at the time of high wetness, and its manufacturing method can be provided.

以下、本発明を詳しく説明するが、本発明の範囲は以下に説明する実施形態に限定されるものではない。
まず、本発明の表面処理ポリアミド系フィルムは、脂肪族ポリアミド樹脂を含んでいる。
ここで、脂肪族ポリアミド樹脂としては、特に制限はないが、環状ラクタムの開環重合物、アミノカルボン酸の重縮合物、ジカルボン酸とジアミンとの重縮合物などが挙げられる。具体的には、ナイロン6と称されるε−カプロラクタムの単独重合体、あるいはナイロン66と称されるポリヘキサメチレンアジパミド等が安価に入手でき、かつ、延伸操作を円滑に遂行し得る点から好ましい。
Hereinafter, the present invention will be described in detail, but the scope of the present invention is not limited to the embodiments described below.
First, the surface-treated polyamide film of the present invention contains an aliphatic polyamide resin.
Here, the aliphatic polyamide resin is not particularly limited, and examples thereof include a ring-opening polymer of cyclic lactam, a polycondensate of aminocarboxylic acid, and a polycondensate of dicarboxylic acid and diamine. Specifically, a homopolymer of ε-caprolactam called nylon 6 or polyhexamethylene adipamide called nylon 66 can be obtained at low cost, and the stretching operation can be performed smoothly. To preferred.

前記表面処理ポリアミド系フィルムにおける脂肪族ポリアミド樹脂の含有割合は、45〜100質量%とすることが可能である。前記脂肪族ポリアミド樹脂の含有割合が45質量%より低い場合、引張強度、衝撃強度等の機械的強度が不十分となる。   The content ratio of the aliphatic polyamide resin in the surface-treated polyamide film can be 45 to 100% by mass. When the content of the aliphatic polyamide resin is lower than 45% by mass, mechanical strength such as tensile strength and impact strength becomes insufficient.

上述したポリアミド系フィルムには、脂肪族ポリアミド樹脂のほか、本発明の主旨を超えない範囲内で適宜必要に応じて、衝撃改良剤、滑剤、帯電防止剤、酸化防止剤、ブロッキング防止剤、安定剤、染料、顔料、無機質微粒子等の各種添加剤を添加することができる。具体例としては、衝撃改良剤(エラストマー等)、アンチブロッキング剤(無機フィラー等)、撥水剤(エチレンビスステアリン酸エステル等)、滑剤(エチレンビスステアリン酸アミド等)を挙げることができる。   In addition to the aliphatic polyamide resin, the above-mentioned polyamide-based film may have an impact modifier, a lubricant, an antistatic agent, an antioxidant, an antiblocking agent, a stable agent, as necessary, within the scope not exceeding the gist of the present invention. Various additives such as an agent, a dye, a pigment, and inorganic fine particles can be added. Specific examples include impact modifiers (such as elastomers), anti-blocking agents (such as inorganic fillers), water repellents (such as ethylene bisstearic acid esters), and lubricants (such as ethylene bisstearic acid amides).

さらに、本発明の表面処理ポリアミド系フィルムには、本発明の主旨を超えない範囲内で適宜必要に応じて、本発明の表面処理ポリアミド系フィルムを製造する際に発生する規格外フィルムや切断端材(耳トリム)を添加することができる。   Furthermore, the surface-treated polyamide-based film of the present invention includes a non-standard film and a cut edge that are generated when the surface-treated polyamide-based film of the present invention is produced, as necessary, within the range not exceeding the gist of the present invention. Material (ear trim) can be added.

本発明の表面処理ポリアミド系フィルムを包装袋として使用する際には、内容物の品質保持や腐敗防止の観点から、さらにガスバリア性樹脂層を積層すること、アルミニウム等の金属や、二酸化珪素、アルミナ等の金属酸化物を蒸着加工すること、ガスバリア性コート剤を塗布すること等により、ガスバリア性や防湿性をさらに向上させることができる。   When using the surface-treated polyamide film of the present invention as a packaging bag, from the viewpoint of maintaining the quality of the contents and preventing spoilage, a gas barrier resin layer is further laminated, a metal such as aluminum, silicon dioxide, and alumina. Gas barrier properties and moisture resistance can be further improved by subjecting metal oxides such as vapor deposition and coating with a gas barrier coating agent.

次に、本発明の表面処理ポリアミド系フィルムは、下記の(1)の特徴を有することが重要あり、(2)、(3)の特徴を有することが好ましい。これらは、フィルムの表面処理のほか、製造条件(延伸倍率、熱固定温度など)により制御することができる。   Next, it is important that the surface-treated polyamide film of the present invention has the following feature (1), and preferably has the features (2) and (3). These can be controlled by manufacturing conditions (stretch ratio, heat setting temperature, etc.) in addition to the surface treatment of the film.

(1)湿潤時のラミネート強度が3.9N/15mm以上であることが必要である。ここで、湿潤時のラミネート強度が3.9N/15mm以上であれば、ラミネート、製袋後のレトルト処理等によって応力がかかった状態でも、デラミ、破袋等のトラブルが発生しにくい。本発明において、「湿潤時のラミネート強度」とは、ラミネートされた表面処理ポリアミド系フィルムとシーラントとの層間の剥離強度をいい、具体的には後述の測定方法により得られた値である。   (1) The laminate strength when wet must be 3.9 N / 15 mm or more. Here, if the laminate strength when wet is 3.9 N / 15 mm or more, troubles such as delamination and broken bags are unlikely to occur even in a state where stress is applied by lamination, retort processing after bag making, or the like. In the present invention, “lamination strength when wet” refers to the peel strength between the laminated surface-treated polyamide film and the sealant, and is specifically a value obtained by the measurement method described below.

(2)95℃×5分におけるフィルムの流れ方向(MD)の熱水収縮率が3.0%以下であることが好ましい。ここで、MDの熱水収縮率が3.0%以下であれば、印刷、ラミネート等の工程での熱収縮によるピッチずれ等のトラブルの発生を抑えることができる。   (2) It is preferable that the hot water shrinkage in the flow direction (MD) of the film at 95 ° C. for 5 minutes is 3.0% or less. Here, if the hot water shrinkage rate of MD is 3.0% or less, it is possible to suppress the occurrence of troubles such as pitch deviation due to heat shrinkage in processes such as printing and laminating.

(3)フィルムの幅方向(TD)の厚み変動率が平均厚みの10%以下であることが好ましい。ここで、厚み変動率が平均厚みの10%以下であれば、厚みムラに起因するシワの発生や、タルミが発生して印刷見当がずれたり、フィルムパスが蛇行して印刷ピッチがずれたりする等のトラブルの発生を抑えることができる。   (3) It is preferable that the thickness variation rate in the width direction (TD) of the film is 10% or less of the average thickness. Here, if the thickness variation rate is 10% or less of the average thickness, wrinkles due to thickness unevenness and / or tarmi are generated and printing registration is shifted, or the film path is meandering and the printing pitch is shifted. The occurrence of such troubles can be suppressed.

このように、(2)、(3)の特徴を有することで、低熱水収縮性や厚み精度にも優れた特性を備えた表面処理ポリアミド系フィルムを得ることができる。 Thus, by having the characteristics of (2) and (3), it is possible to obtain a surface-treated polyamide film having characteristics excellent in low hot water shrinkage and thickness accuracy.

以下、本発明の表面処理ポリアミド系フィルムを得るために好適な製造方法について説明する。   Hereinafter, a production method suitable for obtaining the surface-treated polyamide film of the present invention will be described.

すなわち、ポリアミド系樹脂を原料として用いて、まず、実質的に無定形で配向していないフィルム(以下、「未延伸フィルム」という)を、通常、押出法で製造する。この未延伸フィルムの製造は、例えば、上記原料を押出機により溶融し、フラットダイから押出した後、急冷することによりフラット状の未延伸フィルムとする押出法を採用することができる。 That is, using a polyamide-based resin as a raw material, a film that is substantially amorphous and not oriented (hereinafter referred to as “unstretched film”) is usually produced by an extrusion method. The unstretched film can be produced by, for example, an extrusion method in which the raw material is melted by an extruder, extruded from a flat die, and then rapidly cooled to form a flat unstretched film.

次に、上記の未延伸フィルムを、フィルムの流れ方向(MD)、およびその直交方向である幅方向(TD)で、延伸効果、フィルム強度等の点から、二軸方向に延伸する。二軸延伸の方法としては、テンター式逐次二軸延伸、テンター式同時二軸延伸、チューブラー式同時二軸延伸等、従来公知の延伸方法がいずれも採用できる。例えば、テンター式逐次二軸延伸方法の場合には、未延伸フィルムを50〜110℃の温度範囲に加熱しロール式縦延伸機によって縦方向に2.4倍以上に延伸することが重要である。ここで、縦延伸倍率が2.4倍未満では、延伸ムラが発生し厚みが不均一になったり、配向不足のためにフィルムの強度が低下したりする。   Next, the unstretched film is stretched in the biaxial direction in terms of stretching effect, film strength, and the like in the film flow direction (MD) and the width direction (TD) which is the orthogonal direction. As the biaxial stretching method, any conventionally known stretching method such as tenter-type sequential biaxial stretching, tenter-type simultaneous biaxial stretching, tubular simultaneous biaxial stretching, and the like can be adopted. For example, in the case of the tenter-type sequential biaxial stretching method, it is important that the unstretched film is heated to a temperature range of 50 to 110 ° C. and stretched 2.4 times or more in the longitudinal direction by a roll-type longitudinal stretching machine. . Here, when the longitudinal stretching ratio is less than 2.4 times, stretching unevenness occurs, the thickness becomes non-uniform, or the strength of the film decreases due to insufficient orientation.

上記方法により延伸された縦延伸フィルムは、続いて端部をテンタークリップで保持し、テンター式横延伸機によって60〜140℃の温度範囲内でTDに2.4倍以上、で延伸することが重要である。ここで、横延伸倍率が2.4倍未満では横延伸倍率が低すぎ、未延伸部分が残る等の延伸ムラが発生し、厚みが不均一になったり、配向不足のためにフィルムの強度が低下したりという問題がある。   The longitudinally stretched film stretched by the above method can be subsequently stretched at a TD of 2.4 times or more within a temperature range of 60 to 140 ° C. by a tenter-type lateral stretcher while holding the end with a tenter clip. is important. Here, when the transverse draw ratio is less than 2.4 times, the transverse draw ratio is too low, and non-stretched portions such as unstretched portions are generated, resulting in uneven thickness and insufficient film orientation due to insufficient orientation. There is a problem that it falls.

上記方法により延伸された二軸延伸フィルムは、引き続き端部をテンタークリップで保持し、テンターオーブンにて200℃以上、且つ上記した脂肪族ポリアミド樹脂の補外融解開始温度より10℃高い温度以下で、1秒〜2分程度、好ましくは1秒〜30秒、より好ましくは3〜15秒の時間で熱固定を行う。   The biaxially stretched film stretched by the above method continues to hold the end portion with a tenter clip, at a temperature of 200 ° C. or higher in a tenter oven, and 10 ° C. or lower than the extrapolated melting start temperature of the above aliphatic polyamide resin. The heat setting is performed for about 1 second to 2 minutes, preferably 1 second to 30 seconds, more preferably 3 to 15 seconds.

ここで、熱固定温度が200℃より低い場合や、処理時間が1秒以下となる場合は、MDの熱水収縮率を3.0%以下に抑えることができず、印刷、ラミネート等の工程で収縮してしまいピッチがずれる等のトラブルが発生する。一方、熱固定温度が上記した脂肪族ポリアミド樹脂の補外融解開始温度より10℃高い温度を超える場合や、処理時間が2分を超える場合は、熱固定中のフィルムの溶融や結晶化の応力による破断が生じ、フィルムの機械物性が不足してしまう。   Here, when the heat setting temperature is lower than 200 ° C. or when the processing time is 1 second or less, the hot water shrinkage of MD cannot be suppressed to 3.0% or less, and printing, laminating, and the like. This causes problems such as shrinkage and shift in pitch. On the other hand, if the heat setting temperature exceeds 10 ° C. higher than the extrapolated melting start temperature of the aliphatic polyamide resin described above, or if the treatment time exceeds 2 minutes, the stress of melting or crystallization of the film during heat setting Breakage occurs due to the shortage of mechanical properties of the film.

なお、上記した補外融解開始温度とは、JIS K 7121:1987に記載されている示差走査熱量測定(DSC)における融解ピークの低温側のベースラインを高温側に延長した直線と、融解ピークの低温側の曲線に勾配が最大になる点で引いた接線の交点から求められる温度のことである。   The extrapolated melting start temperature described above is a straight line obtained by extending the low-temperature base line of the melting peak in the differential scanning calorimetry (DSC) described in JIS K 7121: 1987 to the high-temperature side. This is the temperature obtained from the intersection of the tangent lines drawn at the point where the gradient is maximum on the low temperature side curve.

上記方法により延伸された二軸延伸フィルムは、引き続き少なくとも一方の面に不活性ガス濃度99%以上、活性ガス濃度1%以下、反応性ガス濃度1%以下の雰囲気下で、コロナ処理、プラズマ処理、等の放電処理によって表面処理を実施することが必要である。このとき、不活性ガス濃度が99%以上、活性ガス濃度が1%以下で有れば、ラミネートフィルムの湿潤時のラミネート強度が飛躍的に向上し、3.9N/15mm以上を達成することが出来る。   The biaxially stretched film stretched by the above method is subsequently subjected to corona treatment and plasma treatment in an atmosphere having an inert gas concentration of 99% or more, an active gas concentration of 1% or less, and a reactive gas concentration of 1% or less on at least one surface. It is necessary to carry out surface treatment by electric discharge treatment such as. At this time, if the inert gas concentration is 99% or more and the active gas concentration is 1% or less, the laminate strength when the laminate film is wet is drastically improved, and 3.9 N / 15 mm or more can be achieved. I can do it.

不活性ガスの濃度は高いほど、湿潤時のラミネート強度が向上し好ましく、99%以上である必要があり、好ましくは99.9%以上、より好ましくは99.98%以上である。ただし、通常生産する場合での生産性、コスト、を考えた場合、処理の際に、ある程度大気中に含まれる活性ガスである酸素が搬送流として流入してしまう。不活性ガスの吹き込み量を増やせば、活性ガス濃度を下げることが出来るが、製品あたりの不活性ガス使用量が増え、コストが増加してしまう。そのため、充分に効果がある範囲内で、不活性ガスの使用量を抑えることがコストを抑えるために望ましい。また、不活性ガスの吹き込み量を増やせば、排気が間に合わなくなる可能性があり、その場合室内雰囲気の酸素濃度が低下し、作業者が酸欠に陥ってしまうおそれがある。安全性の観点から室内雰囲気の酸素濃度を維持するためにも、不活性ガスの濃度は99.999%までとすることが現実的である。一方、活性ガスの濃度は1%以下である必要があり、好ましくは0.1%以下、より好ましくは0.02%以下である。   The higher the concentration of the inert gas, the better the laminate strength when wet, and it is necessary to be 99% or more, preferably 99.9% or more, more preferably 99.98% or more. However, when productivity and cost in the case of normal production are considered, oxygen, which is an active gas contained in the atmosphere to some extent, flows in as a carrier flow during processing. If the amount of inert gas blown is increased, the concentration of the active gas can be lowered, but the amount of inert gas used per product increases and the cost increases. For this reason, it is desirable to reduce the amount of the inert gas used within a range that is sufficiently effective in order to reduce costs. Further, if the amount of the inert gas blown is increased, exhaust may not be in time, in which case the oxygen concentration in the indoor atmosphere is lowered, and the operator may be deficient in oxygen. In order to maintain the oxygen concentration in the indoor atmosphere from the viewpoint of safety, it is realistic that the concentration of the inert gas is up to 99.999%. On the other hand, the concentration of the active gas needs to be 1% or less, preferably 0.1% or less, more preferably 0.02% or less.

本発明において、不活性ガスとは、窒素、ヘリウム、ネオン、アルゴン、クリプトンなどをいい、窒素、アルゴン等が安価に入手でき、かつ、表面処理操作を安全に、円滑に遂行し得る点から好ましい。また、本発明において、活性ガスとは、酸素、二酸化炭素、一酸化炭素、オゾンなどいい、酸素、二酸化炭素が安価に入手でき、かつ、表面処理操作を安全に、円滑に遂行し得る点から好ましい。上記の不活性ガス、活性ガスは、それぞれ複数の物を混合した物でもかまわない。   In the present invention, the inert gas refers to nitrogen, helium, neon, argon, krypton, etc., and is preferable from the viewpoint that nitrogen, argon, etc. can be obtained at low cost, and the surface treatment operation can be performed safely and smoothly. . Further, in the present invention, the active gas refers to oxygen, carbon dioxide, carbon monoxide, ozone, etc., from the point that oxygen and carbon dioxide can be obtained at low cost, and the surface treatment operation can be performed safely and smoothly. preferable. The inert gas and the active gas may be a mixture of a plurality of substances.

また、湿潤時のラミネート強度をさらに向上させるために、上記不活性ガス、活性ガスに加えさらに反応性ガスを添加することが出来る。反応性ガスの添加量としては、1%以下が表面処理操作を安全に、円滑に遂行し得る点から好ましい。   In order to further improve the laminate strength when wet, a reactive gas can be added in addition to the inert gas and the active gas. The addition amount of the reactive gas is preferably 1% or less from the viewpoint that the surface treatment operation can be performed safely and smoothly.

本発明において、反応性ガスとは、水素、アンモニア、アセチレン、メタン、などをいい、水素、アンモニアが安価に入手でき、かつ、表面処理操作を円滑に遂行し得る点から好ましい。また上記の反応性ガスは、それぞれ複数の物を混合した物でもかまわない。   In the present invention, the reactive gas refers to hydrogen, ammonia, acetylene, methane, etc., and is preferable from the viewpoint that hydrogen and ammonia can be obtained at low cost and the surface treatment operation can be performed smoothly. The reactive gas may be a mixture of a plurality of substances.

前記放電処理の方法としては、特に制限はないが、コロナ処理、大気圧プラズマ処理、リモートプラズマ処理等が挙げられる。具体的にはコロナ処理、大気圧プラズマ処理が、簡便、かつ、表面処理操作を安全に、円滑に遂行し得る点から好ましい。   The discharge treatment method is not particularly limited, and examples thereof include corona treatment, atmospheric pressure plasma treatment, and remote plasma treatment. Specifically, corona treatment and atmospheric pressure plasma treatment are preferable because they are simple and can perform the surface treatment operation safely and smoothly.

本発明の実施形態として、上記表面処理ポリアミド系フィルムの、当該表面処理面に、シーラントフィルムをラミネートしてなることを特徴とする表面処理ポリアミド系ラミネートフィルムがある。   As an embodiment of the present invention, there is a surface-treated polyamide-based laminate film obtained by laminating a sealant film on the surface-treated surface of the surface-treated polyamide-based film.

前記ラミネートフィルムとしては、前記表面処理ポリアミド系積層フィルムの表面処理がなされた少なくとも片側面に、シーラントフィルム(層)が配されたものが例示される。 Examples of the laminate film include those in which a sealant film (layer) is disposed on at least one side surface on which the surface-treated polyamide-based laminate film has been subjected to surface treatment.

前記シーラントフィルムとしては、熱融着できる樹脂であればよく、一般にポリオレフィン系樹脂、ポリエステル系樹脂等が挙げられる。具体的には、ポリプロピレン、低密度ポリエチレン、直鎖状低密度ポリエチレン、エチレン−酢酸ビニル共重合体、エチレン−(メタ)アクリル酸共重合体、エチレン−(メタ)アクリル酸エステル共重合体、アイオノマー樹脂、エチレン・α−オレフィン共重合体、アモルファスポリエステル等が挙げられるが、これらに限定されるものではない。前記シーラントフィルムの厚さは、15〜100μm程度が一般的に好適に使用できる。シーラントフィルムが薄い場合はヒートシール時のシール強度が劣る傾向があり、一方厚すぎる場合は包装用途に適さなくなる傾向がある。 The sealant film may be any resin that can be heat-sealed, and generally includes a polyolefin-based resin, a polyester-based resin, and the like. Specifically, polypropylene, low density polyethylene, linear low density polyethylene, ethylene-vinyl acetate copolymer, ethylene- (meth) acrylic acid copolymer, ethylene- (meth) acrylic acid ester copolymer, ionomer Resins, ethylene / α-olefin copolymers, amorphous polyesters and the like may be mentioned, but are not limited thereto. The thickness of the sealant film is generally preferably about 15 to 100 μm. When the sealant film is thin, the sealing strength at the time of heat sealing tends to be inferior, whereas when it is too thick, it tends to be unsuitable for packaging applications.

また、前記表面処理ポリアミド系積層フィルムとシーラントフィルムとのラミネートの方法としては、特に制限はないが、ドライラミネート法、ウェットラミネート法、押出しラミネート法などが挙げられる。具体的には、ドライラミネート法、押出しラミネート法が通常用いられる。 Further, the method for laminating the surface-treated polyamide-based laminated film and the sealant film is not particularly limited, and examples thereof include a dry laminating method, a wet laminating method, and an extrusion laminating method. Specifically, a dry laminating method and an extrusion laminating method are usually used.

さらに本発明の他の実施形態として、上記表面処理ポリアミド系ラミネートフィルムからなる袋体がある。これは上記ラミネートフィルムを二次加工したものであり、シーラント層同士を熱溶着させて製袋して得られる。袋体の内容物としては、酸素による変質を嫌う食品、医薬品、薬品、香料等を挙げることができる。さらに高い湿潤時のラミネート強度を必要とする用途としては、内容物の重量が大きい場合や、レトルト処理を行う食品等の包装や、エアバッグ式緩衝材等の、内部より高い圧力がかかる用途に、好適に用いられる。   Furthermore, as another embodiment of the present invention, there is a bag made of the surface-treated polyamide-based laminate film. This is a secondary process of the above laminate film, and is obtained by heat-sealing sealant layers to form a bag. Examples of the contents of the bag include foods, pharmaceuticals, chemicals, and fragrances that do not want to be altered by oxygen. For applications that require higher wet laminate strength, such as when the weight of the contents is large, or for applications that require higher pressure than the inside, such as packaging for foods that undergo retort processing, airbag cushioning materials, etc. Are preferably used.

以下、本発明の内容および効果を実施例によりさらに詳細に説明するが、本発明は、その主旨を越えない限り以下の例に限定されるものではない。なお、フィルムの評価および測定法は次の各方法によって行ったものである。   Hereinafter, the contents and effects of the present invention will be described in more detail with reference to examples. However, the present invention is not limited to the following examples unless it exceeds the gist thereof. The evaluation and measurement methods for the film were performed by the following methods.

(1)湿潤時のラミネート強度
ドライラミネート
製膜された表面処理ポリアミド系フィルムの処理面に、接着剤として主剤に東洋モートン社製AD−900を、硬化剤として東洋モートン社製CAT−RT85を、希釈溶剤として酢酸エチルをそれぞれ37.7%、5.7%、56.6%で混合し、グラビアコート塗布後、80℃で乾燥して酢酸エチルを除去して接着剤塗布量を3g/mとした。シーラントとして東セロ社製LLDPEフィルムT.U.X FCS 50μmを90℃でドライラミネートにて接着したのち、40℃で3日間エージングを行った。
(1) Laminate strength when wet
Dry laminate On the treated surface of the surface-treated polyamide film formed, Toyo Morton AD-900 as the main agent, Toyo Morton CAT-RT85 as the curing agent, and acetic acid as the diluting solvent Ethyl was mixed at 37.7%, 5.7%, and 56.6%, respectively, and after gravure coating, it was dried at 80 ° C. to remove ethyl acetate to make the adhesive coating amount 3 g / m 2 . LLDPE film manufactured by Tosero Corporation as a sealant U. After adhering 50 μm of X FCS at 90 ° C. by dry lamination, aging was performed at 40 ° C. for 3 days.

ラミネート後の湿潤時のラミネート強度
上記方法にてドライラミネートされたポリアミド系樹脂積層フィルムとシーラントの層間を水やエタノールを用いてピンセットで剥がす。剥がした部分が1cmほどになったら剥がした部分にかかるようにラピーテープ(セメダイン製18mm幅)をフィルムの縦方向に密着させる。ラピーテープを貼ったフィルムを流れ方向に直角な方向に幅15mm長さ100mmで短冊状に切り出し、水をつけながら50mmほどに剥離部分を広げる。剥がしたフィルムの両側をオートグラフ(東洋精機製)のチャックで掴み、フィルムの剥離部分に水を付けながら、速度50mm/minで引っ張った。最初のピーク値をn=5で測定し、平均値を湿潤時のラミネート強度(N/15mm)とした。
Lamination strength when wet after lamination The layer between the polyamide resin laminated film dry-laminated by the above method and the sealant is peeled off with tweezers using water or ethanol. When the peeled part becomes about 1 cm, a rappy tape (cemedine 18 mm width) is adhered in the longitudinal direction of the film so as to cover the peeled part. The film with the rappy tape is cut into strips with a width of 15 mm and a length of 100 mm in a direction perpendicular to the flow direction, and the peeled portion is expanded to about 50 mm while applying water. Both sides of the peeled film were gripped by an autograph (manufactured by Toyo Seiki) and pulled at a speed of 50 mm / min while water was applied to the peeled portion of the film. The initial peak value was measured at n = 5, and the average value was defined as the laminate strength when wet (N / 15 mm).

測定結果
湿潤時のラミネート強度が3.9N/15mm以上のものは(○)、
湿潤時のラミネート強度が3.9N/15mmに満たないものは(×)
(2)熱水収縮率
得られたフィルムの両端部、及び中央の三点から、MDに120mm×TDに120mmに切り出し、このサンプルのMDに約100mmの基準線を三本引く。このサンプルを23℃、50%RH雰囲気下に24時間放置し基準線を測長する。測長した熱処理前の長さをFとする。このサンプルを95℃に保持した熱水中に浸し、5分間加熱した後取り出す。さらに23℃、50%RH雰囲気下に30分放置した後、前記基準線を測長し、熱処理後の長さをGとする。
Measurement results When the laminate strength when wet is 3.9 N / 15 mm or more (◯),
If the laminate strength when wet is less than 3.9 N / 15 mm (×)
(2) Hot-water shrinkage From the two ends of the obtained film and the central three points, 120 mm × TD is cut into 120 mm on the MD, and three reference lines of about 100 mm are drawn on the MD of this sample. This sample is left in an atmosphere of 23 ° C. and 50% RH for 24 hours, and the reference line is measured. The measured length before heat treatment is F. This sample is immersed in hot water maintained at 95 ° C., heated for 5 minutes, and then taken out. Further, after being left in an atmosphere of 23 ° C. and 50% RH for 30 minutes, the reference line is measured, and the length after the heat treatment is defined as G.

熱水収縮率を、下式で算出し、三本の平均値(平均値の少数第二位を四捨五入)をMDの熱水収縮率とし、両端部、及び中央の三点のうち、最大のものに関して、以下の評価を行った。 The hot water shrinkage rate is calculated by the following formula, and the average value of the three (rounded off the second decimal place of the average value) is the hot water shrinkage rate of MD, and the maximum of the three points at both ends and the center. The following evaluation was performed on the product.

熱水収縮率=[(F−G)/F]×100(%)
MDの熱水収縮率が3.0%以下のものは(○)、3.0%を超えるものは(×)
(3)厚み変動率(%)
打点式厚み計を用い、得られたフィルムの幅方向に20mm間隔で厚みを測定し、そのときの最大値をTmax、最小値をTmin、全測定点を合計し測定点数で割った平均値をTaveとした。
Hot water shrinkage = [(F−G) / F] × 100 (%)
MDs with hot water shrinkage of 3.0% or less (○), those with more than 3.0% (×)
(3) Thickness fluctuation rate (%)
Using a striking-point thickness meter, the thickness is measured at intervals of 20 mm in the width direction of the obtained film, the maximum value at that time is Tmax, the minimum value is Tmin, the average value obtained by summing all the measurement points and dividing by the number of measurement points Tave.

厚み変動率を下式で算出(少数第一位を四捨五入)し、以下の評価を行った。 The thickness fluctuation rate was calculated by the following formula (rounded to the first decimal place), and the following evaluation was performed.

厚み変動率=[(Tmax−Tmin)/Tave]×100(%)
厚み変動率が10%以下のものは(○)、10%を超えるものは(×)
(実施例1)
脂肪族ポリアミド樹脂として、ナイロン6「三菱エンジニアリングプラスチックス(株)、商品名ノバミッド1022C6、補外融解開始温度:215℃」を用い、これを65mmφ単軸押出機(L/D=28)に投入し、設定温度260℃にて溶融、混練し、Tダイにて押出し、30℃のキャストロールに密着急冷し、約140μmの未延伸フィルムを得た。
Thickness variation rate = [(Tmax−Tmin) / Tave] × 100 (%)
Thickness fluctuation rate of 10% or less (○), 10% or more (×)
Example 1
As an aliphatic polyamide resin, nylon 6 “Mitsubishi Engineering Plastics Co., Ltd., trade name Novamid 1022C6, extrapolation melting start temperature: 215 ° C.” was used, and this was put into a 65 mmφ single screw extruder (L / D = 28). Then, it was melted and kneaded at a set temperature of 260 ° C., extruded with a T-die, and closely cooled to a cast roll at 30 ° C. to obtain an unstretched film of about 140 μm.

得られた未延伸フィルムを60℃の条件下でロール式延伸機にて縦方向に2.7倍延伸し、次いで、この縦延伸フィルムの端部をテンタークリップで保持し、テンターオーブン内で100℃の条件下で横方向に3.4倍に延伸した後、215℃で6秒間の熱固定を行った。熱固定を行った後のフィルムは、クリップの把持部に相当する両端部分はトリミングした。   The obtained unstretched film was stretched 2.7 times in the machine direction by using a roll-type stretcher under the condition of 60 ° C., and then the end of the longitudinally stretched film was held with a tenter clip, and 100% in a tenter oven. The film was stretched 3.4 times in the transverse direction under the condition of ° C., and then heat-fixed at 215 ° C. for 6 seconds. The heat-fixed film was trimmed at both end portions corresponding to the clip holding portion.

トリミング後のフィルムの片面に、不活性ガスとして窒素ガスを用い、窒素濃度が99.9%、活性ガスとして酸素ガスを用い、酸素濃度が0.1%の雰囲気下で、コロナ処理を行った。 One side of the trimmed film was subjected to corona treatment in an atmosphere using nitrogen gas as the inert gas, nitrogen concentration of 99.9%, oxygen gas as the active gas, and oxygen concentration of 0.1%. .

表面処理を行った後、フィルムをロール状に巻き取り、厚さが約15μmの表面処理ポリアミド系フィルムを得た。 After the surface treatment, the film was wound into a roll to obtain a surface-treated polyamide film having a thickness of about 15 μm.

得られた表面処理ポリアミド系フィルムを用いて評価した結果を表1に示した。 The results of evaluation using the obtained surface-treated polyamide film are shown in Table 1.

(実施例2)
実施例1で、表面処理時の窒素濃度を99%、酸素濃度を1%とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Example 2)
A film was obtained in the same manner as in Example 1 except that the nitrogen concentration during the surface treatment was 99% and the oxygen concentration was 1%, and the same evaluation was performed. The results are shown in Table 1.

(実施例3)
実施例1で、表面処理時の窒素濃度を99.995%、酸素濃度を0.005%とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Example 3)
A film was obtained in the same manner as in Example 1 except that the nitrogen concentration during the surface treatment was 99.995% and the oxygen concentration was 0.005%, and the same evaluation was performed. The results are shown in Table 1.

(実施例4)
実施例1で、縦方向の延伸倍率を2.4倍とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
Example 4
A film was obtained in the same manner as in Example 1 except that the stretching ratio in the longitudinal direction was 2.4 times, and the same evaluation was performed. The results are shown in Table 1.

(実施例5)
実施例1で、延伸後の熱固定温度を200℃とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Example 5)
A film was obtained in the same manner as in Example 1 except that the heat setting temperature after stretching was 200 ° C., and the same evaluation was performed. The results are shown in Table 1.

(実施例6)
実施例1で、延伸後の熱固定温度を225℃とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Example 6)
A film was obtained in the same manner as in Example 1 except that the heat setting temperature after stretching was 225 ° C., and the same evaluation was performed. The results are shown in Table 1.

(実施例7)
実施例1で、表面処理時の窒素濃度を99.8%、酸素濃度を0.1%とし、さらに反応性ガスとして水素を0.1%添加した以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Example 7)
A film was obtained in the same manner as in Example 1, except that the nitrogen concentration during the surface treatment was 99.8%, the oxygen concentration was 0.1%, and 0.1% of hydrogen was added as a reactive gas. Was evaluated. The results are shown in Table 1.

(比較例1)
実施例1で、表面処理時の窒素濃度を90%、酸素濃度を10%とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Comparative Example 1)
A film was obtained in the same manner as in Example 1 except that the nitrogen concentration during the surface treatment was 90% and the oxygen concentration was 10%, and the same evaluation was performed. The results are shown in Table 1.

(比較例2)
実施例1で、縦方向の延伸倍率を2.3倍とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Comparative Example 2)
A film was obtained in the same manner as in Example 1 except that the stretching ratio in the longitudinal direction was 2.3 times, and the same evaluation was performed. The results are shown in Table 1.

(比較例3)
実施例1で、延伸後の熱固定温度を190℃とした以外は同様の方法でフィルムを得、同様の評価を行った。その結果を表1に示した。
(Comparative Example 3)
A film was obtained in the same manner as Example 1 except that the heat setting temperature after stretching was 190 ° C., and the same evaluation was performed. The results are shown in Table 1.

(比較例4)
実施例1で、延伸後の熱固定温度を230℃とした以外は同様の方法で検討を行ったが、テンター内でフィルムの破断が頻発し、連続して製膜することができなかった。その結果を表1に示した。

Figure 2011079998
(Comparative Example 4)
In Example 1, the same method was used except that the heat setting temperature after stretching was 230 ° C., but the film was frequently broken in the tenter and could not be continuously formed. The results are shown in Table 1.
Figure 2011079998

表1から、本発明フィルムである実施例1から実施例5については、すべての評価項目について良好な結果を示していることが分かる。特に、表面処理時の窒素濃度99%、酸素濃度1%とした実施例2に比べ、表面処理時の窒素濃度を99.9%、酸素濃度を0.1%とした他の実施例はラミネート強度がより優れること、また、縦延伸倍率を2.4倍とした実施例4に比べ、縦延伸倍率を2.7倍とした他の実施例はラミネート強度がより優れることが明らかとなった。さらに、表面処理時の雰囲気を、窒素濃度を99.8%、酸素濃度を0.01%、水素ガスを0.01%とした実施例7は、水素ガスを用いずに表面処理がなされた他の実施例に比べ、ラミネート強度が優れることが明らかとなった。   From Table 1, it can be seen that Examples 1 to 5 which are the films of the present invention show good results for all the evaluation items. In particular, compared with Example 2 in which the nitrogen concentration during the surface treatment is 99% and the oxygen concentration is 1%, the other examples in which the nitrogen concentration during the surface treatment is 99.9% and the oxygen concentration is 0.1% are laminated. It has been clarified that the strength is more excellent, and the laminate strength is superior in other examples in which the longitudinal draw ratio is 2.7 times compared to Example 4 in which the longitudinal draw ratio is 2.4 times. . Furthermore, in Example 7 in which the atmosphere during the surface treatment was such that the nitrogen concentration was 99.8%, the oxygen concentration was 0.01%, and the hydrogen gas was 0.01%, the surface treatment was performed without using hydrogen gas. It became clear that the laminate strength was superior to other examples.

これに対して、表面処理時の窒素ガス比率が90%と高かった比較例1は表面処理の効果が薄く、湿潤時のラミネート強度が低かった。縦延伸倍率が低い比較例2は、延伸ムラが発生し、厚み変動率が大きいフィルムであった。その上、延伸ムラの影響で、湿潤時のラミネート強度も低かった。熱固定温度が低い比較例3では、MDの熱水収縮率が大きいため、印刷、ラミネート等の工程で収縮してしまいピッチがずれる等のトラブルが発生しやすいという問題がある。さらに、延伸配向の影響で、湿潤時のラミネート強度も低かった。熱固定温度が高い比較例4ではテンター内で破断が頻発し、連続して製膜することができなかった。   On the other hand, Comparative Example 1 in which the nitrogen gas ratio during the surface treatment was as high as 90% was less effective for the surface treatment, and the laminate strength when wet was low. Comparative Example 2 having a low longitudinal stretching ratio was a film in which stretching unevenness occurred and the thickness variation rate was large. In addition, the laminate strength when wet was also low due to the effect of stretching unevenness. In Comparative Example 3 where the heat setting temperature is low, the hot water shrinkage rate of MD is large, so that there is a problem that troubles such as shrinkage due to shrinkage in printing, laminating, and the like are likely to occur. Furthermore, the laminate strength when wet was also low due to the effect of stretch orientation. In Comparative Example 4 having a high heat setting temperature, breakage occurred frequently in the tenter, and the film could not be continuously formed.

Claims (8)

脂肪族ポリアミド樹脂を主成分とするポリアミド系フィルムであって、少なくとも一方のフィルム表面に、不活性ガス濃度99%以上、活性ガス濃度1%以下の雰囲気下での放電処理による表面処理がなされた表面処理面の湿潤時のラミネート強度が3.9N/15mm以上であることを特徴とする表面処理ポリアミド系フィルム。 A polyamide-based film containing an aliphatic polyamide resin as a main component, and at least one film surface is subjected to surface treatment by discharge treatment in an atmosphere having an inert gas concentration of 99% or more and an active gas concentration of 1% or less. A surface-treated polyamide film having a laminate strength when the surface-treated surface is wet is 3.9 N / 15 mm or more. 95℃×5分におけるフィルムの流れ方向(MD)の熱水収縮率が3.0%以下であり、且つ、フィルムの幅方向(TD)の厚み変動率が平均厚みの10%以下である請求項1に記載の表面処理ポリアミド系フィルム。 The hot water shrinkage rate in the film flow direction (MD) at 95 ° C. × 5 minutes is 3.0% or less, and the thickness variation rate in the width direction (TD) of the film is 10% or less of the average thickness. Item 2. The surface-treated polyamide film according to Item 1. 前記表面処理時の雰囲気が、不活性ガス濃度99%以上、活性ガス濃度1%以下、反応性ガス濃度1%以下ある請求項1又は2に記載の表面処理ポリアミド系フィルム。 The surface-treated polyamide film according to claim 1 or 2, wherein an atmosphere during the surface treatment has an inert gas concentration of 99% or more, an active gas concentration of 1% or less, and a reactive gas concentration of 1% or less. 前記不活性ガスが窒素、ヘリウム、ネオン、アルゴン、クリプトンから選ばれる少なくとも一種の気体である請求項1から3のいずれか1つに記載の表面処理ポリアミド系フィルム。 The surface-treated polyamide film according to any one of claims 1 to 3, wherein the inert gas is at least one gas selected from nitrogen, helium, neon, argon, and krypton. 請求項1から4のいずれか1つに記載の表面処理ポリアミド系フィルムにおける前記表面処理面が、樹脂積層体の少なくともいずれか一方の表面を構成するよう配置された多層構造からなる表面処理ポリアミド系フィルム A surface-treated polyamide system comprising a multilayer structure in which the surface-treated surface of the surface-treated polyamide film according to any one of claims 1 to 4 is disposed so as to constitute at least one surface of a resin laminate. the film 請求項1から5のいずれか1つに記載の表面処理ポリアミド系フィルムの前記表面処理面に、シーラントフィルムをラミネートしてなることを特徴とする表面処理ポリアミド系ラミネートフィルム。 A surface-treated polyamide-based laminate film obtained by laminating a sealant film on the surface-treated surface of the surface-treated polyamide-based film according to any one of claims 1 to 5. 請求項6記載の表面処理ポリアミド系ラミネートフィルムからなる袋体。 A bag comprising the surface-treated polyamide-based laminate film according to claim 6. フラットダイから押出された脂肪族ポリアミド系樹脂を主成分とする未延伸フィルムをMD、TDともに2.4倍以上の延伸倍率でテンター式逐次二軸延伸法により延伸する工程の後、200℃以上、且つ前記脂肪族ポリアミド系樹脂の補外融解開始温度(JIS K 7121に準拠して測定)より10℃高い温度以下で熱固定を行う工程を経て、フィルムの少なくとも一方の表面に、不活性ガス濃度99%以上、活性ガス濃度1%以下の雰囲気下でのコロナ処理又はプラズマ処理のいずれか一種の放電処理による表面処理を行う工程を有することを特徴とする表面処理ポリアミド系フィルムの製造方法。 After a step of stretching an unstretched film mainly composed of an aliphatic polyamide-based resin extruded from a flat die by a tenter-type sequential biaxial stretching method at a stretching ratio of 2.4 times or more for both MD and TD, 200 ° C or more In addition, an inert gas is formed on at least one surface of the film through a step of heat setting at a temperature not higher than 10 ° C. higher than the extrapolated melting start temperature (measured in accordance with JIS K 7121) of the aliphatic polyamide resin. A method for producing a surface-treated polyamide film, comprising a step of performing a surface treatment by a discharge treatment of any one of corona treatment and plasma treatment in an atmosphere having a concentration of 99% or more and an active gas concentration of 1% or less.
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